JP2006029745A - Hot water storage type hot water supplying heat source device - Google Patents

Hot water storage type hot water supplying heat source device Download PDF

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JP2006029745A
JP2006029745A JP2004213207A JP2004213207A JP2006029745A JP 2006029745 A JP2006029745 A JP 2006029745A JP 2004213207 A JP2004213207 A JP 2004213207A JP 2004213207 A JP2004213207 A JP 2004213207A JP 2006029745 A JP2006029745 A JP 2006029745A
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JP4716352B2 (en
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Akihito Hayano
彰人 早野
Kazuo Murase
一夫 村瀬
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Osaka Gas Co Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a hot water storage type hot water supplying heat source device capable of suitably executing water quality keeping operation for keeping water quality of hot water in a hot water storage tank. <P>SOLUTION: This device is provided with a heating auxiliary heating means 19w for heating a heat medium circulating in a heat medium circulating passage 21 having a heat radiating terminal 6, and a heating heat exchanger 11 for executing heat exchange between hot water supplied from a heating means H to the hot water storage tank 5 and the heat medium circulating in the heat medium circulating passage 21. A control means C executes operation for operating the heating means H as water quality keeping operation so that the state wherein a temperature of a whole of the hot water in the hot water storage tank 5 is equal to or higher than a set water quality keeping temperature is maintained for a set water quality keeping time period, and executes auxiliary temperature raising operation for operating the heating auxiliary heating means 19w in the state wherein the heat medium is circulated in the heat medium circulating passage 21 at least before the temperature of the whole of the hot water in the hot water storage tank 5 is equal to or higher than the set water quality keeping temperature during execution of water quality keeping operation. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

本発明は、給水路を通して給水され且つ給湯路を通して湯水が送出される貯湯タンクと、
その貯湯タンクの湯水を加熱する加熱手段と、
前記給湯路を通流する湯水を目標給湯温度に加熱する補助加熱手段と、
前記貯湯タンクに目標貯湯温度で貯湯されるように前記加熱手段の作動を制御する制御手段とが設けられた貯湯式の給湯熱源装置に関する。
The present invention includes a hot water storage tank that is supplied with water through a water supply channel and that is supplied with hot water through the hot water supply channel.
Heating means for heating the hot water in the hot water storage tank;
Auxiliary heating means for heating hot water flowing through the hot water supply path to a target hot water temperature;
The present invention relates to a hot water storage type hot water supply heat source device provided with a control means for controlling the operation of the heating means so that hot water is stored in the hot water storage tank at a target hot water storage temperature.

かかる貯湯式の給湯熱源装置(以下、単に給湯熱源装置と略称する場合がある)は、一戸建て住宅毎や集合住宅の住戸毎等のように、主として一般家庭毎に設置されるものであり、貯湯タンクに目標貯湯温度で貯湯されるように制御手段により加熱手段の作動が制御され、その貯湯タンクの湯水が給湯路を通して送出されて台所や風呂等の給湯箇所に供給されるようになっており、その給湯路を通流する湯水の温度が目標給湯温度よりも低いときは、補助加熱手段にて目標給湯温度に加熱されるようになっている。
そして、このような給湯熱源装置では、貯湯タンクの湯水の水質が低下する虞があるような状態が起こり得るので、貯湯タンクの湯水の水質を維持するための水質維持運転を実行するようになっている。
Such a hot water storage type hot water supply heat source device (hereinafter sometimes simply referred to as a hot water supply heat source device) is installed mainly in each general household, such as in each detached house or in each apartment house. The operation of the heating means is controlled by the control means so that the hot water is stored in the tank at the target hot water temperature, and the hot water in the hot water storage tank is sent through the hot water supply path and supplied to hot water supply places such as kitchens and baths. When the temperature of the hot water flowing through the hot water supply path is lower than the target hot water temperature, the auxiliary heating means heats the hot water to the target hot water temperature.
In such a hot water supply heat source device, since there is a possibility that the quality of the hot water in the hot water storage tank may be deteriorated, a water quality maintenance operation for maintaining the quality of the hot water in the hot water storage tank is executed. ing.

このように貯湯タンクの湯水の水質の低下を防止するための技術として、従来、毎朝等、定期的に、水質維持運転として、貯湯タンクから給湯路への湯水の送出を継続する状態で、貯湯タンクの湯水を水質維持温度に加熱する運転を実行する技術があった(例えば、特許文献1参照。)。   As a technique for preventing the deterioration of the hot water quality of the hot water storage tank in this way, conventionally, in the morning, etc., as a water quality maintenance operation, the hot water storage from the hot water storage tank to the hot water supply passage is continued. There has been a technique for performing an operation of heating the hot water of a tank to a water quality maintenance temperature (for example, see Patent Document 1).

特開平10−141685号公報Japanese Patent Laid-Open No. 10-141585

しかしながら、従来では、前記水質維持運転として、前記貯湯タンクから前記給湯路への湯水の送出を継続する状態で、貯湯タンクの湯水を前記水質維持温度に加熱する運転を実行するものであることから、つまり、水質維持運転中であっても、給湯需要があると、貯湯タンクの湯水が給湯路を通して送出されることになり、それに伴って、貯湯タンクに給水路を通して給水されるものであるから、貯湯タンクの湯水を水質維持温度にまで迅速に加熱することができない等、水質維持運転を適切に行うことができないという問題があった。   However, conventionally, as the water quality maintenance operation, the operation of heating the hot water in the hot water storage tank to the water quality maintenance temