JP2012057932A - Heating medium supply apparatus - Google Patents

Heating medium supply apparatus Download PDF

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JP2012057932A
JP2012057932A JP2011173226A JP2011173226A JP2012057932A JP 2012057932 A JP2012057932 A JP 2012057932A JP 2011173226 A JP2011173226 A JP 2011173226A JP 2011173226 A JP2011173226 A JP 2011173226A JP 2012057932 A JP2012057932 A JP 2012057932A
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flow path
heat exchanger
hot water
water
channel
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Hideki Hayakawa
秀樹 早川
Hideki Yamaguchi
秀樹 山口
Teru Morita
輝 森田
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Osaka Gas Co Ltd
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02BCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/12Hot water central heating systems using heat pumps

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Abstract

PROBLEM TO BE SOLVED: To provide a heating medium supply apparatus which is easy and simple in piping, requires no employment of a structure like a three-fluid heat exchanger of a complex structure as a heat exchanger, and minimizes the number of circulation pumps and heat exchangers, thereby having simplified configuration and reduced cost.SOLUTION: The heating medium supply apparatus includes a first water channel feeding water taken out of a hot water feed tank 2 by at least the pressure of potable water to a hot-water supply using part 1 via at least a burner heating type heat exchanger 6, and a second water channel for circulating water via the burner heating type heat exchanger 6, a load heat exchanger 7 and a heat pump heating type heat exchanger 5 by the pressure of the circulation pump. In the first water channel and second water channel, the water channel including the burner heating type heat exchanger 6 is configured at least in common, a burner combustion device N is switchable between a combustion state and a non-combustion state, and an operation control means 19 is included that freely switches a heat pump device 4 between an operation state and a non-operation state.

Description

本発明は、給湯利用箇所に供給する水を貯留する給湯タンクと、水路の水を循環させる循環ポンプと、ヒートポンプ装置により水を加熱するヒートポンプ加熱式熱交換器と、バーナー燃焼装置により水を加熱するバーナー加熱式熱交換器と、暖房負荷と追焚負荷の少なくとも一方で熱を消費する負荷熱交換器とを備えた熱媒供給装置に関する。   The present invention relates to a hot water supply tank for storing water to be supplied to a hot water use location, a circulation pump for circulating water in a water channel, a heat pump heating heat exchanger for heating water by a heat pump device, and heating water by a burner combustion device. The present invention relates to a heating medium supply device that includes a burner heating type heat exchanger that performs heating, and a load heat exchanger that consumes heat at least one of a heating load and a tracking load.

このような熱媒供給装置は、給湯タンクに貯留されている水をヒートポンプ加熱式熱交換器やバーナー加熱式熱交換器にて加熱して温水とし、給湯利用箇所に供給するとともに、ヒートポンプ加熱式熱交換器やバーナー加熱式熱交換器にて循環水を加熱して温水とし、その循環温水を負荷熱交換器に供給して暖房負荷や追焚負荷での熱消費に用いている。   Such a heating medium supply device heats water stored in a hot water supply tank with a heat pump heating type heat exchanger or a burner heating type heat exchanger to form hot water, and supplies it to a hot water supply use location. Circulating water is heated by a heat exchanger or a burner heating type heat exchanger to form hot water, and the circulating hot water is supplied to a load heat exchanger to be used for heat consumption in a heating load or a supplementary load.

従来の熱媒供給装置では、上水の圧力で給湯タンクから取り出した水を第1バーナー加熱式熱交換器を経由して給湯利用箇所に供給する給湯用水路と、第1循環ポンプの圧力で給湯タンクから取り出した水をヒートポンプ加熱式熱交換器を経由して給湯タンクに戻すタンク循環用水路と、第2循環ポンプの圧力でヒートポンプ加熱式熱交換器と第2バーナー加熱式熱交換器と負荷熱交換器を経由して水が循環する負荷循環用水路とが備えられている(例えば、特許文献1、2参照。)。   In a conventional heating medium supply device, hot water is supplied at the pressure of the first circulation pump, and a hot water supply channel for supplying water taken out from the hot water supply tank to the hot water use location via the first burner heating type heat exchanger. Water circulation path for returning water taken out from the tank to the hot water supply tank via the heat pump heating type heat exchanger, heat pump heating type heat exchanger, second burner heating type heat exchanger and load heat with the pressure of the second circulation pump And a load circulation water channel through which water circulates via an exchanger (see, for example, Patent Documents 1 and 2).

そして、特許文献1、2に記載の装置では、給湯用水路が、上水の圧力によって給湯タンクに貯留されている温水を給湯利用箇所に供給することができるとともに、給湯タンクに温水が貯留されていないときでも、給湯タンクに貯留されている水を第1バーナー加熱式熱交換器にて加熱して温水とし、その温水を給湯利用箇所に供給可能に構成されている。このように、給湯用水路は、上水の圧力によって、給湯タンクの水を用いて給湯利用箇所に温水を供給するものであるが、タンク循環用水路では、第1循環ポンプの圧力により水を循環させており、負荷循環用水路も、第2循環ポンプの圧力により水を循環させている。   In the apparatuses described in Patent Documents 1 and 2, the hot water supply channel can supply hot water stored in the hot water supply tank to the hot water supply use location by the pressure of clean water, and hot water is stored in the hot water supply tank. Even when there is no water, the water stored in the hot water supply tank is heated by the first burner heating type heat exchanger to be hot water, and the hot water can be supplied to the hot water supply use location. As described above, the hot water supply channel supplies hot water to the hot water use location using the water in the hot water tank by the pressure of the clean water. In the tank circulation channel, the water is circulated by the pressure of the first circulation pump. The load circulation channel also circulates water by the pressure of the second circulation pump.

また、特許文献1、2に記載の装置では、給湯用水路とタンク循環用水路と負荷循環用水路との夫々は、独立して水を通流させる回路として構成されている。そして、給湯用水路及び負荷循環用水路の夫々に、バーナー加熱式熱交換器が各別に設けられており、タンク循環用水路及び負荷循環用水路の夫々に、循環ポンプが各別に設けられている。また、ヒートポンプ加熱式熱交換器では、ヒートポンプ装置の媒体とタンク循環用水路の水とを熱交換させるとともに、ヒートポンプ装置の媒体と負荷循環用水路の水とを熱交換させるために、三流体熱交換器にて構成されている。   In the devices described in Patent Documents 1 and 2, each of the hot water supply channel, the tank circulation channel, and the load circulation channel is configured as a circuit that allows water to flow independently. A burner heating type heat exchanger is provided for each of the hot water supply channel and the load circulation channel, and a circulation pump is provided for each of the tank circulation channel and the load circulation channel. In the heat pump heating type heat exchanger, a three-fluid heat exchanger is used to exchange heat between the medium of the heat pump device and the water in the tank circulation channel, and to exchange heat between the medium of the heat pump device and the water in the load circulation channel. It is composed of.

別の従来の熱媒供給装置では、上水の圧力で給湯タンクから取り出した水をそのまま給湯利用箇所に供給する給湯用水路と、循環ポンプの圧力でヒートポンプ加熱式熱交換器と負荷熱交換器を経由して水が循環する第1負荷循環用水路と、循環ポンプの圧力でバーナー加熱式熱交換器と負荷熱交換器を経由して水が循環する第2負荷循環用水路とが備えられている(例えば、特許文献3参照。)。
この特許文献3に記載の装置では、循環ポンプ及びバーナー加熱式熱交換器が1つずつ設けられており、第1負荷循環用水路と第2負荷循環用水路が、循環ポンプとヒートポンプ加熱式熱交換器とバーナー加熱式熱交換器を含む水路が少なくとも共通に構成されている。
In another conventional heating medium supply device, a hot water supply channel that supplies water taken from a hot water supply tank as it is to the hot water supply location with the pressure of clean water, and a heat pump heating heat exchanger and a load heat exchanger with the pressure of the circulation pump A first load circulation water channel through which water circulates, and a second load circulation water channel through which water circulates through the burner-heated heat exchanger and the load heat exchanger at the pressure of the circulation pump ( For example, see Patent Document 3.)
In the apparatus described in Patent Document 3, one circulation pump and one burner heating type heat exchanger are provided, and the first load circulation channel and the second load circulation channel are the circulation pump and the heat pump heating type heat exchanger. And a water channel including a burner heating type heat exchanger is at least commonly configured.

特開2009−299941号公報JP 2009-299941 A 特開2009−299942号公報JP 2009-299942 A 特開2001−317806号公報Japanese Patent Laid-Open No. 2001-317806

上記特許文献1、2に記載の装置では、給湯用水路とタンク循環用水路と負荷循環用水路との夫々が独立して水を通流させる回路として構成されているので、水を通流させる流路部位を別々に配管しなければならない。よって、流路部位の数が多数になるとともに、その多数の流路部位を限られたスペースに配管しなければならず、配管が複雑になるという問題が生じる。
また、上記特許文献1、2に記載の装置では、循環ポンプ及びバーナー加熱式熱交換器の夫々が2つずつ設けられているので、部材点数が増加してコストアップに繋がるとともに、構成の複雑化を招くものとなっている。しかも、ヒートポンプ加熱式熱交換器が、構造が複雑な三流体熱交換器にて構成されているので、構成の複雑化がより顕著なものとなっている。
In the devices described in Patent Documents 1 and 2, since each of the hot water supply channel, the tank circulation channel, and the load circulation channel is configured as a circuit that allows water to flow independently, a flow channel portion that allows water to flow therethrough. Must be piped separately. Therefore, the number of flow path portions becomes large, and the large number of flow path portions must be piped in a limited space, resulting in a problem of complicated piping.
In addition, in the devices described in Patent Documents 1 and 2, since each of the circulation pump and the burner heating type heat exchanger is provided two by two, the number of members increases, resulting in an increase in cost and a complicated configuration. It has become a cause. And since the heat pump heating type heat exchanger is comprised by the three-fluid heat exchanger with a complicated structure, complication of a structure is more remarkable.

上記特許文献3に記載の装置では、第1負荷循環用水路と第2負荷循環用水路が、循環ポンプとヒートポンプ加熱式熱交換器とバーナー加熱式熱交換器を含む水路が少なくとも共通に構成されているので、特許文献1、2に記載の装置に比べて、流路部位の数を減らすことができ、配管が複雑になるという問題や、構成の複雑化及びコストアップを招くという問題を解消できるとも考えられる。
しかしながら、上記特許文献3に記載の装置では、上記特許文献1、2に記載の装置とは異なり、給湯用水路が、上水の圧力で給湯タンクから取り出した水をそのまま給湯利用箇所に供給する。したがって、給湯タンクの水を加熱して供給することができないため、給湯設定温度より少しでも温度が低い水が給湯タンクに貯留されているときには、温水を給湯タンクから全く供給することができない。そこで、循環ポンプ経由で供給された上水をバーナー加熱式熱交換器を経由して給湯利用箇所に供給する水路等を新たに備えなければならない。その為に、新たな流路部位を備えなければならず、結局、流路部位の数や部材点数が増加し、配管が複雑になり、構成の複雑化を招く虞がある。
In the apparatus described in Patent Document 3, the first load circulation channel and the second load circulation channel are configured to share at least a water channel including a circulation pump, a heat pump heating heat exchanger, and a burner heating heat exchanger. Therefore, compared to the devices described in Patent Documents 1 and 2, the number of flow path parts can be reduced, and the problem that the piping is complicated and the problem that the configuration is complicated and the cost is increased can be solved. Conceivable.
However, in the apparatus described in Patent Document 3, unlike the apparatuses described in Patent Documents 1 and 2, the hot water supply channel supplies the water taken out from the hot water supply tank as it is to the hot water use location with the pressure of the upper water. Therefore, since the water in the hot water supply tank cannot be heated and supplied, hot water cannot be supplied from the hot water supply tank at all when water having a temperature slightly lower than the hot water supply set temperature is stored in the hot water supply tank. Therefore, it is necessary to newly provide a water channel or the like for supplying the clean water supplied via the circulation pump to the hot water supply use location via the burner heating type heat exchanger. Therefore, it is necessary to provide a new flow path part, eventually increasing the number of flow path parts and the number of members, making the piping complicated and possibly complicating the configuration.

本発明は、かかる点に着目してなされたものであり、その目的は、配管が簡易でシンプルなものであり、熱交換器として構造が複雑な三流体熱交換器等の構造を採用する必要がなく、循環ポンプや熱交換器や弁の数を極力少なくして、構成の簡素化及びコストの低減を図ることができる熱媒供給装置を提供する点にある。   The present invention has been made paying attention to such a point, and its purpose is to adopt a structure such as a three-fluid heat exchanger having a simple and simple piping and a complicated structure as a heat exchanger. Therefore, the present invention is to provide a heat medium supply device that can reduce the number of circulation pumps, heat exchangers, and valves as much as possible to simplify the configuration and reduce the cost.

この目的を達成するために、本発明に係る熱媒供給装置の特徴構成は、給湯利用箇所に供給する水を貯留する給湯タンクと、水路の水を循環させる循環ポンプと、ヒートポンプ装置により水を加熱するヒートポンプ加熱式熱交換器と、バーナー燃焼装置により水を加熱するバーナー加熱式熱交換器と、暖房負荷と追焚負荷の少なくとも一方で熱を消費する負荷熱交換器と、少なくとも上水の圧力で前記給湯タンクから取り出した水を少なくとも前記バーナー加熱式熱交換器を経由して前記給湯利用箇所に供給する第1水路と、前記循環ポンプの圧力で前記バーナー加熱式熱交換器と前記負荷熱交換器と前記ヒートポンプ加熱式熱交換器を経由して水が循環する第2水路とを備え、前記第1水路と前記第2水路は、前記バーナー加熱式熱交換器を含む水路が少なくとも共通に構成され、前記バーナー燃焼装置を燃焼状態と非燃焼状態とに切換自在であり、且つ、前記ヒートポンプ装置を作動状態と非作動状態とに切換自在な運転制御手段が備えられている点にある。   In order to achieve this object, the heat medium supply device according to the present invention is characterized by a hot water supply tank that stores water to be supplied to a hot water supply use location, a circulation pump that circulates water in the water channel, and a heat pump device that supplies water. A heat pump heating heat exchanger that heats, a burner heating heat exchanger that heats water by a burner combustion device, a load heat exchanger that consumes heat in at least one of a heating load and an additional load, and at least clean water A first water passage for supplying water taken out from the hot water supply tank by pressure to the hot water supply utilization site via at least the burner heating heat exchanger, and the burner heating heat exchanger and the load by pressure of the circulation pump. A heat exchanger and a second water channel through which water circulates via the heat pump heating type heat exchanger, wherein the first water channel and the second water channel are the burner heating type heat exchanger. A water passage including at least a common configuration, and an operation control means capable of switching the burner combustion device between a combustion state and a non-combustion state and switching the heat pump device between an operation state and a non-operation state. There is in point.

本特徴構成によれば、第1水路が、少なくとも上水の圧力で給湯タンクから取り出した水をバーナー加熱式熱交換器を経由して給湯利用箇所に供給するので、少なくとも上水の圧力によって給湯タンクに貯留されている温水を給湯利用箇所に供給することができるとともに、給湯タンクに給湯設定温度より温度が低い水が貯留されているときでも、給湯タンクに貯留されている水をバーナー加熱式熱交換器にて加熱して温水とし、その温水を給湯利用箇所に供給することができる。これにより、第1水路では、給湯タンクの水をバーナー加熱式熱交換器を経由して給湯利用箇所に供給するために、少なくとも上水の圧力を用いることができる。また、第2水路は、循環ポンプの圧力で、給湯タンクを介さずに、バーナー加熱式熱交換器及びヒートポンプ加熱式熱交換器を経由した水を負荷熱交換器に供給することができる。そして、第2水路にて水を循環させる際に、運転制御手段がバーナー燃焼装置を非燃焼状態に切り換え且つヒートポンプ装置を作動状態に切り換えることで、ヒートポンプ加熱式熱交換器にて加熱された水を負荷熱交換器に供給することができ、運転制御手段がバーナー燃焼装置を燃焼状態に切り換え且つヒートポンプ装置を非作動状態に切り換えることで、バーナー加熱式熱交換器にて加熱された水を負荷熱交換器に供給することができる。したがって、運転制御手段がバーナー燃焼装置及びヒートポンプ装置の状態を切り換えることで、熱源をヒートポンプ装置又はバーナー燃焼装置として加熱された水を負荷熱交換器に供給することができる。   According to this feature, the first water channel supplies the water taken out from the hot water supply tank at least with the pressure of the hot water to the hot water use location via the burner heating type heat exchanger. The hot water stored in the tank can be supplied to the hot water use location, and the water stored in the hot water tank is burner-heated even when the hot water tank stores water whose temperature is lower than the hot water set temperature. It can be heated in a heat exchanger to make hot water, and the hot water can be supplied to a hot water supply use location. Thereby, in the 1st water channel, in order to supply the water of a hot-water supply tank to a hot-water supply utilization location via a burner heating type heat exchanger, the pressure of at least clean water can be used. Moreover, the 2nd water channel can supply the water which passed through the burner heating type heat exchanger and the heat pump heating type heat exchanger to a load heat exchanger by the pressure of a circulation pump, without going through a hot water supply tank. When the water is circulated in the second water channel, the operation control means switches the burner combustion device to the non-combustion state and the heat pump device to the operation state, so that the water heated by the heat pump heating heat exchanger Can be supplied to the load heat exchanger, and the operation control means switches the burner combustion device to the combustion state and the heat pump device to the non-operation state, thereby loading the water heated by the burner heating type heat exchanger. It can be supplied to a heat exchanger. Therefore, the operation control means switches the states of the burner combustion device and the heat pump device, so that heated water can be supplied to the load heat exchanger using the heat source as the heat pump device or the burner combustion device.

そして、水路としては、単に、第1水路と第2水路とを備えればよく、しかも、第1水路と第2水路の間では、バーナー加熱式熱交換器を含む水路が少なくとも共通であるので、1つの流路部位を各水路にて共通のものとして利用でき、流路部位の数を少なくすることができるとともに、循環ポンプ、バーナー加熱式熱交換器、及び、ヒートポンプ加熱式熱交換器の夫々を1つずつ設けるだけでよい。したがって、配管が簡易でシンプルなものであり、熱交換器として構造が複雑な三流体熱交換器等の構造を採用する必要がなく、循環ポンプや熱交換器の数を極力少なくして、構成の簡素化及びコストの低減を図ることができる熱媒供給装置を実現できる。   And as a water channel, what is necessary is just to provide a 1st water channel and a 2nd water channel, and since the water channel containing a burner heating type heat exchanger is at least common between a 1st water channel and a 2nd water channel. One flow path part can be used as a common part in each water channel, and the number of flow path parts can be reduced, and the circulation pump, the burner heating type heat exchanger, and the heat pump heating type heat exchanger It is only necessary to provide each one. Therefore, piping is simple and simple, and it is not necessary to adopt a three-fluid heat exchanger with a complicated structure as a heat exchanger, and the number of circulation pumps and heat exchangers is reduced as much as possible. It is possible to realize a heat medium supply device that can achieve simplification and cost reduction.

本発明に係る熱媒供給装置の更なる特徴構成は、前記給湯タンクに接続されて上水を前記給湯タンクに給水する第1流路部位と、前記給湯タンクと前記バーナー加熱式熱交換器を接続する第2流路部位と、前記バーナー加熱式熱交換器と前記給湯利用箇所を接続する第3流路部位と、前記第3流路部位の途中部位と前記負荷熱交換器を接続する第4流路部位と、前記負荷熱交換器と前記ヒートポンプ加熱式熱交換器を接続する第5流路部位と、前記ヒートポンプ加熱式熱交換器と前記第2流路部位の途中部位を接続して前記循環ポンプが設けられた第6流路部位とを備え、前記第1水路が、前記第1流路部位と前記給湯タンクと前記第2流路部位と前記バーナー加熱式熱交換器と前記第3流路部位と前記第4流路部位と前記負荷熱交換器と前記第5流路部位と前記ヒートポンプ加熱式熱交換器と前記第6流路部位とで構成され、前記第2水路が、前記バーナー加熱式熱交換器と前記第3流路部位の一部と前記第4流路部位と前記負荷熱交換器と前記第5流路部位と前記ヒートポンプ加熱式熱交換器と前記第6流路部位と前記第2流路部位の一部とで構成されている点にある。   A further characteristic configuration of the heat medium supply device according to the present invention includes a first flow path portion connected to the hot water supply tank for supplying clean water to the hot water supply tank, the hot water supply tank, and the burner heating type heat exchanger. A second flow path part to be connected, a third flow path part for connecting the burner heating type heat exchanger and the hot water supply use part, a middle part of the third flow path part and a second part for connecting the load heat exchanger. 4 flow passage portions, a fifth flow passage portion connecting the load heat exchanger and the heat pump heating heat exchanger, and a midway portion of the heat pump heating heat exchanger and the second flow passage portion are connected. A sixth flow path part provided with the circulation pump, and the first water channel includes the first flow path part, the hot water supply tank, the second flow path part, the burner heating type heat exchanger, and the first. Three flow path parts, the fourth flow path part, the load heat exchanger and the front It is composed of a fifth flow path part, the heat pump heating type heat exchanger, and the sixth flow path part, and the second water channel includes the burner heating type heat exchanger, a part of the third flow path part, and the The point comprised by the 4th flow-path part, the said load heat exchanger, the said 5th flow-path part, the said heat pump heating type heat exchanger, the said 6th flow-path part, and a part of said 2nd flow-path part. It is in.

本特徴構成によれば、流路部位として、第1〜第6流路部位の6つの流路部位が備えられるが、第1水路及び第2水路は、複数の流路部位を組み合わせて適切に構成することができる。そして、第1水路と第2水路は、第2流路部位の一部、バーナー加熱式熱交換器、第3流路部位の一部、第4流路部位、負荷熱交換器、第5流路部位、ヒートポンプ加熱式熱交換器、及び、第6流路部位を共通に構成することができる。したがって、第1水路と第2水路の間で、共通な流路部位を備えながら、開閉弁や比例弁を適宜切り換えることで、各水路を適切に構成することができるとともに、開閉弁や比例弁の数を極力少なくして、部材点数の増加を適切に防止して構成の簡素化を図ることができる。   According to this characteristic configuration, the six flow path parts of the first to sixth flow path parts are provided as the flow path parts. The first water channel and the second water channel are appropriately combined with a plurality of flow path parts. Can be configured. The first water channel and the second water channel are a part of the second flow path part, a burner heating type heat exchanger, a part of the third flow path part, a fourth flow path part, a load heat exchanger, and a fifth flow. The path part, the heat pump heating type heat exchanger, and the sixth flow path part can be configured in common. Therefore, while providing a common flow path portion between the first water channel and the second water channel, by appropriately switching the on-off valve and the proportional valve, each water channel can be appropriately configured, and the on-off valve and the proportional valve The number can be reduced as much as possible, and the increase in the number of members can be appropriately prevented, thereby simplifying the configuration.

ちなみに、第1水路と第2水路の回路構成については、給湯タンクに接続されて上水を給湯タンクに給水する第1流路部位と、給湯タンクとバーナー加熱式熱交換器を接続する第2流路部位と、バーナー加熱式熱交換器と給湯利用箇所を接続する第3流路部位と、第3流路部位の途中部位と負荷熱交換器を接続する第4流路部位と、負荷熱交換器とヒートポンプ加熱式熱交換器を接続して循環ポンプが設けられた第5流路部位と、ヒートポンプ加熱式熱交換器と第2流路部位の途中部位を接続する第6流路部位とを備え、第1水路を、第1流路部位と給湯タンクと第2流路部位とバーナー加熱式熱交換器と第3流路部位と第4流路部位と負荷熱交換器と第5流路部位とヒートポンプ加熱式熱交換器と第6流路部位とで構成し、第2水路を、バーナー加熱式熱交換器と第3流路部位の一部と第4流路部位と負荷熱交換器と第5流路部位とヒートポンプ加熱式熱交換器と第6流路部位と第2流路部位の一部とで構成することもできる。   Incidentally, as for the circuit configuration of the first water channel and the second water channel, the first channel part that is connected to the hot water tank and supplies the hot water to the hot water tank, and the second channel that connects the hot water tank and the burner heating type heat exchanger. A flow path part, a third flow path part for connecting the burner heating type heat exchanger and the hot water supply use part, a fourth flow path part for connecting the intermediate part of the third flow path part and the load heat exchanger, and load heat A fifth flow path portion provided with a circulation pump by connecting the exchanger and the heat pump heating heat exchanger, and a sixth flow path portion connecting the heat pump heating heat exchanger and the intermediate portion of the second flow path portion. A first water channel, a hot water tank, a second flow channel, a burner heating heat exchanger, a third flow channel, a fourth flow channel, a load heat exchanger, and a fifth flow. A passage part, a heat pump heating type heat exchanger, and a sixth passage part. Heater, part of third flow path part, fourth flow path part, load heat exchanger, fifth flow path part, heat pump heating type heat exchanger, sixth flow path part and second flow path It can also consist of a part of the part.

本発明に係る熱媒供給装置の更なる特徴構成は、前記運転制御手段は、前記第1水路により前記給湯利用箇所に水を供給する給湯運転と、前記循環ポンプを作動させて前記バーナー燃焼装置を非燃焼状態に切り換え且つ前記ヒートポンプ装置を作動状態に切り換えて前記第2水路により前記ヒートポンプ加熱式熱交換器にて加熱された水を前記負荷熱交換器に供給するヒートポンプ加熱状態での熱消費運転と、前記循環ポンプを作動させて前記バーナー燃焼装置を燃焼状態に切り換え且つ前記ヒートポンプ装置を非作動状態に切り換えて前記第2水路により前記バーナー加熱式熱交換器にて加熱された水を前記負荷熱交換器に供給するバーナー加熱状態での熱消費運転とを実行可能に構成されている点にある。   The heat medium supply device according to the present invention is further characterized in that the operation control means includes a hot water supply operation in which water is supplied to the hot water supply utilization site through the first water channel, and the circulation pump is operated to operate the burner combustion device. Is switched to a non-combustion state, and the heat pump device is switched to an operating state, and water heated in the heat pump heating type heat exchanger through the second water channel is supplied to the load heat exchanger. Operation, switching the burner combustion device to a combustion state by operating the circulation pump and switching the heat pump device to a non-operation state, and heating the water heated by the burner heating heat exchanger through the second water channel The heat consumption operation in the burner heating state supplied to the load heat exchanger can be executed.

本特徴構成によれば、運転制御手段が給湯運転を行うことで、少なくとも上水の圧力で給湯タンクから取り出した水をバーナー加熱式熱交換器を経由して給湯利用箇所に供給することができ、給湯利用箇所への水の供給を適切に行うことができる。そして、運転制御手段がヒートポンプ加熱状態での熱消費運転を行うことで、循環ポンプの圧力で、ヒートポンプ加熱式熱交換器にて加熱された水を、バーナー加熱式熱交換器にて加熱することなく、負荷熱交換器に供給することができる。また、運転制御手段がバーナー加熱状態での熱消費運転を行うことで、循環ポンプの圧力で、バーナー加熱式熱交換器にて加熱された水を、ヒートポンプ加熱式熱交換器にて加熱することなく、負荷熱交換器に供給することができる。このように、運転制御手段が、熱消費運転として、ヒートポンプ加熱状態での熱消費運転とバーナー加熱状態での熱消費運転とに切り換えて実行することで、熱源としてヒートポンプ装置とバーナー燃焼装置とのどちらを使用するかを選択できながら、負荷熱交換器への水の供給を適切に行うことができる。したがって、運転制御手段が各運転を行うことで、給湯、暖房及び追焚に柔軟に対応することができながら、配管が簡易でシンプルなものとして、構成の簡素化及びコストの低減を図ることができる有用な熱媒供給装置を実現できる。   According to this characteristic configuration, when the operation control means performs the hot water supply operation, the water taken out from the hot water supply tank at least with the pressure of the clean water can be supplied to the hot water use location via the burner heating type heat exchanger. In addition, water can be appropriately supplied to the hot water use location. Then, the operation control means performs the heat consumption operation in the heat pump heating state, so that the water heated in the heat pump heating type heat exchanger is heated in the burner heating type heat exchanger with the pressure of the circulation pump. And can be supplied to a load heat exchanger. Moreover, the water heated by the burner heating type heat exchanger is heated by the heat pump heating type heat exchanger at the pressure of the circulation pump by the operation control means performing the heat consumption operation in the burner heating state. And can be supplied to a load heat exchanger. As described above, the operation control means performs the heat consumption operation by switching between the heat consumption operation in the heat pump heating state and the heat consumption operation in the burner heating state, so that the heat pump device and the burner combustion device are used as heat sources. While being able to select which one to use, water can be appropriately supplied to the load heat exchanger. Therefore, when the operation control means performs each operation, it is possible to flexibly cope with hot water supply, heating, and remembrance, and simplify the configuration and reduce the cost by simplifying the piping. It is possible to realize a useful heat medium supply device.

本発明に係る熱媒供給装置の更なる特徴構成は、前記循環ポンプの圧力で少なくとも前記給湯タンクと前記ヒートポンプ加熱式熱交換器を経由して水が循環する第3水路を備え、前記第3水路によって、前記給湯タンクから取り出した水を前記ヒートポンプ加熱式熱交換器にて加熱し、その加熱された水を前記給湯タンクに戻すように水を循環自在に構成され、前記第2水路と前記第3水路は、前記ヒートポンプ加熱式熱交換器を含む水路が少なくとも共通に構成されている点にある。   A further characteristic configuration of the heat medium supply device according to the present invention includes a third water channel through which water circulates at least via the hot water supply tank and the heat pump heating heat exchanger at the pressure of the circulation pump, The water taken out from the hot water supply tank is heated by the heat pump in the heat pump heating type heat exchanger, and the water can be circulated so as to return the heated water to the hot water supply tank. A 3rd water channel exists in the point by which the water channel containing the said heat pump heating type heat exchanger is comprised at least in common.

本特徴構成によれば、第3水路は、循環ポンプの圧力によって、給湯タンクから取り出した水をヒートポンプ加熱式熱交換器にて加熱し、その加熱された水を給湯タンクに戻すことができるので、ヒートポンプ加熱式熱交換器にて水を加熱して温水とし、その温水を給湯タンクに貯湯することができる。したがって、ヒートポンプ装置により外気等から取得した熱を給湯タンクに蓄熱することができる。そして、給湯タンクの水は、第1水路により給湯タンクから取り出されて給湯利用箇所に供給されるので、給湯タンクに蓄熱した熱を有効に活用することができ、エネルギー効率の向上を図ることができる。   According to this characteristic configuration, the third water channel can heat the water taken out from the hot water supply tank by the heat pump heating heat exchanger and return the heated water to the hot water supply tank by the pressure of the circulation pump. The water can be heated to warm water by a heat pump heating type heat exchanger, and the hot water can be stored in a hot water supply tank. Therefore, the heat acquired from the outside air or the like by the heat pump device can be stored in the hot water supply tank. And since the water of a hot-water supply tank is taken out from a hot-water supply tank by a 1st water channel, and is supplied to a hot-water supply utilization location, the heat accumulated in the hot-water supply tank can be used effectively, and energy efficiency can be improved. it can.

本発明に係る熱媒供給装置の更なる特徴構成は、前記給湯タンクに接続されて上水を前記給湯タンクに給水する第1流路部位と、前記給湯タンクと前記バーナー加熱式熱交換器を接続する第2流路部位と、前記負荷熱交換器と前記ヒートポンプ加熱式熱交換器を接続する第5流路部位と、前記ヒートポンプ加熱式熱交換器と前記第2流路部位の途中部位を接続して前記循環ポンプが設けられた第6流路部位と、前記第1流路部位の途中部位と前記第5流路部位の途中部位とを接続する第7流路部位とを備え、前記第3水路が、前記給湯タンクと前記第1流路部位の一部と前記第7流路部位と前記第5流路部位の一部と前記ヒートポンプ加熱式熱交換器と前記第6流路部位と前記第2流路部位の一部とで構成されている点にある。   A further characteristic configuration of the heat medium supply device according to the present invention includes a first flow path portion connected to the hot water supply tank for supplying clean water to the hot water supply tank, the hot water supply tank, and the burner heating type heat exchanger. A second flow path part to be connected, a fifth flow path part to connect the load heat exchanger and the heat pump heating type heat exchanger, and an intermediate part of the heat pump heating type heat exchanger and the second flow path part. A sixth flow path part connected and provided with the circulation pump; and a seventh flow path part for connecting a midway part of the first flow path part and a midway part of the fifth flow path part, The third water channel includes the hot water tank, a part of the first channel part, the seventh channel part, a part of the fifth channel part, the heat pump heating type heat exchanger, and the sixth channel part. And a part of the second flow path part.

本特徴構成によれば、第1流路部位、第2流路部位、第5流路部位、第6流路部位、及び、第7流路部位を組み合わせて第3水路を適切に構成することができる。そして、上述の如く、第1流路部位、第2流路部位、第5流路部位、及び、第6流路部位は、第1水路や第2水路を構成するためにも用いられている。したがって、第1水路、第2水路、及び、第3水路の間で、共通な流路部位を備えながら、開閉弁や比例弁を適宜切り換えることで、各水路を適切に構成することができるとともに、開閉弁や比例弁の数を極力少なくして、部材点数の増加を適切に防止して構成の簡素化を図ることができる。   According to this characteristic configuration, the third channel is appropriately configured by combining the first channel portion, the second channel portion, the fifth channel portion, the sixth channel portion, and the seventh channel portion. Can do. As described above, the first flow path part, the second flow path part, the fifth flow path part, and the sixth flow path part are also used to configure the first water channel and the second water channel. . Therefore, while providing a common flow path portion between the first water channel, the second water channel, and the third water channel, each water channel can be appropriately configured by appropriately switching the on-off valve and the proportional valve. Further, the number of on-off valves and proportional valves can be reduced as much as possible to appropriately prevent an increase in the number of members, thereby simplifying the configuration.

ちなみに、第3水路の回路構成については、給湯タンクに接続されて上水を給湯タンクに給水する第1流路部位と、給湯タンクとバーナー加熱式熱交換器を接続する第2流路部位と、負荷熱交換器とヒートポンプ加熱式熱交換器を接続して循環ポンプが設けられた第5流路部位と、ヒートポンプ加熱式熱交換器と第2流路部位の途中部位を接続する第6流路部位と、第1流路部位の途中部位と第5流路部位における負荷熱交換器と循環ポンプの間の部位とを接続する第7流路部位とを備え、第3水路を、給湯タンクと第1流路部位の一部と第7流路部位と第5流路部位の一部とヒートポンプ加熱式熱交換器と第6流路部位と第2流路部位の一部とで構成することもできる。   Incidentally, as for the circuit configuration of the third water channel, a first channel part connected to the hot water tank and supplying the hot water to the hot water tank, and a second channel part connecting the hot water tank and the burner heating type heat exchanger, The sixth flow connecting the fifth flow path part provided with the circulation pump by connecting the load heat exchanger and the heat pump heating type heat exchanger, and the middle part of the heat pump heating type heat exchanger and the second flow path part. A passage portion, a seventh passage portion connecting the intermediate portion of the first passage portion and the portion between the load heat exchanger and the circulation pump in the fifth passage portion, and the third water passage as a hot water supply tank And a part of the first flow path part, a seventh flow path part, a part of the fifth flow path part, a heat pump heating type heat exchanger, a sixth flow path part, and a part of the second flow path part. You can also

本発明に係る熱媒供給装置の更なる特徴構成は、前記運転制御手段は、前記循環ポンプを作動させて前記ヒートポンプ装置を作動状態に切り換えて前記第3水路により前記ヒートポンプ加熱式熱交換器にて加熱された水を前記給湯タンクに供給する蓄熱運転を実行可能に構成されている点にある。   According to a further characteristic configuration of the heat medium supply device according to the present invention, the operation control means operates the circulation pump to switch the heat pump device to an operating state, and the heat pump heating heat exchanger is switched to the heat pump by the third water channel. The heat storage operation for supplying the heated water to the hot water supply tank is executable.

本特徴構成によれば、運転制御手段が蓄熱運転を行うことで、給湯タンクから取り出した水をヒートポンプ加熱式熱交換器にて加熱し、その加熱された水を給湯タンクに戻して、ヒートポンプ装置から取得した熱を給湯タンクに蓄熱することができる。そして、上述の如く、運転制御手段が、蓄熱運転を行った後、給湯運転を行うことで、給湯タンクに蓄熱されている熱を給湯利用箇所に供給することができ、ヒートポンプ装置から取得した熱を給湯に有効に活用することができ、エネルギー効率の向上を図ることができる。   According to this characteristic configuration, when the operation control means performs the heat storage operation, the water taken out from the hot water supply tank is heated by the heat pump heating type heat exchanger, and the heated water is returned to the hot water supply tank, and the heat pump device The heat acquired from can be stored in the hot water tank. Then, as described above, the operation control means can supply the heat stored in the hot water supply tank to the hot water supply use location by performing the hot water supply operation after performing the heat storage operation, and the heat acquired from the heat pump device. Can be effectively used for hot water supply, and energy efficiency can be improved.

本発明に係る熱媒供給装置の更なる特徴構成は、前記第2水路と前記第3水路は、前記給湯タンクから取り出した水を前記バーナー加熱式熱交換器にて加熱し、その加熱された水を前記給湯タンクに戻すように水を循環自在に構成されている点にある。   According to a further characteristic configuration of the heat medium supply device according to the present invention, the second water channel and the third water channel heat the water taken out from the hot water supply tank by the burner heating type heat exchanger, and are heated. The water circulates so that the water is returned to the hot water supply tank.

本特徴構成によれば、第2水路と第3水路によって、給湯タンクから取り出した水をバーナー加熱式熱交換器にて加熱し、その加熱された水を給湯タンクに戻すことができるので、バーナー燃焼装置を熱源として給湯タンクの水を加熱することができる。したがって、給湯タンクは、水を貯留しているので、レジオネラ菌等が繁殖する可能性があるが、給湯タンクの水を高温として殺菌消毒することができるので、レジオネラ菌等の繁殖を適切に防止することができる。   According to this characteristic configuration, the water taken out from the hot water tank can be heated by the burner heating type heat exchanger by the second water channel and the third water channel, and the heated water can be returned to the hot water tank. The water in the hot water supply tank can be heated using the combustion device as a heat source. Therefore, since the hot water tank stores water, Legionella bacteria and the like may propagate, but the water in the hot water tank can be sterilized at a high temperature, thus preventing the breeding of Legionella bacteria and the like appropriately. can do.

本発明に係る熱媒供給装置の更なる特徴構成は、少なくとも前記バーナー加熱式熱交換器をバイパスして前記循環ポンプの圧力を使わずに上水の圧力で前記給湯タンクから取り出した水を前記給湯利用箇所に供給する第1バイパス水路を形成可能に構成されている点にある。   A further characteristic configuration of the heat medium supply device according to the present invention is that the water taken out from the hot water supply tank by the pressure of clean water without using the pressure of the circulation pump by bypassing at least the burner heating type heat exchanger. It exists in the point comprised so that the 1st bypass water channel supplied to a hot-water supply utilization location can be formed.

本特徴構成によれば、第1バイパス水路では、バーナー加熱式熱交換器を介さずに、給湯タンクの水を給湯利用箇所に供給することができるので、第1バイパス水路にて給湯利用箇所への給湯を行っているときには、バーナー燃焼装置を他の熱源として利用することができる。したがって、第1バイパス水路にて、上水の圧力で給湯タンクから取り出した水を給湯利用箇所に供給することと、バーナー燃焼装置を熱源としてバーナー加熱式熱交換器にて水を加熱することを、お互いに干渉することなく同時に行うことができる。   According to this characteristic configuration, in the first bypass channel, the water in the hot water tank can be supplied to the hot water use location without going through the burner heating type heat exchanger. When the hot water is being supplied, the burner combustion apparatus can be used as another heat source. Therefore, in the first bypass channel, supplying water taken out from the hot water supply tank with the pressure of clean water to the hot water use location, and heating the water in the burner heating type heat exchanger using the burner combustion device as a heat source. , Can be done at the same time without interfering with each other.

本発明に係る熱媒供給装置の更なる特徴構成は、前記給湯タンクに接続されて上水を前記給湯タンクに給水する第1流路部位と、前記給湯タンクと前記バーナー加熱式熱交換器を接続して前記循環ポンプが設けられた第2流路部位と、前記バーナー加熱式熱交換器と前記給湯利用箇所を接続する第3流路部位と、前記第3流路部位の途中部位と前記負荷熱交換器を接続する第4流路部位と、前記負荷熱交換器と前記ヒートポンプ加熱式熱交換器を接続する第5流路部位と、前記ヒートポンプ加熱式熱交換器と前記第2流路部位における前記給湯タンクと前記循環ポンプの間の部位を接続する第6流路部位と、前記第2流路部位における前記給湯タンクと前記第6流路部位への接続箇所までの間の部位及び前記第3流路部位における前記第4流路部位への接続箇所と前記給湯利用箇所までの間の部位を接続する第1バイパス流路部位とを備え、前記第1水路が、前記第1流路部位と前記給湯タンクと前記第2流路部位と前記バーナー加熱式熱交換器と前記第3流路部位とで構成され、前記第1バイパス水路が、前記第1流路部位と前記給湯タンクと前記第2流路部位の一部と前記第1バイパス流路部位と前記第3流路部位の一部とで構成され、前記第2水路が、前記バーナー加熱式熱交換器と前記第3流路部位の一部と前記第4流路部位と前記負荷熱交換器と前記第5流路部位と前記ヒートポンプ加熱式熱交換器と前記第6流路部位と前記第2流路部位の一部とで構成されている点にある。   A further characteristic configuration of the heat medium supply device according to the present invention includes a first flow path portion connected to the hot water supply tank for supplying clean water to the hot water supply tank, the hot water supply tank, and the burner heating type heat exchanger. A second flow path part connected and provided with the circulation pump; a third flow path part connecting the burner heating type heat exchanger and the hot water supply use part; a middle part of the third flow path part; A fourth flow path part for connecting the load heat exchanger, a fifth flow path part for connecting the load heat exchanger and the heat pump heating heat exchanger, the heat pump heating heat exchanger and the second flow path. A sixth flow path part for connecting a part between the hot water tank and the circulation pump in the part, a part between the hot water tank and the connection part to the sixth flow path part in the second flow path part, and The fourth flow in the third flow path part A first bypass flow path portion that connects a connection location to the location and a location between the hot water use location and the first water channel is the first flow path portion, the hot water supply tank, and the second flow channel. A part, the burner heating type heat exchanger, and the third flow path part, and the first bypass water channel includes the first flow path part, the hot water supply tank, a part of the second flow path part, and the The second bypass channel is composed of a first bypass channel part and a part of the third channel part, and the second water channel includes the burner heating type heat exchanger, a part of the third channel part and the fourth channel. It is in the point comprised by the site | part, the said load heat exchanger, the said 5th flow-path part, the said heat pump heating type heat exchanger, the said 6th flow-path part, and a part of said 2nd flow-path part.

本特徴構成によれば、第1〜第6流路部位、及び、第1バイパス流路部位の複数の流路部位を組み合わせて、第1水路、第1バイパス水路、及び、第2水路の夫々を適切に構成することができる。そして、第1水路、第1バイパス水路、及び、第2水路の間で、共通な流路部位を備えながら、開閉弁や比例弁を適宜切り換えることで、各水路を適切に構成することができるとともに、開閉弁や比例弁の数を極力少なくして、部材点数の増加を適切に防止して構成の簡素化を図ることができる。しかも、第1バイパス水路と第2水路とは、独立して水を通流させることができるので、第1バイパス水路にて、上水の圧力で給湯タンクから取り出した水を給湯利用箇所に供給することと、第2水路にて、循環ポンプの圧力でバーナー加熱式熱交換器にて加熱された水を負荷熱交換器に供給することを、お互いに干渉することなく適切に同時に行うことができる。   According to this characteristic configuration, each of the first water channel, the first bypass water channel, and the second water channel is obtained by combining a plurality of flow channel regions of the first to sixth flow channel regions and the first bypass flow channel region. Can be configured appropriately. And while providing a common flow-path part among a 1st waterway, a 1st bypass waterway, and a 2nd waterway, each waterway can be comprised appropriately by switching an on-off valve and a proportional valve suitably. At the same time, the number of on-off valves and proportional valves can be reduced as much as possible to appropriately prevent an increase in the number of members, thereby simplifying the configuration. In addition, since the first bypass channel and the second channel can be made to independently pass water, the water extracted from the hot water supply tank is supplied to the hot water use location by the pressure of the clean water in the first bypass channel. And simultaneously supplying the water heated by the burner heating type heat exchanger to the load heat exchanger at the pressure of the circulation pump in the second water channel without interfering with each other. it can.

ちなみに、第1水路、第1バイパス水路、及び、第2水路の回路構成については、下記のように構成することもできる。
つまり、給湯タンクに接続されて上水を給湯タンクに給水する第1流路部位と、給湯タンクとバーナー加熱式熱交換器を接続する第2流路部位と、バーナー加熱式熱交換器と給湯利用箇所を接続して循環ポンプが設けられた第3流路部位と、第3流路部位における循環ポンプと給湯利用箇所の間の部位と負荷熱交換器を接続する第4流路部位と、負荷熱交換器とヒートポンプ加熱式熱交換器を接続する第5流路部位と、ヒートポンプ加熱式熱交換器と第2流路部位の途中部位を接続する第6流路部位と、第2流路部位における給湯タンクと第6流路部位への接続箇所までの間の部位及び第3流路部位における第4流路部位への接続箇所と給湯利用箇所までの間の部位を接続する第1バイパス流路部位とを備え、第1水路を、第1流路部位と給湯タンクと第2流路部位とバーナー加熱式熱交換器と第3流路部位とで構成し、第1バイパス水路を、第1流路部位と給湯タンクと第2流路部位の一部と第1バイパス流路部位と第3流路部位の一部とで構成し、第2水路を、バーナー加熱式熱交換器と第3流路部位の一部と第4流路部位と負荷熱交換器と第5流路部位とヒートポンプ加熱式熱交換器と第6流路部位と第2流路部位の一部とで構成することができる。
Incidentally, the circuit configurations of the first water channel, the first bypass water channel, and the second water channel can be configured as follows.
That is, a first flow path portion connected to a hot water supply tank for supplying clean water to the hot water supply tank, a second flow path portion connecting the hot water supply tank and the burner heating heat exchanger, a burner heating heat exchanger, and a hot water supply A third flow path part provided with a circulation pump by connecting the use points, a fourth flow path part connecting the load heat exchanger with a part between the circulation pump and the hot water supply use point in the third flow path part, A fifth flow path portion connecting the load heat exchanger and the heat pump heating heat exchanger, a sixth flow path portion connecting the heat pump heating heat exchanger and the second flow path portion, and a second flow path. A first bypass that connects a portion between the hot water supply tank and the connection portion to the sixth flow passage portion in the portion and a portion between the connection portion to the fourth flow passage portion and the hot water supply use portion in the third flow passage portion. And a first water channel with the first flow channel region. A tank, a second flow path part, a burner heating type heat exchanger, and a third flow path part are configured, and the first bypass water channel is formed with a first flow path part, a hot water supply tank, a part of the second flow path part, 1 bypass flow path part and a part of the third flow path part, the second water channel is a burner heating type heat exchanger, a part of the third flow path part, a fourth flow path part and a load heat exchanger And a fifth flow path part, a heat pump heating type heat exchanger, a sixth flow path part, and a part of the second flow path part.

また、給湯タンクに接続されて上水を給湯タンクに給水する第1流路部位と、給湯タンクとバーナー加熱式熱交換器を接続する第2流路部位と、バーナー加熱式熱交換器と給湯利用箇所を接続する第3流路部位と、第3流路部位の途中部位と負荷熱交換器を接続する第4流路部位と、負荷熱交換器とヒートポンプ加熱式熱交換器を接続する第5流路部位と、ヒートポンプ加熱式熱交換器と第2流路部位の途中部位を接続して循環ポンプが設けられた第6流路部位と、第2流路部位における給湯タンクと第6流路部位への接続箇所までの間の部位及び第3流路部位における第4流路部位への接続箇所と給湯利用箇所までの間の部位を接続する第1バイパス流路部位とを備え、第1水路を、第1流路部位と給湯タンクと第2流路部位とバーナー加熱式熱交換器と第3流路部位と第4流路部位と負荷熱交換器と第5流路部位とヒートポンプ加熱式熱交換器と第6流路部位とで構成し、第1バイパス水路を、第1流路部位と給湯タンクと第2流路部位の一部と第1バイパス流路部位と第3流路部位の一部とで構成し、第2水路を、バーナー加熱式熱交換器と第3流路部位の一部と第4流路部位と負荷熱交換器と第5流路部位とヒートポンプ加熱式熱交換器と第6流路部位と第2流路部位の一部とで構成することができる。   In addition, a first flow path part connected to the hot water tank for supplying clean water to the hot water tank, a second flow path part for connecting the hot water tank and the burner heating heat exchanger, the burner heating heat exchanger and the hot water supply A third flow path part for connecting the use location, a fourth flow path part for connecting the intermediate part of the third flow path part and the load heat exchanger, and a second flow path for connecting the load heat exchanger and the heat pump heating type heat exchanger. A fifth flow path part, a heat pump heating heat exchanger and a sixth flow path part provided with a circulation pump by connecting a halfway part of the second flow path part, a hot water supply tank and a sixth flow in the second flow path part A first bypass flow path part for connecting a part between the connection part to the road part and the connection part to the fourth flow path part in the third flow path part and the hot water supply use part, Add 1 channel to 1st channel part, hot water supply tank, 2nd channel part and burner A heat exchanger, a third flow path part, a fourth flow path part, a load heat exchanger, a fifth flow path part, a heat pump heating heat exchanger, and a sixth flow path part, and a first bypass water channel The first flow path part, the hot water tank, a part of the second flow path part, the first bypass flow path part and the part of the third flow path part, and the second water channel is a burner heating type heat exchanger And a part of the third flow path part, a fourth flow path part, a load heat exchanger, a fifth flow path part, a heat pump heating type heat exchanger, a sixth flow path part and a part of the second flow path part. Can be configured.

さらに、給湯タンクに接続されて上水を給湯タンクに給水する第1流路部位と、給湯タンクとバーナー加熱式熱交換器を接続する第2流路部位と、バーナー加熱式熱交換器と給湯利用箇所を接続する第3流路部位と、第3流路部位の途中部位と負荷熱交換器を接続する第4流路部位と、負荷熱交換器とヒートポンプ加熱式熱交換器を接続して循環ポンプが設けられた第5流路部位と、ヒートポンプ加熱式熱交換器と第2流路部位の途中部位を接続する第6流路部位と、第2流路部位における給湯タンクと第6流路部位への接続箇所までの間の部位及び第3流路部位における第4流路部位への接続箇所と給湯利用箇所までの間の部位を接続する第1バイパス流路部位とを備え、第1水路を、第1流路部位と給湯タンクと第2流路部位とバーナー加熱式熱交換器と第3流路部位と第4流路部位と負荷熱交換器と第5流路部位とヒートポンプ加熱式熱交換器と第6流路部位とで構成し、第1バイパス水路を、第1流路部位と給湯タンクと第2流路部位の一部と第1バイパス流路部位と第3流路部位の一部とで構成し、第2水路を、バーナー加熱式熱交換器と第3流路部位の一部と第4流路部位と負荷熱交換器と第5流路部位とヒートポンプ加熱式熱交換器と第6流路部位と第2流路部位の一部とで構成することができる。   Further, a first flow path portion connected to the hot water supply tank for supplying clean water to the hot water supply tank, a second flow path portion connecting the hot water supply tank and the burner heating heat exchanger, a burner heating heat exchanger and hot water supply Connect the third flow path part that connects the use points, the fourth flow path part that connects the intermediate part of the third flow path part and the load heat exchanger, the load heat exchanger, and the heat pump heating type heat exchanger. A fifth flow path part provided with a circulation pump, a sixth flow path part connecting the heat pump heating heat exchanger and the intermediate part of the second flow path part, a hot water supply tank and a sixth flow in the second flow path part A first bypass flow path part for connecting a part between the connection part to the road part and the connection part to the fourth flow path part in the third flow path part and the hot water supply use part, 1 channel, 1st flow path part, hot water supply tank, 2nd flow path part, and burner A heat bypass heat exchanger, a third flow path part, a fourth flow path part, a load heat exchanger, a fifth flow path part, a heat pump heating heat exchanger, and a sixth flow path part, and a first bypass water channel Is composed of a first flow path part, a hot water supply tank, a part of the second flow path part, a first bypass flow path part and a part of the third flow path part, and the second water path is burner heating type heat exchange And a part of the third flow path part, the fourth flow path part, the load heat exchanger, the fifth flow path part, the heat pump heating heat exchanger, the sixth flow path part, and the second flow path part. Can be configured.

加えて、給湯タンクに接続されて上水を給湯タンクに給水する第1流路部位と、給湯タンクとバーナー加熱式熱交換器を接続して、給湯タンクに近い順に循環ポンプとヒートポンプ加熱式熱交換器が設けられた第2流路部位と、バーナー加熱式熱交換器と給湯利用箇所を接続する第3流路部位と、第3流路部位の途中部位と負荷熱交換器を接続する第4流路部位と、負荷熱交換器と第2流路部位における給湯タンクと循環ポンプの間の部位を接続する第6流路部位と、第2流路部位における給湯タンクと第6流路部位への接続箇所までの間の部位及び第3流路部位における第4流路部位への接続箇所と給湯利用箇所までの間の部位を接続する第1バイパス流路部位とを備え、第1水路を、第1流路部位と給湯タンクと第2流路部位とバーナー加熱式熱交換器と第3流路部位とで構成し、第1バイパス水路を、第1流路部位と給湯タンクと第2流路部位の一部と第1バイパス流路部位と第3流路部位の一部とで構成し、第2水路を、バーナー加熱式熱交換器と第3流路部位の一部と第4流路部位と負荷熱交換器と第6流路部位と第2流路部位の一部とで構成することができる。   In addition, the first flow path part connected to the hot water tank for supplying the hot water to the hot water tank, the hot water tank and the burner heating heat exchanger are connected, and the circulation pump and the heat pump heating heat are connected in order from the hot water tank. A second flow path part provided with an exchanger, a third flow path part for connecting a burner heating type heat exchanger and a hot water supply use part, and a middle part of the third flow path part for connecting a load heat exchanger. A fourth flow path portion, a load heat exchanger, a sixth flow path portion connecting the hot water supply tank and the circulation pump in the second flow path portion, and a hot water supply tank and a sixth flow path portion in the second flow path portion. A first bypass channel that includes a part between the connection point to the connection point and a connection point to the fourth channel part in the third channel part and a part between the hot water supply use part and the first water channel. The first flow path part, the hot water tank, the second flow path part and the burner It is composed of a thermal heat exchanger and a third flow path part, and the first bypass water path is made up of the first flow path part, the hot water tank, a part of the second flow path part, the first bypass flow path part, and the third flow. The second water channel is constituted by a burner heating type heat exchanger, a part of the third flow path part, a fourth flow path part, a load heat exchanger, a sixth flow path part, and a second. It can comprise with a part of channel part.

さらに加えて、給湯タンクに接続されて上水を給湯タンクに給水する第1流路部位と、給湯タンクとバーナー加熱式熱交換器を接続して、給湯タンクに近い順にヒートポンプ加熱式熱交換器と循環ポンプが設けられた第2流路部位と、バーナー加熱式熱交換器と給湯利用箇所を接続する第3流路部位と、第3流路部位の途中部位と負荷熱交換器を接続する第4流路部位と、負荷熱交換器と第2流路部位における給湯タンクとヒートポンプ加熱式熱交換器の間の部位を接続する第6流路部位と、第2流路部位における給湯タンクと第6流路部位への接続箇所までの間の部位及び第3流路部位における第4流路部位への接続箇所と給湯利用箇所までの間の部位を接続する第1バイパス流路部位とを備え、第1水路を、第1流路部位と給湯タンクと第2流路部位とバーナー加熱式熱交換器と第3流路部位とで構成し、第1バイパス水路を、第1流路部位と給湯タンクと第2流路部位の一部と第1バイパス流路部位と第3流路部位の一部とで構成し、第2水路を、バーナー加熱式熱交換器と第3流路部位の一部と第4流路部位と負荷熱交換器と第6流路部位と第2流路部位の一部とで構成することができる。   In addition, a heat pump heating type heat exchanger connected to the hot water supply tank is connected to the first flow path part for supplying the hot water to the hot water supply tank, and the hot water supply tank and the burner heating type heat exchanger are connected. And the second flow path part provided with the circulation pump, the third flow path part connecting the burner heating type heat exchanger and the hot water supply use part, and the intermediate part of the third flow path part and the load heat exchanger are connected. A fourth flow path portion, a load heat exchanger, a sixth flow path portion connecting portions between the hot water supply tank in the second flow passage portion and the heat pump heating heat exchanger, and a hot water supply tank in the second flow passage portion A first bypass flow path portion that connects a portion between the connection portion to the sixth flow passage portion and a connection portion to the fourth flow passage portion in the third flow passage portion and a portion between the hot water supply use location and the third flow passage portion; Provided with a first water channel, a first channel part and a hot water supply tank It is composed of two flow path parts, a burner heating type heat exchanger, and a third flow path part, and the first bypass water path is made up of the first flow path part, the hot water tank, a part of the second flow path part, and the first bypass flow. The second water channel is configured by a burner heating type heat exchanger, a part of the third channel part, a fourth channel part, a load heat exchanger, and a sixth channel. It can be composed of a flow path part and a part of the second flow path part.

本発明に係る熱媒供給装置の更なる特徴構成は、前記運転制御手段は、前記給湯運転において、前記給湯タンクの水の温度が前記給湯利用箇所にて要求されている給湯設定温度に対応する切換設定温度以上である場合に、前記第1バイパス水路により前記給湯利用箇所に水を供給するバイパス状態に切り換え、前記給湯タンクの水の温度が前記切換設定温度未満である場合に、前記第1水路により前記給湯利用箇所に水を供給する非バイパス状態に切り換えるように構成されている点にある。   According to a further characteristic configuration of the heat medium supply device according to the present invention, the operation control means corresponds to a hot water supply set temperature at which the temperature of the hot water supply tank is required at the hot water supply use location in the hot water supply operation. When the temperature is equal to or higher than the switching set temperature, the first bypass water channel is switched to a bypass state in which water is supplied to the hot water use location, and when the temperature of the water in the hot water tank is lower than the switching set temperature, the first There exists in the point comprised so that it may switch to the non-bypass state which supplies water to the said hot water supply utilization location by a water channel.

本特徴構成によれば、運転制御手段が給湯運転を行う際に、給湯タンクの水の温度が切換設定温度以上である場合には、運転制御手段がバイパス状態に切り換えて、第1バイパス水路によりバーナー加熱式熱交換器をバイパスして給湯利用箇所に水を直接供給している。これにより、給湯タンクに切換設定温度以上の水が存在する場合には、バーナー加熱式熱交換器をバイパスしてバーナー加熱式熱交換器を通過することによる放熱を防止できながら、給湯タンクの水をそのまま活用して給湯利用箇所に給湯設定温度の水を供給することができる。また、給湯タンクに切換設定温度以上の水が存在しない場合には、第1水路によりバーナー加熱式熱交換器を経由して給湯タンクの水を給湯利用箇所に供給することができるので、バーナー加熱式熱交換器にて給湯タンクの水を加熱して給湯利用箇所に給湯設定温度の水を供給することができる。したがって、給湯タンクの水を有効に活用しながら、給湯利用箇所に給湯設定温度の水を適切に供給することができる。   According to this characteristic configuration, when the operation control means performs the hot water supply operation, if the temperature of the water in the hot water supply tank is equal to or higher than the switching set temperature, the operation control means switches to the bypass state, and the first bypass water channel Bypassing the burner-heated heat exchanger, water is directly supplied to the hot water use location. As a result, when there is water in the hot water supply tank that is higher than the switching set temperature, the water in the hot water supply tank can be prevented while bypassing the burner heating heat exchanger and preventing heat radiation by passing through the burner heating heat exchanger. As it is, the hot water supply temperature can be supplied to the hot water use location. Also, when there is no water above the switching set temperature in the hot water supply tank, the water in the hot water supply tank can be supplied to the hot water use location via the burner heating type heat exchanger through the first water channel. The water in the hot water supply tank can be heated by the heat exchanger to supply the hot water supply temperature to the hot water use location. Therefore, it is possible to appropriately supply the hot water supply temperature to the hot water use location while effectively using the water in the hot water tank.

本発明に係る熱媒供給装置の更なる特徴構成は、前記循環ポンプの圧力で少なくとも前記給湯タンクと前記ヒートポンプ加熱式熱交換器を経由して水が循環する第3水路が、少なくとも前記第1バイパス水路の一部で構成されている点にある。   A further characteristic configuration of the heat medium supply device according to the present invention is that at least a first water channel through which water circulates at least through the hot water supply tank and the heat pump heating heat exchanger at a pressure of the circulation pump. It consists of a part of the bypass channel.

上述の如く、第1バイパス水路は、給湯タンクの水をバーナー加熱式熱交換器をバイパスして給湯利用箇所に供給するための水路であるが、本特徴構成によれば、その第1バイパス水路の一部を用いて、循環ポンプの圧力で少なくとも給湯タンクとヒートポンプ加熱式熱交換器を経由して水が循環する第3水路を構成している。これにより、第1バイパス水路の一部を、給湯タンクの水をバーナー加熱式熱交換器をバイパスして給湯利用箇所に供給するためだけに備えるのではなく、第3水路としても用いることで、構成の簡素化を図ることができる。   As described above, the first bypass water channel is a water channel for supplying the water in the hot water supply tank to the hot water use location by bypassing the burner heating type heat exchanger. According to this characteristic configuration, the first bypass water channel is used. Is used to constitute a third water channel through which water circulates at least via a hot water supply tank and a heat pump heating heat exchanger at the pressure of the circulation pump. Thereby, by using a part of the first bypass water channel not only for supplying the water in the hot water supply tank to the hot water supply use place by bypassing the burner heating type heat exchanger, but also using it as the third water channel, The configuration can be simplified.

本発明に係る熱媒供給装置の更なる特徴構成は、前記給湯タンクに接続されて上水を前記給湯タンクに給水する第1流路部位と、前記給湯タンクと前記バーナー加熱式熱交換器を接続して前記循環ポンプが設けられた第2流路部位と、前記バーナー加熱式熱交換器と前記給湯利用箇所を接続する第3流路部位と、前記第3流路部位の途中部位と前記負荷熱交換器を接続する第4流路部位と、前記負荷熱交換器と前記ヒートポンプ加熱式熱交換器を接続する第5流路部位と、前記ヒートポンプ加熱式熱交換器と前記第2流路部位における前記給湯タンクと前記循環ポンプの間の部位を接続する第6流路部位と、前記第1流路部位の途中部位と前記第5流路部位の途中部位とを接続する第7流路部位と、前記第2流路部位における前記給湯タンクと前記第6流路部位への接続箇所までの間の部位及び前記第3流路部位における前記第4流路部位への接続箇所と前記給湯利用箇所までの間の部位を接続する第1バイパス流路部位とを備え、前記第1水路が、前記第1流路部位と前記給湯タンクと前記第2流路部位と前記バーナー加熱式熱交換器と前記第3流路部位とで構成され、前記第1バイパス水路が、前記第1流路部位と前記給湯タンクと前記第2流路部位の一部と前記第1バイパス流路部位と前記第3流路部位の一部とで構成され、前記第2水路が、前記バーナー加熱式熱交換器と前記第3流路部位の一部と前記第4流路部位と前記負荷熱交換器と前記第5流路部位と前記ヒートポンプ加熱式熱交換器と前記第6流路部位と前記第2流路部位の一部とで構成され、前記第3水路が、前記給湯タンクと前記第1流路部位の一部と前記第7流路部位と前記第5流路部位の一部と前記ヒートポンプ加熱式熱交換器と前記第6流路部位と前記第2流路部位と前記バーナー加熱式熱交換器と前記第3流路部位の一部と前記第1バイパス流路部位とで構成されている点にある。   A further characteristic configuration of the heat medium supply device according to the present invention includes a first flow path portion connected to the hot water supply tank for supplying clean water to the hot water supply tank, the hot water supply tank, and the burner heating type heat exchanger. A second flow path part connected and provided with the circulation pump; a third flow path part connecting the burner heating type heat exchanger and the hot water supply use part; a middle part of the third flow path part; A fourth flow path part for connecting the load heat exchanger, a fifth flow path part for connecting the load heat exchanger and the heat pump heating heat exchanger, the heat pump heating heat exchanger and the second flow path. A sixth flow path portion connecting a portion between the hot water supply tank and the circulation pump in the portion, and a seventh flow path connecting a middle portion of the first flow passage portion and a middle portion of the fifth flow path portion. Part and the hot water supply tank in the second flow path part A first bypass flow that connects a portion between the connection portion to the sixth flow passage portion and a portion between the connection portion to the fourth flow passage portion and the hot water supply use portion in the third flow passage portion. The first water channel is composed of the first flow path part, the hot water supply tank, the second flow path part, the burner heating heat exchanger, and the third flow path part, The first bypass channel is composed of the first channel part, the hot water tank, a part of the second channel part, the first bypass channel part, and a part of the third channel part, The second water channel includes the burner heating type heat exchanger, a part of the third flow path part, the fourth flow path part, the load heat exchanger, the fifth flow path part, and the heat pump heating type heat exchanger. And the sixth flow path part and a part of the second flow path part, the third water channel, The hot water tank, a part of the first flow path part, the seventh flow path part, a part of the fifth flow path part, the heat pump heating type heat exchanger, the sixth flow path part, and the second flow It is in the point comprised by the channel | path site | part, the said burner heating type heat exchanger, a part of said 3rd flow-path part, and the said 1st bypass flow-path part.

本特徴構成によれば、第1〜第7流路部位、及び、第1バイパス流路部位の複数の流路部位を組み合わせて、第1水路、第1バイパス水路、第2水路、及び、第3水路の夫々を適切に構成することができる。そして、第1水路、第1バイパス水路、第2水路、及び、第3水路の間で、共通な流路部位を備えながら、開閉弁や比例弁を適宜切り換えることで、各水路を適切に構成することができるとともに、開閉弁や比例弁の数を極力少なくして、部材点数の増加を適切に防止して構成の簡素化を図ることができる。   According to this characteristic configuration, the first water channel, the first bypass water channel, the second water channel, Each of the three waterways can be configured appropriately. And while providing a common flow-path part among a 1st waterway, a 1st bypass waterway, a 2nd waterway, and a 3rd waterway, each switch is appropriately comprised by switching an on-off valve and a proportional valve suitably In addition, the number of on-off valves and proportional valves can be reduced as much as possible to appropriately prevent an increase in the number of members, thereby simplifying the configuration.

ちなみに、第1水路、第1バイパス水路、第2水路、及び、第3水路の回路構成については、下記のように構成することもできる。
つまり、給湯タンクに接続されて上水を給湯タンクに給水する第1流路部位と、給湯タンクとバーナー加熱式熱交換器を接続する第2流路部位と、バーナー加熱式熱交換器と給湯利用箇所を接続して循環ポンプが設けられた第3流路部位と、第3流路部位における循環ポンプと給湯利用箇所の間の部位と負荷熱交換器を接続する第4流路部位と、負荷熱交換器とヒートポンプ加熱式熱交換器を接続する第5流路部位と、ヒートポンプ加熱式熱交換器と第2流路部位の途中部位とを接続する第6流路部位と、第1流路部位の途中部位と第5流路部位の途中部位とを接続する第7流路部位と、第2流路部位における給湯タンクと第6流路部位への接続箇所までの間の部位及び第3流路部位における第4流路部位への接続箇所と給湯利用箇所までの間の部位を接続する第1バイパス流路部位とを備え、第1水路を、第1流路部位と給湯タンクと第2流路部位とバーナー加熱式熱交換器と第3流路部位とで構成し、第1バイパス水路を、第1流路部位と給湯タンクと第2流路部位の一部と第1バイパス流路部位と第3流路部位の一部とで構成し、第2水路を、バーナー加熱式熱交換器と第3流路部位の一部と第4流路部位と負荷熱交換器と第5流路部位とヒートポンプ加熱式熱交換器と第6流路部位と第2流路部位の一部とで構成し、第3水路を、給湯タンクと第1流路部位の一部と第7流路部位と第5流路部位の一部とヒートポンプ加熱式熱交換器と第6流路部位と第2流路部位とバーナー加熱式熱交換器と第3流路部位の一部と第1バイパス流路部位とで構成することができる。
Incidentally, the circuit configurations of the first water channel, the first bypass water channel, the second water channel, and the third water channel can be configured as follows.
That is, a first flow path portion connected to a hot water supply tank for supplying clean water to the hot water supply tank, a second flow path portion connecting the hot water supply tank and the burner heating heat exchanger, a burner heating heat exchanger, and a hot water supply A third flow path part provided with a circulation pump by connecting the use points, a fourth flow path part connecting the load heat exchanger with a part between the circulation pump and the hot water supply use point in the third flow path part, A fifth flow path portion connecting the load heat exchanger and the heat pump heating heat exchanger, a sixth flow path portion connecting the heat pump heating heat exchanger and the intermediate portion of the second flow path portion, and the first flow A seventh flow path portion connecting the midway portion of the road portion and the midway portion of the fifth flow path portion; a portion between the hot water tank in the second flow path portion and the connection location to the sixth flow path portion; The connection point to the fourth flow path part and the hot water supply use point in the three flow path parts The first bypass channel is connected to the first bypass channel, and the first water channel is composed of a first channel site, a hot water tank, a second channel site, a burner heating heat exchanger, and a third channel site. The first bypass channel is composed of a first channel part, a hot water tank, a part of the second channel part, a part of the first bypass channel part and a part of the third channel part, and the second channel , Burner heating type heat exchanger, part of third flow path part, fourth flow path part, load heat exchanger, fifth flow path part, heat pump heating type heat exchanger, sixth flow path part and second flow The third water channel is composed of a part of the channel part, and the third water channel, part of the first channel part, part of the seventh channel part, part of the fifth channel part, heat pump heating type heat exchanger and It can be constituted by six flow path parts, a second flow path part, a burner heating type heat exchanger, a part of the third flow path part, and a first bypass flow path part.

また、給湯タンクに接続されて上水を給湯タンクに給水する第1流路部位と、給湯タンクとバーナー加熱式熱交換器を接続する第2流路部位と、バーナー加熱式熱交換器と給湯利用箇所を接続する第3流路部位と、第3流路部位の途中部位と負荷熱交換器を接続する第4流路部位と、負荷熱交換器とヒートポンプ加熱式熱交換器を接続する第5流路部位と、ヒートポンプ加熱式熱交換器と第2流路部位の途中部位を接続して循環ポンプが設けられた第6流路部位と、第1流路部位の途中部位と第5流路部位の途中部位とを接続する第7流路部位と、第2流路部位における給湯タンクと第6流路部位への接続箇所までの間の部位及び第3流路部位における第4流路部位への接続箇所と給湯利用箇所までの間の部位を接続する第1バイパス流路部位とを備え、第1水路を、第1流路部位と給湯タンクと第2流路部位とバーナー加熱式熱交換器と第3流路部位と第4流路部位と負荷熱交換器と第5流路部位とヒートポンプ加熱式熱交換器と第6流路部位とで構成し、第1バイパス水路を、第1流路部位と給湯タンクと第2流路部位の一部と第1バイパス流路部位と第3流路部位の一部とで構成し、第2水路を、バーナー加熱式熱交換器と第3流路部位の一部と第4流路部位と負荷熱交換器と第5流路部位とヒートポンプ加熱式熱交換器と第6流路部位と第2流路部位の一部とで構成し、第3水路を、給湯タンクと第1流路部位の一部と第7流路部位と第5流路部位の一部とヒートポンプ加熱式熱交換器と第6流路部位と第2流路部位とバーナー加熱式熱交換器と第3流路部位の一部と第1バイパス流路部位とで構成することができる。   In addition, a first flow path part connected to the hot water tank for supplying clean water to the hot water tank, a second flow path part for connecting the hot water tank and the burner heating heat exchanger, the burner heating heat exchanger and the hot water supply A third flow path part for connecting the use location, a fourth flow path part for connecting the intermediate part of the third flow path part and the load heat exchanger, and a second flow path for connecting the load heat exchanger and the heat pump heating type heat exchanger. A fifth flow path part, a heat pump heating heat exchanger, a sixth flow path part provided with a circulation pump by connecting a midway part of the second flow path part, a midway part of the first flow path part and a fifth flow A seventh flow path part connecting the middle part of the road part, a part between the hot water tank in the second flow path part and the connection part to the sixth flow path part, and a fourth flow path in the third flow path part 1st bypass channel part which connects the site | part between the connection location to a location and a hot-water supply utilization location The first water channel, the first channel part, the hot water tank, the second channel part, the burner heating heat exchanger, the third channel part, the fourth channel part, the load heat exchanger, and the fifth. A flow path part, a heat pump heating type heat exchanger, and a sixth flow path part are configured, and the first bypass water path is formed of the first flow path part, the hot water supply tank, a part of the second flow path part, and the first bypass flow path. And a part of the third flow path part, and the second water channel is composed of a burner heating type heat exchanger, a part of the third flow path part, a fourth flow path part, a load heat exchanger, and a fifth flow. The passage part, the heat pump heating type heat exchanger, the sixth passage part, and a part of the second passage part, and the third water channel, the hot water tank, a part of the first passage part, and the seventh passage Part, part of fifth channel part, heat pump heating type heat exchanger, sixth channel part, second channel part, burner heating type heat exchanger, part of third channel part and first It can be configured with a bypass passage portion.

さらに、給湯タンクに接続されて上水を給湯タンクに給水する第1流路部位と、給湯タンクとバーナー加熱式熱交換器を接続する第2流路部位と、バーナー加熱式熱交換器と給湯利用箇所を接続する第3流路部位と、第3流路部位の途中部位と負荷熱交換器を接続する第4流路部位と、負荷熱交換器とヒートポンプ加熱式熱交換器を接続して循環ポンプが設けられた第5流路部位と、ヒートポンプ加熱式熱交換器と第2流路部位の途中部位を接続する第6流路部位と、第1流路部位の途中部位と第5流路部位における負荷熱交換器と循環ポンプの間の部位とを接続する第7流路部位と、第2流路部位における給湯タンクと第6流路部位への接続箇所までの間の部位及び第3流路部位における第4流路部位への接続箇所と給湯利用箇所までの間の部位を接続する第1バイパス流路部位とを備え、第1水路を、第1流路部位と給湯タンクと第2流路部位とバーナー加熱式熱交換器と第3流路部位と第4流路部位と負荷熱交換器と第5流路部位とヒートポンプ加熱式熱交換器と第6流路部位とで構成し、第1バイパス水路を、第1流路部位と給湯タンクと第2流路部位の一部と第1バイパス流路部位と第3流路部位の一部とで構成し、第2水路を、バーナー加熱式熱交換器と第3流路部位の一部と第4流路部位と負荷熱交換器と第5流路部位とヒートポンプ加熱式熱交換器と第6流路部位と第2流路部位の一部とで構成し、第3水路を、給湯タンクと第1流路部位の一部と第7流路部位と第5流路部位の一部とヒートポンプ加熱式熱交換器と第6流路部位と第2流路部位とバーナー加熱式熱交換器と第3流路部位の一部と第1バイパス流路部位とで構成することができる。   Further, a first flow path portion connected to the hot water supply tank for supplying clean water to the hot water supply tank, a second flow path portion connecting the hot water supply tank and the burner heating heat exchanger, a burner heating heat exchanger and hot water supply Connect the third flow path part that connects the use points, the fourth flow path part that connects the intermediate part of the third flow path part and the load heat exchanger, the load heat exchanger, and the heat pump heating type heat exchanger. A fifth flow path portion provided with a circulation pump, a sixth flow path portion connecting the heat pump heating type heat exchanger and a middle portion of the second flow path portion, a middle portion of the first flow path portion and a fifth flow A seventh passage portion connecting the load heat exchanger and the portion between the circulation pump in the passage portion, a portion between the hot water tank and the connection portion to the sixth passage portion in the second passage portion, and the first Between the connection point to the fourth flow path part and the hot water supply use point in the three flow path parts A first bypass channel connecting the sites, the first water channel, the first channel site, the hot water tank, the second channel site, the burner heating heat exchanger, the third channel site, and the fourth flow. A path part, a load heat exchanger, a fifth flow path part, a heat pump heating type heat exchanger, and a sixth flow path part are configured, and the first bypass water channel is formed by the first flow path part, the hot water supply tank, and the second flow path. A part of the part, a part of the first bypass channel part and a part of the third channel part, and the second water channel is a burner heating type heat exchanger, part of the third channel part and the fourth channel. It comprises a part, a load heat exchanger, a fifth flow path part, a heat pump heating type heat exchanger, a sixth flow path part and a part of the second flow path part, and the third water channel is connected to the hot water supply tank and the first flow. Part of the channel part, part of the seventh channel part, part of the fifth channel part, heat pump heating type heat exchanger, sixth channel part, second channel part, and burner heating type It can be composed of exchanger and a part of the third channel portion and the first bypass passage portion.

本発明に係る熱媒供給装置の更なる特徴構成は、前記給湯タンクに接続されて上水を前記給湯タンクに給水する第1流路部位と、前記給湯タンクと前記バーナー加熱式熱交換器を接続して、前記給湯タンクに近い順に前記循環ポンプと前記ヒートポンプ加熱式熱交換器が設けられた第2流路部位と、前記バーナー加熱式熱交換器と前記給湯利用箇所を接続する第3流路部位と、前記第3流路部位の途中部位と前記負荷熱交換器を接続する第4流路部位と、前記負荷熱交換器と前記第2流路部位における前記給湯タンクと前記循環ポンプの間の部位を接続する第6流路部位と、前記第1流路部位の途中部位と前記第6流路部位の途中部位とを接続する第7流路部位と、前記第2流路部位における前記給湯タンクと前記第6流路部位への接続箇所までの間の部位及び前記第3流路部位における前記第4流路部位への接続箇所と前記給湯利用箇所までの間の部位を接続する第1バイパス流路部位とを備え、前記第1水路が、前記第1流路部位と前記給湯タンクと前記第2流路部位と前記バーナー加熱式熱交換器と前記第3流路部位とで構成され、前記第1バイパス水路が、前記第1流路部位と前記給湯タンクと前記第2流路部位の一部と前記第1バイパス流路部位と前記第3流路部位の一部とで構成され、前記第2水路が、前記バーナー加熱式熱交換器と前記第3流路部位の一部と前記第4流路部位と前記負荷熱交換器と前記第6流路部位と前記第2流路部位の一部とで構成され、前記第3水路が、前記給湯タンクと前記第1流路部位の一部と前記第7流路部位と前記第6流路部位の一部と前記第2流路部位と前記バーナー加熱式熱交換器と前記第3流路部位の一部と前記第1バイパス流路部位とで構成されている点にある。   A further characteristic configuration of the heat medium supply device according to the present invention includes a first flow path portion connected to the hot water supply tank for supplying clean water to the hot water supply tank, the hot water supply tank, and the burner heating type heat exchanger. And a third flow connecting the second flow path part provided with the circulation pump and the heat pump heating type heat exchanger in order from the hot water supply tank, and the burner heating type heat exchanger and the hot water supply use part. A passage portion, a middle portion of the third flow passage portion, a fourth flow passage portion connecting the load heat exchanger, the hot water supply tank in the load heat exchanger, the second flow passage portion, and the circulation pump. A sixth flow path portion that connects a portion therebetween, a seventh flow passage portion that connects a middle portion of the first flow passage portion and a middle portion of the sixth flow passage portion, and a second flow passage portion Connection point between the hot water tank and the sixth flow path part A first bypass flow path portion connecting a portion between the portion between the first flow passage portion and the connection portion to the fourth flow passage portion in the third flow passage portion and the hot water supply utilization portion. Is composed of the first flow path part, the hot water supply tank, the second flow path part, the burner heating heat exchanger, and the third flow path part, and the first bypass water channel is the first flow path. A passage part, the hot water supply tank, a part of the second passage part, a part of the first bypass passage part and a part of the third passage part, and the second water passage is the burner heating type heat. An exchanger, a part of the third flow path part, the fourth flow path part, the load heat exchanger, the sixth flow path part, and a part of the second flow path part; The water channel is a part of the hot water supply tank, the first flow path part, the seventh flow path part, and the sixth flow path part. In that it is constituted by a portion between the first bypass passage portion of the third channel portion and the burner heating heat exchanger and the second flow path portion.

本特徴構成によれば、第1〜第7流路部位、及び、第1バイパス流路部位の複数の流路部位を組み合わせて、第1水路、第1バイパス水路、第2水路、及び、第3水路の夫々を適切に構成することができる。そして、第1水路、第1バイパス水路、第2水路、及び、第3水路の間で、共通な流路部位を備えながら、開閉弁や比例弁を適宜切り換えることで、各水路を適切に構成することができるとともに、開閉弁や比例弁の数を極力少なくして、部材点数の増加を適切に防止して構成の簡素化を図ることができる。しかも、ヒートポンプ加熱式熱交換器が第2流路部位に備えられているので、第2流路部位に備えられた循環ポンプの圧力により、ヒートポンプ加熱式熱交換器、第3流路部位、第1バイパス流路部位、第2流路部位の順に経由させて、ヒートポンプ加熱式熱交換器に戻すように水を循環させることができる。これにより、第1バイパス流路部位等の水の温度が給湯タンクにて要求されている蓄熱温度よりも低下している場合には、ヒートポンプ加熱式熱交換器にて加熱する状態で第1バイパス流路部位等の水を循環させることができ、第1バイパス流路部位等の水の予熱を行うことができる。したがって、第3水路によって給湯タンクへの貯湯を行う場合に、その当初に予熱された水を給湯タンクに供給することができ、その当初から蓄熱温度の水を安定して給湯タンクに供給して給湯タンクへの蓄熱を適切に行うことができる。   According to this characteristic configuration, the first water channel, the first bypass water channel, the second water channel, Each of the three waterways can be configured appropriately. And while providing a common flow-path part among a 1st waterway, a 1st bypass waterway, a 2nd waterway, and a 3rd waterway, each switch is appropriately comprised by switching an on-off valve and a proportional valve suitably In addition, the number of on-off valves and proportional valves can be reduced as much as possible to appropriately prevent an increase in the number of members, thereby simplifying the configuration. In addition, since the heat pump heating type heat exchanger is provided in the second flow path part, the heat pump heating type heat exchanger, the third flow path part, Water can be circulated so as to return to the heat pump heating type heat exchanger through the order of the 1 bypass flow path part and the second flow path part. Thereby, when the temperature of water, such as a 1st bypass channel part, is lower than the heat storage temperature requested | required in a hot water supply tank, it is 1st bypass in the state heated with a heat pump heating type heat exchanger Water in the flow path portion or the like can be circulated, and water in the first bypass flow path portion or the like can be preheated. Therefore, when the hot water is stored in the hot water supply tank by the third water channel, the water preheated at the beginning can be supplied to the hot water supply tank, and the water at the heat storage temperature can be stably supplied to the hot water supply tank from the beginning. Heat storage in the hot water tank can be performed appropriately.

本発明に係る熱媒供給装置の更なる特徴構成は、前記給湯タンクに接続されて上水を前記給湯タンクに給水する第1流路部位と、前記給湯タンクと前記バーナー加熱式熱交換器を接続して、前記給湯タンクに近い順に前記ヒートポンプ加熱式熱交換器と前記循環ポンプが設けられた第2流路部位と、前記バーナー加熱式熱交換器と前記給湯利用箇所を接続する第3流路部位と、前記第3流路部位の途中部位と前記負荷熱交換器を接続する第4流路部位と、前記負荷熱交換器と前記第2流路部位における前記給湯タンクと前記ヒートポンプ加熱式熱交換器の間の部位を接続する第6流路部位と、前記第1流路部位の途中部位と前記第6流路部位の途中部位とを接続する第7流路部位と、前記第2流路部位における前記給湯タンクと前記第6流路部位への接続箇所までの間の部位及び前記第3流路部位における前記第4流路部位への接続箇所と前記給湯利用箇所までの間の部位を接続する第1バイパス流路部位とを備え、前記第1水路が、前記第1流路部位と前記給湯タンクと前記第2流路部位と前記バーナー加熱式熱交換器と前記第3流路部位とで構成され、前記第1バイパス水路が、前記第1流路部位と前記給湯タンクと前記第2流路部位の一部と前記第1バイパス流路部位と前記第3流路部位の一部とで構成され、前記第2水路が、前記バーナー加熱式熱交換器と前記第3流路部位の一部と前記第4流路部位と前記負荷熱交換器と前記第6流路部位と前記第2流路部位の一部とで構成され、前記第3水路が、前記給湯タンクと前記第1流路部位の一部と前記第7流路部位と前記第6流路部位の一部と前記第2流路部位と前記バーナー加熱式熱交換器と前記第3流路部位の一部と前記第1バイパス流路部位とで構成されている点にある。   A further characteristic configuration of the heat medium supply device according to the present invention includes a first flow path portion connected to the hot water supply tank for supplying clean water to the hot water supply tank, the hot water supply tank, and the burner heating type heat exchanger. And a third flow connecting the second flow path portion provided with the heat pump heating heat exchanger and the circulation pump, and the burner heating heat exchanger and the hot water use location in the order closer to the hot water tank. A road portion, a fourth passage portion connecting the intermediate portion of the third passage portion and the load heat exchanger, the hot water supply tank in the load heat exchanger, the second passage portion, and the heat pump heating type A sixth flow path portion for connecting portions between the heat exchangers, a seventh flow path portion for connecting a midway portion of the first flow path portion and a midway portion of the sixth flow path portion, and the second The hot water supply tank and the sixth flow path in the flow path part And a first bypass flow path portion that connects a portion between the connection portion to the fourth flow passage portion in the third flow passage portion and a portion between the hot water supply use location and the third flow passage portion. The first water channel is composed of the first channel part, the hot water supply tank, the second channel part, the burner heating heat exchanger, and the third channel part, and the first bypass channel is The first flow path part, the hot water tank, a part of the second flow path part, the first bypass flow path part, and a part of the third flow path part, and the second water channel, The burner heating type heat exchanger, a part of the third flow path part, the fourth flow path part, the load heat exchanger, the sixth flow path part, and a part of the second flow path part. And the third water channel includes the hot water supply tank, a part of the first channel part, the seventh channel part, and the first channel part. In that it is constituted by a portion between the first bypass flow path portion of a part and the second flow path portion and the burner heating type heat exchanger wherein the third flow path portion of the channel region.

本特徴構成によれば、第1〜第7流路部位、及び、第1バイパス流路部位の複数の流路部位を組み合わせて、第1水路、第1バイパス水路、第2水路、及び、第3水路の夫々を適切に構成することができる。そして、第1水路、第1バイパス水路、第2水路、及び、第3水路の間で、共通な流路部位を備えながら、開閉弁や比例弁を適宜切り換えることで、各水路を適切に構成することができるとともに、開閉弁や比例弁の数を極力少なくして、部材点数の増加を適切に防止して構成の簡素化を図ることができる。しかも、ヒートポンプ加熱式熱交換器が第2流路部位に備えられているので、第2流路部位に備えられた循環ポンプの圧力により、ヒートポンプ加熱式熱交換器、第3流路部位、第1バイパス流路部位、第2流路部位の順に経由させて、ヒートポンプ加熱式熱交換器に戻すように水を循環させることができる。これにより、第1バイパス流路部位等の水の温度が給湯タンクにて要求されている蓄熱温度よりも低下している場合には、ヒートポンプ加熱式熱交換器にて加熱する状態で第1バイパス流路部位等の水を循環させることができ、第1バイパス流路部位等の水の予熱を行うことができる。したがって、第3水路によって給湯タンクへの貯湯を行う場合に、その当初に予熱された水を給湯タンクに供給することができ、その当初から蓄熱温度の水を安定して給湯タンクに供給して給湯タンクへの蓄熱を適切に行うことができる。   According to this characteristic configuration, the first water channel, the first bypass water channel, the second water channel, Each of the three waterways can be configured appropriately. And while providing a common flow-path part among a 1st waterway, a 1st bypass waterway, a 2nd waterway, and a 3rd waterway, each switch is appropriately comprised by switching an on-off valve and a proportional valve suitably In addition, the number of on-off valves and proportional valves can be reduced as much as possible to appropriately prevent an increase in the number of members, thereby simplifying the configuration. In addition, since the heat pump heating type heat exchanger is provided in the second flow path part, the heat pump heating type heat exchanger, the third flow path part, Water can be circulated so as to return to the heat pump heating type heat exchanger through the order of the 1 bypass flow path part and the second flow path part. Thereby, when the temperature of water, such as a 1st bypass channel part, is lower than the heat storage temperature requested | required in a hot water supply tank, it is 1st bypass in the state heated with a heat pump heating type heat exchanger Water in the flow path portion or the like can be circulated, and water in the first bypass flow path portion or the like can be preheated. Therefore, when the hot water is stored in the hot water supply tank by the third water channel, the water preheated at the beginning can be supplied to the hot water supply tank, and the water at the heat storage temperature can be stably supplied to the hot water supply tank from the beginning. Heat storage in the hot water tank can be performed appropriately.

本発明に係る熱媒供給装置の更なる特徴構成は、少なくとも前記第1バイパス水路の一部で構成されている前記第3水路は、前記給湯タンクから取り出した水を前記バーナー加熱式熱交換器にて加熱し、その加熱された水を前記給湯タンクに戻すように水を循環自在に構成されている点にある。   A further characteristic configuration of the heating medium supply device according to the present invention is that the third water channel configured by at least a part of the first bypass water channel is configured such that the water taken out from the hot water tank is the burner heating type heat exchanger. And the water is circulated so that the heated water is returned to the hot water supply tank.

本特徴構成によれば、少なくとも第1バイパス水路の一部で構成されている第3水路によって、給湯タンクから取り出した水をバーナー加熱式熱交換器にて加熱し、その加熱された水を給湯タンクに戻すことができるので、バーナー燃焼装置を熱源として給湯タンクの水を加熱することができる。したがって、第3水路を少なくとも第1バイパス水路の一部で構成することによって、構成の簡素化を図ることができながら、給湯タンクの水を高温として殺菌消毒して、レジオネラ菌等の繁殖を適切に防止することができる。   According to this characteristic configuration, the water taken out from the hot water supply tank is heated by the burner heating type heat exchanger by the third water channel constituted by at least a part of the first bypass water channel, and the heated water is supplied with the hot water. Since it can be returned to the tank, the water in the hot water supply tank can be heated using the burner combustion device as a heat source. Therefore, by constructing the third water channel by at least a part of the first bypass water channel, the structure can be simplified, and the water in the hot water tank can be sterilized and disinfected at a high temperature to appropriately propagate Legionella bacteria and the like. Can be prevented.

本発明に係る熱媒供給装置の更なる特徴構成は、前記バーナー加熱式熱交換器が、前記バーナー燃焼装置の燃焼ガスの顕熱により水を加熱する顕熱回収熱交換器と前記バーナー燃焼装置の燃焼ガスの潜熱により水を加熱する潜熱回収熱交換器とで構成され、前記潜熱回収熱交換器と前記顕熱回収熱交換器は、前記第1水路における水の通流方向で、前記潜熱回収熱交換器、前記顕熱回収熱交換器の順に備えられ、前記第1バイパス水路は、前記潜熱回収熱交換器及び前記顕熱回収熱交換器をバイパスして前記給湯タンクから取り出した水を前記給湯利用箇所に供給するように構成されている点にある。   According to still another aspect of the present invention, there is provided a sensible heat recovery heat exchanger in which the burner heating heat exchanger heats water by sensible heat of combustion gas of the burner combustion device, and the burner combustion device. A latent heat recovery heat exchanger that heats water by the latent heat of the combustion gas, and the latent heat recovery heat exchanger and the sensible heat recovery heat exchanger are arranged in the direction of water flow in the first water channel. A recovery heat exchanger and the sensible heat recovery heat exchanger are provided in this order, and the first bypass water channel bypasses the latent heat recovery heat exchanger and the sensible heat recovery heat exchanger and removes water taken from the hot water supply tank. It exists in the point comprised so that it may supply to the said hot water supply utilization location.

本特徴構成によれば、第1バイパス水路によって給湯利用箇所への給湯を行う場合には、給湯タンクから取り出した水が第1バイパス水路により潜熱回収熱交換器及び顕熱回収熱交換器をバイパスして給湯利用箇所に供給することができる。したがって、潜熱回収熱交換器及び顕熱回収熱交換器を通過することによる放熱を防止できながら、給湯タンクの水をそのまま活用して給湯利用箇所に給湯設定温度の水を供給することができる。しかも、第1水路によって給湯利用箇所への給湯を行う場合には、給湯タンクから取り出した水を第1水路により潜熱回収熱交換器及び顕熱回収熱交換器を経由して給湯利用箇所に供給することができる。したがって、顕熱回収熱交換器における燃焼ガスの顕熱だけでなく、潜熱回収熱交換器における燃焼ガスの潜熱によっても水を加熱して加熱能力の向上を図ることで、省エネ性の向上を図ることができる。   According to this characteristic configuration, when hot water is supplied to the hot water use location through the first bypass channel, the water taken out from the hot water tank bypasses the latent heat recovery heat exchanger and the sensible heat recovery heat exchanger through the first bypass channel. Then, it can be supplied to the hot water use location. Therefore, water at the hot water supply set temperature can be supplied to the hot water supply use location by using the water in the hot water supply tank as it is, while preventing heat radiation due to passing through the latent heat recovery heat exchanger and the sensible heat recovery heat exchanger. In addition, when hot water is supplied to the hot water use location by the first water channel, the water taken out from the hot water tank is supplied to the hot water usage location via the latent heat recovery heat exchanger and the sensible heat recovery heat exchanger by the first water channel. can do. Therefore, not only the sensible heat of the combustion gas in the sensible heat recovery heat exchanger but also the water is heated not only by the sensible heat of the combustion gas in the latent heat recovery heat exchanger, but also by improving the heating capacity, thereby improving energy savings. be able to.

本発明に係る熱媒供給装置の更なる特徴構成は、前記運転制御手段は、前記バーナー燃焼装置を非燃焼状態に切り換え且つ前記ヒートポンプ装置を作動状態に切り換えて前記ヒートポンプ加熱式熱交換器にて加熱した水を前記負荷熱交換器に供給するヒートポンプ加熱状態と、前記バーナー燃焼装置を燃焼状態に切り換え且つ前記ヒートポンプ装置を非作動状態に切り換えて前記バーナー加熱式熱交換器にて加熱した水を前記負荷熱交換器に供給するバーナー加熱状態とに切換自在で、且つ、前記負荷熱交換器で要求されている熱負荷に対して、前記バーナー加熱状態に切り換えた場合と前記ヒートポンプ加熱状態に切り換えた場合との1次エネルギー消費量が小さい方を選択して切り換えるように構成されている点にある。   According to a further feature of the heat medium supply device according to the present invention, the operation control means switches the burner combustion device to a non-combustion state and switches the heat pump device to an operation state. A heat pump heating state in which heated water is supplied to the load heat exchanger, and the water heated by the burner heating type heat exchanger by switching the burner combustion device to a combustion state and switching the heat pump device to a non-operational state. Switchable between the burner heating state supplied to the load heat exchanger and the heat load required in the load heat exchanger when switched to the burner heating state and the heat pump heating state The primary energy consumption with respect to the case where the primary energy consumption is smaller is selected and switched.

本特徴構成によれば、運転制御手段が、ヒートポンプ加熱状態とバーナー加熱状態とで1次エネルギー消費量が小さい方に切り換えて、負荷熱交換器への熱供給を行うことができるので、負荷熱交換器に熱供給を行うに当たり、水を加熱するために必要となる1次エネルギー消費量をより小さく抑えることができ、省エネ性の向上を効果的に図ることができる。   According to this feature configuration, the operation control means can switch the heat consumption to the load heat exchanger by switching the heat consumption to the smaller one in the heat pump heating state and the burner heating state. In supplying heat to the exchanger, the primary energy consumption required for heating water can be further reduced, and energy saving can be effectively improved.

本発明に係る熱媒供給装置の更なる特徴構成は、前記運転制御手段は、前記ヒートポンプ装置を作動状態に切り換えた状態において前記ヒートポンプ加熱式熱交換器に供給される水の温度が所定温度より高い場合に、前記ヒートポンプ装置を非作動状態に切り換える点にある。   A further characteristic configuration of the heat medium supply device according to the present invention is that the operation control means is configured such that the temperature of water supplied to the heat pump heating heat exchanger is higher than a predetermined temperature in a state where the heat pump device is switched to an operating state. When it is high, the heat pump device is switched to a non-operating state.

ヒートポンプ装置を作動状態に切り換えている場合には、ヒートポンプ加熱式熱交換器にて水を加熱することができるが、ヒートポンプ加熱式熱交換器に供給される水の温度が所定温度より高くなると、ヒートポンプ装置の成績係数(COP)が低下して、エネルギー効率が低下することになる。そこで、本特徴構成によれば、運転制御手段は、ヒートポンプ装置を作動状態に切り換えた状態においてヒートポンプ加熱式熱交換器に供給される水の温度が所定温度より高い場合に、ヒートポンプ装置を非作動状態に切り換えるので、効率が低下した状態でヒートポンプ装置の運転が継続されることを防止することができる。その結果、ヒートポンプ装置の効率の低下を防止することができ、エネルギー効率の向上を図ることができる。   When the heat pump device is switched to the operating state, water can be heated in the heat pump heating type heat exchanger, but when the temperature of the water supplied to the heat pump heating type heat exchanger becomes higher than a predetermined temperature, As a result, the coefficient of performance (COP) of the heat pump device is lowered, and the energy efficiency is lowered. Therefore, according to this characteristic configuration, the operation control means deactivates the heat pump device when the temperature of the water supplied to the heat pump heating heat exchanger is higher than a predetermined temperature in the state where the heat pump device is switched to the activated state. Since switching to the state, it is possible to prevent the operation of the heat pump apparatus from being continued in a state where the efficiency is lowered. As a result, a decrease in efficiency of the heat pump device can be prevented, and energy efficiency can be improved.

本発明に係る熱媒供給装置の更なる特徴構成は、前記第1水路により前記給湯利用箇所に水を供給しており前記ヒートポンプ装置を作動状態に切り換えた状態において前記ヒートポンプ加熱式熱交換器に供給される水の温度が所定温度より高い場合に、前記ヒートポンプ加熱式熱交換器に供給される水に給水して、前記ヒートポンプ加熱式熱交換器に供給される水の温度を前記所定温度以下に調整自在な給水手段が備えられている点にある。   A further characteristic configuration of the heat medium supply device according to the present invention is that the water is supplied to the hot water supply use location by the first water channel, and the heat pump heating type heat exchanger is in a state where the heat pump device is switched to an operating state. When the temperature of the supplied water is higher than a predetermined temperature, water is supplied to the water supplied to the heat pump heating heat exchanger, and the temperature of the water supplied to the heat pump heating heat exchanger is equal to or lower than the predetermined temperature. Is provided with an adjustable water supply means.

上述の如く、ヒートポンプ装置を作動状態に切り換えている場合には、ヒートポンプ加熱式熱交換器に供給される水の温度が所定温度より高くなると、ヒートポンプ装置の成績係数(COP)が低下して効率が低下することになる。そこで、本特徴構成によれば、給水手段を備え、その給水手段によってヒートポンプ加熱式熱交換器に供給される水の温度を所定温度以下になるようにしている。つまり、給水手段は、ヒートポンプ加熱式熱交換器に供給される水に給水するので、ヒートポンプ加熱式熱交換器に供給される水の温度が低下してその温度を所定温度以下とすることができる。そして、給水手段は、ヒートポンプ加熱式熱交換器に供給される水に給水する給水量を調整することで、ヒートポンプ加熱式熱交換器に供給される水の温度を所定温度以下に調整することができる。このように、給水手段によってヒートポンプ加熱式熱交換器に供給される水の温度を所定温度以下とすることで、効率の低下を招くことなく、ヒートポンプ装置の運転を継続することができる。そして、第1水路により給湯タンクの水を給湯利用箇所に供給しているので、給湯タンクに給水していることから、給水手段によってその給水先をヒートポンプ加熱式熱交換器に変更するだけで、給湯利用箇所への水の供給をそのまま維持しながら、ヒートポンプ装置の効率の低下を防止することができる。   As described above, when the heat pump device is switched to the operating state, if the temperature of the water supplied to the heat pump heating type heat exchanger becomes higher than a predetermined temperature, the coefficient of performance (COP) of the heat pump device is reduced and the efficiency is increased. Will drop. Therefore, according to the present characteristic configuration, the water supply means is provided, and the temperature of the water supplied to the heat pump heating type heat exchanger by the water supply means is set to a predetermined temperature or less. That is, since the water supply means supplies water to the water supplied to the heat pump heating type heat exchanger, the temperature of the water supplied to the heat pump heating type heat exchanger can be lowered and the temperature can be kept below a predetermined temperature. . And a water supply means can adjust the temperature of the water supplied to a heat pump heating type heat exchanger below predetermined temperature by adjusting the amount of water supplied to the water supplied to a heat pump heating type heat exchanger. it can. Thus, the operation of the heat pump device can be continued without causing a decrease in efficiency by setting the temperature of the water supplied to the heat pump heating type heat exchanger by the water supply means to a predetermined temperature or less. And since the water in the hot water supply tank is supplied to the hot water supply use location by the first water channel, since the hot water supply tank is supplied with water, only by changing the water supply destination to the heat pump heating type heat exchanger by the water supply means, While maintaining the supply of water to the hot water use location as it is, it is possible to prevent a decrease in the efficiency of the heat pump device.

本発明に係る熱媒供給装置の更なる特徴構成は、前記給湯タンクから取り出した水を太陽熱にて加熱し、その加熱された水を前記給湯タンクに戻す太陽熱加熱水路と、前記給湯タンクから取り出した水を熱電併給装置にて発生した排熱にて加熱し、その加熱された水を前記給湯タンクに戻す排熱加熱水路の少なくとも一方が、少なくとも、前記循環ポンプの圧力で少なくとも前記給湯タンクと前記ヒートポンプ加熱式熱交換器を経由して水が循環する第3水路と兼用となっている点にある。   A further characteristic configuration of the heat medium supply device according to the present invention is that the water taken out from the hot water supply tank is heated by solar heat, and the heated water channel for returning the heated water to the hot water supply tank is taken out from the hot water supply tank. At least one of the exhaust heat heating water channels that heats the heated water with exhaust heat generated by the combined heat and power unit and returns the heated water to the hot water supply tank, at least with the pressure of the circulation pump and at least the hot water supply tank. It is in the point which serves as the 3rd waterway through which water circulates via the heat pump heating type heat exchanger.

本特徴構成によれば、太陽熱加熱水路と排熱加熱水路の少なくとも一方を、第3水路と兼用としているので、太陽熱加熱水路と排熱加熱水路の少なくとも一方は、第3水路と共通の流路部位としながら、太陽熱や熱電併給装置の排熱を給湯タンクに蓄熱することができる。   According to this characteristic configuration, at least one of the solar heat heating channel and the exhaust heat heating channel is also used as the third water channel. Therefore, at least one of the solar heating channel and the exhaust heat heating channel is a flow channel common to the third water channel. The solar heat and the exhaust heat of the combined heat and power supply device can be stored in the hot water tank while being a part.

ちなみに、上述した本発明に係る熱媒供給装置の特徴構成と同一の特徴構成を有するものについては、上述にて述べた作用効果と同一の作用効果を奏するものである。   Incidentally, what has the same characteristic configuration as the characteristic configuration of the heat medium supply device according to the present invention described above exhibits the same operational effects as those described above.

本発明に係る熱媒供給装置における給湯運転を示す図The figure which shows the hot water supply operation in the heat carrier supply apparatus which concerns on this invention 本発明に係る熱媒供給装置におけるヒートポンプ加熱状態での暖房運転を示す図The figure which shows the heating operation in the heat pump heating state in the heat carrier supply apparatus which concerns on this invention 本発明に係る熱媒供給装置における蓄熱運転を示す図The figure which shows the thermal storage driving | operation in the heat-medium supply apparatus which concerns on this invention 本発明に係る熱媒供給装置における給湯運転+ヒートポンプ加熱状態での暖房運転を示す図The figure which shows the heating operation in the hot water supply operation + heat pump heating state in the heat carrier supply apparatus which concerns on this invention 本発明に係る熱媒供給装置における給水手段を示す図The figure which shows the water supply means in the heat-medium supply apparatus which concerns on this invention 本発明に係る熱媒供給装置における蓄熱運転+ヒートポンプ加熱状態での暖房運転を示す図The figure which shows the heating operation in the heat storage driving | operation + heat pump heating state in the heat carrier supply apparatus which concerns on this invention 本発明に係る熱媒供給装置における高温加熱運転を示す図The figure which shows the high temperature heating operation in the heat carrier supply apparatus which concerns on this invention 第2実施形態の熱媒供給装置におけるバイパス状態での給湯運転を示す図The figure which shows the hot water supply operation in the bypass state in the heat carrier supply apparatus of 2nd Embodiment. 第2実施形態の熱媒供給装置における非バイパス状態での給湯運転を示す図The figure which shows the hot water supply operation in the non-bypass state in the heat carrier supply apparatus of 2nd Embodiment. 第2実施形態の熱媒供給装置におけるヒートポンプ加熱状態での暖房運転を示す図The figure which shows the heating operation in the heat pump heating state in the heat carrier supply apparatus of 2nd Embodiment. 第2実施形態の熱媒供給装置における蓄熱運転を示す図The figure which shows the thermal storage driving | operation in the heat carrier supply apparatus of 2nd Embodiment. 第2実施形態の熱媒供給装置におけるバイパス状態での給湯運転+ヒートポンプ加熱状態での暖房運転を示す図The figure which shows the heating operation in the hot water supply operation + heat pump heating state in the bypass state in the heat carrier supply apparatus of 2nd Embodiment 第2実施形態の熱媒供給装置における非バイパス状態での給湯運転+ヒートポンプ加熱状態での暖房運転を示す図The figure which shows the heating operation in the hot water supply operation + heat pump heating state in the non-bypass state in the heat carrier supply apparatus of 2nd Embodiment 第2実施形態の熱媒供給装置における給水手段を示す図The figure which shows the water supply means in the heat-medium supply apparatus of 2nd Embodiment. 第2実施形態の熱媒供給装置における蓄熱運転+ヒートポンプ加熱状態での暖房運転を示す図The figure which shows the heating operation in the heat storage operation + heat pump heating state in the heat carrier supply apparatus of 2nd Embodiment. 第2実施形態の熱媒供給装置における高温加熱運転を示す図The figure which shows the high temperature heating operation in the heat carrier supply apparatus of 2nd Embodiment. 第3実施形態の熱媒供給装置の概略構成を示す図The figure which shows schematic structure of the heat-medium supply apparatus of 3rd Embodiment. 第3実施形態の熱媒供給装置の概略構成を示す図The figure which shows schematic structure of the heat-medium supply apparatus of 3rd Embodiment. 第4実施形態の熱媒供給装置の概略構成を示す図The figure which shows schematic structure of the heat-medium supply apparatus of 4th Embodiment. 第4実施形態の熱媒供給装置の概略構成を示す図The figure which shows schematic structure of the heat-medium supply apparatus of 4th Embodiment. 第5実施形態の熱媒供給装置の概略構成を示す図The figure which shows schematic structure of the heat-medium supply apparatus of 5th Embodiment. 第6実施形態の熱媒供給装置における非バイパス状態での給湯運転を示す図The figure which shows the hot water supply operation in the non-bypass state in the heat carrier supply apparatus of 6th Embodiment 第6実施形態の熱媒供給装置における非バイパス状態での給湯運転を示す図The figure which shows the hot water supply operation in the non-bypass state in the heat carrier supply apparatus of 6th Embodiment 第7実施形態の熱媒供給装置におけるバイパス状態での給湯運転を示す図The figure which shows the hot water supply operation in the bypass state in the heat carrier supply apparatus of 7th Embodiment 第7実施形態の熱媒供給装置における非バイパス状態での給湯運転を示す図The figure which shows the hot water supply operation in the non-bypass state in the heat carrier supply apparatus of 7th Embodiment 第7実施形態の熱媒供給装置におけるヒートポンプ加熱状態での暖房運転を示す図The figure which shows the heating operation in the heat pump heating state in the heat carrier supply apparatus of 7th Embodiment. 第7実施形態の熱媒供給装置における蓄熱運転を示す図The figure which shows the thermal storage driving | operation in the heat carrier supply apparatus of 7th Embodiment 第7実施形態の熱媒供給装置における蓄熱予備運転を示す図The figure which shows the thermal storage preliminary operation in the heat carrier supply apparatus of 7th Embodiment 第7実施形態の熱媒供給装置におけるバイパス状態での給湯運転+ヒートポンプ加熱状態での暖房運転を示す図The figure which shows the heating operation in the hot water supply operation + heat pump heating state in the bypass state in the heat carrier supply apparatus of 7th Embodiment 第7実施形態の熱媒供給装置における非バイパス状態での給湯運転+ヒートポンプ加熱状態での暖房運転を示す図The figure which shows the heating operation in the hot water supply operation + heat pump heating state in the non-bypass state in the heat carrier supply apparatus of 7th Embodiment 第7実施形態の熱媒供給装置における蓄熱運転+ヒートポンプ加熱状態での暖房運転を示す図The figure which shows the heating operation in the heat storage driving | operation + heat pump heating state in the heat carrier supply apparatus of 7th Embodiment 第7実施形態の熱媒供給装置における蓄熱運転中にバイパス状態での給湯運転を行う場合を示す図The figure which shows the case where the hot water supply operation in a bypass state is performed during the heat storage driving | operation in the heat carrier supply apparatus of 7th Embodiment. 第7実施形態の熱媒供給装置における高温加熱運転を示すThe high temperature heating driving | operation in the heat carrier supply apparatus of 7th Embodiment is shown. 第8実施形態の熱媒供給装置の概略構成を示す図The figure which shows schematic structure of the heat-medium supply apparatus of 8th Embodiment. 第9実施形態の熱媒供給装置の概略構成を示す図The figure which shows schematic structure of the heat-medium supply apparatus of 9th Embodiment.

本発明に係る熱媒供給装置の実施形態について、図面に基づいて説明する。
〔第1実施形態〕
この熱媒供給装置は、図1〜3に示すように、給湯利用箇所1(例えば給湯栓)に供給する水を貯留する給湯タンク2と、水路の水を循環させる循環ポンプ3と、ヒートポンプ装置4により水を加熱するヒートポンプ加熱式熱交換器5と、バーナー燃焼装置Nにより水を加熱するバーナー加熱式熱交換器6と、暖房負荷と追焚負荷の少なくとも一方で熱を消費する負荷熱交換器7とを備えている。ここで、図1〜図3は、本発明に係る熱媒供給装置の概略構成を示すものであり、同一の概略構成を示しているが、水や熱媒が通流する部位が異なるので、その水や熱媒が通流する部位を太線にて示している。
An embodiment of a heat medium supply device according to the present invention will be described with reference to the drawings.
[First Embodiment]
As shown in FIGS. 1 to 3, the heat medium supply device includes a hot water tank 2 that stores water to be supplied to a hot water supply location 1 (for example, a hot water tap), a circulation pump 3 that circulates water in the water channel, and a heat pump device. 4, heat pump heating type heat exchanger 5 that heats water, burner heating type heat exchanger 6 that heats water by burner combustion device N, and load heat exchange that consumes heat at least one of a heating load and a memorial load And a container 7. Here, FIG. 1 to FIG. 3 show a schematic configuration of the heat medium supply device according to the present invention and show the same schematic configuration, but the parts through which water and the heat medium flow are different. The part through which the water or heat medium flows is indicated by a thick line.

給湯タンク2は、例えば、密閉型のタンクにて構成されており、温度が高い水(温水)は上方側に且つ温度が低い水は下方側に温度成層を形成する状態で水を貯留自在に構成されている。ヒートポンプ装置4は、圧縮機8、凝縮器としてのヒートポンプ加熱式熱交換器5、膨張弁9、蒸発器10の順に媒体(冷媒)を循環させる媒体回路11を備えた圧縮式ヒートポンプ装置にて構成されている。これにより、ヒートポンプ装置4の媒体(冷媒)は、蒸発器10において外気等から熱を取得し、ヒートポンプ加熱式熱交換器5は、ヒートポンプ装置4の媒体(冷媒)が外気等から取得した熱により水を加熱自在に構成されている。バーナー加熱式熱交換器6は、例えば、ガス燃料等を燃焼させるバーナー燃焼装置Nにて発生する熱にて水を加熱自在に構成されている。   The hot water supply tank 2 is configured by, for example, a sealed tank, and water can be stored in a state in which high temperature water (hot water) forms a temperature stratification on the upper side and low temperature water forms a temperature stratification on the lower side. It is configured. The heat pump device 4 is configured by a compression heat pump device including a compressor 8, a heat pump heating type heat exchanger 5 as a condenser, an expansion valve 9, and a medium circuit 11 that circulates a medium (refrigerant) in this order. Has been. Thereby, the medium (refrigerant) of the heat pump device 4 acquires heat from outside air or the like in the evaporator 10, and the heat pump heating type heat exchanger 5 uses the heat acquired by the medium (refrigerant) of the heat pump device 4 from outside air or the like. The water can be heated freely. The burner heating type heat exchanger 6 is configured to be able to heat water with heat generated by a burner combustion apparatus N that burns gas fuel or the like, for example.

負荷熱交換器7として、暖房負荷用の第1負荷熱交換器7aと追焚負荷用の第2負荷熱交換器7bとが設けられ、第1負荷熱交換器7aと第2負荷熱交換器7bとが並列状態で設けられている。そして、第1負荷熱交換器7aと暖房負荷としての暖房端末12との間で熱媒を循環自在な第1熱媒循環路13が設けられ、その第1熱媒循環路13には、熱媒を貯留自在な大気開放型の熱媒タンク14、第1熱媒循環ポンプ15が設けられている。これにより、第1熱媒循環路13は、第1熱媒循環ポンプ15の圧力で第1負荷熱交換器7aと暖房端末12を経由して熱媒を循環させるように構成されている。ここで、図示は省略するが、暖房端末12としては、要求される熱負荷が高い高温暖房端末(例えば浴室乾燥装置)や高温暖房端末よりも要求される熱負荷が低い低温暖房端末(例えば床暖房装置)が適応可能であり、高温暖房端末と低温暖房端末とを並列状態で備えることができる。また、第2負荷熱交換器7bと追焚負荷としての浴槽16との間で熱媒(浴槽水)を循環自在な第2熱媒循環路17が設けられ、その第2熱媒循環路17には、第2熱媒循環ポンプ18が設けられている。これにより、第2熱媒循環路17は、第2熱媒循環ポンプ18の圧力で第2負荷熱交換器7bと浴槽16を経由して熱媒(浴槽水)を循環させるように構成されている。   As the load heat exchanger 7, a first load heat exchanger 7 a for heating load and a second load heat exchanger 7 b for additional load are provided, and the first load heat exchanger 7 a and the second load heat exchanger are provided. 7b is provided in parallel. And the 1st heat-medium circulation path 13 which can circulate a heat medium freely between the 1st load heat exchanger 7a and the heating terminal 12 as a heating load is provided. An open-air heat medium tank 14 and a first heat medium circulation pump 15 that can store the medium are provided. Accordingly, the first heat medium circulation path 13 is configured to circulate the heat medium via the first load heat exchanger 7 a and the heating terminal 12 with the pressure of the first heat medium circulation pump 15. Here, although illustration is omitted, as the heating terminal 12, a high-temperature heating terminal (for example, a bathroom drying device) that requires a high heat load or a low-temperature heating terminal (for example, a floor) that requires a lower heat load than a high-temperature heating terminal. Heating device) can be applied, and a high temperature heating terminal and a low temperature heating terminal can be provided in parallel. Moreover, the 2nd heat-medium circulation path 17 which can freely circulate a heat medium (tub water) between the 2nd load heat exchanger 7b and the bathtub 16 as an additional load is provided, The 2nd heat-medium circulation path 17 is provided. Is provided with a second heat medium circulation pump 18. Thus, the second heat medium circulation path 17 is configured to circulate the heat medium (tub water) via the second load heat exchanger 7b and the bathtub 16 by the pressure of the second heat medium circulation pump 18. Yes.

本発明に係る熱媒供給装置では、水を通流させる水路として、第1水路W1(図1参照)、第2水路W2(図2参照)、第3水路W3(図3参照)の3つの水路を備えている。第1水路W1は、図1に示すように、少なくとも上水の圧力で給湯タンク2から取り出した水を少なくともバーナー加熱式熱交換器6を経由して給湯利用箇所1に供給するように構成されている。第2水路W2は、図2に示すように、循環ポンプ3の圧力でバーナー加熱式熱交換器6と負荷熱交換器7とヒートポンプ加熱式熱交換器5を経由して水が循環するように構成されている。第3水路W3は、図3に示すように、循環ポンプ3の圧力で少なくとも給湯タンク2とヒートポンプ加熱式熱交換器5を経由して水が循環するように構成されている。   In the heat medium supply device according to the present invention, there are three water channels for flowing water, the first water channel W1 (see FIG. 1), the second water channel W2 (see FIG. 2), and the third water channel W3 (see FIG. 3). Has a waterway. As shown in FIG. 1, the first water channel W <b> 1 is configured to supply water extracted from the hot water supply tank 2 at least with the pressure of clean water to the hot water supply use location 1 via at least the burner heating type heat exchanger 6. ing. As shown in FIG. 2, the second water passage W <b> 2 is configured so that water circulates through the burner heating type heat exchanger 6, the load heat exchanger 7, and the heat pump heating type heat exchanger 5 with the pressure of the circulation pump 3. It is configured. As shown in FIG. 3, the third water channel W <b> 3 is configured such that water circulates at least via the hot water supply tank 2 and the heat pump heating heat exchanger 5 with the pressure of the circulation pump 3.

このように、本発明に係る熱媒供給装置は、第1〜第3水路W1〜W3の3つの水路を備えているが、各水路は、複数の流路部位を組み合わせて構成されているので、各流路部位について説明する。
つまり、本発明に係る熱媒供給装置では、流路部位として、第1流路部位R1、第2流路部位R2、第3流路部位R3、第4流路部位R4、第5流路部位R5、第6流路部位R6、第7流路部位R7の7つの流路部位が備えられている。
As described above, the heating medium supply device according to the present invention includes the three water channels of the first to third water channels W1 to W3, but each water channel is configured by combining a plurality of flow channel parts. Each flow path part will be described.
That is, in the heat medium supply device according to the present invention, the first flow path part R1, the second flow path part R2, the third flow path part R3, the fourth flow path part R4, and the fifth flow path part are used as the flow path parts. Seven flow path portions R5, a sixth flow path portion R6, and a seventh flow path portion R7 are provided.

図1〜図3に示すように、第1流路部位R1は、給湯タンク2の下部に接続されて上水を給湯タンク2に給水するように構成されている。第2流路部位R2は、給湯タンク2の上部とバーナー加熱式熱交換器6を接続するように構成され、その途中部位に第1開閉弁K1が備えられている。第3流路部位R3は、バーナー加熱式熱交換器6と給湯利用箇所1を接続するように構成されている。第4流路部位R4は、第3流路部位の途中部位と負荷熱交換器7を接続するように構成されている。そして、上述の如く、負荷熱交換器7として、第1負荷熱交換器7aと第2負荷熱交換器7bとの2つの負荷熱交換器が備えられており、第1負荷熱交換器7aと第2負荷熱交換器7bとが並列状態で設けられているので、第4流路部位R4において水の通流方向の下流側部位が2つの分岐流路部位に分岐されており、一方の分岐流路部位が第1負荷熱交換器7aに接続され、他方の分岐流路部位が第2負荷熱交換器7bに接続されている。第5流路部位R5は、負荷熱交換器7とヒートポンプ加熱式熱交換器5を接続するように構成されている。上述の如く、第1負荷熱交換器7aと第2負荷熱交換器7bとが並列状態で設けられているので、第5流路部位R5は、第1負荷熱交換器7aと第2負荷熱交換器7bとに各別に接続された2つの分岐流路部位が1つの流路部位に合流してヒートポンプ加熱式熱交換器5に接続されている。そして、第5流路部位R5において第1負荷熱交換器7aに接続された分岐流路部位には、第2開閉弁K2が備えられ、第5流路部位R5において第2負荷熱交換器7bに接続された分岐流路部位には、第3開閉弁K3が備えられている。この第2開閉弁K2及び第3開閉弁K3の開閉動作を制御することで、第1負荷熱交換器7aに水を供給する状態と第2負荷熱交換器7bに水を供給する状態とに切換自在に構成されている。第6流路部位R6は、ヒートポンプ加熱式熱交換器5と第2流路部位R2における第1開閉弁K1とバーナー加熱式熱交換器6との間の部位を接続するように構成され、その途中部位に循環ポンプ3が設けられている。第7流路部位R7は、第1流路部位R1の途中部位と第5流路部位R5の途中部位(2つの分岐流路部位が1つの流路部位に合流する箇所よりも水の通流方向で下流側部位)とを接続するように構成され、その途中部位に第1比例弁H1が備えられている。   As shown in FIGS. 1 to 3, the first flow path part R <b> 1 is connected to the lower part of the hot water supply tank 2 and configured to supply hot water to the hot water supply tank 2. 2nd flow-path part R2 is comprised so that the upper part of the hot water supply tank 2 and the burner heating type heat exchanger 6 may be connected, and the 1st on-off valve K1 is provided in the middle part. 3rd flow-path site | part R3 is comprised so that the burner heating type heat exchanger 6 and the hot water supply utilization location 1 may be connected. The fourth flow path part R4 is configured to connect the intermediate part of the third flow path part and the load heat exchanger 7. As described above, the load heat exchanger 7 includes two load heat exchangers, the first load heat exchanger 7a and the second load heat exchanger 7b, and the first load heat exchanger 7a and Since the second load heat exchanger 7b is provided in parallel, the downstream portion of the fourth flow passage portion R4 in the water flow direction is branched into two branch flow passage portions. The flow path part is connected to the first load heat exchanger 7a, and the other branch flow path part is connected to the second load heat exchanger 7b. The fifth flow path portion R5 is configured to connect the load heat exchanger 7 and the heat pump heating type heat exchanger 5. As described above, since the first load heat exchanger 7a and the second load heat exchanger 7b are provided in parallel, the fifth flow path portion R5 includes the first load heat exchanger 7a and the second load heat exchanger. Two branch flow path portions connected separately to the exchanger 7b merge into one flow path portion and are connected to the heat pump heating type heat exchanger 5. A branch flow passage portion connected to the first load heat exchanger 7a in the fifth flow passage portion R5 is provided with a second on-off valve K2, and the second load heat exchanger 7b is provided in the fifth flow passage portion R5. The branch channel portion connected to is provided with a third on-off valve K3. By controlling the opening / closing operation of the second on-off valve K2 and the third on-off valve K3, the water is supplied to the first load heat exchanger 7a and the water is supplied to the second load heat exchanger 7b. It is configured to be switchable. 6th flow-path part R6 is comprised so that the site | part between the 1st on-off valve K1 in the heat pump heating type heat exchanger 5 and 2nd flow-path part R2 and the burner heating type heat exchanger 6 may be connected, A circulation pump 3 is provided at an intermediate position. The seventh flow path part R7 has a middle part of the first flow path part R1 and a middle part of the fifth flow path part R5 (the flow of water more than the part where the two branch flow path parts merge into one flow path part. The first proportional valve H <b> 1 is provided at a midway portion thereof.

第1水路W1は、図1に示すように、第1流路部位R1と給湯タンク2と第2流路部位R2とバーナー加熱式熱交換器6と第3流路部位R3と第4流路部位R4と負荷熱交換器7と第5流路部位R5とヒートポンプ加熱式熱交換器5と第6流路部位R6とで構成されている。第1流路部位R1は、給湯タンク2の下部に接続されており、第1流路部位R1にて給水される上水の圧力が給湯タンク2に作用している。そして、給湯タンク2の上部には、第2流路部位R2が接続され、その第2流路部位R2にバーナー加熱式熱交換器6を介して第3流路部位R3が接続されているので、第2流路部位R2及び第3流路部位R3にも上水の圧力が作用している。これにより、給湯利用箇所1にて給湯栓を開くことで、上水の圧力によって給湯タンク2の上部から第2流路部位R2に水が取り出され、その取り出された水がバーナー加熱式熱交換器6及び第3流路部位R3を経由して給湯利用箇所1に供給される。そして、循環ポンプ3を作動させることで、循環ポンプ3の圧力でバーナー加熱式熱交換器6と負荷熱交換器7とヒートポンプ加熱式熱交換器5を経由して循環される水をも給湯利用箇所1に供給される。このようにして、第1水路W1は、上水の圧力だけでなく、循環ポンプ3の圧力をも利用して、給湯利用箇所1に水を供給自在に構成されている。   As shown in FIG. 1, the first water channel W1 includes a first flow path part R1, a hot water supply tank 2, a second flow path part R2, a burner heating type heat exchanger 6, a third flow path part R3, and a fourth flow path. It is comprised by site | part R4, the load heat exchanger 7, 5th flow-path part R5, the heat pump heating type heat exchanger 5, and 6th flow-path part R6. The first flow path part R1 is connected to the lower part of the hot water supply tank 2, and the pressure of clean water supplied in the first flow path part R1 acts on the hot water supply tank 2. And since the 2nd flow-path part R2 is connected to the upper part of the hot water supply tank 2, the 3rd flow-path part R3 is connected to the 2nd flow-path part R2 via the burner heating type heat exchanger 6. Also, the pressure of clean water is acting on the second flow path part R2 and the third flow path part R3. Thereby, by opening the hot water tap at the hot water use location 1, water is taken out from the upper part of the hot water tank 2 to the second flow path part R2 by the pressure of the hot water, and the taken out water is burner heating type heat exchange. It is supplied to the hot water supply utilization point 1 via the vessel 6 and the third flow path part R3. And by operating the circulation pump 3, the water circulated through the burner heating type heat exchanger 6, the load heat exchanger 7, and the heat pump heating type heat exchanger 5 with the pressure of the circulation pump 3 is also used. Supplied to location 1. In this way, the first water channel W1 is configured to be able to supply water to the hot water supply use location 1 by using not only the pressure of clean water but also the pressure of the circulation pump 3.

第2水路W2は、図2に示すように、バーナー加熱式熱交換器6と第3流路部位R3の一部(バーナー加熱式熱交換器6との接続箇所から第4流路部位R4との接続箇所までの間の部位)と第4流路部位R4と負荷熱交換器7と第5流路部位R5とヒートポンプ加熱式熱交換器5と第6流路部位R6と第2流路部位R2の一部(第6流路部位R6との接続箇所からバーナー加熱式熱交換器6との接続箇所までの間の部位)とから構成されている。   As shown in FIG. 2, the second water channel W2 includes a part of the burner heating type heat exchanger 6 and the third flow path part R3 (from the connection point between the burner heating type heat exchanger 6 and the fourth flow path part R4. To the connection portion), the fourth flow passage portion R4, the load heat exchanger 7, the fifth flow passage portion R5, the heat pump heating type heat exchanger 5, the sixth flow passage portion R6, and the second flow passage portion. Part of R2 (a part between a connection part with the sixth flow path part R6 and a connection part with the burner heating type heat exchanger 6).

第3水路W3は、図3に示すように、給湯タンク2と第1流路部位R1の一部(給湯タンク2との接続箇所から第7流路部位R7との接続箇所までの間の部位)と第7流路部位R7と第5流路部位R5の一部(第7流路部位R7との接続箇所からヒートポンプ加熱式熱交換器5との接続箇所までの間の部位)とヒートポンプ加熱式熱交換器5と第6流路部位R6と第2流路部位R2の一部(第6流路部位R6との接続箇所から給湯タンク2との接続箇所までの間の部位)とから構成されている。   As shown in FIG. 3, the third water channel W3 is a part of the hot water supply tank 2 and a part of the first flow path part R1 (the part between the connection point of the hot water supply tank 2 and the connection point of the seventh flow path part R7. ), A part of the seventh flow path part R7 and a part of the fifth flow path part R5 (a part between the connection point of the seventh flow path part R7 and the connection point of the heat pump heating type heat exchanger 5) and the heat pump heating. It comprises a heat exchanger 5, a sixth flow path part R 6, and a part of the second flow path part R 2 (parts between the connection point with the sixth flow path part R 6 and the connection point with the hot water tank 2). Has been.

本発明に係る熱媒供給装置は、第1水路W1と第2水路W2は、第2流路部位R2の一部、バーナー加熱式熱交換器6、第3流路部位R3の一部、第4流路部位R4、負荷熱交換器7、第5流路部位R5、ヒートポンプ加熱式熱交換器5、及び、第6流路部位R6(図1及び図2の双方で太線にて示した部位)が共通であり、循環ポンプ3とバーナー加熱式熱交換器6と負荷熱交換器7とヒートポンプ加熱式熱交換器5を含む水路が少なくとも共通に構成されている。第2水路W2と第3水路W3は、第5流路部位R5の一部、ヒートポンプ加熱式熱交換器5、及び、第6流路部位R6(図2及び図3の双方で太線にて示した部位)が共通であり、ヒートポンプ加熱式熱交換器5を含む水路が少なくとも共通に構成されている。第1水路W1と第3水路W3は、第1流路部位R1の一部、給湯タンク2、第2流路部位R2の一部、第5流路部位R5の一部、ヒートポンプ加熱式熱交換器5、及び、第6流路部位R6(図1及び図3の双方で太線にて示した部位)が共通であり、給湯タンク2を含む水路及びヒートポンプ加熱式熱交換器5を含む水路が少なくとも共通に構成されている。このように、本発明に係る熱媒供給装置では、第1水路W1と第2水路W2と第3水路W3の間で共通の流路部位があり、配管が簡易でシンプルなものとなる。そして、熱交換器として構造が複雑な三流体熱交換器等の構造を採用することなく、単一の循環ポンプ3、単一のヒートポンプ加熱式熱交換器5、単一のバーナー加熱式熱交換器6を備えるだけでよく、循環ポンプや熱交換器の数を極力少なくして、構成の簡素化及びコストの低減を図ることができる。   In the heat medium supply device according to the present invention, the first water channel W1 and the second water channel W2 are a part of the second flow path part R2, the burner heating heat exchanger 6, a part of the third flow path part R3, the first 4 flow path part R4, load heat exchanger 7, 5th flow path part R5, heat pump heating type heat exchanger 5, and 6th flow path part R6 (part shown with the thick line in both FIG.1 and FIG.2) ) And the water channel including the circulation pump 3, the burner heating type heat exchanger 6, the load heat exchanger 7, and the heat pump heating type heat exchanger 5 is configured at least in common. The second water channel W2 and the third water channel W3 are a part of the fifth flow path part R5, the heat pump heating type heat exchanger 5, and the sixth flow path part R6 (shown in bold lines in both FIGS. 2 and 3). The water channel including the heat pump heating type heat exchanger 5 is at least commonly configured. The first water channel W1 and the third water channel W3 are a part of the first channel part R1, a hot water tank 2, a part of the second channel part R2, a part of the fifth channel part R5, a heat pump heating type heat exchange. And the water channel including the hot water tank 2 and the water channel including the heat pump heating type heat exchanger 5 are the same. It is at least commonly configured. Thus, in the heat medium supply device according to the present invention, there is a common flow path portion among the first water channel W1, the second water channel W2, and the third water channel W3, and the piping becomes simple and simple. And, without adopting a structure such as a three-fluid heat exchanger having a complicated structure as a heat exchanger, a single circulation pump 3, a single heat pump heating type heat exchanger 5, a single burner heating type heat exchange The number of circulation pumps and heat exchangers can be reduced as much as possible, and the configuration can be simplified and the cost can be reduced.

この熱媒供給装置の運転を制御するコンピュータを備えた運転制御手段19が設けられており、この運転制御手段19は、熱媒供給装置の運転を指令する人為操作式の熱媒供給装置用リモコン(図示は省略する)との間で各種の情報を通信可能に構成されている。熱媒供給装置用リモコンは、例えば、台所や浴室等の夫々に設けられており、給湯設定温度等を設定可能であるとともに、各種スイッチのON操作により各種運転の運転要求を要求可能に構成されている。また、運転制御手段19は、暖房端末12の運転を指令する人為操作式の暖房端末用リモコンとの間で各種の情報を通信可能に構成されている。   An operation control means 19 having a computer for controlling the operation of the heat medium supply device is provided. The operation control means 19 is a manually operated remote controller for the heat medium supply device that commands the operation of the heat medium supply device. Various types of information can be communicated with (not shown). The remote control for the heating medium supply device is provided in each of the kitchen and bathroom, for example, and can set the hot water supply set temperature, etc., and can request operation requests of various operations by turning on various switches. ing. The operation control means 19 is configured to be able to communicate various types of information with an artificially operated heating terminal remote controller that commands the operation of the heating terminal 12.

運転制御手段19は、熱媒供給装置用リモコンの運転スイッチがON操作されると制御可能な状態となり、給湯利用箇所1の給湯栓が開操作されると、給湯利用箇所1に給湯する給湯運転を実行する。そして、運転制御手段19は、例えば、給湯タンク2に貯留されている温水量が設定量以下になる、或いは、給湯利用箇所1に給湯する給湯時間帯よりも設定時間手前の蓄熱時間帯になる等の蓄熱条件が満たされると、蓄熱運転の運転要求があったとして、給湯タンク2に蓄熱する蓄熱運転を実行する。また、運転制御手段19は、暖房端末用リモコンの暖房運転スイッチがON操作されて暖房端末12から運転要求が要求されると暖房運転を実行し、追焚スイッチがON操作されて追焚要求が要求されると追焚運転を実行する。ここで、暖房運転と追焚運転が、熱消費運転に相当する。
以下、各運転について説明する。
The operation control means 19 is in a controllable state when the operation switch of the remote controller for the heat medium supply device is turned ON, and when the hot water tap at the hot water supply use location 1 is opened, the hot water supply operation for supplying hot water to the hot water use usage location 1 Execute. Then, the operation control means 19 is, for example, the amount of hot water stored in the hot water supply tank 2 is equal to or less than the set amount, or is in the heat storage time zone that is a set time before the hot water supply time zone in which the hot water supply location 1 is supplied with hot water. When the heat storage conditions such as the above are satisfied, the heat storage operation for storing heat in the hot water supply tank 2 is executed on the assumption that there is an operation request for the heat storage operation. Further, the operation control means 19 executes the heating operation when the heating operation switch of the remote control for the heating terminal is turned ON and an operation request is requested from the heating terminal 12, and the remedy switch is turned ON and the memorial request is issued. Carry out memorial operation when requested. Here, the heating operation and the memorial operation correspond to the heat consumption operation.
Hereinafter, each operation will be described.

(蓄熱運転)
運転制御手段19は、図3に示すように、ヒートポンプ装置4を作動状態に切り換え、バーナー燃焼装置Nを非燃焼状態に切り換え、循環ポンプ3を作動させるとともに、第1開閉弁K1及び第1比例弁H1を開動作させる。これにより、運転制御手段19は、第3水路W3によって、循環ポンプ3の圧力で、給湯タンク2の下部から水を第1流路部位R1に取り出し、その取り出した水を第7流路部位R7及び第5流路部位R5を経由してヒートポンプ加熱式熱交換器5に供給して加熱し、その加熱された水を第6流路部位R6及び第2流路部位R2を経由して給湯タンク2の上部に戻している。このようにして、給湯タンク2から取り出された水がヒートポンプ加熱式熱交換器5にて加熱されて温水となり、その温水が給湯タンク2に戻されて、給湯タンク2に蓄熱している。ここで、運転制御手段19は、給湯タンク2の上部に戻す温水の温度が所定温度になるように、循環ポンプ3の回転速度及び第1比例弁H1の開度を調整してヒートポンプ加熱式熱交換器5に供給する水の供給量を調整している。
(Heat storage operation)
As shown in FIG. 3, the operation control means 19 switches the heat pump device 4 to the operating state, switches the burner combustion device N to the non-burning state, operates the circulation pump 3, and operates the first on-off valve K1 and the first proportionality. The valve H1 is opened. Thereby, the operation control means 19 takes out the water from the lower part of the hot water supply tank 2 to the first flow path part R1 by the pressure of the circulation pump 3 through the third water path W3, and takes the taken-out water into the seventh flow path part R7. And the heat pump heating type heat exchanger 5 via the fifth flow path part R5 and heated, and the heated water is supplied to the hot water supply tank via the sixth flow path part R6 and the second flow path part R2. Return to the top of 2. In this way, the water taken out from the hot water supply tank 2 is heated by the heat pump heating type heat exchanger 5 to become hot water, and the hot water is returned to the hot water supply tank 2 to store heat in the hot water supply tank 2. Here, the operation control means 19 adjusts the rotational speed of the circulation pump 3 and the opening of the first proportional valve H1 so that the temperature of the hot water returned to the upper part of the hot water supply tank 2 becomes a predetermined temperature, and heat pump heating type heat The amount of water supplied to the exchanger 5 is adjusted.

(給湯運転)
この給湯運転では、図1に示すように、運転制御手段19が、第1開閉弁K1を開動作させることで、給湯利用箇所1の給湯栓が開操作されることによって、上水の圧力で、給湯タンク2の上部から水を第2流路部位R2に取り出し、その取り出した水をバーナー加熱式熱交換器6に供給して加熱し、その加熱された水を第3流路部位R3にて給湯利用箇所1に供給している。また、運転制御手段19は、循環ポンプ3を作動させるとともに、第4流路部位R4からの水を第1負荷熱交換器7a及び第2負荷熱交換器7bの両方又は一方に供給するように第2開閉弁K2及び第3開閉弁K3の開閉動作を制御している。これにより、循環ポンプ3の圧力でバーナー加熱式熱交換器6と負荷熱交換器7とヒートポンプ加熱式熱交換器5を経由して水が循環されている。ここで、第2開閉弁K2及び第3開閉弁K3の開閉動作について、図1では、第4流路部位R4からの水を第1負荷熱交換器7aの一方に供給するように第2開閉弁K2及び第3開閉弁K3の開閉動作を制御した場合を示している。
(Hot water operation)
In this hot water supply operation, as shown in FIG. 1, the operation control means 19 opens the first on-off valve K1 to open the hot water tap at the hot water use location 1 so that the water supply pressure is increased. The water is taken out from the upper part of the hot water supply tank 2 to the second flow path part R2, the taken-out water is supplied to the burner heating type heat exchanger 6 and heated, and the heated water is supplied to the third flow path part R3. The hot water supply location 1 is supplied. Further, the operation control means 19 operates the circulation pump 3 and supplies water from the fourth flow path portion R4 to both or one of the first load heat exchanger 7a and the second load heat exchanger 7b. The opening / closing operation of the second opening / closing valve K2 and the third opening / closing valve K3 is controlled. Accordingly, water is circulated through the burner heating heat exchanger 6, the load heat exchanger 7, and the heat pump heating heat exchanger 5 with the pressure of the circulation pump 3. Here, regarding the opening / closing operation of the second opening / closing valve K2 and the third opening / closing valve K3, in FIG. 1, the second opening / closing is performed so as to supply water from the fourth flow path part R4 to one of the first load heat exchangers 7a. The case where the opening / closing operation | movement of the valve K2 and the 3rd on-off valve K3 is controlled is shown.

このようにして、運転制御手段19は、給湯運転において、第1水路W1によって、上水の圧力で給湯タンク2の水を給湯利用箇所1に供給するとともに、循環ポンプ3の圧力でバーナー加熱式熱交換器6と負荷熱交換器7とヒートポンプ加熱式熱交換器5を経由して循環される水を給湯利用箇所1に供給している。これにより、給湯タンク2から取り出した水だけでなく、バーナー加熱式熱交換器6と負荷熱交換器7とヒートポンプ加熱式熱交換器5を経由して循環される水をも、給湯利用箇所1に供給することができるので、給湯利用箇所1に供給する水の水量として十分な水量を確保することができる。しかも、給湯タンク2から取り出した水がバーナー加熱式熱交換器6にて加熱された水と混合されて、その混合された水がバーナー加熱式熱交換器6に供給されるので、バーナー加熱式熱交換器6に供給される水の温度が比較的安定した温度となり、その結果、給湯利用箇所1にて要求されている給湯設定温度の水を安定して供給することができる。   In this way, in the hot water supply operation, the operation control means 19 supplies the water in the hot water tank 2 to the hot water use location 1 with the pressure of the clean water through the first water channel W1, and the burner heating type with the pressure of the circulation pump 3 Water circulated through the heat exchanger 6, the load heat exchanger 7, and the heat pump heating type heat exchanger 5 is supplied to the hot water supply utilization location 1. Thereby, not only the water taken out from the hot water supply tank 2 but also the water circulated through the burner heating type heat exchanger 6, the load heat exchanger 7 and the heat pump heating type heat exchanger 5 are used in the hot water supply use place 1. Therefore, it is possible to secure a sufficient amount of water as the amount of water to be supplied to the hot water supply use location 1. Moreover, since the water taken out from the hot water supply tank 2 is mixed with the water heated in the burner heating type heat exchanger 6 and the mixed water is supplied to the burner heating type heat exchanger 6, the burner heating type The temperature of the water supplied to the heat exchanger 6 becomes a relatively stable temperature, and as a result, it is possible to stably supply the water at the hot water supply set temperature required at the hot water supply use location 1.

ここで、図示は省略しているが、給湯利用箇所1に供給される水の温度が給湯利用箇所1にて要求されている給湯設定温度よりも高い場合には、運転制御手段19が、第3流路部位R3の第4流路部位R4との接続箇所と給湯利用箇所1の間に設置した、上水との混合を行う三方弁を作動させ、その混合後の水の温度が給湯利用箇所1にて要求されている給湯設定温度となるように、三方弁による上水との混合量を調整している。   Here, although illustration is omitted, when the temperature of the water supplied to the hot water supply usage location 1 is higher than the hot water supply set temperature required at the hot water usage usage location 1, the operation control means 19 A three-way valve for mixing with clean water, which is installed between the connection point of the third flow path part R3 with the fourth flow path part R4 and the hot water supply use part 1, is operated, and the temperature of the mixed water is used for hot water supply. The amount of mixing with clean water by the three-way valve is adjusted so that the hot water supply set temperature required at the location 1 is obtained.

(暖房運転)
運転制御手段19は、図2に示すように、循環ポンプ3を作動させるとともに、第4流路部位R4からの水を第1負荷熱交換器7aに供給するように第2開閉弁K2及び第3開閉弁K3の開閉動作を制御する。これにより、第2水路W2によって、循環ポンプ3の圧力でバーナー加熱式熱交換器6と第1負荷熱交換器7aとヒートポンプ加熱式熱交換器5を経由して水を循環させている。
(Heating operation)
As shown in FIG. 2, the operation control means 19 operates the circulation pump 3 and supplies the second on-off valve K2 and the second valve so as to supply water from the fourth flow path portion R4 to the first load heat exchanger 7a. The opening / closing operation of the 3 on-off valve K3 is controlled. Thereby, the water is circulated by the pressure of the circulation pump 3 through the burner heating type heat exchanger 6, the first load heat exchanger 7a, and the heat pump heating type heat exchanger 5 by the second water passage W2.

そして、運転制御手段19は、第2水路W2にて水を循環させている状態で、バーナー燃焼装置Nを燃焼状態と非燃焼状態とに切り換えるとともに、ヒートポンプ装置4を作動状態と非作動状態とに切り換えることで、バーナー加熱式熱交換器6にて加熱した水を第1負荷熱交換器7aに供給するバーナー加熱状態とヒートポンプ加熱式熱交換器5にて加熱した水を第1負荷熱交換器7aに供給するヒートポンプ加熱状態とに切換自在に構成されている。そして、暖房運転を行うに当たり、運転制御手段19は、第1負荷熱交換器7aで要求されている熱負荷に対して、バーナー加熱状態に切り換えた場合とヒートポンプ加熱状態に切り換えた場合との夫々の1次エネルギー消費量を求め、その求めた1次エネルギー消費量が小さい方に切り換えている。   Then, the operation control means 19 switches the burner combustion device N between the combustion state and the non-combustion state in a state where water is circulated in the second water passage W2, and the heat pump device 4 is switched between the operation state and the non-operation state. By switching to, the burner heating state in which the water heated by the burner heating type heat exchanger 6 is supplied to the first load heat exchanger 7a and the water heated by the heat pump heating type heat exchanger 5 are converted to the first load heat exchange. It is configured to be switchable to a heat pump heating state supplied to the vessel 7a. Then, when performing the heating operation, the operation control means 19 respectively switches the burner heating state and the heat pump heating state to the heat load required in the first load heat exchanger 7a. The primary energy consumption amount is calculated, and the calculated primary energy consumption amount is switched to the smaller one.

バーナー加熱状態に切り換えた場合の1次エネルギー消費量の求め方については、第1負荷熱交換器7aで要求されている熱負荷を変換効率にて除算することにより、その熱負荷を賄うためのガス需要を求める。ここで、変換効率は、バーナー加熱状態に切り換えてバーナー加熱式熱交換器6にて水を加熱したときの変換効率を用いる。そして、求めたガス需要を所定の換算値を用いて1次エネルギー消費量に換算している。
ヒートポンプ加熱状態に切り換えた場合の1次エネルギー消費量の求め方については、第1負荷熱交換器7aで要求されている熱負荷をCOP(成績係数)にて除算することにより、その熱負荷を賄うための電気需要を求める。ここで、COPは、ヒートポンプ加熱状態に切り換えてヒートポンプ加熱式熱交換器5にて水を加熱したときのCOPを用いる。そして、求めた電気需要を所定の換算値を用いて1次エネルギー消費量に換算している。
Regarding how to obtain the primary energy consumption when switching to the burner heating state, the heat load required in the first load heat exchanger 7a is divided by the conversion efficiency to cover the heat load. Demand gas demand. Here, the conversion efficiency is the conversion efficiency when water is heated by the burner heating type heat exchanger 6 after switching to the burner heating state. And the calculated | required gas demand is converted into the primary energy consumption using a predetermined conversion value.
The primary energy consumption when switching to the heat pump heating state is calculated by dividing the heat load required by the first load heat exchanger 7a by the COP (coefficient of performance). Demand electricity demand to cover. Here, COP uses COP when it switches to a heat pump heating state and water is heated with the heat pump heating type heat exchanger 5. FIG. And the calculated | required electricity demand is converted into the primary energy consumption using a predetermined conversion value.

図2に示すように、ヒートポンプ加熱状態に切り換える場合には、運転制御手段19が、バーナー燃焼装置Nを非燃焼状態に切り換えるとともに、ヒートポンプ装置4を作動状態に切り換え、第1熱媒循環ポンプ15を作動させる。これにより、ヒートポンプ加熱式熱交換器5にて水が加熱されて温水となり、その温水が第6流路部位R6、第2流路部位R2、バーナー加熱式熱交換器6、第3流路部位R3、及び、第4流路部位R4を経由して第1負荷熱交換器7aに供給されて第1熱媒循環路13の熱媒を加熱する。このとき、バーナー燃焼装置Nを非燃焼状態に切り換えているので、バーナー加熱式熱交換器6では水が加熱されない。第1負荷熱交換器7aにおいて加熱された熱媒は、第1熱媒循環路13にて暖房端末12に供給されて暖房端末12での暖房を行う。   As shown in FIG. 2, when switching to the heat pump heating state, the operation control means 19 switches the burner combustion device N to the non-burning state, switches the heat pump device 4 to the operating state, and the first heat medium circulation pump 15. Is activated. Thereby, water is heated in the heat pump heating type heat exchanger 5 to become warm water, and the warm water is the sixth flow path part R6, the second flow path part R2, the burner heating type heat exchanger 6, the third flow path part. The heat medium in the first heat medium circulation path 13 is heated by being supplied to the first load heat exchanger 7a via R3 and the fourth flow path part R4. At this time, since the burner combustion apparatus N is switched to the non-burning state, the burner heating heat exchanger 6 does not heat water. The heat medium heated in the first load heat exchanger 7 a is supplied to the heating terminal 12 through the first heat medium circulation path 13 and is heated in the heating terminal 12.

一方、バーナー加熱状態に切り換える場合には、図2に示したヒートポンプ加熱状態に切り換える場合と比べて、水や熱媒の通流する部位は同様であり、バーナー燃焼装置N及びヒートポンプ装置4の状態が異なるだけであるので、図示を省略して説明する。
運転制御手段19が、バーナー燃焼装置Nを燃焼状態に切り換えるとともに、ヒートポンプ装置4を非作動状態に切り換え、第1熱媒循環ポンプ15を作動させる。これにより、バーナー加熱式熱交換器6にて水が加熱されて温水となり、その温水が第3流路部位R3及び第4流路部位R4を経由して第1負荷熱交換器7aに供給されて第1熱媒循環路13の熱媒を加熱する。このとき、ヒートポンプ装置4を非作動状態に切り換えているので、ヒートポンプ加熱式熱交換器5では水が加熱されない。第1負荷熱交換器7aにおいて加熱された熱媒は、第1熱媒循環路13により暖房端末12に供給されて暖房端末12での暖房を行う。
On the other hand, when switching to the burner heating state, compared with the case of switching to the heat pump heating state shown in FIG. 2, the part through which water and heat medium flow is the same, and the state of the burner combustion device N and the heat pump device 4 Are different from each other, and the illustration is omitted.
The operation control means 19 switches the burner combustion device N to the combustion state, switches the heat pump device 4 to the non-operation state, and operates the first heat medium circulation pump 15. Thereby, water is heated in the burner heating type heat exchanger 6 to become warm water, and the warm water is supplied to the first load heat exchanger 7a via the third flow path part R3 and the fourth flow path part R4. The heating medium in the first heating medium circulation path 13 is heated. At this time, since the heat pump device 4 is switched to the non-operating state, water is not heated in the heat pump heating type heat exchanger 5. The heat medium heated in the first load heat exchanger 7 a is supplied to the heating terminal 12 by the first heat medium circulation path 13 and is heated in the heating terminal 12.

(追焚運転)
上述の暖房運転では、運転制御手段19が、第4流路部位R4からの水を第1負荷熱交換器7aに供給するように第2開閉弁K2及び第3開閉弁K3の開閉動作を制御しているが、この追焚運転では、運転制御手段19が、第4流路部位R4からの水を第2負荷熱交換器7bに供給するように第2開閉弁K2及び第3開閉弁K3の開閉動作を制御している点が上述の暖房運転と異なるだけであるので、図示は省略して簡単に説明する。
(Memorial operation)
In the heating operation described above, the operation control means 19 controls the opening / closing operations of the second on-off valve K2 and the third on-off valve K3 so as to supply water from the fourth flow path part R4 to the first load heat exchanger 7a. However, in this chasing operation, the operation control means 19 supplies the second on-off valve K2 and the third on-off valve K3 so as to supply water from the fourth flow path portion R4 to the second load heat exchanger 7b. The point of controlling the opening / closing operation is different from that of the above-described heating operation, so that the illustration will be omitted briefly.

運転制御手段19は、上述の暖房運転と同様に、循環ポンプ3を作動させるとともに、第4流路部位R4からの水を第2負荷熱交換器7bに供給するように第2開閉弁K2及び第3開閉弁K3の開閉動作を制御する。そして、運転制御手段19は、バーナー燃焼装置Nを燃焼状態と非燃焼状態とに切り換えるとともに、ヒートポンプ装置4を作動状態と非作動状態とに切り換えることで、バーナー加熱式熱交換器6にて加熱した水を第2負荷熱交換器7bに供給するバーナー加熱状態とヒートポンプ加熱式熱交換器5にて加熱した水を第2負荷熱交換器7bに供給するヒートポンプ加熱状態とに切換自在に構成されている。そして、追焚運転を行うに当たり、運転制御手段19は、第2負荷熱交換器7bで要求されている熱負荷に対して、バーナー加熱状態に切り換えた場合とヒートポンプ加熱状態に切り換えた場合との夫々の1次エネルギー消費量を求め、その求めた1次エネルギー消費量が小さい方に切り換えている。   Similarly to the heating operation described above, the operation control means 19 operates the circulation pump 3 and supplies the second on-off valve K2 and the water from the fourth flow path portion R4 to the second load heat exchanger 7b. The opening / closing operation of the third opening / closing valve K3 is controlled. Then, the operation control means 19 switches the burner combustion device N between the combustion state and the non-combustion state and switches the heat pump device 4 between the operation state and the non-operation state, thereby heating the burner heating type heat exchanger 6. It is possible to switch between a burner heating state in which the water is supplied to the second load heat exchanger 7b and a heat pump heating state in which the water heated in the heat pump heating type heat exchanger 5 is supplied to the second load heat exchanger 7b. ing. And in performing a memorial operation, the operation control means 19 is the case where it switches to a burner heating state with respect to the heat load requested | required by the 2nd load heat exchanger 7b, and the case where it switches to a heat pump heating state. Each primary energy consumption is determined, and the calculated primary energy consumption is switched to a smaller one.

上述の如く、本発明に係る熱媒供給装置は、蓄熱運転、給湯運転、ヒートポンプ加熱状態での暖房運転、バーナー加熱状態での暖房運転、ヒートポンプ加熱状態での追焚運転、バーナー加熱状態での追焚運転の各運転を単独で行うことが可能であるが、2つの運転を同時に行うことも可能である。   As described above, the heat medium supply device according to the present invention includes a heat storage operation, a hot water supply operation, a heating operation in a heat pump heating state, a heating operation in a burner heating state, a memorial operation in a heat pump heating state, and a burner heating state. Each operation of the memorial operation can be performed independently, but two operations can be performed simultaneously.

(給湯運転+ヒートポンプ加熱状態での暖房運転の同時運転)
給湯運転とヒートポンプ加熱状態での暖房運転とを同時に行う場合には、図4に示すように、運転制御手段19は、ヒートポンプ装置4を作動状態に切り換え、バーナー燃焼装置Nを燃焼状態に切り換え、循環ポンプ3及び第1熱媒循環ポンプ15を作動させるとともに、第4流路部位R4からの水を第1負荷熱交換器7aに供給するように第2開閉弁K2及び第3開閉弁K3の開閉動作を制御している。これにより、運転制御手段19は、第1水路W1にて給湯タンク2の水とバーナー加熱式熱交換器6と第1負荷熱交換器7aとヒートポンプ加熱式熱交換器5を経由して循環される水とを給湯利用箇所1に供給する給湯運転と、第2水路W2にてヒートポンプ加熱式熱交換器5にて加熱された水を第1負荷熱交換器7aに供給するヒートポンプ加熱状態での暖房運転とを同時に行うことができる。
(Simultaneous operation of hot water supply operation + heating operation with heat pump heated)
When simultaneously performing the hot water supply operation and the heating operation in the heat pump heating state, as shown in FIG. 4, the operation control means 19 switches the heat pump device 4 to the operating state, switches the burner combustion device N to the combustion state, The second on-off valve K2 and the third on-off valve K3 are operated so that the circulation pump 3 and the first heat medium circulation pump 15 are operated and water from the fourth flow path part R4 is supplied to the first load heat exchanger 7a. Controls opening and closing operations. Thereby, the operation control means 19 is circulated in the first water channel W1 through the water in the hot water supply tank 2, the burner heating type heat exchanger 6, the first load heat exchanger 7a, and the heat pump heating type heat exchanger 5. In the heat pump heating state in which the water heated by the heat pump heating type heat exchanger 5 in the second water passage W2 is supplied to the first load heat exchanger 7a. Heating operation can be performed simultaneously.

そして、図4に示すように、給湯運転とヒートポンプ加熱状態での暖房運転とを同時に行っている場合には、ヒートポンプ加熱式熱交換器5に供給される水の温度が徐々に上昇していき、ヒートポンプ加熱式熱交換器5に供給される水の温度が所定温度(例えば40℃)よりも高くなる場合がある。このように、ヒートポンプ加熱式熱交換器5に供給される水の温度が所定温度(例えば40℃)よりも高くなると、ヒートポンプ装置4のCOP(成績係数)が低下するので、COP(成績係数)が低下した状態でヒートポンプ装置4の運転が継続されると、エネルギー効率が低下することになる。
そこで、給湯運転とヒートポンプ加熱状態での暖房運転とを同時に行っている場合に、ヒートポンプ加熱式熱交換器5に供給される水の温度が所定温度(例えば40℃)よりも高くなると、図5に示すように、運転制御手段19は、第1比例弁H1を開動作させている。ここで、ヒートポンプ加熱式熱交換器5に供給される水の温度については、図示は省略するが、第5流路部位R5においてヒートポンプ加熱式熱交換器5の入口部位に水の温度を検出する温度センサを備えており、この温度センサの検出温度をヒートポンプ加熱式熱交換器5に供給される水の温度としている。これにより、第1流路部位R1及び第7流路部位R7を経由して給水される水が第5流路部位R5にてヒートポンプ加熱式熱交換器5に供給される水に混合されて、ヒートポンプ加熱式熱交換器5に供給される水の温度が低下する。そして、運転制御手段19は、ヒートポンプ加熱式熱交換器5に供給される水の温度が所定温度(例えば40℃)以下となるように、第1比例弁H1の開度を調整している。このように、第1水路W1にて給湯利用箇所1に水を供給する給湯運転を行っており、ヒートポンプ装置4を作動状態に切り換えている場合に、ヒートポンプ加熱式熱交換器5に供給される水の温度が所定温度(例えば40℃)よりも高くなると、ヒートポンプ加熱式熱交換器5に供給される水に給水して、ヒートポンプ加熱式熱交換器5に供給される水の温度を所定温度(例えば40℃)以下に調整自在な給水手段20が備えられている。この給水手段20は、第1流路部位R1の一部、第7流路部位R7、第1比例弁H1、及び、運転制御手段19から構成されている。この給水手段20を備えることで、COP(成績係数)が低下した状態でヒートポンプ装置4の運転が継続されるのを防止して、エネルギー効率が低下するのを防止することができる。
As shown in FIG. 4, when the hot water supply operation and the heating operation in the heat pump heating state are simultaneously performed, the temperature of the water supplied to the heat pump heating heat exchanger 5 gradually increases. The temperature of water supplied to the heat pump heating type heat exchanger 5 may be higher than a predetermined temperature (for example, 40 ° C.). As described above, when the temperature of the water supplied to the heat pump heating type heat exchanger 5 is higher than a predetermined temperature (for example, 40 ° C.), the COP (coefficient of performance) of the heat pump device 4 is lowered. If the operation of the heat pump device 4 is continued in a state where the temperature is lowered, the energy efficiency is lowered.
Therefore, when the hot water supply operation and the heating operation in the heat pump heating state are performed simultaneously, when the temperature of the water supplied to the heat pump heating type heat exchanger 5 becomes higher than a predetermined temperature (for example, 40 ° C.), FIG. As shown, the operation control means 19 opens the first proportional valve H1. Here, although illustration is abbreviate | omitted about the temperature of the water supplied to the heat pump heating type heat exchanger 5, the temperature of water is detected in the entrance site | part of the heat pump heating type heat exchanger 5 in 5th flow-path part R5. A temperature sensor is provided, and the temperature detected by this temperature sensor is the temperature of the water supplied to the heat pump heating type heat exchanger 5. Thereby, the water supplied through the first flow path part R1 and the seventh flow path part R7 is mixed with the water supplied to the heat pump heating heat exchanger 5 in the fifth flow path part R5, The temperature of the water supplied to the heat pump heating type heat exchanger 5 is lowered. And the operation control means 19 adjusts the opening degree of the 1st proportional valve H1 so that the temperature of the water supplied to the heat pump heating type heat exchanger 5 may become below predetermined temperature (for example, 40 degreeC). Thus, when the hot water supply operation which supplies water to the hot-water supply utilization location 1 is performed in the 1st water channel W1, and the heat pump apparatus 4 is switched to an operation state, it is supplied to the heat pump heating type heat exchanger 5. When the temperature of the water becomes higher than a predetermined temperature (for example, 40 ° C.), the water supplied to the heat pump heating type heat exchanger 5 is supplied with water, and the temperature of the water supplied to the heat pump heating type heat exchanger 5 is set to the predetermined temperature. A water supply means 20 that can be adjusted below (for example, 40 ° C.) is provided. The water supply means 20 includes a part of the first flow path part R1, a seventh flow path part R7, a first proportional valve H1, and an operation control means 19. By providing this water supply means 20, it is possible to prevent the operation of the heat pump device 4 from being continued in a state where the COP (coefficient of performance) is lowered, and to prevent the energy efficiency from being lowered.

(給湯運転+バーナー加熱状態での暖房運転の同時運転)
給湯運転とバーナー加熱状態での暖房運転とを同時に行う場合には、図4に示した給湯運転とヒートポンプ加熱状態での暖房運転とを同時に行う場合と比べて、水や熱媒の通流する部位は同様であり、バーナー燃焼装置N及びヒートポンプ装置4の状態が異なるだけであるので、図示を省略して説明する。
運転制御手段19は、ヒートポンプ装置4を非作動状態に切り換え、バーナー燃焼装置Nを燃焼状態に切り換え、循環ポンプ3及び第1熱媒循環ポンプ15を作動させるとともに、第4流路部位R4からの水を第1負荷熱交換器7aに供給するように第2開閉弁K2及び第3開閉弁K3の開閉動作を制御している。これにより、運転制御手段19は、第1水路W1にて給湯タンク2の水とバーナー加熱式熱交換器6と第1負荷熱交換器7aとヒートポンプ加熱式熱交換器5を経由して循環される水とを給湯利用箇所1に供給する給湯運転と、第2水路W2にてバーナー加熱式熱交換器6にて加熱された水を第1負荷熱交換器7aに供給するバーナー加熱状態での暖房運転とを同時に行うことができる。
(Simultaneous operation of hot water supply operation + heating operation with burner heating)
In the case where the hot water supply operation and the heating operation in the burner heating state are performed simultaneously, water or a heat medium flows as compared with the case where the hot water supply operation and the heating operation in the heat pump heating state shown in FIG. 4 are performed simultaneously. Since the parts are the same and only the states of the burner combustion apparatus N and the heat pump apparatus 4 are different, the description is omitted.
The operation control means 19 switches the heat pump device 4 to the non-operating state, switches the burner combustion device N to the combustion state, operates the circulation pump 3 and the first heat medium circulation pump 15, and outputs from the fourth flow path part R4. The opening / closing operations of the second on-off valve K2 and the third on-off valve K3 are controlled so as to supply water to the first load heat exchanger 7a. Thereby, the operation control means 19 is circulated in the first water channel W1 through the water in the hot water supply tank 2, the burner heating type heat exchanger 6, the first load heat exchanger 7a, and the heat pump heating type heat exchanger 5. In the burner heating state in which the water heated by the burner heating type heat exchanger 6 in the second water passage W2 is supplied to the first load heat exchanger 7a. Heating operation can be performed simultaneously.

(蓄熱運転+ヒートポンプ加熱状態での暖房運転の同時運転)
蓄熱運転とヒートポンプ加熱状態での暖房運転とを同時に行う場合には、運転制御手段19は、図6に示すように、ヒートポンプ装置4を作動状態に切り換え、バーナー燃焼装置Nを非燃焼状態に切り換え、循環ポンプ3及び第1熱媒循環ポンプ15を作動させるとともに、第4流路部位R4からの水を第1負荷熱交換器7aに供給するように第2開閉弁K2及び第3開閉弁K3の開閉動作を制御し、第1開閉弁K1及び第1比例弁H1を開動作させる。これにより、ヒートポンプ加熱式熱交換器5にて加熱された水を給湯タンク2に供給して給湯タンク2への蓄熱を行う蓄熱運転と、ヒートポンプ加熱式熱交換器5にて加熱された水を第1負荷熱交換器7aに供給するヒートポンプ加熱状態での暖房運転とを同時に行うことができる。
(Simultaneous operation of heat storage operation + heating operation in heat pump heating state)
When the heat storage operation and the heating operation in the heat pump heating state are performed simultaneously, the operation control means 19 switches the heat pump device 4 to the operating state and switches the burner combustion device N to the non-burning state as shown in FIG. The second on-off valve K2 and the third on-off valve K3 are operated so that the circulation pump 3 and the first heat medium circulation pump 15 are operated and the water from the fourth flow path part R4 is supplied to the first load heat exchanger 7a. The first on-off valve K1 and the first proportional valve H1 are opened. Thereby, the heat storage operation which supplies the water heated by the heat pump heating type heat exchanger 5 to the hot water supply tank 2 to store heat in the hot water supply tank 2, and the water heated by the heat pump heating type heat exchanger 5 The heating operation in the heat pump heating state supplied to the first load heat exchanger 7a can be performed simultaneously.

(蓄熱運転+バーナー加熱状態での暖房運転の同時運転)
蓄熱運転とバーナー加熱状態での暖房運転とを同時に行う場合には、図6に示した蓄熱運転とヒートポンプ加熱状態での暖房運転とを同時に行う場合と比べて、水や熱媒の通流する部位は同様であり、バーナー燃焼装置N及びヒートポンプ装置4の状態が異なるだけであるので、図示を省略して説明する。
運転制御手段19は、ヒートポンプ装置4を作動状態に切り換え、バーナー燃焼装置Nを燃焼状態に切り換え、循環ポンプ3及び第1熱媒循環ポンプ15を作動させるとともに、第4流路部位R4からの水を第1負荷熱交換器7aに供給するように第2開閉弁K2及び第3開閉弁K3の開閉動作を制御し、第1開閉弁K1及び第1比例弁H1を開動作させる。これにより、ヒートポンプ加熱式熱交換器5にて加熱された水を給湯タンク2に供給して給湯タンク2への蓄熱を行う蓄熱運転と、バーナー加熱式熱交換器6にて加熱された水を第1負荷熱交換器7aに供給するバーナー加熱状態での暖房運転とを同時に行うことができる。
(Simultaneous operation of heat storage operation + heating operation with burner heating)
In the case where the heat storage operation and the heating operation in the burner heating state are performed simultaneously, water or a heat medium flows as compared to the case where the heat storage operation and the heating operation in the heat pump heating state shown in FIG. 6 are performed simultaneously. Since the parts are the same and only the states of the burner combustion apparatus N and the heat pump apparatus 4 are different, the description is omitted.
The operation control means 19 switches the heat pump device 4 to the operating state, switches the burner combustion device N to the combustion state, operates the circulation pump 3 and the first heat medium circulation pump 15, and supplies water from the fourth flow path part R4. Is controlled to open and close the first on-off valve K1 and the first proportional valve H1. Thereby, the heat storage operation which supplies the water heated by the heat pump heating type heat exchanger 5 to the hot water supply tank 2 and stores the heat in the hot water supply tank 2, and the water heated by the burner heating type heat exchanger 6 The heating operation in the burner heating state supplied to the first load heat exchanger 7a can be performed simultaneously.

(給湯運転+追焚運転の同時運転)
給湯運転とヒートポンプ加熱状態での追焚運転とを同時に行う場合は、図4及び図5に示した給湯運転とヒートポンプ加熱状態での暖房運転とを同時に行う場合と比べて、ヒートポンプ加熱式熱交換器5にて加熱した水を第2負荷熱交換器7bに供給する点が異なるだけである。ちなみに、この場合にも、図5に示すように、ヒートポンプ加熱式熱交換器5に供給される水の温度が所定温度(例えば40℃)よりも高くなると、給水手段20が、ヒートポンプ加熱式熱交換器5に供給される水に給水して、ヒートポンプ加熱式熱交換器5に供給される水の温度を所定温度(例えば40℃)以下に調整自在に構成されている。
給湯運転とバーナー加熱状態での追焚運転とを同時に行う場合も、給湯運転とバーナー加熱状態での暖房運転とを同時に行う場合と比べて、バーナー加熱式熱交換器6にて加熱した水を第2負荷熱交換器7bに供給する点が異なるだけである。
(Simultaneous operation of hot water supply operation + memorial operation)
When the hot water supply operation and the chasing operation in the heat pump heating state are performed simultaneously, the heat pump heating type heat exchange is performed as compared with the case where the hot water supply operation and the heating operation in the heat pump heating state illustrated in FIGS. The only difference is that the water heated in the vessel 5 is supplied to the second load heat exchanger 7b. Incidentally, in this case as well, as shown in FIG. 5, when the temperature of the water supplied to the heat pump heating type heat exchanger 5 becomes higher than a predetermined temperature (for example, 40 ° C.), the water supply means 20 The water supplied to the exchanger 5 is supplied with water, and the temperature of the water supplied to the heat pump heating type heat exchanger 5 is adjustable to a predetermined temperature (for example, 40 ° C.) or less.
Even when the hot water supply operation and the chasing operation in the burner heating state are performed simultaneously, the water heated by the burner heating type heat exchanger 6 is compared with the case where the hot water supply operation and the heating operation in the burner heating state are performed simultaneously. The only difference is the supply to the second load heat exchanger 7b.

(蓄熱運転+追焚運転の同時運転)
蓄熱運転とヒートポンプ加熱状態での追焚運転とを同時に行う場合は、図6に示した蓄熱運転とヒートポンプ加熱状態での暖房運転とを同時に行う場合と比べて、ヒートポンプ加熱式熱交換器5にて加熱した水を第2負荷熱交換器7bに供給する点が異なるだけである。
蓄熱運転とバーナー加熱状態での追焚運転とを同時に行う場合も、上述の蓄熱運転とバーナー加熱状態での暖房運転とを同時に行う場合と比べて、バーナー加熱式熱交換器6にて加熱した水を第2負荷熱交換器7bに供給する点が異なるだけである。
(Simultaneous operation of heat storage operation + memorial operation)
When the heat storage operation and the chasing operation in the heat pump heating state are performed simultaneously, the heat pump heating type heat exchanger 5 is compared with the case where the heat storage operation and the heating operation in the heat pump heating state shown in FIG. 6 are performed simultaneously. The only difference is that the heated water is supplied to the second load heat exchanger 7b.
Even in the case where the heat storage operation and the chasing operation in the burner heating state are performed at the same time, compared to the case where the heat storage operation and the heating operation in the burner heating state are performed at the same time, heating is performed by the burner heating type heat exchanger 6. The only difference is that water is supplied to the second load heat exchanger 7b.

本発明に係る熱媒供給装置では、運転制御手段19が、蓄熱運転、給湯運転、バーナー加熱状態での暖房運転、ヒートポンプ加熱状態での暖房運転、バーナー加熱状態での追焚運転、ヒートポンプ加熱状態での追焚運転に加えて、給湯タンク2の水を高温に加熱する高温加熱運転を実行可能に構成されている。   In the heat medium supply device according to the present invention, the operation control means 19 includes a heat storage operation, a hot water supply operation, a heating operation in a burner heating state, a heating operation in a heat pump heating state, a memorial operation in a burner heating state, and a heat pump heating state. In addition to the chasing operation, the high-temperature heating operation for heating the water in the hot water supply tank 2 to a high temperature is executable.

(高温加熱運転)
この高温加熱運転では、図7に示すように、運転制御手段19が、バーナー燃焼装置Nを燃焼状態に切り換え、ヒートポンプ装置4を非作動状態に切り換え、循環ポンプ3を作動させるとともに、第4流路部位R4からの水を第1負荷熱交換器7a及び第2負荷熱交換器7bの両方又は一方に供給するように第2開閉弁K2及び第3開閉弁K3の開閉動作を制御し、第1開閉弁K1及び第1比例弁H1を開動作させる。これにより、第2水路W2と第3水路W3が、給湯タンク2から取り出した水をバーナー加熱式熱交換器6にて加熱し、その加熱された水を給湯タンク2に戻すように水を循環自在に構成されている。したがって、給湯タンク2の水を高温として殺菌消毒することができるので、レジオネラ菌等の繁殖を適切に防止することができる。
(High temperature heating operation)
In this high temperature heating operation, as shown in FIG. 7, the operation control means 19 switches the burner combustion device N to the combustion state, switches the heat pump device 4 to the non-operation state, operates the circulation pump 3, and Controlling the opening / closing operation of the second on-off valve K2 and the third on-off valve K3 so as to supply water from the road part R4 to both or one of the first load heat exchanger 7a and the second load heat exchanger 7b, The 1 on-off valve K1 and the first proportional valve H1 are opened. Accordingly, the second water passage W2 and the third water passage W3 circulate the water so that the water taken out from the hot water supply tank 2 is heated by the burner heating type heat exchanger 6 and the heated water is returned to the hot water supply tank 2. It is configured freely. Therefore, since the water in the hot water supply tank 2 can be sterilized and disinfected at a high temperature, propagation of Legionella bacteria and the like can be appropriately prevented.

〔第2実施形態〕
この第2実施形態では、上記第1実施形態において、図8に示すように、少なくともバーナー加熱式熱交換器6をバイパスして循環ポンプ3の圧力を使わずに上水の圧力で給湯タンク2から取り出した水を給湯利用箇所1に直接供給する第1バイパス水路V1を形成可能に構成されている。
[Second Embodiment]
In the second embodiment, as shown in FIG. 8, in the first embodiment, at least the burner heating type heat exchanger 6 is bypassed and the hot water supply tank 2 is used with the pressure of clean water without using the pressure of the circulation pump 3. It is comprised so that the 1st bypass water channel V1 which supplies the water taken out from the hot water supply location 1 directly can be formed.

この第2実施形態では、上記第1実施形態にて述べた如く、第1〜第7流路部位R1〜R7に加えて、第2流路部位R2における給湯タンク2と第6流路部位R6への接続箇所までの間の部位及び第3流路部位R3における第4流路部位R4への接続箇所と給湯利用箇所1までの間の部位を接続する第1バイパス流路部位B1が備えられている。   In the second embodiment, as described in the first embodiment, in addition to the first to seventh flow path portions R1 to R7, the hot water supply tank 2 and the sixth flow path portion R6 in the second flow path portion R2. And a first bypass flow path part B1 for connecting a part between the connection part to the fourth flow path part R4 in the third flow path part R3 and a part between the hot water supply use part 1 and the third flow path part R3. ing.

上記第1実施形態では、循環ポンプ3を第6流路部位R6に配置していたが、この第2実施形態では、循環ポンプ3を第2流路部位R2に配置している。循環ポンプ3は、第2流路部位R2において第6流路部位R6への接続箇所とバーナー加熱式熱交換器6との間の部位に配置されている。そして、第2流路部位R2において第1バイパス流路部位B1への接続箇所と第6流路部位R6への接続箇所までの間の部位に第2比例弁H2が備えられ、第6流路部位R6の途中部位に第3比例弁H3が備えられている。また、第3流路部位R3において第4流路部位R4への接続箇所と第1バイパス流路部位B1からの接続箇所の間の部位に第4比例弁H4が備えられている。さらに、上記第1実施形態では、第7流路部位R7に第1比例弁H1が備えられていたが、この第1比例弁H1が省略され、第1流路部位R1と第7流路部位R7との接続箇所に第1切換弁S1が備えられている。   In the said 1st Embodiment, although the circulation pump 3 was arrange | positioned in 6th flow-path part R6, in this 2nd Embodiment, the circulation pump 3 is arrange | positioned in 2nd flow-path part R2. The circulation pump 3 is disposed in a portion between the connection portion to the sixth flow passage portion R6 and the burner heating heat exchanger 6 in the second flow passage portion R2. A second proportional valve H2 is provided in a portion between the connection location to the first bypass flow passage portion B1 and the connection location to the sixth flow passage portion R6 in the second flow passage portion R2, and the sixth flow passage is provided. A third proportional valve H3 is provided in the middle of the part R6. In addition, a fourth proportional valve H4 is provided in a portion between the connection portion to the fourth flow passage portion R4 and the connection portion from the first bypass flow passage portion B1 in the third flow passage portion R3. Further, in the first embodiment, the first proportional valve H1 is provided in the seventh flow path part R7. However, the first proportional valve H1 is omitted, and the first flow path part R1 and the seventh flow path part. The 1st switching valve S1 is provided in the connection location with R7.

この第2実施形態では、上述の如く、図8に示すように、第1バイパス水路V1が備えられているが、上記第1実施形態と同様に、第1水路W1(図9参照)、第2水路W2(図10参照)、第3水路W3(図11参照)が備えられている。第1バイパス水路V1は、図8に示すように、第1流路部位R1と給湯タンク2と第2流路部位R2の一部と第1バイパス流路部位B1と第3流路部位R3の一部とから構成されている。第1水路W1は、図9に示すように、第1流路部位R1、給湯タンク2、第2流路部位R2、バーナー加熱式熱交換器6、第3流路部位R3から構成されている。第2水路W2は、図10に示すように、バーナー加熱式熱交換器6と第3流路部位R3の一部と第4流路部位R4と負荷熱交換器7と第5流路部位R5とヒートポンプ加熱式熱交換器5と第6流路部位R6と第2流路部位R2の一部とから構成されている。第3水路W3は、図11に示すように、給湯タンク2、第1流路部位R1の一部、第7流路部位R7、第5流路部位R5の一部、ヒートポンプ加熱式熱交換器5、第6流路部位R6,第2流路部位R2、バーナー加熱式熱交換器6、第3流路部位R3の一部、及び、第1バイパス流路部位B1から構成されている。これにより、第3水路W3は、図8に示す第1バイパス水路V1における第1流路部位R1の一部、第2流路部位R2の一部及び第1バイパス流路部位B1を含んでいるので、第3水路W3は、少なくとも第1バイパス水路V1の一部から構成されている。   In the second embodiment, as described above, the first bypass water channel V1 is provided as shown in FIG. 8, but, as in the first embodiment, the first water channel W1 (see FIG. 9), A two water channel W2 (see FIG. 10) and a third water channel W3 (see FIG. 11) are provided. As shown in FIG. 8, the first bypass water channel V1 includes a first flow path part R1, a hot water supply tank 2, a part of the second flow path part R2, a first bypass flow path part B1, and a third flow path part R3. It consists of a part. As shown in FIG. 9, the first water channel W1 includes a first flow path part R1, a hot water supply tank 2, a second flow path part R2, a burner heating type heat exchanger 6, and a third flow path part R3. . As shown in FIG. 10, the second water channel W2 includes the burner heating type heat exchanger 6, a part of the third flow path part R3, the fourth flow path part R4, the load heat exchanger 7, and the fifth flow path part R5. And a heat pump heating type heat exchanger 5, a sixth flow path part R6, and a part of the second flow path part R2. As shown in FIG. 11, the third water channel W3 includes a hot water tank 2, a part of the first flow path part R1, a seventh flow path part R7, a part of the fifth flow path part R5, a heat pump heating type heat exchanger. 5, the sixth flow path part R6, the second flow path part R2, the burner heating type heat exchanger 6, a part of the third flow path part R3, and the first bypass flow path part B1. Accordingly, the third water channel W3 includes a part of the first flow path part R1, a part of the second flow path part R2, and the first bypass flow path part B1 in the first bypass water path V1 shown in FIG. Therefore, the 3rd waterway W3 is comprised from a part of 1st bypass waterway V1 at least.

この第2実施形態においても、運転制御手段19は、上記第1実施形態と同様に、蓄熱運転、給湯運転、暖房運転、追焚運転、及び、高温加熱運転を実行可能であるので、図8〜図11に基づいて、各運転について説明する。   Also in the second embodiment, since the operation control means 19 can execute the heat storage operation, the hot water supply operation, the heating operation, the memorial operation, and the high temperature heating operation as in the first embodiment, FIG. Each operation will be described with reference to FIG.

(蓄熱運転)
運転制御手段19は、図11に示すように、ヒートポンプ装置4を作動状態に切り換え、バーナー燃焼装置Nを非燃焼状態に切り換え、循環ポンプ3を作動させるとともに、給湯タンク2から第1流路部位R1に取り出した水を第7流路部位R7に供給する状態に第1切換弁S1を切り換え、第2比例弁H2、第3比例弁H3、及び、第4比例弁H4を開動作させる。運転制御手段19は、第3水路W3によって、循環ポンプ3の圧力で、給湯タンク2の下部から水を第1流路部位R1に取り出し、その取り出した水を第7流路部位R7及び第5流路部位R5を経由してヒートポンプ加熱式熱交換器5に供給して加熱し、その加熱された水を第6流路部位R6、第2流路部位R2、バーナー加熱式熱交換器6、第3流路部位R3、第1バイパス流路部位B1、第2流路部位R2を経由して給湯タンク2の上部に戻している。第1バイパス流路部位B1を経由した水は、その一部が第2流路部位R2を経由して給湯タンク2の上部に供給され、残りの一部が第2流路部位R2を経由してバーナー加熱式熱交換器6に供給されている。このようにして、給湯タンク2から取り出された水がヒートポンプ加熱式熱交換器5にて加熱されて温水となり、その温水が給湯タンク2に戻されて、給湯タンク2に蓄熱している。ここで、運転制御手段19は、給湯タンク2の上部に戻す温水の温度が所定温度になるように、循環ポンプ3の回転速度及び第3比例弁H3の開度を調整してヒートポンプ加熱式熱交換器5に供給する水の供給量を調整している。
(Heat storage operation)
As shown in FIG. 11, the operation control means 19 switches the heat pump device 4 to the operating state, switches the burner combustion device N to the non-combusting state, operates the circulation pump 3, and connects the hot water supply tank 2 to the first flow path portion. The first switching valve S1 is switched to a state in which the water taken out to R1 is supplied to the seventh flow path part R7, and the second proportional valve H2, the third proportional valve H3, and the fourth proportional valve H4 are opened. The operation control means 19 takes out water from the lower part of the hot water supply tank 2 to the first flow path part R1 by the pressure of the circulation pump 3 through the third water channel W3, and extracts the extracted water from the seventh flow path part R7 and the fifth flow path R5. The heat pump heating type heat exchanger 5 is supplied to the heat pump heating type heat exchanger 5 through the flow path part R5 and heated, and the heated water is supplied to the sixth flow path part R6, the second flow path part R2, the burner heating type heat exchanger 6, It is returned to the upper part of the hot water supply tank 2 via the third flow path part R3, the first bypass flow path part B1, and the second flow path part R2. A part of the water that has passed through the first bypass flow path part B1 is supplied to the upper part of the hot water tank 2 via the second flow path part R2, and the remaining part of the water passes through the second flow path part R2. The burner heating type heat exchanger 6 is supplied. In this way, the water taken out from the hot water supply tank 2 is heated by the heat pump heating type heat exchanger 5 to become hot water, and the hot water is returned to the hot water supply tank 2 to store heat in the hot water supply tank 2. Here, the operation control means 19 adjusts the rotational speed of the circulation pump 3 and the opening of the third proportional valve H3 so that the temperature of the hot water returned to the upper part of the hot water supply tank 2 becomes a predetermined temperature, and heat pump heating type heat The amount of water supplied to the exchanger 5 is adjusted.

(給湯運転)
この給湯運転では、運転制御手段19が、図8に示すように、バーナー加熱式熱交換器6をバイパスして循環ポンプ3の圧力を使わずに上水の圧力で給湯タンク2から取り出した水を給湯利用箇所1に直接供給するバイパス状態と、図9に示すように、上水の圧力に加えて循環ポンプ3の圧力で給湯タンク2から取り出した水をバーナー加熱式熱交換器6を経由して給湯利用箇所1に供給する非バイパス状態とに切換自在に構成されている。そして、運転制御手段19は、給湯タンク2の水の温度が給湯利用箇所1にて要求されている給湯設定温度と同等の温度又はその給湯設定温度よりも所定温度だけ高い温度に設定された切換設定温度以上であると、バイパス状態に切り換え、給湯タンク2の水の温度が切換設定温度未満であると、非バイパス状態に切り換える。ここで、給湯タンク2の水の温度については、図示を省略するが、給湯タンク2における上方側部位における水の温度を検出する温度センサが備えられ、その温度センサの検出温度を給湯タンク2の水の温度としている。
(Hot water operation)
In this hot water supply operation, as shown in FIG. 8, the operation control means 19 bypasses the burner heating type heat exchanger 6, and the water taken out from the hot water supply tank 2 with the pressure of clean water without using the pressure of the circulation pump 3. As shown in FIG. 9, the water taken out from the hot water tank 2 by the pressure of the circulating pump 3 in addition to the pressure of the clean water passes through the burner heating type heat exchanger 6. Thus, it is configured to be switchable to a non-bypass state to be supplied to the hot water supply utilization location 1. Then, the operation control means 19 switches the temperature of the water in the hot water supply tank 2 to a temperature equivalent to the hot water supply set temperature required at the hot water use location 1 or a temperature higher than the hot water set temperature by a predetermined temperature. When the temperature is higher than the set temperature, the state is switched to the bypass state. When the temperature of the water in the hot water supply tank 2 is lower than the switch set temperature, the state is switched to the non-bypass state. Here, although the illustration of the temperature of the water in the hot water supply tank 2 is omitted, a temperature sensor for detecting the temperature of the water in the upper portion of the hot water supply tank 2 is provided. The water temperature.

バイパス状態に切り換える場合には、図8に示すように、運転制御手段19が、第2比例弁H2及び第4比例弁H4を閉動作させたままとしており、第1バイパス水路V1によって、上水の圧力で給湯タンク2から取り出した水をバーナー加熱式熱交換器6をバイパスして給湯利用箇所1に供給している。
非バイパス状態に切り換える場合には、図9に示すように、運転制御手段19が、第2比例弁H2及び第4比例弁H4を開動作させるとともに、循環ポンプ3を作動させて、給湯タンク2から取り出した水を、循環ポンプ3の圧力で第2流路部位R2にてバーナー加熱式熱交換器6に供給し、そのバーナー加熱式熱交換器6を経由した水を給湯利用箇所1に供給している。
When switching to the bypass state, as shown in FIG. 8, the operation control means 19 keeps the second proportional valve H2 and the fourth proportional valve H4 closed, and the first bypass water channel V1 causes the The water taken out from the hot water supply tank 2 at a pressure of 2 is supplied to the hot water supply use location 1 by bypassing the burner heating type heat exchanger 6.
In the case of switching to the non-bypass state, as shown in FIG. 9, the operation control means 19 opens the second proportional valve H2 and the fourth proportional valve H4 and activates the circulation pump 3 so that the hot water supply tank 2 The water taken out from the water is supplied to the burner heating type heat exchanger 6 at the second flow path part R2 by the pressure of the circulation pump 3, and the water passing through the burner heating type heat exchanger 6 is supplied to the hot water supply use point 1. is doing.

(暖房運転)
運転制御手段19は、図10に示すように、循環ポンプ3を作動させるとともに、第4流路部位R4からの水を第1負荷熱交換器7aに供給するように第2開閉弁K2及び第3開閉弁K3の開閉動作を制御し、第2比例弁H2及び第4比例弁H4を閉動作させたままとし、第3比例弁H3を開動作させる。これにより、第2水路W2によって、循環ポンプ3の圧力でバーナー加熱式熱交換器6と第1負荷熱交換器7aとヒートポンプ加熱式熱交換器5を経由して水を循環させている。そして、上記第1実施形態と同様に、運転制御手段19は、第2水路W2にて水を循環させている状態で、バーナー燃焼装置Nを燃焼状態と非燃焼状態とに切り換えるとともに、ヒートポンプ装置4を作動状態と非作動状態とに切り換えることで、バーナー加熱状態とヒートポンプ加熱状態とに切換自在に構成されており、第1負荷熱交換器7aで要求されている熱負荷に対して、バーナー加熱状態に切り換えた場合とヒートポンプ加熱状態に切り換えた場合との夫々の1次エネルギー消費量を求め、その求めた1次エネルギー消費量が小さい方に切り換えている。
(Heating operation)
As shown in FIG. 10, the operation control means 19 operates the circulation pump 3 and supplies the second on-off valve K2 and the second valve so as to supply water from the fourth flow path portion R4 to the first load heat exchanger 7a. The opening / closing operation of the third opening / closing valve K3 is controlled, the second proportional valve H2 and the fourth proportional valve H4 are kept closed, and the third proportional valve H3 is opened. Thereby, the water is circulated by the pressure of the circulation pump 3 through the burner heating type heat exchanger 6, the first load heat exchanger 7a, and the heat pump heating type heat exchanger 5 by the second water passage W2. As in the first embodiment, the operation control means 19 switches the burner combustion device N between the combustion state and the non-combustion state in a state where water is circulated in the second water passage W2, and the heat pump device. 4 can be switched between a burner heating state and a heat pump heating state by switching between an operating state and a non-operating state, and with respect to the thermal load required by the first load heat exchanger 7a, The primary energy consumption amount in each of the case of switching to the heating state and the case of switching to the heat pump heating state is obtained, and the obtained primary energy consumption amount is switched to the smaller one.

ヒートポンプ加熱状態に切り換える場合には、図10に示すように、運転制御手段19が、バーナー燃焼装置Nを非燃焼状態に切り換えるとともに、ヒートポンプ装置4を作動状態に切り換え、第1熱媒循環ポンプ15を作動させる。これにより、ヒートポンプ加熱式熱交換器5にて水が加熱されて温水となり、その温水が第6流路部位R6、第2流路部位R2、バーナー加熱式熱交換器6、第3流路部位R3、及び、第4流路部位R4を経由して第1負荷熱交換器7aに供給されて第1熱媒循環路13の熱媒を加熱する。このとき、バーナー燃焼装置Nを非燃焼状態に切り換えているので、バーナー加熱式熱交換器6では水が加熱されない。第1負荷熱交換器7aにおいて加熱された熱媒は、第1熱媒循環路13にて暖房端末12に供給されて暖房端末12での暖房を行う。   In the case of switching to the heat pump heating state, as shown in FIG. 10, the operation control means 19 switches the burner combustion device N to the non-burning state, switches the heat pump device 4 to the operating state, and the first heat medium circulation pump 15. Is activated. Thereby, water is heated in the heat pump heating type heat exchanger 5 to become warm water, and the warm water is the sixth flow path part R6, the second flow path part R2, the burner heating type heat exchanger 6, the third flow path part. The heat medium in the first heat medium circulation path 13 is heated by being supplied to the first load heat exchanger 7a via R3 and the fourth flow path part R4. At this time, since the burner combustion apparatus N is switched to the non-burning state, the burner heating heat exchanger 6 does not heat water. The heat medium heated in the first load heat exchanger 7 a is supplied to the heating terminal 12 through the first heat medium circulation path 13 and is heated in the heating terminal 12.

一方、バーナー加熱状態に切り換える場合には、図10に示したヒートポンプ加熱状態に切り換える場合と比べて、水や熱媒の通流する部位は同様であり、バーナー燃焼装置N及びヒートポンプ装置4の状態が異なるだけであるので、図示を省略して説明する。
運転制御手段19は、バーナー燃焼装置Nを燃焼状態に切り換えるとともに、ヒートポンプ装置4を非作動状態に切り換え、第1熱媒循環ポンプ15を作動させる。これにより、バーナー加熱式熱交換器6にて水が加熱されて温水となり、その温水が第3流路部位R3及び第4流路部位R4を経由して第1負荷熱交換器7aに供給されて第1熱媒循環路13の熱媒を加熱する。このとき、ヒートポンプ装置4を非作動状態に切り換えているので、ヒートポンプ加熱式熱交換器5では水が加熱されない。第1負荷熱交換器7aにおいて加熱された熱媒は、第1熱媒循環路13により暖房端末12に供給されて暖房端末12での暖房を行う。
On the other hand, in the case of switching to the burner heating state, compared with the case of switching to the heat pump heating state shown in FIG. 10, the parts through which water and heat medium flow are the same, and the states of the burner combustion device N and the heat pump device 4 are the same. Are different from each other, and the illustration is omitted.
The operation control means 19 switches the burner combustion device N to the combustion state, switches the heat pump device 4 to the non-operation state, and operates the first heat medium circulation pump 15. Thereby, water is heated in the burner heating type heat exchanger 6 to become warm water, and the warm water is supplied to the first load heat exchanger 7a via the third flow path part R3 and the fourth flow path part R4. The heating medium in the first heating medium circulation path 13 is heated. At this time, since the heat pump device 4 is switched to the non-operating state, water is not heated in the heat pump heating type heat exchanger 5. The heat medium heated in the first load heat exchanger 7 a is supplied to the heating terminal 12 by the first heat medium circulation path 13 and is heated in the heating terminal 12.

(追焚運転)
上記第1実施形態と同様に、この追焚運転では、運転制御手段19が、第4流路部位R4からの水を第2負荷熱交換器7bに供給するように第2開閉弁K2及び第3開閉弁K3の開閉動作を制御している点が上述の暖房運転と異なるだけであるので、説明は省略する。
(Memorial operation)
As in the first embodiment, in the chasing operation, the operation control means 19 supplies the second on-off valve K2 and the second valve so as to supply water from the fourth flow path portion R4 to the second load heat exchanger 7b. Since the point which controls the opening / closing operation | movement of 3 on-off valve K3 is only different from the above-mentioned heating operation, description is abbreviate | omitted.

(バイパス状態での給湯運転+ヒートポンプ加熱状態での暖房運転の同時運転)
バイパス状態での給湯運転とヒートポンプ加熱状態での暖房運転とを同時に行う場合には、図12に示すように、運転制御手段19は、ヒートポンプ装置4を作動状態に切り換え、バーナー燃焼装置Nを非燃焼状態に切り換え、循環ポンプ3及び第1熱媒循環ポンプ15を作動させるとともに、第4流路部位R4からの水を第1負荷熱交換器7aに供給するように第2開閉弁K2及び第3開閉弁K3の開閉動作を制御し、第1流路部位R1にてそのまま給湯タンク2に給水する状態に第1切換弁S1を切り換え、第2比例弁H2及び第4比例弁H4を閉動作させたままとし、第3比例弁H3を開動作させる。これにより、運転制御手段19は、第1バイパス水路V1にて給湯タンク2の水をバーナー加熱式熱交換器6をバイパスして給湯利用箇所1に供給する給湯運転と、第2水路W2にてヒートポンプ加熱式熱交換器5にて加熱された水を第1負荷熱交換器7aに供給するヒートポンプ加熱状態での暖房運転とを同時に行うことができる。この場合、第1バイパス水路V1と第2水路W2とは独立して水を通流自在に構成されており、第1バイパス水路V1による給湯利用箇所1への水の供給と第2水路W2によるヒートポンプ加熱式熱交換器5にて加熱された水の第1負荷熱交換器7aへの供給とを、お互いに干渉することなく同時に行うことができる。
(Simultaneous operation of hot water supply operation in bypass state + heating operation in heat pump heating state)
When the hot water supply operation in the bypass state and the heating operation in the heat pump heating state are performed simultaneously, as shown in FIG. 12, the operation control means 19 switches the heat pump device 4 to the operating state and turns off the burner combustion device N. Switching to the combustion state, operating the circulation pump 3 and the first heat medium circulation pump 15, and supplying the second on-off valve K2 and the second so as to supply water from the fourth flow path part R4 to the first load heat exchanger 7a. The opening / closing operation of the 3 opening / closing valve K3 is controlled, the first switching valve S1 is switched to the state where the hot water supply tank 2 is directly supplied with water in the first flow path part R1, and the second proportional valve H2 and the fourth proportional valve H4 are closed. Then, the third proportional valve H3 is opened. As a result, the operation control means 19 uses the hot water supply operation in which the water in the hot water supply tank 2 is bypassed the burner heating type heat exchanger 6 and supplied to the hot water use location 1 in the first bypass water channel V1, and in the second water channel W2. The heating operation in the heat pump heating state in which the water heated by the heat pump heating type heat exchanger 5 is supplied to the first load heat exchanger 7a can be performed simultaneously. In this case, the 1st bypass water channel V1 and the 2nd water channel W2 are constituted so that water can flow independently, and the supply of water to the hot water supply use location 1 by the first bypass water channel V1 and the second water channel W2 Supply of the water heated by the heat pump heating type heat exchanger 5 to the first load heat exchanger 7a can be performed simultaneously without interfering with each other.

(バイパス状態での給湯運転+バーナー加熱状態での暖房運転の同時運転)
バイパス状態での給湯運転とバーナー加熱状態での暖房運転とを同時に行う場合には、図12に示したバイパス状態での給湯運転とヒートポンプ加熱状態での暖房運転とを同時に行う場合と比べて、水や熱媒の通流する部位は同様であり、バーナー燃焼装置N及びヒートポンプ装置4の状態が異なるだけであるので、図示を省略して説明する。
運転制御手段19は、ヒートポンプ装置4を非作動状態に切り換え、バーナー燃焼装置Nを燃焼状態に切り換え、循環ポンプ3及び第1熱媒循環ポンプ15を作動させるとともに、第4流路部位R4からの水を第1負荷熱交換器7aに供給するように第2開閉弁K2及び第3開閉弁K3の開閉動作を制御している。これにより、運転制御手段19は、第1バイパス水路V1にて給湯タンク2の水をバーナー加熱式熱交換器6をバイパスして給湯利用箇所1に供給する給湯運転と、第2水路W2にてバーナー加熱式熱交換器6にて加熱された水を第1負荷熱交換器7aに供給するバーナー加熱状態での暖房運転とを同時に行うことができる。
(Simultaneous operation of hot water supply operation in bypass state + heating operation in burner heating state)
In the case where the hot water supply operation in the bypass state and the heating operation in the burner heating state are performed simultaneously, compared to the case where the hot water supply operation in the bypass state and the heating operation in the heat pump heating state shown in FIG. The parts through which water and the heat medium flow are the same, and only the states of the burner combustion apparatus N and the heat pump apparatus 4 are different.
The operation control means 19 switches the heat pump device 4 to the non-operating state, switches the burner combustion device N to the combustion state, operates the circulation pump 3 and the first heat medium circulation pump 15, and outputs from the fourth flow path part R4. The opening / closing operations of the second on-off valve K2 and the third on-off valve K3 are controlled so as to supply water to the first load heat exchanger 7a. As a result, the operation control means 19 uses the hot water supply operation in which the water in the hot water supply tank 2 is bypassed the burner heating type heat exchanger 6 and supplied to the hot water use location 1 in the first bypass water channel V1, and in the second water channel W2. The heating operation in the burner heating state in which the water heated by the burner heating type heat exchanger 6 is supplied to the first load heat exchanger 7a can be performed simultaneously.

(非バイパス状態での給湯運転+ヒートポンプ加熱状態での暖房運転の同時運転)
非バイパス状態での給湯運転とヒートポンプ加熱状態での暖房運転とを同時に行う場合には、図13に示すように、運転制御手段19は、ヒートポンプ装置4を作動状態に切り換え、バーナー燃焼装置Nを燃焼状態に切り換え、循環ポンプ3及び第1熱媒循環ポンプ15を作動させるとともに、第4流路部位R4からの水を第1負荷熱交換器7aに供給するように第2開閉弁K2及び第3開閉弁K3の開閉動作を制御し、第1流路部位R1にてそのまま給湯タンク2に給水する状態に第1切換弁S1を切り換え、第2比例弁H2、第3比例弁H3及び第4比例弁H4を開動作させる。これにより、運転制御手段19は、第1水路W1にて給湯タンク2の水をバーナー加熱式熱交換器6を経由して給湯利用箇所1に供給する給湯運転と、第2水路W2にてヒートポンプ加熱式熱交換器5にて加熱された水を第1負荷熱交換器7aに供給するヒートポンプ加熱状態での暖房運転とを同時に行うことができる。
(Simultaneous operation of hot water supply operation in non-bypass state + heating operation in heat pump heating state)
When the hot water supply operation in the non-bypass state and the heating operation in the heat pump heating state are performed simultaneously, as shown in FIG. 13, the operation control means 19 switches the heat pump device 4 to the operating state and turns the burner combustion device N on. Switching to the combustion state, operating the circulation pump 3 and the first heat medium circulation pump 15, and supplying the second on-off valve K2 and the second so as to supply water from the fourth flow path part R4 to the first load heat exchanger 7a. The opening / closing operation of the 3 on-off valve K3 is controlled, the first switching valve S1 is switched to the state where the hot water tank 2 is directly supplied with water in the first flow path part R1, the second proportional valve H2, the third proportional valve H3 and the fourth The proportional valve H4 is opened. Thereby, the operation control means 19 includes a hot water supply operation in which the water in the hot water supply tank 2 is supplied to the hot water supply use location 1 via the burner heating type heat exchanger 6 in the first water channel W1, and a heat pump in the second water channel W2. The heating operation in the heat pump heating state in which the water heated in the heating heat exchanger 5 is supplied to the first load heat exchanger 7a can be performed simultaneously.

非バイパス状態での給湯運転とヒートポンプ加熱状態での暖房運転とを同時に行っている場合には、ヒートポンプ加熱式熱交換器5に供給される水の温度が徐々に上昇していき、ヒートポンプ加熱式熱交換器5に供給される水の温度が所定温度(例えば40℃)よりも高くなる場合がある。そこで、上記第1実施形態と同様に、図14に示すように、給湯利用箇所1に水を供給する給湯運転を行っており、ヒートポンプ装置4を作動状態に切り換えている場合に、ヒートポンプ加熱式熱交換器5に供給される水の温度が所定温度(例えば40℃)よりも高くなると、ヒートポンプ加熱式熱交換器5に供給される水に給水して、ヒートポンプ加熱式熱交換器5に供給される水の温度を所定温度(例えば40℃)以下に調整自在な給水手段20が備えられている。つまり、ヒートポンプ加熱式熱交換器5に供給される水の温度が所定温度(例えば40℃)よりも高くなると、運転制御手段19は、第1流路部位R1の水を第7流路部位R7に供給する状態に第1切換弁S1を切り換え、ヒートポンプ加熱式熱交換器5に供給される水の温度が所定温度(例えば40℃)以下となるように、第3比例弁H3の開度を調整している。   When the hot water supply operation in the non-bypass state and the heating operation in the heat pump heating state are performed simultaneously, the temperature of the water supplied to the heat pump heating type heat exchanger 5 gradually increases, and the heat pump heating type The temperature of the water supplied to the heat exchanger 5 may be higher than a predetermined temperature (for example, 40 ° C.). Therefore, as in the first embodiment, as shown in FIG. 14, when a hot water supply operation for supplying water to the hot water supply use location 1 is performed and the heat pump device 4 is switched to the operating state, the heat pump heating type When the temperature of the water supplied to the heat exchanger 5 becomes higher than a predetermined temperature (for example, 40 ° C.), the water supplied to the heat pump heating type heat exchanger 5 is supplied and supplied to the heat pump heating type heat exchanger 5. A water supply means 20 is provided that can adjust the temperature of the water to be adjusted to a predetermined temperature (for example, 40 ° C.) or less. That is, when the temperature of the water supplied to the heat pump heating type heat exchanger 5 becomes higher than a predetermined temperature (for example, 40 ° C.), the operation control means 19 supplies the water in the first flow path part R1 to the seventh flow path part R7. The first switching valve S1 is switched to the state of supplying to the heat pump, and the opening of the third proportional valve H3 is set so that the temperature of the water supplied to the heat pump heating type heat exchanger 5 becomes a predetermined temperature (for example, 40 ° C.) or less. It is adjusted.

(非バイパス状態での給湯運転+バーナー加熱状態での暖房運転の同時運転)
非バイパス状態での給湯運転とバーナー加熱状態での暖房運転とを同時に行う場合には、図13に示した非バイパス状態での給湯運転とヒートポンプ加熱状態での暖房運転とを同時に行う場合と比べて、水や熱媒の通流する部位は同様であり、バーナー燃焼装置N及びヒートポンプ装置4の状態が異なるだけであるので、図示を省略して説明する。
運転制御手段19は、ヒートポンプ装置4を非作動状態に切り換え、バーナー燃焼装置Nを燃焼状態に切り換え、循環ポンプ3及び第1熱媒循環ポンプ15を作動させるとともに、第4流路部位R4からの水を第1負荷熱交換器7aに供給するように第2開閉弁K2及び第3開閉弁K3の開閉動作を制御している。これにより、運転制御手段19は、第1水路W1にて給湯タンク2の水をバーナー加熱式熱交換器6を経由して給湯利用箇所1に供給する給湯運転と、第2水路W2にてバーナー加熱式熱交換器6にて加熱された水を第1負荷熱交換器7aに供給するバーナー加熱状態での暖房運転とを同時に行うことができる。
(Simultaneous operation of hot water supply operation in non-bypass state + heating operation in burner heating state)
Compared to the case where the hot water supply operation in the non-bypass state and the heating operation in the burner heating state are performed simultaneously, compared to the case where the hot water supply operation in the non-bypass state and the heating operation in the heat pump heating state shown in FIG. The parts through which water and the heat medium flow are the same, and only the states of the burner combustion device N and the heat pump device 4 are different.
The operation control means 19 switches the heat pump device 4 to the non-operating state, switches the burner combustion device N to the combustion state, operates the circulation pump 3 and the first heat medium circulation pump 15, and outputs from the fourth flow path part R4. The opening / closing operations of the second on-off valve K2 and the third on-off valve K3 are controlled so as to supply water to the first load heat exchanger 7a. As a result, the operation control means 19 uses the hot water supply operation in which the water in the hot water supply tank 2 is supplied to the hot water use location 1 via the burner heating heat exchanger 6 in the first water channel W1, and the burner in the second water channel W2. The heating operation in the burner heating state in which the water heated by the heating heat exchanger 6 is supplied to the first load heat exchanger 7a can be performed simultaneously.

(蓄熱運転+ヒートポンプ加熱状態での暖房運転の同時運転)
蓄熱運転とヒートポンプ加熱状態での暖房運転とを同時に行う場合には、運転制御手段19は、図15に示すように、ヒートポンプ装置4を作動状態に切り換え、バーナー燃焼装置Nを非燃焼状態に切り換え、循環ポンプ3及び第1熱媒循環ポンプ15を作動させるとともに、第4流路部位R4からの水を第1負荷熱交換器7aに供給するように第2開閉弁K2及び第3開閉弁K3の開閉動作を制御し、給湯タンク2から第1流路部位R1に取り出した水を第7流路部位R7に供給する状態に第1切換弁S1を切り換え、第2比例弁H2、第3比例弁H3、及び、第4比例弁H4を開動作させる。これにより、ヒートポンプ加熱式熱交換器5にて加熱された水を給湯タンク2に供給して給湯タンク2への蓄熱を行う蓄熱運転と、ヒートポンプ加熱式熱交換器5にて加熱された水を第1負荷熱交換器7aに供給するヒートポンプ加熱状態での暖房運転とを同時に行うことができる。また、この場合、運転制御手段19は、第2比例弁H2について、第2比例弁H2を開動作させるのではなく、第2比例弁H2を閉動作させたままとしてもよい。
(Simultaneous operation of heat storage operation + heating operation in heat pump heating state)
When simultaneously performing the heat storage operation and the heating operation in the heat pump heating state, the operation control means 19 switches the heat pump device 4 to the operating state and switches the burner combustion device N to the non-burning state, as shown in FIG. The second on-off valve K2 and the third on-off valve K3 are operated so that the circulation pump 3 and the first heat medium circulation pump 15 are operated and the water from the fourth flow path part R4 is supplied to the first load heat exchanger 7a. The first switching valve S1 is switched to a state in which water taken out from the hot water supply tank 2 to the first flow path part R1 is supplied to the seventh flow path part R7, and the second proportional valve H2 and the third proportional valve are controlled. The valve H3 and the fourth proportional valve H4 are opened. Thereby, the heat storage operation which supplies the water heated by the heat pump heating type heat exchanger 5 to the hot water supply tank 2 to store heat in the hot water supply tank 2, and the water heated by the heat pump heating type heat exchanger 5 The heating operation in the heat pump heating state supplied to the first load heat exchanger 7a can be performed simultaneously. In this case, the operation control means 19 may keep the second proportional valve H2 closed for the second proportional valve H2 instead of opening the second proportional valve H2.

(蓄熱運転+バーナー加熱状態での暖房運転の同時運転)
蓄熱運転とバーナー加熱状態での暖房運転とを同時に行う場合には、図15に示す蓄熱運転とヒートポンプ加熱状態での暖房運転とを同時に行う場合と比べて、水や熱媒の通流する部位は同様であり、バーナー燃焼装置N及びヒートポンプ装置4の状態が異なるだけであるので、図示を省略して説明する。
運転制御手段19は、ヒートポンプ装置4を作動状態に切り換え、バーナー燃焼装置Nを燃焼状態に切り換え、循環ポンプ3及び第1熱媒循環ポンプ15を作動させるとともに、第4流路部位R4からの水を第1負荷熱交換器7aに供給するように第2開閉弁K2及び第3開閉弁K3の開閉動作を制御し、給湯タンク2から第1流路部位R1に取り出した水を第7流路部位R7に供給する状態に第1切換弁S1を切り換え、第2比例弁H2、第3比例弁H3、及び、第4比例弁H4を開動作させる。これにより、ヒートポンプ加熱式熱交換器5にて加熱された水を給湯タンク2に供給して給湯タンク2への蓄熱を行う蓄熱運転と、バーナー加熱式熱交換器6にて加熱された水を第1負荷熱交換器7aに供給するバーナー加熱状態での暖房運転とを同時に行うことができる。
(Simultaneous operation of heat storage operation + heating operation with burner heating)
In the case where the heat storage operation and the heating operation in the burner heating state are performed at the same time, compared with the case where the heat storage operation and the heating operation in the heat pump heating state shown in FIG. Are the same, and only the states of the burner combustion apparatus N and the heat pump apparatus 4 are different, so that the illustration is omitted.
The operation control means 19 switches the heat pump device 4 to the operating state, switches the burner combustion device N to the combustion state, operates the circulation pump 3 and the first heat medium circulation pump 15, and supplies water from the fourth flow path part R4. Is controlled to open and close the second on-off valve K2 and the third on-off valve K3 so that the water taken out from the hot water tank 2 to the first flow path part R1 is supplied to the seventh flow path 7a. The first switching valve S1 is switched to the state to be supplied to the part R7, and the second proportional valve H2, the third proportional valve H3, and the fourth proportional valve H4 are opened. Thereby, the heat storage operation which supplies the water heated by the heat pump heating type heat exchanger 5 to the hot water supply tank 2 and stores the heat in the hot water supply tank 2, and the water heated by the burner heating type heat exchanger 6 The heating operation in the burner heating state supplied to the first load heat exchanger 7a can be performed simultaneously.

(給湯運転+追焚運転の同時運転)
バイパス状態での給湯運転とヒートポンプ加熱状態での追焚運転とを同時に行う場合は、図12に示すバイパス状態での給湯運転とヒートポンプ加熱状態での暖房運転とを同時に行う場合と比べて、ヒートポンプ加熱式熱交換器5にて加熱した水を第2負荷熱交換器7bに供給する点が異なるだけである。
非バイパス状態での給湯運転とヒートポンプ加熱状態での追焚運転とを同時に行う場合は、図13及び図14に示す非バイパス状態での給湯運転とヒートポンプ加熱状態での暖房運転とを同時に行う場合と比べて、ヒートポンプ加熱式熱交換器5にて加熱した水を第2負荷熱交換器7bに供給する点が異なるだけである。ちなみに、この場合にも、図14に示すように、ヒートポンプ加熱式熱交換器5に供給される水の温度が所定温度(例えば40℃)よりも高くなると、給水手段20が、ヒートポンプ加熱式熱交換器5に供給される水に給水して、ヒートポンプ加熱式熱交換器5に供給される水の温度を所定温度(例えば40℃)以下に調整自在に構成されている。
バイパス状態での給湯運転とバーナー加熱状態での追焚運転とを同時に行う場合も、バイパス状態での給湯運転とバーナー加熱状態での暖房運転とを同時に行う場合と比べて、バーナー加熱式熱交換器6にて加熱した水を第2負荷熱交換器7bに供給する点が異なるだけである。
非バイパス状態での給湯運転とバーナー加熱状態での追焚運転とを同時に行う場合も、非バイパス状態での給湯運転とバーナー加熱状態での暖房運転とを同時に行う場合と比べて、バーナー加熱式熱交換器6にて加熱した水を第2負荷熱交換器7bに供給する点が異なるだけである。
(Simultaneous operation of hot water supply operation + memorial operation)
When the hot water supply operation in the bypass state and the memorial operation in the heat pump heating state are performed simultaneously, the heat pump is compared with the case where the hot water supply operation in the bypass state and the heating operation in the heat pump heating state are performed simultaneously as shown in FIG. The only difference is that the water heated by the heating heat exchanger 5 is supplied to the second load heat exchanger 7b.
When simultaneously performing the hot water supply operation in the non-bypass state and the chasing operation in the heat pump heating state, simultaneously performing the hot water supply operation in the non-bypass state and the heating operation in the heat pump heating state shown in FIGS. 13 and 14 The difference is that water heated by the heat pump heating type heat exchanger 5 is supplied to the second load heat exchanger 7b. Incidentally, also in this case, as shown in FIG. 14, when the temperature of the water supplied to the heat pump heating type heat exchanger 5 becomes higher than a predetermined temperature (for example, 40 ° C.), the water supply means 20 The water supplied to the exchanger 5 is supplied with water, and the temperature of the water supplied to the heat pump heating type heat exchanger 5 is adjustable to a predetermined temperature (for example, 40 ° C.) or less.
Compared with simultaneous hot water supply operation in the bypass state and heating operation in the burner heating state, both the hot water supply operation in the bypass state and the memorial operation in the burner heating state are performed simultaneously. The only difference is that the water heated in the vessel 6 is supplied to the second load heat exchanger 7b.
Burner heating type when hot water supply operation in a non-bypass state and a chasing operation in a burner heating state are performed at the same time as compared with a case in which hot water supply operation in a non-bypass state and heating operation in a burner heating state are performed simultaneously. The only difference is that the water heated by the heat exchanger 6 is supplied to the second load heat exchanger 7b.

(蓄熱運転+追焚運転の同時運転)
蓄熱運転とヒートポンプ加熱状態での追焚運転とを同時に行う場合は、図15に示す蓄熱運転とヒートポンプ加熱状態での暖房運転とを同時に行う場合と比べて、ヒートポンプ加熱式熱交換器5にて加熱した水を第2負荷熱交換器7bに供給する点が異なるだけである。
蓄熱運転とバーナー加熱状態での追焚運転とを同時に行う場合も、上述の蓄熱運転とバーナー加熱状態での暖房運転とを同時に行う場合と比べて、バーナー加熱式熱交換器6にて加熱した水を第2負荷熱交換器7bに供給する点が異なるだけである。
(Simultaneous operation of heat storage operation + memorial operation)
In the case where the heat storage operation and the chasing operation in the heat pump heating state are performed simultaneously, the heat pump heating type heat exchanger 5 is compared with the case where the heat storage operation and the heating operation in the heat pump heating state shown in FIG. 15 are performed simultaneously. The only difference is that the heated water is supplied to the second load heat exchanger 7b.
Even in the case where the heat storage operation and the chasing operation in the burner heating state are performed at the same time, compared to the case where the heat storage operation and the heating operation in the burner heating state are performed at the same time, heating is performed by the burner heating type heat exchanger 6. The only difference is that water is supplied to the second load heat exchanger 7b.

(高温加熱運転)
この高温加熱運転では、図16に示すように、運転制御手段19が、バーナー燃焼装置Nを燃焼状態に切り換え、ヒートポンプ装置4を非作動状態に切り換え、循環ポンプ3を作動させるとともに、給湯タンク2から第1流路部位R1に取り出した水を第7流路部位R7に供給する状態に第1切換弁S1を切り換え、第2比例弁H2、第3比例弁H3、及び、第4比例弁H4を開動作させる。これにより、給湯タンク2の下部から取り出した水を、第1流路部位R1、第7流路部位R7、第5流路部位R5、ヒートポンプ加熱式熱交換器5、第6流路部位R6、第2流路部位R2の順に経由してバーナー加熱式熱交換器6に供給して加熱し、その加熱された水を、第3流路部位R3、第1バイパス流路部位B1、第2流路部位R2の順に経由して給湯タンク2の上部に戻している。第1バイパス流路部位B1を経由した水は、その一部が第2流路部位R2を経由して給湯タンク2の上部に供給され、残りの一部が第2流路部位R2を経由してバーナー加熱式熱交換器6に供給されている。第3水路W3は、図11に示すように、上述の蓄熱運転にて述べた如く、少なくとも第1バイパス水路V1の一部から構成されているが、この少なくとも第1バイパス水路V1の一部から構成されている第3水路W3は、給湯タンク2から取り出した水をバーナー加熱式熱交換器6にて加熱し、その加熱された水を給湯タンク2に戻すように水を循環自在に構成されている。そして、バーナー加熱式熱交換器6にて加熱された水を給湯タンク2に戻すことにより、給湯タンク2の水を高温として殺菌消毒することができるので、レジオネラ菌等の繁殖を適切に防止することができる。
(High temperature heating operation)
In this high temperature heating operation, as shown in FIG. 16, the operation control means 19 switches the burner combustion device N to the combustion state, switches the heat pump device 4 to the non-operation state, operates the circulation pump 3, and hot water supply tank 2. The first switching valve S1 is switched to a state where the water taken out from the first flow passage portion R1 is supplied to the seventh flow passage portion R7, and the second proportional valve H2, the third proportional valve H3, and the fourth proportional valve H4. Is opened. Thereby, the water taken out from the lower part of the hot water supply tank 2 is supplied to the first flow path part R1, the seventh flow path part R7, the fifth flow path part R5, the heat pump heating heat exchanger 5, the sixth flow path part R6, It supplies to the burner heating type heat exchanger 6 via the 2nd flow path site | part R2 in order, it heats, and the heated water is made into 3rd flow path site | part R3, 1st bypass flow path site | part B1, 2nd flow. It returns to the upper part of the hot water supply tank 2 through the order of the road part R2. A part of the water that has passed through the first bypass flow path part B1 is supplied to the upper part of the hot water tank 2 via the second flow path part R2, and the remaining part of the water passes through the second flow path part R2. The burner heating type heat exchanger 6 is supplied. As described in the above-described heat storage operation, the third water channel W3 is composed of at least a part of the first bypass water channel V1, but from at least a part of the first bypass water channel V1, as shown in FIG. The configured third water channel W3 is configured to freely circulate the water so that the water taken out from the hot water supply tank 2 is heated by the burner heating type heat exchanger 6 and the heated water is returned to the hot water supply tank 2. ing. And since the water heated by the burner heating type heat exchanger 6 is returned to the hot water supply tank 2, the water in the hot water supply tank 2 can be sterilized and disinfected at a high temperature, so that breeding of Legionella bacteria and the like is appropriately prevented. be able to.

〔第3実施形態〕
この第3実施形態は、上記第1及び第2実施形態において、循環ポンプ3の配置形態の別実施形態である。その他の構成については、上記第1及び第2実施形態と同様であるので、その他の構成については説明を省略し、循環ポンプ3の配置形態を中心に説明する。
[Third Embodiment]
This 3rd Embodiment is another embodiment of the arrangement | positioning form of the circulation pump 3 in the said 1st and 2nd embodiment. Since other configurations are the same as those of the first and second embodiments, description of other configurations will be omitted, and description will be made focusing on an arrangement form of the circulation pump 3.

上記第1実施形態では、図1に示すように、循環ポンプ3が第6流路部位R6に配置されていたが、図17に示すように、循環ポンプ3を第5流路部位R5に配置することができる。そして、第5流路部位R5において第7流路部位R7からの接続箇所とヒートポンプ加熱式熱交換器5の間の部位に循環ポンプ3が配置されている。これにより、第5流路部位R5が、その途中部位に循環ポンプ3が設けられて負荷熱交換器7とヒートポンプ加熱式熱交換器5を接続するように構成されている。   In the first embodiment, as shown in FIG. 1, the circulation pump 3 is arranged in the sixth flow path part R6. However, as shown in FIG. 17, the circulation pump 3 is arranged in the fifth flow path part R5. can do. The circulation pump 3 is disposed in a portion between the connection portion from the seventh flow passage portion R7 and the heat pump heating heat exchanger 5 in the fifth flow passage portion R5. Thereby, 5th flow-path part R5 is comprised so that the circulation pump 3 may be provided in the middle part, and the load heat exchanger 7 and the heat pump heating type heat exchanger 5 may be connected.

上記第2実施形態では、図8に示すように、循環ポンプ3が第2流路部位R2に配置されていたが、図18に示すように、循環ポンプ3を第3流路部位R3に配置することができる。そして、第3流路部位R3においてバーナー加熱式熱交換器6と第4流路部位R4への接続箇所の間の部位に循環ポンプ3が配置されている。これにより、第3流路部位R3が、その途中部位に循環ポンプ3が設けられてバーナー加熱式熱交換器6と給湯利用箇所1を接続するように構成されている。
また、循環ポンプ3の配置形態の別実施形態としては、図18中点線にて示すように、第6流路部位R6においてヒートポンプ加熱式熱交換器5と第3比例弁H3との間の部位に循環ポンプ3を配置することもできる。さらに、図18中一点鎖線にて示すように、第5流路部位R5において第7流路部位R7からの接続箇所とヒートポンプ加熱式熱交換器5の間の部位に循環ポンプ3を配置することもできる。このように、循環ポンプ3を第6流路部位R6又は第5流路部位R5に配置した場合には、第1水路W1を、第1流路部位R1と給湯タンク2と第2流路部位R2とバーナー加熱式熱交換器6と第3流路部位R3と第4流路部位R4と負荷熱交換器7と第5流路部位R5とヒートポンプ加熱式熱交換器5と第6流路部位R6とで構成している。これにより、上水の圧力により給湯タンク2の水を給湯利用箇所1に供給することに加えて、循環ポンプ3の圧力でバーナー加熱式熱交換器6と負荷熱交換器7とヒートポンプ加熱式熱交換器5とを経由して循環される水をも給湯利用箇所1に供給することができる。
In the second embodiment, as shown in FIG. 8, the circulation pump 3 is arranged in the second flow path part R2. However, as shown in FIG. 18, the circulation pump 3 is arranged in the third flow path part R3. can do. And the circulation pump 3 is arrange | positioned in the site | part between the connection part to the burner heating type heat exchanger 6 and 4th channel site | part R4 in 3rd channel site | part R3. Thereby, 3rd flow-path site | part R3 is comprised so that the circulation pump 3 may be provided in the middle site | part, and the burner heating type heat exchanger 6 and the hot water supply utilization location 1 may be connected.
Further, as another embodiment of the arrangement form of the circulation pump 3, as shown by a dotted line in FIG. 18, a portion between the heat pump heating heat exchanger 5 and the third proportional valve H3 in the sixth flow path portion R6. The circulation pump 3 can also be arranged in the front. Further, as shown by a one-dot chain line in FIG. 18, the circulation pump 3 is arranged in a portion between the connection portion from the seventh flow passage portion R7 and the heat pump heating type heat exchanger 5 in the fifth flow passage portion R5. You can also. Thus, when the circulation pump 3 is arranged in the sixth flow path part R6 or the fifth flow path part R5, the first water path W1 is replaced with the first flow path part R1, the hot water supply tank 2, and the second flow path part. R2, burner heating type heat exchanger 6, third flow path part R3, fourth flow path part R4, load heat exchanger 7, fifth flow path part R5, heat pump heating type heat exchanger 5 and sixth flow path part And R6. Thereby, in addition to supplying the water in the hot water supply tank 2 to the hot water supply utilization point 1 by the pressure of the clean water, the burner heating type heat exchanger 6, the load heat exchanger 7 and the heat pump heating type heat are used by the pressure of the circulation pump 3. Water that is circulated through the exchanger 5 can also be supplied to the hot water supply utilization point 1.

〔第4実施形態〕
この第4実施形態は、上記第1及び第2実施形態において、給湯タンク2の水を加熱するための構成を追加した別実施形態である。その他の構成については、上記第1及び第2実施形態と同様であるので、その他の構成については説明を省略し、追加した給湯タンク2の水を加熱するための構成を中心に説明する。
[Fourth Embodiment]
This 4th Embodiment is another embodiment which added the structure for heating the water of the hot water supply tank 2 in the said 1st and 2nd embodiment. Since other configurations are the same as those of the first and second embodiments, description of other configurations will be omitted, and the configuration for heating the water in the added hot water supply tank 2 will be mainly described.

まず、上記第1実施形態において、給湯タンク2の水を加熱するための構成を追加した熱媒供給装置の別実施形態について、図19に基づいて説明する。
この熱媒供給装置では、熱と電力を発生する熱電併給装置(図示省略)が設けられており、その熱電併給装置の排熱にて給湯タンク2の水を加熱する排熱熱交換器21が備えられている。排熱熱交換器21は、第6流路部位R6において循環ポンプ3と第2流路部位R2の接続箇所の間の部位に配置されている。ここで、熱電併給装置は、例えば、エンジンとそのエンジンの出力にて駆動される発電機とを組み合わせたもの、或いは、燃料電池装置を適応することができる。そして、この熱媒供給装置には、循環ポンプ3の圧力で、給湯タンク2から取り出した水を排熱熱交換器21において熱電併給装置の排熱にて加熱し、その加熱された水を給湯タンク2に戻す排熱加熱水路Xが備えられており、この排熱加熱水路Xは、第3水路W3と兼用に構成されている。つまり、排熱加熱水路Xと第3水路W3の双方は、給湯タンク2、第1流路部位R1の一部、第7流路部位R7、第5流路部位R5の一部、ヒートポンプ加熱式熱交換器5、第6流路部位R6、排熱熱交換器21、及び、第2流路部位R2の一部との共通の構成から構成されている。
First, another embodiment of the heat medium supply device to which the configuration for heating the water in the hot water supply tank 2 is added in the first embodiment will be described with reference to FIG.
In this heating medium supply device, a combined heat and power supply device (not shown) that generates heat and electric power is provided, and an exhaust heat exchanger 21 that heats the water in the hot water supply tank 2 with the exhaust heat of the combined heat and power supply device is provided. Is provided. The exhaust heat exchanger 21 is disposed at a position between the connection points of the circulation pump 3 and the second flow path part R2 in the sixth flow path part R6. Here, the combined heat and power device can be applied to, for example, a combination of an engine and a generator driven by the output of the engine, or a fuel cell device. And in this heat medium supply device, the water taken out from the hot water supply tank 2 is heated by the exhaust heat of the combined heat and power supply device in the exhaust heat exchanger 21 with the pressure of the circulation pump 3, and the heated water is supplied to the hot water supply An exhaust heat heating water channel X returning to the tank 2 is provided, and this exhaust heat heating water channel X is configured to be used also as the third water channel W3. That is, both the exhaust heat heating water channel X and the third water channel W3 are the hot water supply tank 2, a part of the first flow path part R1, the seventh flow path part R7, a part of the fifth flow path part R5, a heat pump heating type. The heat exchanger 5, the sixth flow path part R6, the exhaust heat exchanger 21, and a part of the second flow path part R2 are configured in common.

そして、図示は省略するが、熱電併給装置にて発生した電力がヒートポンプ装置4の駆動用電力として供給自在に構成されており、運転制御手段19は、熱電併給装置が発生する電力のうち、電力供給部(例えば、照明やテレビ等の電力消費機器)にて消費されない余剰電力の少なくとも一部をヒートポンプ装置4に供給することで、その余剰電力の少なくとも一部を用いてヒートポンプ装置4を作動自在に構成されている。この場合には、余剰電力が発生すると、例えば、運転制御手段19は、蓄熱条件が満たされたとして、上述の蓄熱運転を行う。これにより、余剰電力が発生すると、その余剰電力を熱に変換して給湯タンク2に蓄熱し、その蓄熱された熱を給湯利用箇所1に供給することができ、余剰電力を給湯利用箇所1にて利用される熱として有効に活用することができ、エネルギー効率の向上を図ることができる。   And although illustration is abbreviate | omitted, it has comprised so that the electric power which generate | occur | produced in the combined heat and power supply apparatus can be freely supplied as drive electric power of the heat pump apparatus 4, and the operation control means 19 is electric power among the electric power which a combined heat and power supply apparatus generates. By supplying at least a part of surplus power that is not consumed by a supply unit (for example, a power consuming device such as an illumination or a television) to the heat pump apparatus 4, the heat pump apparatus 4 can be operated using at least a part of the surplus power. It is configured. In this case, when surplus power is generated, for example, the operation control means 19 performs the above-described heat storage operation on the assumption that the heat storage condition is satisfied. As a result, when surplus power is generated, the surplus power is converted into heat and stored in the hot water supply tank 2, and the stored heat can be supplied to the hot water use location 1, and surplus power can be supplied to the hot water use location 1. It can be effectively used as heat that is used and energy efficiency can be improved.

追加する給湯タンク2の水を加熱するための構成として、熱電併給装置にて発生する排熱により給湯タンク2の水を加熱する構成を述べたが、排熱熱交換器21に代えて、太陽熱により給湯タンク2の水を加熱する太陽熱熱交換器を備えることで、太陽熱により給湯タンク2の水を加熱して給湯タンク2に蓄熱することもできる。この場合、循環ポンプ3の圧力で、給湯タンク2から取り出した水を太陽熱熱交換器において太陽熱にて加熱し、その加熱された水を給湯タンク2に戻す太陽熱加熱水路を備えることになるが、この太陽熱加熱水路を第3水路W3と兼用して構成することができる。また、排熱熱交換器21に加えて、太陽熱により水を加熱する太陽熱熱交換器を備え、熱電併給装置の排熱及び太陽熱の双方にて給湯タンク2の水を加熱することもできる。   As the configuration for heating the water in the hot water supply tank 2 to be added, the configuration in which the water in the hot water supply tank 2 is heated by the exhaust heat generated in the combined heat and power supply device has been described. By providing a solar heat exchanger that heats the water in the hot water supply tank 2, the water in the hot water supply tank 2 can be heated by solar heat and stored in the hot water supply tank 2. In this case, the water taken out from the hot water supply tank 2 is heated by solar heat in the solar heat exchanger with the pressure of the circulation pump 3, and a solar heat heating channel for returning the heated water to the hot water supply tank 2 is provided. This solar heating water channel can also be configured to serve as the third water channel W3. Moreover, in addition to the exhaust heat exchanger 21, the solar heat exchanger which heats water with a solar heat is provided, and the water of the hot water supply tank 2 can also be heated with both the exhaust heat and solar heat of a cogeneration apparatus.

次に、上記第2実施形態において、給湯タンク2の水を加熱するための構成を追加した熱媒供給装置の別実施形態について、図20に基づいて説明する。
この熱媒供給装置でも、図19と同様に、熱電併給装置の排熱にて給湯タンク2の水を加熱する排熱熱交換器21が備えられ、その排熱熱交換器21は、第2流路部位R2において循環ポンプ3とバーナー加熱式熱交換器6の間の部位に配置されている。そして、この場合でも、図19と同様に、排熱加熱水路Xは、第3水路W3と兼用に構成されている。つまり、排熱加熱水路Xと第3水路W3の双方は、給湯タンク2、第1流路部位R1の一部、第7流路部位R7、第5流路部位R5の一部、ヒートポンプ加熱式熱交換器5、第6流路部位R6、第2流路部位R2、排熱熱交換器21、バーナー加熱式熱交換器6、第3流路部位R3の一部、及び、第1バイパス流路部位B1との共通の構成から構成されている。
Next, another embodiment of the heat medium supply device to which the structure for heating the water in the hot water supply tank 2 is added in the second embodiment will be described with reference to FIG.
Similarly to FIG. 19, this heat medium supply device is also provided with a waste heat heat exchanger 21 that heats the water in the hot water supply tank 2 with the waste heat of the combined heat and power supply device. It arrange | positions in the site | part between the circulation pump 3 and the burner heating type heat exchanger 6 in flow path site | part R2. Even in this case, as in FIG. 19, the exhaust heat heating water channel X is also used as the third water channel W <b> 3. That is, both the exhaust heat heating water channel X and the third water channel W3 are the hot water supply tank 2, a part of the first flow path part R1, the seventh flow path part R7, a part of the fifth flow path part R5, a heat pump heating type. Heat exchanger 5, sixth flow path part R6, second flow path part R2, exhaust heat exchanger 21, burner heating heat exchanger 6, part of third flow path part R3, and first bypass flow It is comprised from the common structure with road part B1.

ここで、排熱熱交換器21の配置形態については、上述の如く、第2流路部位R2において循環ポンプ3とバーナー加熱式熱交換器6の間の部位だけでなく、図20中点線にて示すように、第6流路部位R6においてヒートポンプ加熱式熱交換器5と第3比例弁H3の間の部位に排熱熱交換器21を配置することもできる。   Here, as to the arrangement form of the exhaust heat exchanger 21, as described above, not only the portion between the circulation pump 3 and the burner heating heat exchanger 6 in the second flow path portion R2, but also the dotted line in FIG. As shown, the exhaust heat exchanger 21 can be disposed in a portion between the heat pump heating type heat exchanger 5 and the third proportional valve H3 in the sixth flow path portion R6.

また、これらの場合でも、図19と同様に、熱電併給装置にて発生した電力がヒートポンプ装置4の駆動用電力として供給自在に構成されており、運転制御手段19は、熱電併給装置が発生する電力のうち、電力供給部(例えば、照明やテレビ等の電力消費機器)にて消費されない余剰電力の少なくとも一部をヒートポンプ装置4に供給することで、その余剰電力の少なくとも一部を用いてヒートポンプ装置4を作動自在に構成されている。さらに、排熱熱交換器21に代えて、太陽熱により給湯タンク2の水を加熱する太陽熱熱交換器を備えたり、或いは、排熱熱交換器21に加えて、太陽熱により水を加熱する太陽熱熱交換器を備え、熱電併給装置の排熱及び太陽熱の双方にて給湯タンク2の水を加熱することもできる。   Also in these cases, similarly to FIG. 19, the electric power generated in the combined heat and power supply device is configured to be freely supplied as the driving power for the heat pump device 4, and the operation control means 19 is generated by the combined heat and power supply device. By supplying at least a part of surplus power that is not consumed by a power supply unit (for example, a power consuming device such as an illumination or a television) to the heat pump device 4, the heat pump uses at least a part of the surplus power. The device 4 is configured to be operable. Furthermore, it replaces with the exhaust heat exchanger 21, the solar heat exchanger which heats the water of the hot water supply tank 2 with a solar heat is provided, or the solar heat which heats water with a solar heat in addition to the exhaust heat exchanger 21 An exchanger is provided, and the water in the hot water supply tank 2 can be heated by both exhaust heat and solar heat of the combined heat and power supply device.

この第4実施形態においても、上記第3実施形態で述べた如く、図17及び図18に示すように、循環ポンプ3の配置形態を変更することもできる。   Also in the fourth embodiment, as described in the third embodiment, as shown in FIGS. 17 and 18, the arrangement form of the circulation pump 3 can be changed.

〔第5実施形態〕
この第5実施形態は、上記第1及び第2実施形態において、第1負荷熱交換器7aと第2負荷熱交換器7bとの配置形態の別実施形態である。その他の構成については、上記第1及び第2実施形態と同様であるので、その他の構成については説明を省略し、第1負荷熱交換器7aと第2負荷熱交換器7bとの配置形態を中心に説明する。
[Fifth Embodiment]
This 5th Embodiment is another embodiment of the arrangement | positioning form of the 1st load heat exchanger 7a and the 2nd load heat exchanger 7b in the said 1st and 2nd embodiment. Since other configurations are the same as those in the first and second embodiments, description of other configurations is omitted, and an arrangement configuration of the first load heat exchanger 7a and the second load heat exchanger 7b is omitted. The explanation is centered.

上記第1及び第2実施形態では、第1負荷熱交換器7aと第2負荷熱交換器7bが並列状態で設けられているが、この第5実施形態では、図21に示すように、第1負荷熱交換器7aと第2負荷熱交換器7bが直列状態で設けられている。   In the first and second embodiments, the first load heat exchanger 7a and the second load heat exchanger 7b are provided in parallel, but in the fifth embodiment, as shown in FIG. A 1-load heat exchanger 7a and a second load heat exchanger 7b are provided in series.

この第5実施形態においても、上記第3実施形態で述べた如く、図17及び図18に示すように、循環ポンプ3の配置形態を変更することもできる。また、この第5実施形態においても、上述の第4実施形態にて述べた如く、図19及び図20に示すように、給湯タンク2の水を加熱するための構成を追加することもできる。   Also in the fifth embodiment, as described in the third embodiment, as shown in FIGS. 17 and 18, the arrangement form of the circulation pump 3 can be changed. Also in the fifth embodiment, as described in the fourth embodiment, as shown in FIGS. 19 and 20, a configuration for heating the water in the hot water supply tank 2 can be added.

〔第6実施形態〕
この第6実施形態は、上記第2実施形態における第1水路W1の別実施形態である。その他の構成は、上記第2実施形態と同様であるので、その他の構成については説明を省略し、第1水路W1の構成を中心に説明する。
[Sixth Embodiment]
The sixth embodiment is another embodiment of the first water channel W1 in the second embodiment. Since the other configuration is the same as that of the second embodiment, description of the other configuration is omitted, and the configuration of the first water channel W1 will be mainly described.

上記第2実施形態では、図9に示すように、第1水路W1を、第1流路部位R1と給湯タンク2と第2流路部位R2とバーナー加熱式熱交換器6と第3流路部位R3とで構成している。
それに対して、この第6実施形態では、図22に示すように、第1水路W1が、第1流路部位R1と給湯タンク2と第2流路部位R2とバーナー加熱式熱交換器6と第3流路部位R3と第7流路部位R7と第5流路部位R5の一部(第7流路部位R7との接続箇所からヒートポンプ加熱式熱交換器5までの間の部位)とヒートポンプ加熱式熱交換器5と第6流路部位R6とで構成されている。これにより、第1水路W1は、上水の圧力及び循環ポンプ3の圧力によって、給湯タンク2から取り出した水に第6流路部位R6からの水を混合させて、その混合水をバーナー加熱式熱交換器6を経由して給湯利用箇所1に供給するように構成されている。
In the second embodiment, as shown in FIG. 9, the first water channel W <b> 1 is divided into the first flow path part R <b> 1, the hot water tank 2, the second flow path part R <b> 2, the burner heating heat exchanger 6, and the third flow path. It consists of site | part R3.
On the other hand, in the sixth embodiment, as shown in FIG. 22, the first water channel W1 includes the first flow path part R1, the hot water supply tank 2, the second flow path part R2, the burner heating type heat exchanger 6 and Third flow path part R3, seventh flow path part R7 and part of fifth flow path part R5 (parts from the connection point with seventh flow path part R7 to heat pump heating type heat exchanger 5) and heat pump It is comprised by the heating type heat exchanger 5 and 6th flow-path part R6. Thereby, the 1st water channel W1 mixes the water from 6th flow-path part R6 with the water taken out from the hot water supply tank 2 with the pressure of clean water, and the pressure of the circulation pump 3, and this mixed water is burner heating type. It is configured so as to be supplied to the hot water supply utilization point 1 via the heat exchanger 6.

非バイパス状態での給湯運転では、図22に示すように、運転制御手段19が、循環ポンプ3を作動させ、第2比例弁H2、第3比例弁H3及び第4比例弁H4を開動作させ、第1流路部位R1の水の一部をそのまま給湯タンク2に供給するとともに、第1流路部位R1の水の残りの一部を第7流路部位R7に供給する状態に第1切換弁S1を切り換えている。例えば、給湯タンク2の水の温度が比較的高温である場合には、その給湯タンク2から取り出した水だけをバーナー加熱式熱交換器6に供給すると、バーナー燃焼装置Nを最小燃焼量にて燃焼させても、バーナー加熱式熱交換器6にて加熱された水の温度が給湯利用箇所1にて要求されている給湯設定温度よりも高温になる場合がある。そこで、上述の如く、第1水路Wが、給湯タンク2から取り出した水に第6流路部位R6からの水を混合させることで、バーナー加熱式熱交換器6に供給する水の温度を低下させることができる。これにより、バーナー加熱式熱交換器6にて加熱された水の温度が給湯設定温度よりも高温になるのを防止することができ、給湯設定温度の水を安定して供給することができる。   In the hot water supply operation in the non-bypass state, as shown in FIG. 22, the operation control means 19 operates the circulation pump 3 and opens the second proportional valve H2, the third proportional valve H3, and the fourth proportional valve H4. The first switching to a state in which a part of the water in the first flow path part R1 is supplied to the hot water supply tank 2 as it is and the remaining part of the water in the first flow path part R1 is supplied to the seventh flow path part R7. The valve S1 is switched. For example, when the temperature of the water in the hot water supply tank 2 is relatively high, if only the water taken out from the hot water supply tank 2 is supplied to the burner heating type heat exchanger 6, the burner combustion device N can be operated at the minimum combustion amount. Even if it is made to burn, the temperature of the water heated by the burner heating type heat exchanger 6 may be higher than the hot water supply set temperature required at the hot water supply use location 1. Therefore, as described above, the temperature of the water supplied to the burner heating type heat exchanger 6 is decreased by the first water channel W mixing the water from the sixth channel part R6 with the water taken out from the hot water supply tank 2. Can be made. Thereby, it can prevent that the temperature of the water heated with the burner heating type heat exchanger 6 becomes higher than hot water supply preset temperature, and can supply the water of hot water preset temperature stably.

また、図22に示すものに代えて、図23に示すように、第1水路W1を、第1流路部位R1と給湯タンク2と第2流路部位R2とバーナー加熱式熱交換器6と第3流路部位R3と第4流路部位R4と負荷熱交換器7と第5流路部位R5とヒートポンプ加熱式熱交換器5と第6流路部位R6とで構成することもできる。これにより、第1水路W1は、上水の圧力で給湯タンク2の水を給湯利用箇所1に供給するとともに、循環ポンプ3の圧力でバーナー加熱式熱交換器6と負荷熱交換器7とヒートポンプ加熱式熱交換器5を経由して循環される水を給湯利用箇所1に供給するように構成されている。   Further, instead of the one shown in FIG. 22, as shown in FIG. 23, the first water channel W1 is replaced with a first flow path part R1, a hot water supply tank 2, a second flow path part R2, and a burner heating type heat exchanger 6. The third flow path part R3, the fourth flow path part R4, the load heat exchanger 7, the fifth flow path part R5, the heat pump heating type heat exchanger 5, and the sixth flow path part R6 may be used. Thereby, the 1st water channel W1 supplies the water of the hot-water supply tank 2 to the hot-water supply utilization location 1 with the pressure of clean water, and the burner heating type heat exchanger 6, the load heat exchanger 7, and the heat pump with the pressure of the circulation pump 3 The water circulated via the heating heat exchanger 5 is configured to be supplied to the hot water supply utilization location 1.

非バイパス状態での給湯運転では、図23に示すように、運転制御手段19が、循環ポンプ3を作動させ、第2比例弁H2、第3比例弁H3及び第4比例弁H4を開動作させ、第4流路部位R4からの水を第1負荷熱交換器7a及び第2負荷熱交換器7bの両方又は一方に供給するように第2開閉弁K2及び第3開閉弁K3の開閉動作を制御している。ここで、第2開閉弁K2及び第3開閉弁K3の開閉動作について、図23では、第4流路部位R4からの水を第1負荷熱交換器7aの一方に供給するように第2開閉弁K2及び第3開閉弁K3の開閉動作を制御した場合を示している。これにより、給湯タンク2から取り出した水だけでなく、バーナー加熱式熱交換器6と負荷熱交換器7とヒートポンプ加熱式熱交換器5を経由して循環される水をも、給湯利用箇所1に供給することができるので、給湯利用箇所1に供給する水の水量として十分な水量を確保することができる。しかも、給湯タンク2から取り出した水がバーナー加熱式熱交換器6にて加熱された水と混合されて、その混合された水がバーナー加熱式熱交換器6に供給されるので、バーナー加熱式熱交換器6に供給される水の温度が比較的安定した温度となり、その結果、給湯利用箇所1にて要求されている給湯設定温度の水を安定して供給することができる。   In the hot water supply operation in the non-bypass state, as shown in FIG. 23, the operation control means 19 operates the circulation pump 3 and opens the second proportional valve H2, the third proportional valve H3, and the fourth proportional valve H4. The opening / closing operation of the second on-off valve K2 and the third on-off valve K3 is performed so that the water from the fourth flow path part R4 is supplied to both or one of the first load heat exchanger 7a and the second load heat exchanger 7b. I have control. Here, regarding the opening / closing operation of the second opening / closing valve K2 and the third opening / closing valve K3, in FIG. 23, the second opening / closing is performed so that water from the fourth flow path part R4 is supplied to one of the first load heat exchangers 7a. The case where the opening / closing operation | movement of the valve K2 and the 3rd on-off valve K3 is controlled is shown. Thereby, not only the water taken out from the hot water supply tank 2 but also the water circulated through the burner heating type heat exchanger 6, the load heat exchanger 7 and the heat pump heating type heat exchanger 5 are used in the hot water supply use place 1. Therefore, it is possible to secure a sufficient amount of water as the amount of water to be supplied to the hot water supply use location 1. Moreover, since the water taken out from the hot water supply tank 2 is mixed with the water heated in the burner heating type heat exchanger 6 and the mixed water is supplied to the burner heating type heat exchanger 6, the burner heating type The temperature of the water supplied to the heat exchanger 6 becomes a relatively stable temperature, and as a result, it is possible to stably supply the water at the hot water supply set temperature required at the hot water supply use location 1.

この第6実施形態においても、上記第3実施形態で述べた如く、図18に示すように、循環ポンプ3の配置形態を変更することもできる。また、この第6実施形態においても、上述の第4実施形態にて述べた如く、図20に示すように、給湯タンク2の水を加熱するための構成を追加することもできる。さらに、この第6実施形態においても、上述の第5実施形態にて述べた如く、図21に示すように、第1負荷熱交換器7aと第2負荷熱交換器7bを直列状態で設けることもできる。   Also in the sixth embodiment, as described in the third embodiment, the arrangement form of the circulation pump 3 can be changed as shown in FIG. Also in the sixth embodiment, as described in the fourth embodiment, a configuration for heating the water in the hot water supply tank 2 can be added as shown in FIG. Further, in the sixth embodiment, as described in the fifth embodiment, as shown in FIG. 21, the first load heat exchanger 7a and the second load heat exchanger 7b are provided in series. You can also.

〔第7実施形態〕
この第7実施形態は、上記第2実施形態におけるヒートポンプ加熱式熱交換器5の配置形態の別実施形態である。その他の構成については、上記第2実施形態と同様であるので、その他の構成については説明を省略し、ヒートポンプ加熱式熱交換器5の配置形態を中心に説明する。
[Seventh Embodiment]
This 7th Embodiment is another embodiment of the arrangement | positioning form of the heat pump heating type heat exchanger 5 in the said 2nd Embodiment. Since the other configuration is the same as that of the second embodiment, the description of the other configuration is omitted, and the arrangement of the heat pump heating type heat exchanger 5 will be mainly described.

上記第2実施形態では、図8に示すように、ヒートポンプ加熱式熱交換器5の上流側端部が第5流路部位R5に接続され、ヒートポンプ加熱式熱交換器5の下流側端部が第6流路部位R6に接続されており、第5流路部位R5と第6流路部位R6との間にヒートポンプ加熱式熱交換器5が配置されている。
それに対して、この第7実施形態では、図24に示すように、第2流路部位R2において循環ポンプ3とバーナー加熱式熱交換器6との接続箇所の間の部位に、ヒートポンプ加熱式熱交換器5が配置されている。そして、この第7実施形態では、第6流路部位R6が、負荷熱交換器7と第2流路部位R2における給湯タンク2と循環ポンプ3の間の部位に接続するように構成されており、第5流路部位R5が備えられていない。
In the second embodiment, as shown in FIG. 8, the upstream end of the heat pump heating type heat exchanger 5 is connected to the fifth flow path part R5, and the downstream end of the heat pump heating type heat exchanger 5 is The heat pump heating type heat exchanger 5 is arranged between the fifth flow path part R5 and the sixth flow path part R6.
On the other hand, in the seventh embodiment, as shown in FIG. 24, in the second flow path part R2, a heat pump heating type heat is provided in a part between the connection points of the circulation pump 3 and the burner heating type heat exchanger 6. An exchanger 5 is arranged. And in this 7th Embodiment, 6th flow-path part R6 is comprised so that it may connect to the site | part between the hot water supply tank 2 and the circulation pump 3 in the load heat exchanger 7 and 2nd flow-path part R2. The fifth flow path part R5 is not provided.

つまり、この第7実施形態では、流路部位として、給湯タンク2に接続されて上水を給湯タンク2に給水する第1流路部位R1と、給湯タンク2とバーナー加熱式熱交換器6を接続して、給湯タンク2に近い順に循環ポンプ3とヒートポンプ加熱式熱交換器5が設けられた第2流路部位R2と、バーナー加熱式熱交換器6と給湯利用箇所1を接続する第3流路部位R3と、第3流路部位R3の途中部位と負荷熱交換器7を接続する第4流路部位R4と、負荷熱交換器7と第2流路部位R2における給湯タンク2と循環ポンプ3の間の部位を接続する第6流路部位R6と、第1流路部位R1の途中部位と第6流路部位R6の途中部位とを接続する第7流路部位R7と、第2流路部位R2における給湯タンク2と第6流路部位R6への接続箇所までの間の部位及び第3流路部位R3における第4流路部位R4への接続箇所と給湯利用箇所1までの間の部位を接続する第1バイパス流路部位B1とを備えている。   In other words, in the seventh embodiment, the first flow path portion R1 that is connected to the hot water supply tank 2 and supplies hot water to the hot water supply tank 2, and the hot water supply tank 2 and the burner heating type heat exchanger 6 are provided as flow path portions. The third flow path part R2 in which the circulation pump 3 and the heat pump heating type heat exchanger 5 are provided, and the burner heating type heat exchanger 6 and the hot water supply use part 1 are connected in the order close to the hot water supply tank 2. The flow path part R3, the fourth flow path part R4 connecting the intermediate part of the third flow path part R3 and the load heat exchanger 7, the hot water tank 2 and the circulation in the load heat exchanger 7 and the second flow path part R2 A sixth flow path part R6 for connecting parts between the pumps 3, a seventh flow path part R7 for connecting a midway part of the first flow path part R1 and a midway part of the sixth flow path part R6, and a second Connection point between hot water tank 2 and sixth flow path part R6 in flow path part R2 And a first bypass passage portion B1 that connects a site between the site and connected to a point and hot water use position 1 to the fourth channel region R4 in the third flow path portion R3 between.

そして、第1水路W1が、図25に示すように、第1流路部位R1と給湯タンク2と第2流路部位R2とバーナー加熱式熱交換器6と第3流路部位R3とで構成されている。第1バイパス水路V1が、図24に示すように、第1流路部位R1と給湯タンク2と第2流路部位R2の一部と第1バイパス流路部位B1と第3流路部位R3の一部とで構成されている。第2水路W2が、図26に示すように、バーナー加熱式熱交換器6と第3流路部位R3の一部と第4流路部位R4と負荷熱交換器7と第6流路部位R6と第2流路部位の一部とで構成されている。第3水路W3は、図27に示すように、給湯タンク2と第1流路部位R1の一部と第7流路部位R7と第6流路部位R6の一部と第2流路部位R2とバーナー加熱式熱交換器6と第3流路部位R3の一部と第1バイパス流路部位B1とから構成されている。   Then, as shown in FIG. 25, the first water channel W1 includes a first flow path part R1, a hot water supply tank 2, a second flow path part R2, a burner heating heat exchanger 6, and a third flow path part R3. Has been. As shown in FIG. 24, the first bypass water channel V1 includes a first flow path part R1, a hot water supply tank 2, a part of the second flow path part R2, a first bypass flow path part B1, and a third flow path part R3. It consists of a part. As shown in FIG. 26, the second water channel W2 includes the burner heating type heat exchanger 6, a part of the third flow path part R3, the fourth flow path part R4, the load heat exchanger 7, and the sixth flow path part R6. And a part of the second flow path part. As shown in FIG. 27, the third water channel W3 includes a hot water tank 2, a part of the first flow path part R1, a seventh flow path part R7, a part of the sixth flow path part R6, and a second flow path part R2. And a burner heating type heat exchanger 6, a part of the third flow path part R3, and a first bypass flow path part B1.

この第7実施形態においても、運転制御手段19は、上記第2実施形態と同様に、蓄熱運転、給湯運転、暖房運転、追焚運転、及び、高温加熱運転を実行可能であるので、図24〜図27に基づいて、各運転について説明する。   Also in the seventh embodiment, the operation control means 19 can execute the heat storage operation, the hot water supply operation, the heating operation, the memorial operation, and the high temperature heating operation as in the second embodiment. Each operation will be described with reference to FIG.

(蓄熱運転)
運転制御手段19は、図27に示すように、ヒートポンプ装置4を作動状態に切り換え、バーナー燃焼装置Nを非燃焼状態に切り換え、循環ポンプ3を作動させるとともに、給湯タンク2から第1流路部位R1に取り出した水を第7流路部位R7に供給する状態に第1切換弁S1を切り換え、第2比例弁H2、第3比例弁H3、及び、第4比例弁H4を開動作させる。運転制御手段19は、第3水路W3によって、循環ポンプ3の圧力で、給湯タンク2の下部から水を第1流路部位R1に取り出し、その取り出した水を第7流路部位R7、第6流路部位R6及び第2流路部位R2を経由してヒートポンプ加熱式熱交換器5に供給して加熱し、その加熱された水を第3流路部位R3、第1バイパス流路部位B1、第2流路部位R2を経由して給湯タンク2の上部に戻している。第1バイパス流路部位B1を経由した水は、その一部が第2流路部位R2を経由して給湯タンク2の上部に供給され、残りの一部が第2流路部位R2を経由してヒートポンプ加熱式熱交換器5に供給されている。このようにして、給湯タンク2から取り出された水がヒートポンプ加熱式熱交換器5にて加熱されて温水となり、その温水が給湯タンク2に戻されて、給湯タンク2に蓄熱している。ここで、運転制御手段19は、給湯タンク2の上部に戻す温水の温度が所定温度になるように、循環ポンプ3の回転速度及び第3比例弁H3の開度を調整してヒートポンプ加熱式熱交換器5に供給する水の供給量を調整している。
(Heat storage operation)
As shown in FIG. 27, the operation control means 19 switches the heat pump device 4 to the operating state, switches the burner combustion device N to the non-burning state, operates the circulation pump 3, and supplies the first flow path portion from the hot water tank 2. The first switching valve S1 is switched to a state in which the water taken out to R1 is supplied to the seventh flow path part R7, and the second proportional valve H2, the third proportional valve H3, and the fourth proportional valve H4 are opened. The operation control means 19 takes out the water from the lower part of the hot water supply tank 2 to the first flow path part R1 by the pressure of the circulation pump 3 by the third water passage W3, and takes the taken-out water into the seventh flow path part R7, the sixth flow path R6. The heat pump heating type heat exchanger 5 is supplied and heated via the flow path part R6 and the second flow path part R2, and the heated water is supplied to the third flow path part R3, the first bypass flow path part B1, It is returned to the upper part of the hot water supply tank 2 via the second flow path part R2. A part of the water that has passed through the first bypass flow path part B1 is supplied to the upper part of the hot water tank 2 via the second flow path part R2, and the remaining part of the water passes through the second flow path part R2. To the heat pump heating type heat exchanger 5. In this way, the water taken out from the hot water supply tank 2 is heated by the heat pump heating type heat exchanger 5 to become hot water, and the hot water is returned to the hot water supply tank 2 to store heat in the hot water supply tank 2. Here, the operation control means 19 adjusts the rotational speed of the circulation pump 3 and the opening of the third proportional valve H3 so that the temperature of the hot water returned to the upper part of the hot water supply tank 2 becomes a predetermined temperature, and heat pump heating type heat The amount of water supplied to the exchanger 5 is adjusted.

ここで、例えば、暖房運転を行った後に貯湯運転を行うときに、暖房運転にて第1負荷熱交換器7aにて要求されている暖房温度の方が蓄熱運転にて給湯タンク2の上部に戻すのに要求されている蓄熱温度よりも低温である場合、或いは、第3水路W3の水が蓄熱運転にて給湯タンク2の上部に戻すのに要求されている蓄熱温度よりも低温である場合には、ヒートポンプ加熱式熱交換器5にて加熱しても蓄熱温度まで加熱できない可能性がある。そこで、この第7実施形態では、運転制御手段19が、上述の蓄熱運転を行う前に、ヒートポンプ加熱式熱交換器5にて加熱する状態で第3水路W3の一部にて水を循環させる蓄熱予備運転を行うように構成されている。   Here, for example, when the hot water storage operation is performed after the heating operation is performed, the heating temperature requested by the first load heat exchanger 7a in the heating operation is higher in the upper portion of the hot water tank 2 in the heat storage operation. When the temperature is lower than the heat storage temperature required for returning, or when the temperature of the water in the third water channel W3 is lower than the heat storage temperature required for returning to the upper part of the hot water tank 2 in the heat storage operation. However, even if it heats with the heat pump heating type heat exchanger 5, there is a possibility that it cannot be heated to the heat storage temperature. Therefore, in the seventh embodiment, the operation control means 19 circulates water in a part of the third water channel W3 while being heated by the heat pump heating heat exchanger 5 before performing the above-described heat storage operation. The heat storage preliminary operation is performed.

この蓄熱予備運転では、図28に示すように、運転制御手段19が、ヒートポンプ装置4を作動状態に切り換え、バーナー燃焼装置Nを非燃焼状態に切り換え、循環ポンプ3を作動させるとともに、第2比例弁H2、及び、第4比例弁H4を開動作させる。これにより、ヒートポンプ加熱式熱交換器5にて加熱された水は、第2流路部位R2、バーナー加熱式熱交換器6、第3流路部位R3、第1バイパス流路部位B1、第2流路部位R2を経由して、ヒートポンプ加熱式熱交換器5に戻されている。このようにして、ヒートポンプ加熱式熱交換器5にて加熱する状態で第3水路W3の一部にて水を循環させて、その循環される水の予熱を行っている。そして、運転制御手段19は、第3水路W3の一部にて循環される水の温度(例えば、第1バイパス流路部位B1の水の温度)が蓄熱温度に達すると、蓄熱予備運転を終了して、上述の蓄熱運転を開始するようにしている。   In this heat storage preliminary operation, as shown in FIG. 28, the operation control means 19 switches the heat pump device 4 to the operating state, switches the burner combustion device N to the non-combusting state, operates the circulation pump 3, and the second proportionality. The valve H2 and the fourth proportional valve H4 are opened. Thereby, the water heated in the heat pump heating type heat exchanger 5 is supplied to the second flow path part R2, the burner heating type heat exchanger 6, the third flow path part R3, the first bypass flow path part B1, and the second. It is returned to the heat pump heating type heat exchanger 5 via the flow path part R2. In this manner, water is circulated in a part of the third water channel W3 while being heated by the heat pump heating type heat exchanger 5, and the circulated water is preheated. And the operation control means 19 will complete | finish a thermal storage preliminary operation, if the temperature (for example, the temperature of the water of 1st bypass flow-path part B1) of the water circulated in a part of 3rd water channel W3 reaches thermal storage temperature. Then, the above-described heat storage operation is started.

(給湯運転)
この給湯運転では、運転制御手段19が、図24に示すように、バーナー加熱式熱交換器6をバイパスして循環ポンプ3の圧力を使わずに上水の圧力で給湯タンク2から取り出した水を給湯利用箇所1に直接供給するバイパス状態と、図25に示すように、上水の圧力に加えて循環ポンプ3の圧力で給湯タンク2から取り出した水をバーナー加熱式熱交換器6を経由して給湯利用箇所1に供給する非バイパス状態とに切換自在に構成されている。そして、運転制御手段19は、上記第2実施形態と同様に、給湯タンク2の水の温度が切換設定温度以上であると、バイパス状態に切り換え、給湯タンク2の水の温度が切換設定温度未満であると、非バイパス状態に切り換える。
(Hot water operation)
In this hot water supply operation, as shown in FIG. 24, the operation control means 19 bypasses the burner heating type heat exchanger 6 and uses the water taken out from the hot water tank 2 with the pressure of the clean water without using the pressure of the circulation pump 3. As shown in FIG. 25, the water taken out from the hot water tank 2 by the pressure of the circulating pump 3 in addition to the pressure of the clean water passes through the burner heating type heat exchanger 6. Thus, it is configured to be switchable to a non-bypass state to be supplied to the hot water supply utilization location 1. Then, the operation control means 19 switches to the bypass state when the temperature of the water in the hot water supply tank 2 is equal to or higher than the switching set temperature, and the temperature of the water in the hot water supply tank 2 is less than the switching set temperature, as in the second embodiment. If it is, it will switch to a non-bypass state.

バイパス状態に切り換える場合には、図24に示すように、運転制御手段19が、第2比例弁H2及び第4比例弁H4を閉動作させたままとしており、第1バイパス水路V1によって、上水の圧力で給湯タンク2から取り出した水をバーナー加熱式熱交換器6をバイパスして給湯利用箇所1に供給している。
非バイパス状態に切り換える場合には、図25に示すように、運転制御手段19が、第2比例弁H2及び第4比例弁H4を開動作させるとともに、循環ポンプ3を作動させて、給湯タンク2から取り出した水を、循環ポンプ3の圧力で第2流路部位R2にてバーナー加熱式熱交換器6に供給し、そのバーナー加熱式熱交換器6を経由した水を給湯利用箇所1に供給している。
In the case of switching to the bypass state, as shown in FIG. 24, the operation control means 19 keeps the second proportional valve H2 and the fourth proportional valve H4 closed, and the first bypass water channel V1 causes the The water taken out from the hot water supply tank 2 at a pressure of 2 is supplied to the hot water supply use location 1 by bypassing the burner heating type heat exchanger 6.
In the case of switching to the non-bypass state, as shown in FIG. 25, the operation control means 19 opens the second proportional valve H2 and the fourth proportional valve H4 and operates the circulation pump 3 so that the hot water supply tank 2 The water taken out from the water is supplied to the burner heating type heat exchanger 6 at the second flow path part R2 by the pressure of the circulation pump 3, and the water passing through the burner heating type heat exchanger 6 is supplied to the hot water supply use point 1. is doing.

この第7実施形態においても、上述の第6実施形態にて述べた如く、図22に示すように、第1水路W1を、第1流路部位R1と給湯タンク2と第2流路部位R2とバーナー加熱式熱交換器6と第3流路部位R3と第7流路部位R7と第6流路部位R6の一部(第7流路部位R7との接続箇所から第2流路部位R2との接続箇所までの間の部位)とで構成することもできる。また、上述の第6実施形態にて述べた如く、図23に示すように、第1水路W1を、第1流路部位R1と給湯タンク2と第2流路部位R2とバーナー加熱式熱交換器6と第3流路部位R3と第4流路部位R4と負荷熱交換器7と第6流路部位R6とで構成することもできる。   Also in the seventh embodiment, as described in the sixth embodiment, as shown in FIG. 22, the first water channel W1 is divided into the first flow path part R1, the hot water tank 2, and the second flow path part R2. And the burner heating type heat exchanger 6, the third flow path part R3, the seventh flow path part R7, and a part of the sixth flow path part R6 (from the connection point of the seventh flow path part R7 to the second flow path part R2 It is also possible to configure the system with a part between the connection part and the part. Further, as described in the sixth embodiment described above, as shown in FIG. 23, the first water channel W1, the first flow path part R1, the hot water supply tank 2, the second flow path part R2, and the burner heating type heat exchange. It can also be constituted by the vessel 6, the third flow path part R3, the fourth flow path part R4, the load heat exchanger 7, and the sixth flow path part R6.

(暖房運転)
運転制御手段19は、図26に示すように、循環ポンプ3を作動させるとともに、第4流路部位R4からの水を第1負荷熱交換器7aに供給するように第2開閉弁K2及び第3開閉弁K3の開閉動作を制御し、第2比例弁H2及び第4比例弁H4を閉動作させたままとし、第3比例弁H3を開動作させる。これにより、第2水路W2によって、循環ポンプ3の圧力でバーナー加熱式熱交換器6と第1負荷熱交換器7aとヒートポンプ加熱式熱交換器5を経由して水を循環させている。そして、上記第2実施形態と同様に、運転制御手段19は、第2水路W2にて水を循環させている状態で、バーナー燃焼装置Nを燃焼状態と非燃焼状態とに切り換えるとともに、ヒートポンプ装置4を作動状態と非作動状態とに切り換えることで、バーナー加熱状態とヒートポンプ加熱状態とに切換自在に構成されており、第1負荷熱交換器7aで要求されている熱負荷に対して、バーナー加熱状態に切り換えた場合とヒートポンプ加熱状態に切り換えた場合との夫々の1次エネルギー消費量を求め、その求めた1次エネルギー消費量が小さい方に切り換えている。
(Heating operation)
As shown in FIG. 26, the operation control means 19 operates the circulation pump 3, and supplies the second on-off valve K2 and the second valve so as to supply water from the fourth flow path portion R4 to the first load heat exchanger 7a. The opening / closing operation of the third opening / closing valve K3 is controlled, the second proportional valve H2 and the fourth proportional valve H4 are kept closed, and the third proportional valve H3 is opened. Thereby, the water is circulated by the pressure of the circulation pump 3 through the burner heating type heat exchanger 6, the first load heat exchanger 7a, and the heat pump heating type heat exchanger 5 by the second water passage W2. As in the second embodiment, the operation control means 19 switches the burner combustion device N between the combustion state and the non-combustion state while the water is circulating in the second water passage W2, and the heat pump device. 4 can be switched between a burner heating state and a heat pump heating state by switching between an operating state and a non-operating state, and with respect to the thermal load required by the first load heat exchanger 7a, The primary energy consumption amount in each of the case of switching to the heating state and the case of switching to the heat pump heating state is obtained, and the obtained primary energy consumption amount is switched to the smaller one.

ヒートポンプ加熱状態に切り換える場合には、図26に示すように、運転制御手段19が、バーナー燃焼装置Nを非燃焼状態に切り換えるとともに、ヒートポンプ装置4を作動状態に切り換え、第1熱媒循環ポンプ15を作動させる。これにより、ヒートポンプ加熱式熱交換器5にて水が加熱されて温水となり、その温水が第2流路部位R2、バーナー加熱式熱交換器6、第3流路部位R3、及び、第4流路部位R4を経由して第1負荷熱交換器7aに供給されて第1熱媒循環路13の熱媒を加熱する。このとき、バーナー燃焼装置Nを非燃焼状態に切り換えているので、バーナー加熱式熱交換器6では水が加熱されない。第1負荷熱交換器7aにおいて加熱された熱媒は、第1熱媒循環路13にて暖房端末12に供給されて暖房端末12での暖房を行う。   In the case of switching to the heat pump heating state, as shown in FIG. 26, the operation control means 19 switches the burner combustion device N to the non-combustion state, switches the heat pump device 4 to the operating state, and the first heat medium circulation pump 15. Is activated. Thereby, water is heated in the heat pump heating type heat exchanger 5 to become warm water, and the warm water is the second flow path part R2, the burner heating type heat exchanger 6, the third flow path part R3, and the fourth flow. The heat medium in the first heat medium circulation path 13 is heated by being supplied to the first load heat exchanger 7a via the path portion R4. At this time, since the burner combustion apparatus N is switched to the non-burning state, the burner heating heat exchanger 6 does not heat water. The heat medium heated in the first load heat exchanger 7 a is supplied to the heating terminal 12 through the first heat medium circulation path 13 and is heated in the heating terminal 12.

一方、バーナー加熱状態に切り換える場合には、図26に示したヒートポンプ加熱状態に切り換える場合と比べて、水や熱媒の通流する部位は同様であり、バーナー燃焼装置N及びヒートポンプ装置4の状態が異なるだけであるので、図示を省略して説明する。
運転制御手段19は、バーナー燃焼装置Nを燃焼状態に切り換えるとともに、ヒートポンプ装置4を非作動状態に切り換え、第1熱媒循環ポンプ15を作動させる。これにより、バーナー加熱式熱交換器6にて水が加熱されて温水となり、その温水が第3流路部位R3及び第4流路部位R4を経由して第1負荷熱交換器7aに供給されて第1熱媒循環路13の熱媒を加熱する。このとき、ヒートポンプ装置4を非作動状態に切り換えているので、ヒートポンプ加熱式熱交換器5では水が加熱されない。第1負荷熱交換器7aにおいて加熱された熱媒は、第1熱媒循環路13により暖房端末12に供給されて暖房端末12での暖房を行う。
On the other hand, in the case of switching to the burner heating state, compared with the case of switching to the heat pump heating state shown in FIG. 26, the part through which water and the heat medium flow is the same, and the state of the burner combustion device N and the heat pump device 4 Are different from each other, and the illustration is omitted.
The operation control means 19 switches the burner combustion device N to the combustion state, switches the heat pump device 4 to the non-operation state, and operates the first heat medium circulation pump 15. Thereby, water is heated in the burner heating type heat exchanger 6 to become warm water, and the warm water is supplied to the first load heat exchanger 7a via the third flow path part R3 and the fourth flow path part R4. The heating medium in the first heating medium circulation path 13 is heated. At this time, since the heat pump device 4 is switched to the non-operating state, water is not heated in the heat pump heating type heat exchanger 5. The heat medium heated in the first load heat exchanger 7 a is supplied to the heating terminal 12 by the first heat medium circulation path 13 and is heated in the heating terminal 12.

(追焚運転)
上記第2実施形態と同様に、この追焚運転では、運転制御手段19が、第4流路部位R4からの水を第2負荷熱交換器7bに供給するように第2開閉弁K2及び第3開閉弁K3の開閉動作を制御している点が上述の暖房運転と異なるだけであるので、説明は省略する。
(Memorial operation)
Similar to the second embodiment, in the chasing operation, the operation control means 19 supplies the second on-off valve K2 and the second valve so as to supply water from the fourth flow path portion R4 to the second load heat exchanger 7b. Since the point which controls the opening / closing operation | movement of 3 on-off valve K3 is only different from the above-mentioned heating operation, description is abbreviate | omitted.

(バイパス状態での給湯運転+ヒートポンプ加熱状態での暖房運転の同時運転)
バイパス状態での給湯運転とヒートポンプ加熱状態での暖房運転とを同時に行う場合には、図29に示すように、運転制御手段19は、ヒートポンプ装置4を作動状態に切り換え、バーナー燃焼装置Nを非燃焼状態に切り換え、循環ポンプ3及び第1熱媒循環ポンプ15を作動させるとともに、第4流路部位R4からの水を第1負荷熱交換器7aに供給するように第2開閉弁K2及び第3開閉弁K3の開閉動作を制御し、第1流路部位R1にてそのまま給湯タンク2に給水する状態に第1切換弁S1を切り換え、第2比例弁H2及び第4比例弁H4を閉動作させたままとし、第3比例弁H3を開動作させる。これにより、運転制御手段19は、第1バイパス水路V1にて給湯タンク2の水をバーナー加熱式熱交換器6をバイパスして給湯利用箇所1に供給する給湯運転と、第2水路W2にてヒートポンプ加熱式熱交換器5にて加熱された水を第1負荷熱交換器7aに供給するヒートポンプ加熱状態での暖房運転とを同時に行うことができる。この場合、第1バイパス水路V1と第2水路W2とは独立して水を通流自在に構成されており、第1バイパス水路V1による給湯利用箇所1への水の供給と第2水路W2によるヒートポンプ加熱式熱交換器5にて加熱された水の第1負荷熱交換器7aへの供給とを、お互いに干渉することなく同時に行うことができる。
(Simultaneous operation of hot water supply operation in bypass state + heating operation in heat pump heating state)
When the hot water supply operation in the bypass state and the heating operation in the heat pump heating state are performed simultaneously, as shown in FIG. 29, the operation control means 19 switches the heat pump device 4 to the operating state and turns the burner combustion device N into the non-operation state. Switching to the combustion state, operating the circulation pump 3 and the first heat medium circulation pump 15, and supplying the second on-off valve K2 and the second so as to supply water from the fourth flow path part R4 to the first load heat exchanger 7a. The opening / closing operation of the 3 opening / closing valve K3 is controlled, the first switching valve S1 is switched to the state where the hot water supply tank 2 is directly supplied with water in the first flow path part R1, and the second proportional valve H2 and the fourth proportional valve H4 are closed. Then, the third proportional valve H3 is opened. As a result, the operation control means 19 uses the hot water supply operation in which the water in the hot water supply tank 2 is bypassed the burner heating type heat exchanger 6 and supplied to the hot water use location 1 in the first bypass water channel V1, and in the second water channel W2. The heating operation in the heat pump heating state in which the water heated by the heat pump heating type heat exchanger 5 is supplied to the first load heat exchanger 7a can be performed simultaneously. In this case, the 1st bypass water channel V1 and the 2nd water channel W2 are constituted so that water can flow independently, and the supply of water to the hot water supply use location 1 by the first bypass water channel V1 and the second water channel W2 Supply of the water heated by the heat pump heating type heat exchanger 5 to the first load heat exchanger 7a can be performed simultaneously without interfering with each other.

また、給湯運転とヒートポンプ加熱状態での暖房運転とを同時に行っている場合には、ヒートポンプ加熱式熱交換器5に供給される水の温度が徐々に上昇していき、ヒートポンプ加熱式熱交換器5に供給される水の温度が所定温度(例えば40℃)よりも高くなる場合がある。このように、ヒートポンプ加熱式熱交換器5に供給される水の温度が所定温度(例えば40℃)よりも高くなると、ヒートポンプ装置4のCOP(成績係数)が低下するので、COP(成績係数)が低下した状態でヒートポンプ装置4の運転が継続されると、エネルギー効率が低下することになる。
そこで、給湯運転とヒートポンプ加熱状態での暖房運転とを同時に行っている場合に、ヒートポンプ加熱式熱交換器5に供給される水の温度が所定温度(例えば40℃)よりも高くなると、図29中点線矢印にて示すように、運転制御手段19は、第1流路部位R1の水の一部をそのまま給湯タンク2に供給するとともに、第1流路部位R1の水の残りの一部を第7流路部位R7に供給する状態に第1切換弁S1を切り換え、第4比例弁H4を開動作させている。これにより、第1流路部位R1及び第7流路部位R7を経由して給水される水が第6流路部位R6の水に混合されて、ヒートポンプ加熱式熱交換器5に供給される水の温度が低下する。そして、運転制御手段19は、ヒートポンプ加熱式熱交換器5に供給される水の温度が所定温度(例えば40℃)以下となるように、第1切換弁S1の開度を調整している。このように、ヒートポンプ装置4を作動状態に切り換えている場合に、ヒートポンプ加熱式熱交換器5に供給される水の温度が所定温度(例えば40℃)よりも高くなると、ヒートポンプ加熱式熱交換器5に供給される水に給水して、ヒートポンプ加熱式熱交換器5に供給される水の温度を所定温度(例えば40℃)以下に調整自在な給水手段20が備えられている。この給水手段20は、第1流路部位R1の一部、第7流路部位R7、第1切換弁S1、第4比例弁H4、及び、運転制御手段19から構成されている。この給水手段20を備えることで、COP(成績係数)が低下した状態でヒートポンプ装置4の運転が継続されるのを防止して、エネルギー効率が低下するのを防止することができる。
Further, when the hot water supply operation and the heating operation in the heat pump heating state are performed simultaneously, the temperature of the water supplied to the heat pump heating type heat exchanger 5 gradually increases, and the heat pump heating type heat exchanger The temperature of the water supplied to 5 may be higher than a predetermined temperature (for example, 40 ° C.). As described above, when the temperature of the water supplied to the heat pump heating type heat exchanger 5 is higher than a predetermined temperature (for example, 40 ° C.), the COP (coefficient of performance) of the heat pump device 4 is lowered. If the operation of the heat pump device 4 is continued in a state where the temperature is lowered, the energy efficiency is lowered.
Therefore, when the hot water supply operation and the heating operation in the heat pump heating state are simultaneously performed, when the temperature of the water supplied to the heat pump heating type heat exchanger 5 becomes higher than a predetermined temperature (for example, 40 ° C.), FIG. As indicated by the middle dotted line arrow, the operation control means 19 supplies a part of the water in the first flow path part R1 to the hot water supply tank 2 as it is and the remaining part of the water in the first flow path part R1. The first switching valve S1 is switched to the state of supplying to the seventh flow path part R7, and the fourth proportional valve H4 is opened. Thereby, the water supplied through the first flow path part R1 and the seventh flow path part R7 is mixed with the water of the sixth flow path part R6 and supplied to the heat pump heating type heat exchanger 5 Temperature drops. And the operation control means 19 adjusts the opening degree of 1st switching valve S1 so that the temperature of the water supplied to the heat pump heating type heat exchanger 5 may become below predetermined temperature (for example, 40 degreeC). Thus, when the heat pump device 4 is switched to the operating state, if the temperature of the water supplied to the heat pump heating type heat exchanger 5 becomes higher than a predetermined temperature (for example, 40 ° C.), the heat pump heating type heat exchanger 5 is provided with water supply means 20 that can adjust the temperature of water supplied to the heat supplied to the heat pump 5 to a heat pump heating type heat exchanger 5 to a predetermined temperature (for example, 40 ° C.) or less. The water supply means 20 includes a part of the first flow path part R1, a seventh flow path part R7, a first switching valve S1, a fourth proportional valve H4, and an operation control means 19. By providing this water supply means 20, it is possible to prevent the operation of the heat pump device 4 from being continued in a state where the COP (coefficient of performance) is lowered, and to prevent the energy efficiency from being lowered.

(バイパス状態での給湯運転+バーナー加熱状態での暖房運転の同時運転)
バイパス状態での給湯運転とバーナー加熱状態での暖房運転とを同時に行う場合には、図29に示したバイパス状態での給湯運転とヒートポンプ加熱状態での暖房運転とを同時に行う場合と比べて、水や熱媒の通流する部位は同様であり、バーナー燃焼装置N及びヒートポンプ装置4の状態が異なるだけであるので、図示を省略して説明する。
運転制御手段19は、ヒートポンプ装置4を非作動状態に切り換え、バーナー燃焼装置Nを燃焼状態に切り換え、循環ポンプ3及び第1熱媒循環ポンプ15を作動させるとともに、第4流路部位R4からの水を第1負荷熱交換器7aに供給するように第2開閉弁K2及び第3開閉弁K3の開閉動作を制御している。これにより、運転制御手段19は、第1バイパス水路V1にて給湯タンク2の水をバーナー加熱式熱交換器6をバイパスして給湯利用箇所1に供給する給湯運転と、第2水路W2にてバーナー加熱式熱交換器6にて加熱された水を第1負荷熱交換器7aに供給するバーナー加熱状態での暖房運転とを同時に行うことができる。
(Simultaneous operation of hot water supply operation in bypass state + heating operation in burner heating state)
In the case where the hot water supply operation in the bypass state and the heating operation in the burner heating state are performed simultaneously, compared to the case where the hot water supply operation in the bypass state and the heating operation in the heat pump heating state shown in FIG. 29 are performed simultaneously, The parts through which water and the heat medium flow are the same, and only the states of the burner combustion apparatus N and the heat pump apparatus 4 are different.
The operation control means 19 switches the heat pump device 4 to the non-operating state, switches the burner combustion device N to the combustion state, operates the circulation pump 3 and the first heat medium circulation pump 15, and outputs from the fourth flow path part R4. The opening / closing operations of the second on-off valve K2 and the third on-off valve K3 are controlled so as to supply water to the first load heat exchanger 7a. As a result, the operation control means 19 uses the hot water supply operation in which the water in the hot water supply tank 2 is bypassed the burner heating type heat exchanger 6 and supplied to the hot water use location 1 in the first bypass water channel V1, and in the second water channel W2. The heating operation in the burner heating state in which the water heated by the burner heating type heat exchanger 6 is supplied to the first load heat exchanger 7a can be performed simultaneously.

(非バイパス状態での給湯運転+ヒートポンプ加熱状態での暖房運転の同時運転)
非バイパス状態での給湯運転とヒートポンプ加熱状態での暖房運転とを同時に行う場合には、図30に示すように、運転制御手段19は、ヒートポンプ装置4を作動状態に切り換え、バーナー燃焼装置Nを燃焼状態に切り換え、循環ポンプ3及び第1熱媒循環ポンプ15を作動させるとともに、第4流路部位R4からの水を第1負荷熱交換器7aに供給するように第2開閉弁K2及び第3開閉弁K3の開閉動作を制御し、第1流路部位R1にてそのまま給湯タンク2に給水する状態に第1切換弁S1を切り換え、第2比例弁H2、第3比例弁H3及び第4比例弁H4を開動作させる。これにより、運転制御手段19は、第1水路W1にて給湯タンク2の水をヒートポンプ加熱式熱交換器5とバーナー加熱式熱交換器6で加熱して給湯利用箇所1に供給する給湯運転と、第2水路W2にてヒートポンプ加熱式熱交換器5とバーナー加熱式熱交換器6にて加熱された水を第1負荷熱交換器7aに供給するヒートポンプ加熱状態での暖房運転とを同時に行うことができる。
(Simultaneous operation of hot water supply operation in non-bypass state + heating operation in heat pump heating state)
When the hot water supply operation in the non-bypass state and the heating operation in the heat pump heating state are performed simultaneously, as shown in FIG. 30, the operation control means 19 switches the heat pump device 4 to the operating state and turns the burner combustion device N on. Switching to the combustion state, operating the circulation pump 3 and the first heat medium circulation pump 15, and supplying the second on-off valve K2 and the second so as to supply water from the fourth flow path part R4 to the first load heat exchanger 7a. The opening / closing operation of the 3 on-off valve K3 is controlled, the first switching valve S1 is switched to the state where the hot water tank 2 is directly supplied with water in the first flow path part R1, the second proportional valve H2, the third proportional valve H3 and the fourth The proportional valve H4 is opened. As a result, the operation control means 19 uses the hot water supply operation in which the water in the hot water supply tank 2 is heated by the heat pump heating type heat exchanger 5 and the burner heating type heat exchanger 6 in the first water channel W1 and supplied to the hot water supply use location 1. The heating operation in the heat pump heating state in which the water heated by the heat pump heating type heat exchanger 5 and the burner heating type heat exchanger 6 is supplied to the first load heat exchanger 7a in the second water channel W2 is simultaneously performed. be able to.

(非バイパス状態での給湯運転+バーナー加熱状態での暖房運転の同時運転)
非バイパス状態での給湯運転とバーナー加熱状態での暖房運転とを同時に行う場合には、図30に示した非バイパス状態での給湯運転とヒートポンプ加熱状態での暖房運転とを同時に行う場合と比べて、水や熱媒の通流する部位は同様であり、バーナー燃焼装置N及びヒートポンプ装置4の状態が異なるだけであるので、図示を省略して説明する。
運転制御手段19は、ヒートポンプ装置4を非作動状態に切り換え、バーナー燃焼装置Nを燃焼状態に切り換え、循環ポンプ3及び第1熱媒循環ポンプ15を作動させるとともに、第4流路部位R4からの水を第1負荷熱交換器7aに供給するように第2開閉弁K2及び第3開閉弁K3の開閉動作を制御している。これにより、運転制御手段19は、第1水路W1にて給湯タンク2の水をバーナー加熱式熱交換器6で加熱して給湯利用箇所1に供給する給湯運転と、第2水路W2にてバーナー加熱式熱交換器6にて加熱された水を第1負荷熱交換器7aに供給するバーナー加熱状態での暖房運転とを同時に行うことができる。
(Simultaneous operation of hot water supply operation in non-bypass state + heating operation in burner heating state)
Compared with the case where the hot water supply operation in the non-bypass state and the heating operation in the burner heating state are performed simultaneously, compared to the case where the hot water supply operation in the non-bypass state and the heating operation in the heat pump heating state shown in FIG. 30 are performed simultaneously. The parts through which water and the heat medium flow are the same, and only the states of the burner combustion device N and the heat pump device 4 are different.
The operation control means 19 switches the heat pump device 4 to the non-operating state, switches the burner combustion device N to the combustion state, operates the circulation pump 3 and the first heat medium circulation pump 15, and outputs from the fourth flow path part R4. The opening / closing operations of the second on-off valve K2 and the third on-off valve K3 are controlled so as to supply water to the first load heat exchanger 7a. As a result, the operation control means 19 uses the hot water supply operation in which the water in the hot water supply tank 2 is heated by the burner heating type heat exchanger 6 in the first water passage W1 and supplied to the hot water supply use location 1, and the burner in the second water passage W2. The heating operation in the burner heating state in which the water heated by the heating heat exchanger 6 is supplied to the first load heat exchanger 7a can be performed simultaneously.

(蓄熱運転+ヒートポンプ加熱状態での暖房運転の同時運転)
蓄熱運転とヒートポンプ加熱状態での暖房運転とを同時に行う場合には、運転制御手段19は、図31に示すように、ヒートポンプ装置4を作動状態に切り換え、バーナー燃焼装置Nを非燃焼状態に切り換え、循環ポンプ3及び第1熱媒循環ポンプ15を作動させるとともに、第4流路部位R4からの水を第1負荷熱交換器7aに供給するように第2開閉弁K2及び第3開閉弁K3の開閉動作を制御し、給湯タンク2から第1流路部位R1に取り出した水を第7流路部位R7に供給する状態に第1切換弁S1を切り換え、第2比例弁H2を閉動作させたままとし、第3比例弁H3、及び、第4比例弁H4を開動作させる。これにより、ヒートポンプ加熱式熱交換器5にて加熱された水を給湯タンク2に供給して給湯タンク2への蓄熱を行う蓄熱運転と、ヒートポンプ加熱式熱交換器5にて加熱された水を第1負荷熱交換器7aに供給するヒートポンプ加熱状態での暖房運転とを同時に行うことができる。
(Simultaneous operation of heat storage operation + heating operation in heat pump heating state)
When simultaneously performing the heat storage operation and the heating operation in the heat pump heating state, the operation control means 19 switches the heat pump device 4 to the operating state and switches the burner combustion device N to the non-burning state, as shown in FIG. The second on-off valve K2 and the third on-off valve K3 are operated so that the circulation pump 3 and the first heat medium circulation pump 15 are operated and the water from the fourth flow path part R4 is supplied to the first load heat exchanger 7a. The first switching valve S1 is switched to a state where the water taken out from the hot water supply tank 2 to the first flow path part R1 is supplied to the seventh flow path part R7, and the second proportional valve H2 is closed. The third proportional valve H3 and the fourth proportional valve H4 are opened. Thereby, the heat storage operation which supplies the water heated by the heat pump heating type heat exchanger 5 to the hot water supply tank 2 to store heat in the hot water supply tank 2, and the water heated by the heat pump heating type heat exchanger 5 The heating operation in the heat pump heating state supplied to the first load heat exchanger 7a can be performed simultaneously.

ここで、蓄熱運転中にバーナー加熱状態での暖房運転を行う場合等、蓄熱運転とバーナー加熱状態での暖房運転との同時運転を行う場合は、運転制御手段19は、蓄熱運転とバーナー加熱状態での暖房運転との同時運転を行わず、蓄熱運転を強制停止して、バーナー加熱状態での暖房運転のみを行うように構成されている。   Here, in the case of performing the simultaneous operation of the heat storage operation and the heating operation in the burner heating state, such as when performing the heating operation in the burner heating state during the heat storage operation, the operation control means 19 is provided with the heat storage operation and the burner heating state. The heat storage operation is forcibly stopped and only the heating operation in the burner heating state is performed without performing the simultaneous operation with the heating operation.

(給湯運転+追焚運転の同時運転)
バイパス状態での給湯運転とヒートポンプ加熱状態での追焚運転とを同時に行う場合は、図29に示すバイパス状態での給湯運転とヒートポンプ加熱状態での暖房運転とを同時に行う場合と比べて、ヒートポンプ加熱式熱交換器5にて加熱した水を第2負荷熱交換器7bに供給する点が異なるだけである。
非バイパス状態での給湯運転とヒートポンプ加熱状態での追焚運転とを同時に行う場合は、図30に示す非バイパス状態での給湯運転とヒートポンプ加熱状態での暖房運転とを同時に行う場合と比べて、ヒートポンプ加熱式熱交換器5にて加熱した水を第2負荷熱交換器7bに供給する点が異なるだけである。
(Simultaneous operation of hot water supply operation + memorial operation)
When the hot water supply operation in the bypass state and the memorial operation in the heat pump heating state are performed simultaneously, the heat pump is compared with the case where the hot water supply operation in the bypass state and the heating operation in the heat pump heating state are performed simultaneously as shown in FIG. The only difference is that the water heated by the heating heat exchanger 5 is supplied to the second load heat exchanger 7b.
Compared with the case where the hot water supply operation in the non-bypass state and the chasing operation in the heat pump heating state are performed at the same time as compared with the case where the hot water supply operation in the non-bypass state and the heating operation in the heat pump heating state are performed simultaneously as shown in FIG. The only difference is that the water heated by the heat pump heating type heat exchanger 5 is supplied to the second load heat exchanger 7b.

バイパス状態での給湯運転とバーナー加熱状態での追焚運転とを同時に行う場合も、バイパス状態での給湯運転とバーナー加熱状態での暖房運転とを同時に行う場合と比べて、バーナー加熱式熱交換器6にて加熱した水を第2負荷熱交換器7bに供給する点が異なるだけである。
非バイパス状態での給湯運転とバーナー加熱状態での追焚運転とを同時に行う場合も、非バイパス状態での給湯運転とバーナー加熱状態での暖房運転とを同時に行う場合と比べて、バーナー加熱式熱交換器6にて加熱した水を第2負荷熱交換器7bに供給する点が異なるだけである。
Compared with simultaneous hot water supply operation in the bypass state and heating operation in the burner heating state, both the hot water supply operation in the bypass state and the memorial operation in the burner heating state are performed simultaneously. The only difference is that the water heated in the vessel 6 is supplied to the second load heat exchanger 7b.
Burner heating type when hot water supply operation in a non-bypass state and a chasing operation in a burner heating state are performed at the same time as compared with a case in which hot water supply operation in a non-bypass state and heating operation in a burner heating state are performed simultaneously. The only difference is that the water heated by the heat exchanger 6 is supplied to the second load heat exchanger 7b.

(蓄熱運転+追焚運転の同時運転)
蓄熱運転とヒートポンプ加熱状態での追焚運転とを同時に行う場合は、図31に示す蓄熱運転とヒートポンプ加熱状態での暖房運転とを同時に行う場合と比べて、ヒートポンプ加熱式熱交換器5にて加熱した水を第2負荷熱交換器7bに供給する点が異なるだけである。
ここで、蓄熱運転中にバーナー加熱状態での追焚運転を行う場合等、蓄熱運転とバーナー加熱状態での追焚運転との同時運転を行う場合は、運転制御手段19は、蓄熱運転とバーナー加熱状態での追焚運転との同時運転を行わず、蓄熱運転を強制停止して、バーナー加熱状態での追焚運転のみを行うように構成されている。
(Simultaneous operation of heat storage operation + memorial operation)
In the case where the heat storage operation and the memorial operation in the heat pump heating state are performed simultaneously, the heat pump heating type heat exchanger 5 is compared with the case where the heat storage operation and the heating operation in the heat pump heating state shown in FIG. 31 are performed simultaneously. The only difference is that the heated water is supplied to the second load heat exchanger 7b.
Here, in the case of performing simultaneous operation of the heat storage operation and the chasing operation in the burner heating state, such as when performing the chasing operation in the burner heating state during the heat accumulating operation, the operation control means 19 includes the heat storage operation and the burner. The heat storage operation is forcibly stopped without performing simultaneous operation with the chasing operation in the heating state, and only the chasing operation in the burner heating state is performed.

(蓄熱運転中にバイパス状態での給湯運転を行う場合)
蓄熱運転中にバイパス状態での給湯運転を行う場合には、図32に示すように、運転制御手段19は、ヒートポンプ装置4を作動状態に切り換え、バーナー燃焼装置Nを非燃焼状態に切り換え、循環ポンプ3を作動させ、第1流路部位R1の水の一部をそのまま給湯タンク2に給水するとともに、第1流路部位R1の水の残りの一部を第7流路部位R7に供給する状態に第1切換弁S1を切り換え、第2比例弁H2を閉動作させたままとし、第3比例弁H3及び第4比例弁H4を開動作させる。これにより、運転制御手段19は、第1バイパス水路V1にて給湯タンク2の水をバーナー加熱式熱交換器6をバイパスして給湯利用箇所1に供給する給湯運転に加え、ヒートポンプ加熱式熱交換器5にて加熱された水をも給湯利用箇所1に供給するようにしている。
(When performing hot water supply operation in bypass state during heat storage operation)
When performing the hot water supply operation in the bypass state during the heat storage operation, as shown in FIG. 32, the operation control means 19 switches the heat pump device 4 to the operating state, switches the burner combustion device N to the non-combustion state, and circulates. The pump 3 is operated to supply a part of the water in the first flow path part R1 to the hot water tank 2 as it is, and supply the remaining part of the water in the first flow path part R1 to the seventh flow path part R7. The first switching valve S1 is switched to the state, the second proportional valve H2 is kept closed, and the third proportional valve H3 and the fourth proportional valve H4 are opened. Thereby, the operation control means 19 adds to the hot water supply operation which bypasses the burner heating type heat exchanger 6 and supplies the water in the hot water supply tank 2 to the hot water use location 1 in the first bypass water channel V1, and heat pump heating type heat exchange. The water heated by the vessel 5 is also supplied to the hot water supply use location 1.

(蓄熱運転中に非バイパス状態での給湯運転を行う場合)
蓄熱運転中に非バイパス状態での給湯運転を行う場合には、図25に示す非バイパス状態での給湯運転を行う場合と比べて、水や熱媒の通流する部位は同様であり、ヒートポンプ装置4の状態が異なるだけであるので、図示を省略して説明する。
運転制御手段19は、ヒートポンプ装置4を作動状態に切り換え、バーナー燃焼装置Nを燃焼状態に切り換え、循環ポンプ3を作動させ、第1流路部位R1にてそのまま給湯タンク2に給水する状態に第1切換弁S1を切り換え、第3比例弁H3を閉動作させたままとし、第2比例弁H2及び第4比例弁H4を開動作させる。これにより、運転制御手段19は、第1水路W1にて給湯タンク2の水をバーナー加熱式熱交換器6を経由して給湯利用箇所1に供給する給湯運転に加え、ヒートポンプ加熱式熱交換器5にて加熱された水をも給湯利用箇所1に供給するようにしている。
(When performing hot water supply operation in non-bypass state during heat storage operation)
When the hot water supply operation in the non-bypass state is performed during the heat storage operation, the portion through which water or the heat medium flows is the same as in the case of performing the hot water supply operation in the non-bypass state shown in FIG. Since only the state of the device 4 is different, the illustration is omitted.
The operation control means 19 switches the heat pump device 4 to the operating state, switches the burner combustion device N to the combustion state, operates the circulation pump 3, and supplies water to the hot water supply tank 2 as it is in the first flow path portion R1. The first switching valve S1 is switched, the third proportional valve H3 is kept closed, and the second proportional valve H2 and the fourth proportional valve H4 are opened. Thereby, the operation control means 19 is added to the hot water supply operation which supplies the water of the hot water supply tank 2 to the hot water supply use location 1 via the burner heating type heat exchanger 6 in the first water channel W1, and the heat pump heating type heat exchanger. The water heated at 5 is also supplied to the hot water supply use location 1.

(高温加熱運転)
この高温加熱運転では、図33に示すように、運転制御手段19が、バーナー燃焼装置Nを燃焼状態に切り換え、ヒートポンプ装置4を非作動状態に切り換え、循環ポンプ3を作動させるとともに、給湯タンク2から第1流路部位R1に取り出した水を第7流路部位R7に供給する状態に第1切換弁S1を切り換え、第2比例弁H2、第3比例弁H3、及び、第4比例弁H4を開動作させる。これにより、給湯タンク2の下部から取り出した水を、第1流路部位R1、第7流路部位R7、第6流路部位R6、第2流路部位R2の順に経由してバーナー加熱式熱交換器6に供給して加熱し、その加熱された水を、第3流路部位R3、第1バイパス流路部位B1、第2流路部位R2の順に経由して給湯タンク2の上部に戻している。第1バイパス流路部位B1を経由した水は、その一部が第2流路部位R2を経由して給湯タンク2の上部に供給され、残りの一部が第2流路部位R2を経由してバーナー加熱式熱交換器6に供給されている。第3水路W3は、図27に示すように、上述の蓄熱運転にて述べた如く、少なくとも第1バイパス水路V1の一部から構成されているが、この少なくとも第1バイパス水路V1の一部から構成されている第3水路W3は、給湯タンク2から取り出した水をバーナー加熱式熱交換器6にて加熱し、その加熱された水を給湯タンク2に戻すように水を循環自在に構成されている。そして、バーナー加熱式熱交換器6にて加熱された水を給湯タンク2に戻すことにより、給湯タンク2の水を高温として殺菌消毒することができるので、レジオネラ菌等の繁殖を適切に防止することができる。
(High temperature heating operation)
In this high temperature heating operation, as shown in FIG. 33, the operation control means 19 switches the burner combustion device N to the combustion state, switches the heat pump device 4 to the non-operation state, operates the circulation pump 3, and hot water supply tank 2 The first switching valve S1 is switched to a state where the water taken out from the first flow passage portion R1 is supplied to the seventh flow passage portion R7, and the second proportional valve H2, the third proportional valve H3, and the fourth proportional valve H4. Is opened. Thereby, the water taken out from the lower part of the hot water supply tank 2 is burner-heated heat via the first flow path part R1, the seventh flow path part R7, the sixth flow path part R6, and the second flow path part R2. It is supplied to the exchanger 6 and heated, and the heated water is returned to the upper part of the hot water supply tank 2 through the third flow path part R3, the first bypass flow path part B1, and the second flow path part R2 in this order. ing. A part of the water that has passed through the first bypass flow path part B1 is supplied to the upper part of the hot water tank 2 via the second flow path part R2, and the remaining part of the water passes through the second flow path part R2. The burner heating type heat exchanger 6 is supplied. As shown in FIG. 27, the third water channel W3 is composed of at least a part of the first bypass water channel V1, as described in the above heat storage operation, but from at least a part of the first bypass water channel V1. The configured third water channel W3 is configured to freely circulate the water so that the water taken out from the hot water supply tank 2 is heated by the burner heating type heat exchanger 6 and the heated water is returned to the hot water supply tank 2. ing. And since the water heated by the burner heating type heat exchanger 6 is returned to the hot water supply tank 2, the water in the hot water supply tank 2 can be sterilized and disinfected at a high temperature, so that breeding of Legionella bacteria and the like is appropriately prevented. be able to.

この第7実施形態においても、上述の第4実施形態にて述べた如く、図20に示すように、給湯タンク2の水を加熱するための構成を追加することもできる。また、この第7実施形態においても、上述の第5実施形態にて述べた如く、図21に示すように、第1負荷熱交換器7aと第2負荷熱交換器7bを直列状態で設けることもできる。   Also in the seventh embodiment, as described in the fourth embodiment, a configuration for heating the water in the hot water supply tank 2 can be added as shown in FIG. Also in the seventh embodiment, as described in the fifth embodiment, as shown in FIG. 21, the first load heat exchanger 7a and the second load heat exchanger 7b are provided in series. You can also.

〔第8実施形態〕
この第8実施形態は、上記第7実施形態と同様に、上記第2実施形態におけるヒートポンプ加熱式熱交換器5の配置形態の別実施形態である。その他の構成については、上記第2実施形態と同様であるので、その他の構成については説明を省略し、ヒートポンプ加熱式熱交換器5の配置形態を中心に説明する。
[Eighth Embodiment]
This 8th Embodiment is another embodiment of the arrangement | positioning form of the heat pump heating type heat exchanger 5 in the said 2nd Embodiment similarly to the said 7th Embodiment. Since the other configuration is the same as that of the second embodiment, the description of the other configuration is omitted, and the arrangement of the heat pump heating type heat exchanger 5 will be mainly described.

この第8実施形態では、図34に示すように、第2流路部位R2において第6流路部位R6の接続箇所と循環ポンプ3との間の部位に、ヒートポンプ加熱式熱交換器5が配置されている。そして、この第8実施形態では、上記第7実施形態と同様に、第6流路部位R6が、負荷熱交換器7と第2流路部位R2における給湯タンク2とヒートポンプ加熱式熱交換器5の間の部位に接続するように構成されており、第5流路部位R5が備えられていない。   In the eighth embodiment, as shown in FIG. 34, the heat pump heating type heat exchanger 5 is arranged in a portion between the connection portion of the sixth flow passage portion R6 and the circulation pump 3 in the second flow passage portion R2. Has been. In the eighth embodiment, as in the seventh embodiment, the sixth flow path portion R6 includes the load heat exchanger 7 and the hot water supply tank 2 and the heat pump heating heat exchanger 5 in the second flow path portion R2. The fifth channel portion R5 is not provided.

つまり、この第8実施形態では、流路部位として、給湯タンク2に接続されて上水を給湯タンク2に給水する第1流路部位R1と、給湯タンク2とバーナー加熱式熱交換器6を接続して、給湯タンク2に近い順にヒートポンプ加熱式熱交換器5と循環ポンプ3が設けられた第2流路部位R2と、バーナー加熱式熱交換器6と給湯利用箇所1を接続する第3流路部位R3と、第3流路部位R3の途中部位と負荷熱交換器7を接続する第4流路部位R4と、負荷熱交換器7と第2流路部位R2における給湯タンク2とヒートポンプ加熱式熱交換器5の間の部位を接続する第6流路部位R6と、第1流路部位R1の途中部位と第6流路部位R6の途中部位とを接続する第7流路部位R7と、第2流路部位R2における給湯タンク2と第6流路部位R6への接続箇所までの間の部位及び第3流路部位R3における第4流路部位R4への接続箇所と給湯利用箇所1までの間の部位を接続する第1バイパス流路部位B1とを備えている。   That is, in the eighth embodiment, the first flow path portion R1 that is connected to the hot water supply tank 2 and supplies hot water to the hot water supply tank 2, and the hot water supply tank 2 and the burner heating type heat exchanger 6 are connected as the flow path portions. A third flow path part R2 provided with the heat pump heating type heat exchanger 5 and the circulation pump 3, the burner heating type heat exchanger 6 and the hot water supply use point 1 is connected in the order of connection to the hot water supply tank 2. The flow path part R3, the fourth flow path part R4 connecting the intermediate part of the third flow path part R3 and the load heat exchanger 7, the hot water supply tank 2 and the heat pump in the load heat exchanger 7 and the second flow path part R2 A sixth flow path part R6 that connects the parts between the heating heat exchangers 5, and a seventh flow path part R7 that connects the middle part of the first flow path part R1 and the middle part of the sixth flow path part R6. And the hot water supply tank 2 and the sixth flow path portion R in the second flow path portion R2. A first bypass flow path part B1 for connecting a part between the connection part and the connection part to the fourth flow path part R4 in the third flow path part R3 and a part between the hot water supply use part 1 and the third flow path part R3. ing.

そして、第1水路W1が、第1流路部位R1と給湯タンク2と第2流路部位R2とバーナー加熱式熱交換器6と第3流路部位R3とで構成されている。第1バイパス水路V1が、第1流路部位R1と給湯タンク2と第2流路部位R2の一部と第1バイパス流路部位B1と第3流路部位R3の一部とで構成されている。第2水路W2が、バーナー加熱式熱交換器6と第3流路部位R3の一部と第4流路部位R4と負荷熱交換器7と第6流路部位R6と第2流路部位の一部とで構成されている。第3水路W3は、給湯タンク2と第1流路部位R1の一部と第7流路部位R7と第6流路部位R6の一部と第2流路部位R2とバーナー加熱式熱交換器6と第3流路部位R3の一部と第1バイパス流路部位B1とで構成されている。これにより、第3水路W3は、第1バイパス水路V1における第1流路部位R1の一部、第2流路部位R2の一部及び第1バイパス流路部位B1を含んでいるので、第3水路W3は、少なくとも第1バイパス水路V1の一部から構成されている。   And the 1st water channel W1 is comprised by 1st flow-path part R1, the hot water supply tank 2, 2nd flow-path part R2, the burner heating type heat exchanger 6, and 3rd flow-path part R3. The first bypass water channel V1 is composed of the first flow path part R1, the hot water supply tank 2, a part of the second flow path part R2, the first bypass flow path part B1, and a part of the third flow path part R3. Yes. The second water channel W2 includes the burner heating type heat exchanger 6, part of the third flow path part R3, the fourth flow path part R4, the load heat exchanger 7, the sixth flow path part R6, and the second flow path part. It consists of a part. The third water channel W3 includes a hot water supply tank 2, a part of the first channel part R1, a seventh channel part R7, a part of the sixth channel part R6, a second channel part R2, and a burner heating type heat exchanger. 6 and a part of the third flow path part R3 and the first bypass flow path part B1. Thereby, since the 3rd waterway W3 contains a part of 1st flow path site | part R1 in the 1st bypass water channel V1, a part of 2nd flow path site | part R2, and 1st bypass flow path site | part B1, 3rd The water channel W3 is composed of at least a part of the first bypass water channel V1.

この第8実施形態においても、上記第7実施形態と同様に、運転制御手段19は、蓄熱運転、給湯運転、暖房運転、追焚運転、及び、高温加熱運転を実行可能であるが、上記第7実施形態と比べて、第2流路部位R2における循環ポンプ3とヒートポンプ加熱式熱交換器5の配置関係が水の通流方向で反対となっているだけであるので、各運転の説明については省略する。   Also in the eighth embodiment, as in the seventh embodiment, the operation control means 19 can execute a heat storage operation, a hot water supply operation, a heating operation, a memorial operation, and a high temperature heating operation. Compared to the seventh embodiment, the arrangement relationship between the circulation pump 3 and the heat pump heating heat exchanger 5 in the second flow path part R2 is merely opposite in the direction of water flow. Is omitted.

この第8実施形態においても、上述の第4実施形態にて述べた如く、図20に示すように、給湯タンク2の水を加熱するための構成を追加することもできる。また、この第8実施形態においても、上述の第5実施形態にて述べた如く、図21に示すように、第1負荷熱交換器7aと第2負荷熱交換器7bを直列状態で設けることもできる。   Also in the eighth embodiment, as described in the fourth embodiment, a configuration for heating the water in the hot water supply tank 2 can be added as shown in FIG. Also in the eighth embodiment, as described in the fifth embodiment, as shown in FIG. 21, the first load heat exchanger 7a and the second load heat exchanger 7b are provided in series. You can also.

〔第9実施形態〕
この第9実施形態では、上記第2、第7及び第8実施形態において、バーナー加熱式熱交換器6が、バーナー燃焼装置Nの燃焼ガスの顕熱により水を加熱する顕熱回収熱交換器6aとバーナー燃焼装置Nの燃焼ガスの潜熱により水を加熱する潜熱回収熱交換器6bとで構成されている。その他の構成については、上記第2、第7及び第8実施形態と同様であるので、その他の構成については説明を省略し、バーナー加熱式熱交換器6の構成を中心に説明する。
[Ninth Embodiment]
In the ninth embodiment, in the second, seventh and eighth embodiments, the sensible heat recovery heat exchanger in which the burner heating type heat exchanger 6 heats water by the sensible heat of the combustion gas of the burner combustion device N. 6a and a latent heat recovery heat exchanger 6b that heats water by the latent heat of the combustion gas of the burner combustion device N. Since other configurations are the same as those of the second, seventh, and eighth embodiments, description of other configurations is omitted, and the configuration of the burner heating type heat exchanger 6 will be mainly described.

図35に示すように、バーナー加熱式熱交換器6は、顕熱回収熱交換器6aと潜熱回収熱交換器6bとで構成されており、潜熱回収熱交換器6bと顕熱回収熱交換器6aは、第1水路W1における水の通流方向で、潜熱回収熱交換器6b、顕熱回収熱交換器6aの順に備えられている。つまり、第1水路W1の一部である第2流路部位R2は、給湯タンク2と顕熱回収熱交換器6aを接続しており、潜熱回収熱交換器6bは、その第2流路部位R2における第1バイパス流路部位B1との接続箇所から顕熱回収熱交換器6aまでの間の部位に備えられている。そして、給湯タンク2から取り出した水を第1バイパス水路V1の一部である第1バイパス流路部位B1を通して給湯利用箇所1に供給することで、第1バイパス水路V1は、潜熱回収熱交換器6b及び顕熱回収熱交換器6aをバイパスして給湯タンク2から取り出した水を給湯利用箇所1に供給している。図35では、上記第7実施形態において、バーナー加熱式熱交換器6を顕熱回収熱交換器6aと潜熱回収熱交換器6bとで構成し、その潜熱回収熱交換器6bを、第2流路部位R2における第1バイパス流路部位B1との接続箇所から第6流路部位R6との接続箇所までの間の部位に備えた場合を示している。この場合に、潜熱回収熱交換器6bの他の設置位置として、第2流路部位R2において、図35中、A点、B点、C点の何れかに備えることができる。   As shown in FIG. 35, the burner heating type heat exchanger 6 includes a sensible heat recovery heat exchanger 6a and a latent heat recovery heat exchanger 6b, and the latent heat recovery heat exchanger 6b and the sensible heat recovery heat exchanger. 6a is a flow direction of water in the first water channel W1, and is provided in the order of a latent heat recovery heat exchanger 6b and a sensible heat recovery heat exchanger 6a. That is, the second flow path part R2 which is a part of the first water channel W1 connects the hot water supply tank 2 and the sensible heat recovery heat exchanger 6a, and the latent heat recovery heat exchanger 6b is the second flow path part. It is provided in a portion between the connection portion with the first bypass flow passage portion B1 in R2 and the sensible heat recovery heat exchanger 6a. And the 1st bypass water channel V1 is a latent heat recovery heat exchanger by supplying the water taken out from the hot water supply tank 2 to the hot water supply use location 1 through the first bypass flow channel site B1 which is a part of the first bypass water channel V1. 6 b and the sensible heat recovery heat exchanger 6 a are bypassed, and the water taken out from the hot water supply tank 2 is supplied to the hot water supply use location 1. In FIG. 35, in the seventh embodiment, the burner heating type heat exchanger 6 includes a sensible heat recovery heat exchanger 6a and a latent heat recovery heat exchanger 6b, and the latent heat recovery heat exchanger 6b is connected to the second flow. The case where it provided in the site | part from the connection location with 1st bypass flow-path site | part B1 in the path | route site | part R2 to the connection location with 6th flow-path site | part R6 is shown. In this case, as another installation position of the latent heat recovery heat exchanger 6b, the second flow path part R2 can be provided at any one of the points A, B, and C in FIG.

これにより、バイパス状態での給湯運転では、給湯タンク2から取り出した水が第1バイパス流路部位B1により潜熱回収熱交換器6b及び顕熱回収熱交換器6aをバイパスして給湯利用箇所1に供給することができる。したがって、潜熱回収熱交換器6b及び顕熱回収熱交換器6aを通過することによる放熱を防止できながら、給湯タンクの水をそのまま活用して給湯利用箇所1に給湯設定温度の水を供給することができる。
また、非バイパス状態での給湯運転では、給湯タンク2から取り出した水を第1水路W1により潜熱回収熱交換器6b及び顕熱回収熱交換器6aを経由して給湯利用箇所1に供給することができる。したがって、顕熱回収熱交換器6aにおける燃焼ガスの顕熱だけでなく、潜熱回収熱交換器6bにおける燃焼ガスの潜熱によっても水を加熱して加熱能力の向上を図ることで、省エネ性の向上を図ることができる。
Thereby, in the hot water supply operation in the bypass state, the water taken out from the hot water supply tank 2 bypasses the latent heat recovery heat exchanger 6b and the sensible heat recovery heat exchanger 6a by the first bypass flow path part B1, and enters the hot water supply use point 1. Can be supplied. Accordingly, while preventing heat radiation due to passing through the latent heat recovery heat exchanger 6b and the sensible heat recovery heat exchanger 6a, the water in the hot water supply tank 1 is used as it is and the water at the hot water supply set point 1 is supplied to the hot water use location 1. Can do.
Moreover, in the hot water supply operation in the non-bypass state, the water taken out from the hot water supply tank 2 is supplied to the hot water supply use location 1 through the first water passage W1 via the latent heat recovery heat exchanger 6b and the sensible heat recovery heat exchanger 6a. Can do. Therefore, not only the sensible heat of the combustion gas in the sensible heat recovery heat exchanger 6a but also the water is heated not only by the sensible heat of the combustion gas in the latent heat recovery heat exchanger 6b, but also by improving the heating capacity, thereby improving the energy saving performance. Can be achieved.

この第9実施形態においても、上述の第4実施形態にて述べた如く、図20に示すように、給湯タンク2の水を加熱するための構成を追加することもできる。また、この第9実施形態においても、上述の第5実施形態にて述べた如く、図21に示すように、第1負荷熱交換器7aと第2負荷熱交換器7bを直列状態で設けることもできる。   Also in the ninth embodiment, as described in the fourth embodiment, a configuration for heating the water in the hot water supply tank 2 can be added as shown in FIG. Also in the ninth embodiment, as described in the fifth embodiment, as shown in FIG. 21, the first load heat exchanger 7a and the second load heat exchanger 7b are provided in series. You can also.

〔別実施形態〕
(1)上記第1、第2及び第7実施形態では、暖房運転及び追焚運転において、運転制御手段19が、負荷熱交換器7で要求されている熱負荷に対して、バーナー加熱状態に切り換えた場合とヒートポンプ加熱状態に切り換えた場合との夫々の1次エネルギー消費量を求め、その求めた1次エネルギー消費量が小さい方に切り換えているが、この構成に代えて、例えば、高温暖房端末から運転要求があると、バーナー加熱状態での暖房運転を行い、低温暖房端末から運転要求があると、ヒートポンプ加熱状態での暖房運転を行うことができ、どの暖房端末から運転要求があるかによって、バーナー加熱状態とヒートポンプ加熱状態を切り換えて暖房運転を行うことができる。また、追焚運転として、浴槽水の温度を目標温度まで上昇させる時間が短い高速追焚運転と、その高速追焚運転よりも浴槽水の温度を目標温度まで上昇させる時間が長い低速追焚運転とを備え、高速追焚運転が要求されたときには、バーナー加熱状態での追焚運転を行い、低速追焚運転が要求されたときには、ヒートポンプ加熱状態での追焚運転を行い、高速追焚運転と低速追焚運転とのどちらが要求されているかによってバーナー加熱状態とヒートポンプ加熱状態を切り換えて追焚運転を行うことができる。また、運転制御手段19に、外気温度や浴槽温度等に基づいて、バーナー加熱状態とヒートポンプ加熱状態を切り換えるための切換条件を設定しておき、運転制御手段19が、切換条件を満たしているか否かによって、バーナー加熱状態とヒートポンプ加熱状態を切り換えて暖房運転及び追焚運転を行うこともできる。
[Another embodiment]
(1) In the first, second, and seventh embodiments, in the heating operation and the memorial operation, the operation control means 19 is in a burner heating state with respect to the heat load required by the load heat exchanger 7. The primary energy consumption amount in each of the case of switching and the case of switching to the heat pump heating state is obtained, and the obtained primary energy consumption amount is switched to a smaller one. When there is an operation request from the terminal, the heating operation is performed in the burner heating state, and when the operation request is from the low temperature heating terminal, the heating operation can be performed in the heat pump heating state, and from which heating terminal is the operation request Thus, the heating operation can be performed by switching between the burner heating state and the heat pump heating state. In addition, as a memorial operation, a high-speed memorial operation in which the time for raising the bath water temperature to the target temperature is short, and a low-speed memorial operation in which the time for raising the bath water temperature to the target temperature is longer than that in the high-speed memorial operation. When high-speed memorial operation is required, perform memorial operation in the burner heating state, and when low-speed memorial operation is requested, perform memorial operation in the heat pump heating state, and perform high-speed memorial operation Depending on whether the low-speed chasing operation or the low-speed chasing operation is required, the chasing operation can be performed by switching between the burner heating state and the heat pump heating state. Further, a switching condition for switching between the burner heating state and the heat pump heating state is set in the operation control means 19 based on the outside air temperature, the bathtub temperature, etc., and whether or not the operation control means 19 satisfies the switching condition. Depending on the situation, the heating operation and the chasing operation can be performed by switching between the burner heating state and the heat pump heating state.

(2)上記第1、第2及び第7実施形態では、COP(成績係数)が低下した状態でヒートポンプ装置4の運転が継続されるのを防止するために、給水手段20を備える構成を示したが、この構成に代えて、下記の構成を採用することもできる。
つまり、図4、図13及び図30に示すように、ヒートポンプ装置4を作動状態に切り換えている状態においてヒートポンプ加熱式熱交換器5に供給される水の温度が所定温度(例えば40℃)よりも高くなると、運転制御手段19は、ヒートポンプ装置4を作動状態から非作動状態に切り換えて、ヒートポンプ装置4の運転を停止する。これにより、COP(成績係数)が低下した状態でヒートポンプ装置4の運転が継続されるのを防止することができ、エネルギー効率が低下するのを防止することができる。この場合には、ヒートポンプ装置4を非作動状態に切り換えるので、ヒートポンプ加熱式熱交換器5では水を加熱することができないが、図4、図13及び図30に示すように、バーナー燃焼装置Nを燃焼状態に切り換えており、バーナー加熱式熱交換器6にて水を加熱することができるので、給湯利用箇所1への水の供給、及び、第1負荷熱交換器7aへの水の供給は継続して行うことができる。
(2) In the first, second, and seventh embodiments, the configuration including the water supply means 20 is shown in order to prevent the operation of the heat pump device 4 from being continued in a state where the COP (coefficient of performance) is lowered. However, the following configuration may be employed instead of this configuration.
That is, as shown in FIGS. 4, 13, and 30, the temperature of the water supplied to the heat pump heating type heat exchanger 5 is higher than a predetermined temperature (for example, 40 ° C.) in a state where the heat pump device 4 is switched to the operating state. If it becomes higher, the operation control means 19 switches the heat pump device 4 from the operating state to the non-operating state, and stops the operation of the heat pump device 4. Thereby, it is possible to prevent the operation of the heat pump device 4 from being continued in a state where the COP (coefficient of performance) is lowered, and it is possible to prevent the energy efficiency from being lowered. In this case, since the heat pump device 4 is switched to the non-operating state, the heat pump heating type heat exchanger 5 cannot heat water, but as shown in FIGS. 4, 13 and 30, the burner combustion device N Is switched to the combustion state, and the water can be heated by the burner heating type heat exchanger 6, so that water is supplied to the hot water supply location 1 and water is supplied to the first load heat exchanger 7a. Can continue.

(3)上記第1、第2及び第7実施形態では、第1開閉弁K1や第2開閉弁K2等の開閉弁を備える例を示しているが、この開閉弁に代えて、比例弁とすることもできる。例えば、第1開閉弁K1を第1比例弁とし、第2開閉弁K2を第2比例弁とすることができる。また、上記第2及び第7実施形態では、第2比例弁H2と第3比例弁H3に代えて、第2流路部位R2と第6流路部位R6の接続箇所に三方弁を備えることもできる。つまり、開閉弁や比例弁等の各種の弁については、比例弁や三方弁等の各種の弁に適宜変更することができる。 (3) In the first, second, and seventh embodiments, an example is shown in which an on-off valve such as the first on-off valve K1 or the second on-off valve K2 is provided. You can also For example, the first on-off valve K1 can be a first proportional valve and the second on-off valve K2 can be a second proportional valve. Moreover, in the said 2nd and 7th embodiment, it replaces with the 2nd proportional valve H2 and the 3rd proportional valve H3, and a three-way valve may be provided in the connection location of 2nd flow-path part R2 and 6th flow-path part R6. it can. That is, various valves such as on-off valves and proportional valves can be appropriately changed to various valves such as proportional valves and three-way valves.

本発明は、給湯利用箇所に供給する水を貯留する給湯タンクと、水路の水を循環させる循環ポンプと、ヒートポンプ装置により水を加熱するヒートポンプ加熱式熱交換器と、バーナー燃焼装置により水を加熱するバーナー加熱式熱交換器と、暖房負荷と追焚負荷の少なくとも一方で熱を消費する負荷熱交換器とを備え、配管が簡易でシンプルなものであり、熱交換器として構造が複雑な三流体熱交換器等の構造を採用する必要がなく、循環ポンプや熱交換器の数を極力少なくして、構成の簡素化及びコストの低減を図ることができる各種の熱媒供給装置に適応可能である。   The present invention relates to a hot water supply tank for storing water to be supplied to a hot water use location, a circulation pump for circulating water in a water channel, a heat pump heating heat exchanger for heating water by a heat pump device, and heating water by a burner combustion device. A heat exchanger that heats the burner and a load heat exchanger that consumes heat at least one of the heating load and the additional load, and the piping is simple and simple, and the heat exchanger has a complicated structure. It is not necessary to adopt a structure such as a fluid heat exchanger, and can be applied to various heat medium supply devices that can reduce the number of circulation pumps and heat exchangers as much as possible, simplifying the configuration and reducing costs. It is.

1 給湯利用箇所
2 給湯タンク
3 循環ポンプ
4 ヒートポンプ装置
5 ヒートポンプ加熱式熱交換器
6 バーナー加熱式熱交換器
6a 顕熱回収熱交換器
6b 潜熱回収熱交換器
7 負荷熱交換器
7a 第1負荷熱交換器
7b 第2負荷熱交換器
19 運転制御手段
B1 第1バイパス流路部位
V1 第1バイパス水路
W1 第1水路
W2 第2水路
W3 第3水路
X 排熱加熱水路
R1 第1流路部位
R2 第2流路部位
R3 第3流路部位
R4 第4流路部位
R5 第5流路部位
R6 第6流路部位
R7 第7流路部位
DESCRIPTION OF SYMBOLS 1 Hot water use location 2 Hot water tank 3 Circulation pump 4 Heat pump device 5 Heat pump heating type heat exchanger 6 Burner heating type heat exchanger 6a Sensible heat recovery heat exchanger 6b Latent heat recovery heat exchanger 7 Load heat exchanger 7a First load heat Exchanger 7b Second load heat exchanger 19 Operation control means B1 First bypass channel portion V1 First bypass channel W1 First channel W2 Second channel W3 Third channel X Waste heat heating channel R1 First channel region R2 First 2nd flow path part R3 3rd flow path part R4 4th flow path part R5 5th flow path part R6 6th flow path part R7 7th flow path part

Claims (23)

給湯利用箇所に供給する水を貯留する給湯タンクと、水路の水を循環させる循環ポンプと、ヒートポンプ装置により水を加熱するヒートポンプ加熱式熱交換器と、バーナー燃焼装置により水を加熱するバーナー加熱式熱交換器と、暖房負荷と追焚負荷の少なくとも一方で熱を消費する負荷熱交換器と、少なくとも上水の圧力で前記給湯タンクから取り出した水を少なくとも前記バーナー加熱式熱交換器を経由して前記給湯利用箇所に供給する第1水路と、前記循環ポンプの圧力で前記バーナー加熱式熱交換器と前記負荷熱交換器と前記ヒートポンプ加熱式熱交換器を経由して水が循環する第2水路とを備え、前記第1水路と前記第2水路は、前記バーナー加熱式熱交換器を含む水路が少なくとも共通に構成され、前記バーナー燃焼装置を燃焼状態と非燃焼状態とに切換自在であり、且つ、前記ヒートポンプ装置を作動状態と非作動状態とに切換自在な運転制御手段が備えられている熱媒供給装置。   A hot water supply tank for storing water to be supplied to a hot water supply location, a circulation pump for circulating water in the water channel, a heat pump heating type heat exchanger for heating water by a heat pump device, and a burner heating type for heating water by a burner combustion device A heat exchanger, a load heat exchanger that consumes heat in at least one of a heating load and a memorial load, and at least water taken out from the hot water tank at a pressure of clean water through the burner-heated heat exchanger A first water channel to be supplied to the hot water use location, and a second water that circulates through the burner heating heat exchanger, the load heat exchanger, and the heat pump heating heat exchanger at a pressure of the circulation pump. A water channel, and the first water channel and the second water channel are configured to share at least a water channel including the burner-heated heat exchanger, and burn the burner combustion device. On purpose it is freely switched to the non-combustion state, and, a heating medium supply device capable of switching the operation control means is provided to the operating state and the inoperative state the heat pump device. 前記給湯タンクに接続されて上水を前記給湯タンクに給水する第1流路部位と、前記給湯タンクと前記バーナー加熱式熱交換器を接続する第2流路部位と、前記バーナー加熱式熱交換器と前記給湯利用箇所を接続する第3流路部位と、前記第3流路部位の途中部位と前記負荷熱交換器を接続する第4流路部位と、前記負荷熱交換器と前記ヒートポンプ加熱式熱交換器を接続する第5流路部位と、前記ヒートポンプ加熱式熱交換器と前記第2流路部位の途中部位を接続して前記循環ポンプが設けられた第6流路部位とを備え、
前記第1水路が、前記第1流路部位と前記給湯タンクと前記第2流路部位と前記バーナー加熱式熱交換器と前記第3流路部位と前記第4流路部位と前記負荷熱交換器と前記第5流路部位と前記ヒートポンプ加熱式熱交換器と前記第6流路部位とで構成され、前記第2水路が、前記バーナー加熱式熱交換器と前記第3流路部位の一部と前記第4流路部位と前記負荷熱交換器と前記第5流路部位と前記ヒートポンプ加熱式熱交換器と前記第6流路部位と前記第2流路部位の一部とで構成されている請求項1に記載の熱媒供給装置。
A first flow path portion connected to the hot water tank for supplying clean water to the hot water tank, a second flow path portion for connecting the hot water tank and the burner heating heat exchanger, and the burner heating heat exchange A third flow path part for connecting a hot water supply and the hot water supply use location, a fourth flow path part for connecting the intermediate part of the third flow path part and the load heat exchanger, the load heat exchanger and the heat pump heating A fifth flow path portion that connects the heat exchanger, and a sixth flow path portion that connects the heat pump heating heat exchanger and a middle portion of the second flow path portion and is provided with the circulation pump. ,
The first water channel includes the first channel part, the hot water tank, the second channel part, the burner heating heat exchanger, the third channel part, the fourth channel part, and the load heat exchange. And the fifth flow path part, the heat pump heating heat exchanger and the sixth flow path part, and the second water channel is one of the burner heating heat exchanger and the third flow path part. Part, the fourth flow path part, the load heat exchanger, the fifth flow path part, the heat pump heating type heat exchanger, the sixth flow path part, and a part of the second flow path part. The heating medium supply device according to claim 1.
前記運転制御手段は、前記第1水路により前記給湯利用箇所に水を供給する給湯運転と、前記循環ポンプを作動させて前記バーナー燃焼装置を非燃焼状態に切り換え且つ前記ヒートポンプ装置を作動状態に切り換えて前記第2水路により前記ヒートポンプ加熱式熱交換器にて加熱された水を前記負荷熱交換器に供給するヒートポンプ加熱状態での熱消費運転と、前記循環ポンプを作動させて前記バーナー燃焼装置を燃焼状態に切り換え且つ前記ヒートポンプ装置を非作動状態に切り換えて前記第2水路により前記バーナー加熱式熱交換器にて加熱された水を前記負荷熱交換器に供給するバーナー加熱状態での熱消費運転とを実行可能に構成されている請求項1又は2に記載の熱媒供給装置。   The operation control means includes a hot water supply operation for supplying water to the hot water supply use location through the first water channel, the circulation pump is operated to switch the burner combustion device to a non-combustion state, and the heat pump device is switched to an operation state. The heat consumption operation in a heat pump heating state in which water heated by the heat pump heating type heat exchanger through the second water channel is supplied to the load heat exchanger, and the circulation pump is operated to operate the burner combustion apparatus. Switching to a combustion state and switching the heat pump device to a non-operating state and supplying water heated in the burner heating heat exchanger by the second water channel to the load heat exchanger in a heat consumption operation in a burner heating state The heat-medium supply apparatus of Claim 1 or 2 comprised so that execution is possible. 前記循環ポンプの圧力で少なくとも前記給湯タンクと前記ヒートポンプ加熱式熱交換器を経由して水が循環する第3水路を備え、前記第3水路によって、前記給湯タンクから取り出した水を前記ヒートポンプ加熱式熱交換器にて加熱し、その加熱された水を前記給湯タンクに戻すように水を循環自在に構成され、前記第2水路と前記第3水路は、前記ヒートポンプ加熱式熱交換器を含む水路が少なくとも共通に構成されている請求項1〜3の何れか1項に記載の熱媒供給装置。   A third water passage through which water circulates at least via the hot water supply tank and the heat pump heating type heat exchanger at a pressure of the circulation pump, and the water taken out from the hot water supply tank is supplied to the heat pump heating type by the third water passage; Water is configured to be freely circulated so that the heated water is returned to the hot water supply tank, and the second water channel and the third water channel are water channels including the heat pump heating type heat exchanger. The heating medium supply device according to any one of claims 1 to 3, wherein the at least one is configured in common. 前記給湯タンクに接続されて上水を前記給湯タンクに給水する第1流路部位と、前記給湯タンクと前記バーナー加熱式熱交換器を接続する第2流路部位と、前記負荷熱交換器と前記ヒートポンプ加熱式熱交換器を接続する第5流路部位と、前記ヒートポンプ加熱式熱交換器と前記第2流路部位の途中部位を接続して前記循環ポンプが設けられた第6流路部位と、前記第1流路部位の途中部位と前記第5流路部位の途中部位とを接続する第7流路部位とを備え、
前記第3水路が、前記給湯タンクと前記第1流路部位の一部と前記第7流路部位と前記第5流路部位の一部と前記ヒートポンプ加熱式熱交換器と前記第6流路部位と前記第2流路部位の一部とで構成されている請求項4に記載の熱媒供給装置。
A first flow path portion connected to the hot water supply tank for supplying clean water to the hot water supply tank; a second flow path portion connecting the hot water supply tank and the burner heating heat exchanger; and the load heat exchanger; A fifth flow path part for connecting the heat pump heating heat exchanger, and a sixth flow path part for connecting the intermediate part of the heat pump heating heat exchanger and the second flow path part to provide the circulation pump And a seventh flow path part for connecting a midway part of the first flow path part and a midway part of the fifth flow path part,
The third water channel includes the hot water supply tank, a part of the first channel part, the seventh channel part, a part of the fifth channel part, the heat pump heating heat exchanger, and the sixth channel. The heat-medium supply apparatus of Claim 4 comprised by the site | part and a part of said 2nd flow-path site | part.
前記運転制御手段は、前記循環ポンプを作動させて前記ヒートポンプ装置を作動状態に切り換えて前記第3水路により前記ヒートポンプ加熱式熱交換器にて加熱された水を前記給湯タンクに供給する蓄熱運転を実行可能に構成されている請求項4又は5に記載の熱媒供給装置。   The operation control means performs a heat storage operation for operating the circulation pump to switch the heat pump device to an operating state and supplying water heated by the heat pump heating heat exchanger through the third water channel to the hot water supply tank. The heating medium supply device according to claim 4 or 5, which is configured to be executable. 前記第2水路と前記第3水路は、前記給湯タンクから取り出した水を前記バーナー加熱式熱交換器にて加熱し、その加熱された水を前記給湯タンクに戻すように水を循環自在に構成されている請求項4〜6の何れか1項に記載の熱媒供給装置。   The second water channel and the third water channel are configured such that water extracted from the hot water supply tank is heated by the burner heating type heat exchanger, and water can be circulated so as to return the heated water to the hot water supply tank. The heating-medium supply apparatus of any one of Claims 4-6. 少なくとも前記バーナー加熱式熱交換器をバイパスして前記循環ポンプの圧力を使わずに上水の圧力で前記給湯タンクから取り出した水を前記給湯利用箇所に供給する第1バイパス水路を形成可能に構成されている請求項1に記載の熱媒供給装置。   It is possible to form a first bypass water channel that bypasses at least the burner heating type heat exchanger and supplies water taken out from the hot water supply tank with the pressure of clean water without using the pressure of the circulation pump to the hot water use location. The heating medium supply device according to claim 1. 前記給湯タンクに接続されて上水を前記給湯タンクに給水する第1流路部位と、前記給湯タンクと前記バーナー加熱式熱交換器を接続して前記循環ポンプが設けられた第2流路部位と、前記バーナー加熱式熱交換器と前記給湯利用箇所を接続する第3流路部位と、前記第3流路部位の途中部位と前記負荷熱交換器を接続する第4流路部位と、前記負荷熱交換器と前記ヒートポンプ加熱式熱交換器を接続する第5流路部位と、前記ヒートポンプ加熱式熱交換器と前記第2流路部位における前記給湯タンクと前記循環ポンプの間の部位を接続する第6流路部位と、前記第2流路部位における前記給湯タンクと前記第6流路部位への接続箇所までの間の部位及び前記第3流路部位における前記第4流路部位への接続箇所と前記給湯利用箇所までの間の部位を接続する第1バイパス流路部位とを備え、
前記第1水路が、前記第1流路部位と前記給湯タンクと前記第2流路部位と前記バーナー加熱式熱交換器と前記第3流路部位とで構成され、前記第1バイパス水路が、前記第1流路部位と前記給湯タンクと前記第2流路部位の一部と前記第1バイパス流路部位と前記第3流路部位の一部とで構成され、前記第2水路が、前記バーナー加熱式熱交換器と前記第3流路部位の一部と前記第4流路部位と前記負荷熱交換器と前記第5流路部位と前記ヒートポンプ加熱式熱交換器と前記第6流路部位と前記第2流路部位の一部とで構成されている請求項8に記載の熱媒供給装置。
A first flow path portion connected to the hot water supply tank for supplying clean water to the hot water supply tank, and a second flow path portion provided with the circulation pump by connecting the hot water supply tank and the burner heating heat exchanger. A third flow path portion connecting the burner heating type heat exchanger and the hot water supply utilization location, a fourth flow path portion connecting the load heat exchanger and a midway portion of the third flow path portion, A fifth flow path part for connecting the load heat exchanger and the heat pump heating type heat exchanger, and a part between the hot water supply tank and the circulation pump in the heat pump heating type heat exchanger and the second flow path part are connected. To the fourth flow path part in the third flow path part and the part between the hot water supply tank in the second flow path part and the connection part to the sixth flow path part. Between the connection point and the hot water use point And a first bypass passage portion for connecting site,
The first water channel is composed of the first channel part, the hot water tank, the second channel part, the burner heating heat exchanger, and the third channel part, and the first bypass channel is The first flow path part, the hot water tank, a part of the second flow path part, the first bypass flow path part, and a part of the third flow path part, the second water channel, Burner heating type heat exchanger, part of the third flow path part, the fourth flow path part, the load heat exchanger, the fifth flow path part, the heat pump heating type heat exchanger, and the sixth flow path The heat medium supply device according to claim 8, comprising a part and a part of the second flow path part.
前記運転制御手段は、前記給湯運転において、前記給湯タンクの水の温度が前記給湯利用箇所にて要求されている給湯設定温度に対応する切換設定温度以上である場合に、前記第1バイパス水路により前記給湯利用箇所に水を供給するバイパス状態に切り換え、前記給湯タンクの水の温度が前記切換設定温度未満である場合に、前記第1水路により前記給湯利用箇所に水を供給する非バイパス状態に切り換えるように構成されている請求項8又は9に記載の熱媒供給装置。   In the hot water supply operation, when the temperature of the water in the hot water supply tank is equal to or higher than a switching set temperature corresponding to the hot water supply set temperature required at the hot water supply use location, the operation control means uses the first bypass water channel. Switching to a bypass state in which water is supplied to the hot water use location, and when the temperature of the water in the hot water tank is lower than the switching set temperature, a non-bypass state is set in which water is supplied to the hot water usage location by the first water channel. The heat-medium supply apparatus of Claim 8 or 9 comprised so that it may switch. 前記運転制御手段は、前記第1水路により前記給湯利用箇所に水を供給する給湯運転と、前記循環ポンプを作動させて前記バーナー燃焼装置を非燃焼状態に切り換え且つ前記ヒートポンプ装置を作動状態に切り換えて前記第2水路により前記ヒートポンプ加熱式熱交換器にて加熱された水を前記負荷熱交換器に供給するヒートポンプ加熱状態での熱消費運転と、前記循環ポンプを作動させて前記バーナー燃焼装置を燃焼状態に切り換え且つ前記ヒートポンプ装置を非作動状態に切り換えて前記第2水路により前記バーナー加熱式熱交換器にて加熱された水を前記負荷熱交換器に供給するバーナー加熱状態での熱消費運転とを実行可能に構成されている請求項8〜10の何れか1項に記載の熱媒供給装置。   The operation control means includes a hot water supply operation for supplying water to the hot water supply use location through the first water channel, the circulation pump is operated to switch the burner combustion device to a non-combustion state, and the heat pump device is switched to an operation state. The heat consumption operation in a heat pump heating state in which water heated by the heat pump heating type heat exchanger through the second water channel is supplied to the load heat exchanger, and the circulation pump is operated to operate the burner combustion apparatus. Switching to a combustion state and switching the heat pump device to a non-operating state and supplying water heated in the burner heating heat exchanger by the second water channel to the load heat exchanger in a heat consumption operation in a burner heating state The heat medium supply device according to claim 8, wherein the heat medium supply device is configured to be executable. 前記循環ポンプの圧力で少なくとも前記給湯タンクと前記ヒートポンプ加熱式熱交換器を経由して水が循環する第3水路を備え、前記第3水路によって、前記給湯タンクから取り出した水を前記ヒートポンプ加熱式熱交換器にて加熱し、その加熱された水を前記給湯タンクに戻すように水を循環自在に構成され、前記第2水路と前記第3水路は、前記ヒートポンプ加熱式熱交換器を含む水路が少なくとも共通に構成されている請求項8〜11の何れか1項に記載の熱媒供給装置。   A third water passage through which water circulates at least via the hot water supply tank and the heat pump heating type heat exchanger at a pressure of the circulation pump, and the water taken out from the hot water supply tank is supplied to the heat pump heating type by the third water passage; Water is configured to be freely circulated so that the heated water is returned to the hot water supply tank, and the second water channel and the third water channel are water channels including the heat pump heating type heat exchanger. The heating medium supply device according to any one of claims 8 to 11, wherein the at least one is configured in common. 前記循環ポンプの圧力で少なくとも前記給湯タンクと前記ヒートポンプ加熱式熱交換器を経由して水が循環する第3水路が、少なくとも前記第1バイパス水路の一部で構成されている請求項8〜12の何れか1項に記載の熱媒供給装置。   The third water channel through which water circulates through at least the hot water supply tank and the heat pump heating heat exchanger at the pressure of the circulation pump is configured by at least a part of the first bypass water channel. The heating medium supply device according to any one of the above. 前記給湯タンクに接続されて上水を前記給湯タンクに給水する第1流路部位と、前記給湯タンクと前記バーナー加熱式熱交換器を接続して前記循環ポンプが設けられた第2流路部位と、前記バーナー加熱式熱交換器と前記給湯利用箇所を接続する第3流路部位と、前記第3流路部位の途中部位と前記負荷熱交換器を接続する第4流路部位と、前記負荷熱交換器と前記ヒートポンプ加熱式熱交換器を接続する第5流路部位と、前記ヒートポンプ加熱式熱交換器と前記第2流路部位における前記給湯タンクと前記循環ポンプの間の部位を接続する第6流路部位と、前記第1流路部位の途中部位と前記第5流路部位の途中部位とを接続する第7流路部位と、前記第2流路部位における前記給湯タンクと前記第6流路部位への接続箇所までの間の部位及び前記第3流路部位における前記第4流路部位への接続箇所と前記給湯利用箇所までの間の部位を接続する第1バイパス流路部位とを備え、
前記第1水路が、前記第1流路部位と前記給湯タンクと前記第2流路部位と前記バーナー加熱式熱交換器と前記第3流路部位とで構成され、前記第1バイパス水路が、前記第1流路部位と前記給湯タンクと前記第2流路部位の一部と前記第1バイパス流路部位と前記第3流路部位の一部とで構成され、前記第2水路が、前記バーナー加熱式熱交換器と前記第3流路部位の一部と前記第4流路部位と前記負荷熱交換器と前記第5流路部位と前記ヒートポンプ加熱式熱交換器と前記第6流路部位と前記第2流路部位の一部とで構成され、前記第3水路が、前記給湯タンクと前記第1流路部位の一部と前記第7流路部位と前記第5流路部位の一部と前記ヒートポンプ加熱式熱交換器と前記第6流路部位と前記第2流路部位と前記バーナー加熱式熱交換器と前記第3流路部位の一部と前記第1バイパス流路部位とで構成されている請求項13に記載の熱媒供給装置。
A first flow path portion connected to the hot water supply tank for supplying clean water to the hot water supply tank, and a second flow path portion provided with the circulation pump by connecting the hot water supply tank and the burner heating heat exchanger. A third flow path portion connecting the burner heating type heat exchanger and the hot water supply utilization location, a fourth flow path portion connecting the load heat exchanger and a midway portion of the third flow path portion, A fifth flow path part for connecting the load heat exchanger and the heat pump heating type heat exchanger, and a part between the hot water supply tank and the circulation pump in the heat pump heating type heat exchanger and the second flow path part are connected. A sixth flow path portion, a seventh flow path portion connecting a midway portion of the first flow path portion and a midway portion of the fifth flow path portion, the hot water supply tank in the second flow path portion, and the Part between the connection point to the sixth flow path part And a first bypass passage portion connected to a site until the hot water utilization portion and the connecting portion of the to fourth channel site in fine the third flow path part,
The first water channel is composed of the first channel part, the hot water tank, the second channel part, the burner heating heat exchanger, and the third channel part, and the first bypass channel is The first flow path part, the hot water tank, a part of the second flow path part, the first bypass flow path part, and a part of the third flow path part, the second water channel, Burner heating type heat exchanger, part of the third flow path part, the fourth flow path part, the load heat exchanger, the fifth flow path part, the heat pump heating type heat exchanger, and the sixth flow path And a part of the second flow path part, and the third water channel includes the hot water tank, a part of the first flow path part, the seventh flow path part, and the fifth flow path part. A part, the heat pump heating type heat exchanger, the sixth channel part, the second channel part, and the burner heating type heat exchanger Vessel and heating medium supply apparatus according to claim 13 which is composed of a part and the first bypass passage portion of the third flow path part.
前記給湯タンクに接続されて上水を前記給湯タンクに給水する第1流路部位と、前記給湯タンクと前記バーナー加熱式熱交換器を接続して、前記給湯タンクに近い順に前記循環ポンプと前記ヒートポンプ加熱式熱交換器が設けられた第2流路部位と、前記バーナー加熱式熱交換器と前記給湯利用箇所を接続する第3流路部位と、前記第3流路部位の途中部位と前記負荷熱交換器を接続する第4流路部位と、前記負荷熱交換器と前記第2流路部位における前記給湯タンクと前記循環ポンプの間の部位を接続する第6流路部位と、前記第1流路部位の途中部位と前記第6流路部位の途中部位とを接続する第7流路部位と、前記第2流路部位における前記給湯タンクと前記第6流路部位への接続箇所までの間の部位及び前記第3流路部位における前記第4流路部位への接続箇所と前記給湯利用箇所までの間の部位を接続する第1バイパス流路部位とを備え、
前記第1水路が、前記第1流路部位と前記給湯タンクと前記第2流路部位と前記バーナー加熱式熱交換器と前記第3流路部位とで構成され、前記第1バイパス水路が、前記第1流路部位と前記給湯タンクと前記第2流路部位の一部と前記第1バイパス流路部位と前記第3流路部位の一部とで構成され、前記第2水路が、前記バーナー加熱式熱交換器と前記第3流路部位の一部と前記第4流路部位と前記負荷熱交換器と前記第6流路部位と前記第2流路部位の一部とで構成され、前記第3水路が、前記給湯タンクと前記第1流路部位の一部と前記第7流路部位と前記第6流路部位の一部と前記第2流路部位と前記バーナー加熱式熱交換器と前記第3流路部位の一部と前記第1バイパス流路部位とで構成されている請求項13に記載の熱媒供給装置。
A first flow path portion connected to the hot water supply tank for supplying clean water to the hot water supply tank, the hot water supply tank and the burner heating heat exchanger are connected, and the circulation pump and the A second flow path portion provided with a heat pump heating heat exchanger, a third flow path portion connecting the burner heating heat exchanger and the hot water supply utilization location, a midway portion of the third flow path portion, and the A fourth flow path portion for connecting a load heat exchanger, a sixth flow path portion for connecting a portion between the hot water tank and the circulation pump in the load heat exchanger and the second flow path portion, and the first 7th flow path part which connects the middle part of the 1st flow path part and the middle part of the 6th flow path part, and the connection place to the hot water supply tank and the 6th flow path part in the 2nd flow path part In front of the part between and the third flow path part And a first bypass passage portion connected to a site until the hot water utilization portion and the connection into the fourth channel region,
The first water channel is composed of the first channel part, the hot water tank, the second channel part, the burner heating heat exchanger, and the third channel part, and the first bypass channel is The first flow path part, the hot water tank, a part of the second flow path part, the first bypass flow path part, and a part of the third flow path part, the second water channel, It comprises a burner heating type heat exchanger, a part of the third flow path part, the fourth flow path part, the load heat exchanger, the sixth flow path part, and a part of the second flow path part. The third water channel includes the hot water supply tank, a part of the first channel part, the seventh channel part, a part of the sixth channel part, the second channel part, and the burner heating type heat. The heating medium supply device according to claim 13, comprising an exchanger, a part of the third flow path part, and the first bypass flow path part. .
前記給湯タンクに接続されて上水を前記給湯タンクに給水する第1流路部位と、前記給湯タンクと前記バーナー加熱式熱交換器を接続して、前記給湯タンクに近い順に前記ヒートポンプ加熱式熱交換器と前記循環ポンプが設けられた第2流路部位と、前記バーナー加熱式熱交換器と前記給湯利用箇所を接続する第3流路部位と、前記第3流路部位の途中部位と前記負荷熱交換器を接続する第4流路部位と、前記負荷熱交換器と前記第2流路部位における前記給湯タンクと前記ヒートポンプ加熱式熱交換器の間の部位を接続する第6流路部位と、前記第1流路部位の途中部位と前記第6流路部位の途中部位とを接続する第7流路部位と、前記第2流路部位における前記給湯タンクと前記第6流路部位への接続箇所までの間の部位及び前記第3流路部位における前記第4流路部位への接続箇所と前記給湯利用箇所までの間の部位を接続する第1バイパス流路部位とを備え、
前記第1水路が、前記第1流路部位と前記給湯タンクと前記第2流路部位と前記バーナー加熱式熱交換器と前記第3流路部位とで構成され、前記第1バイパス水路が、前記第1流路部位と前記給湯タンクと前記第2流路部位の一部と前記第1バイパス流路部位と前記第3流路部位の一部とで構成され、前記第2水路が、前記バーナー加熱式熱交換器と前記第3流路部位の一部と前記第4流路部位と前記負荷熱交換器と前記第6流路部位と前記第2流路部位の一部とで構成され、前記第3水路が、前記給湯タンクと前記第1流路部位の一部と前記第7流路部位と前記第6流路部位の一部と前記第2流路部位と前記バーナー加熱式熱交換器と前記第3流路部位の一部と前記第1バイパス流路部位とで構成されている請求項13に記載の熱媒供給装置。
The heat pump heating type heat is connected to the hot water supply tank, connected to the first flow path part for supplying clean water to the hot water tank, the hot water tank and the burner heating type heat exchanger, and in order from the hot water tank. A second flow path portion provided with an exchanger and the circulation pump, a third flow path portion connecting the burner heating type heat exchanger and the hot water supply utilization location, an intermediate portion of the third flow path portion, and the A fourth flow path part for connecting the load heat exchanger, and a sixth flow path part for connecting a part between the hot water tank and the heat pump heating heat exchanger in the load heat exchanger and the second flow path part. And a seventh flow path portion connecting a midway portion of the first flow path portion and a midway portion of the sixth flow path portion, to the hot water supply tank and the sixth flow path portion in the second flow path portion And the third flow between the connection point and the third flow And a first bypass passage portion for connecting site between the connection point of the to fourth channel region at a site to the hot water usage position,
The first water channel is composed of the first channel part, the hot water tank, the second channel part, the burner heating heat exchanger, and the third channel part, and the first bypass channel is The first flow path part, the hot water tank, a part of the second flow path part, the first bypass flow path part, and a part of the third flow path part, the second water channel, It comprises a burner heating type heat exchanger, a part of the third flow path part, the fourth flow path part, the load heat exchanger, the sixth flow path part, and a part of the second flow path part. The third water channel includes the hot water supply tank, a part of the first channel part, the seventh channel part, a part of the sixth channel part, the second channel part, and the burner heating type heat. The heating medium supply device according to claim 13, comprising an exchanger, a part of the third flow path part, and the first bypass flow path part. .
前記運転制御手段は、前記循環ポンプを作動させて前記ヒートポンプ装置を作動状態に切り換えて前記第3水路により前記ヒートポンプ加熱式熱交換器にて加熱された水を前記給湯タンクに供給する蓄熱運転を実行可能に構成されている請求項12〜16の何れか1項に記載の熱媒供給装置。   The operation control means performs a heat storage operation for operating the circulation pump to switch the heat pump device to an operating state and supplying water heated by the heat pump heating heat exchanger through the third water channel to the hot water supply tank. The heat-medium supply apparatus of any one of Claims 12-16 comprised so that execution is possible. 少なくとも前記第1バイパス水路の一部で構成されている前記第3水路は、前記給湯タンクから取り出した水を前記バーナー加熱式熱交換器にて加熱し、その加熱された水を前記給湯タンクに戻すように水を循環自在に構成されている請求項12〜17の何れか1項に記載の熱媒供給装置。   The third water channel constituted by at least a part of the first bypass water channel heats the water taken out from the hot water supply tank by the burner heating type heat exchanger, and supplies the heated water to the hot water supply tank. The heating medium supply device according to any one of claims 12 to 17, wherein water is circulated so as to be returned. 前記バーナー加熱式熱交換器が、前記バーナー燃焼装置の燃焼ガスの顕熱により水を加熱する顕熱回収熱交換器と前記バーナー燃焼装置の燃焼ガスの潜熱により水を加熱する潜熱回収熱交換器とで構成され、前記潜熱回収熱交換器と前記顕熱回収熱交換器は、前記第1水路における水の通流方向で、前記潜熱回収熱交換器、前記顕熱回収熱交換器の順に備えられ、前記第1バイパス水路は、前記潜熱回収熱交換器及び前記顕熱回収熱交換器をバイパスして前記給湯タンクから取り出した水を前記給湯利用箇所に供給するように構成されている請求項8〜18の何れか1項に記載の熱媒供給装置。   The sensible heat recovery heat exchanger in which the burner heating type heat exchanger heats water by sensible heat of combustion gas of the burner combustion device, and a latent heat recovery heat exchanger in which water is heated by latent heat of combustion gas of the burner combustion device The latent heat recovery heat exchanger and the sensible heat recovery heat exchanger are provided in the order of the latent heat recovery heat exchanger and the sensible heat recovery heat exchanger in the flow direction of water in the first water channel. The first bypass water channel is configured to supply water extracted from the hot water supply tank by bypassing the latent heat recovery heat exchanger and the sensible heat recovery heat exchanger to the hot water use location. The heating medium supply device according to any one of 8 to 18. 前記運転制御手段は、前記バーナー燃焼装置を非燃焼状態に切り換え且つ前記ヒートポンプ装置を作動状態に切り換えて前記ヒートポンプ加熱式熱交換器にて加熱した水を前記負荷熱交換器に供給するヒートポンプ加熱状態と、前記バーナー燃焼装置を燃焼状態に切り換え且つ前記ヒートポンプ装置を非作動状態に切り換えて前記バーナー加熱式熱交換器にて加熱した水を前記負荷熱交換器に供給するバーナー加熱状態とに切換自在で、且つ、前記負荷熱交換器で要求されている熱負荷に対して、前記バーナー加熱状態に切り換えた場合と前記ヒートポンプ加熱状態に切り換えた場合との1次エネルギー消費量が小さい方を選択して切り換えるように構成されている請求項1〜19の何れか1項に記載の熱媒供給装置。   The operation control means is a heat pump heating state in which the burner combustion device is switched to a non-burning state and the heat pump device is switched to an operating state and water heated by the heat pump heating heat exchanger is supplied to the load heat exchanger The burner combustion device can be switched to a combustion state and the heat pump device can be switched to a non-operational state to switch to a burner heating state in which water heated by the burner heating heat exchanger is supplied to the load heat exchanger. In addition, for the heat load required in the load heat exchanger, the one with the smaller primary energy consumption when switched to the burner heating state and when switched to the heat pump heating state is selected. The heating medium supply device according to any one of claims 1 to 19, wherein the heating medium supply device is configured to be switched. 前記運転制御手段は、前記ヒートポンプ装置を作動状態に切り換えた状態において前記ヒートポンプ加熱式熱交換器に供給される水の温度が所定温度より高い場合に、前記ヒートポンプ装置を非作動状態に切り換える請求項1〜20の何れか1項に記載の熱媒供給装置。   The operation control means switches the heat pump device to a non-operating state when a temperature of water supplied to the heat pump heating heat exchanger is higher than a predetermined temperature in a state where the heat pump device is switched to an operating state. The heating medium supply device according to any one of 1 to 20. 前記第1水路により前記給湯利用箇所に水を供給しており前記ヒートポンプ装置を作動状態に切り換えた状態において前記ヒートポンプ加熱式熱交換器に供給される水の温度が所定温度より高い場合に、前記ヒートポンプ加熱式熱交換器に供給される水に給水して、前記ヒートポンプ加熱式熱交換器に供給される水の温度を前記所定温度以下に調整自在な給水手段が備えられている請求項1〜20の何れか1項に記載の熱媒供給装置。   When the temperature of the water supplied to the heat pump heating type heat exchanger is higher than a predetermined temperature in a state where water is supplied to the hot water use location by the first water channel and the heat pump device is switched to an operating state, A water supply means for supplying water to the water supplied to the heat pump heating type heat exchanger and capable of adjusting the temperature of the water supplied to the heat pump heating type heat exchanger below the predetermined temperature is provided. The heating medium supply device according to any one of 20. 前記給湯タンクから取り出した水を太陽熱にて加熱し、その加熱された水を前記給湯タンクに戻す太陽熱加熱水路と、前記給湯タンクから取り出した水を熱電併給装置にて発生した排熱にて加熱し、その加熱された水を前記給湯タンクに戻す排熱加熱水路の少なくとも一方が、少なくとも、前記循環ポンプの圧力で少なくとも前記給湯タンクと前記ヒートポンプ加熱式熱交換器を経由して水が循環する第3水路と兼用となっている請求項1〜22の何れか1項に記載の熱媒供給装置。   The water extracted from the hot water tank is heated by solar heat, the heated water is returned to the hot water tank, and the water extracted from the hot water tank is heated by exhaust heat generated by the combined heat and power supply device. Then, at least one of the exhaust heat heating water channels for returning the heated water to the hot water supply tank circulates at least through the hot water supply tank and the heat pump heating heat exchanger at least by the pressure of the circulation pump. The heating medium supply device according to any one of claims 1 to 22, which is also used as a third water channel.
JP2011173226A 2010-08-09 2011-08-08 Heating medium supply apparatus Withdrawn JP2012057932A (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013142491A (en) * 2012-01-10 2013-07-22 Rinnai Corp Hot water supply and heating apparatus
JP2013224769A (en) * 2012-04-20 2013-10-31 Asahi Kasei Homes Co Hot water supply system
JP2014142108A (en) * 2013-01-23 2014-08-07 Panasonic Corp Hot water supply system

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013142491A (en) * 2012-01-10 2013-07-22 Rinnai Corp Hot water supply and heating apparatus
JP2013224769A (en) * 2012-04-20 2013-10-31 Asahi Kasei Homes Co Hot water supply system
JP2014142108A (en) * 2013-01-23 2014-08-07 Panasonic Corp Hot water supply system

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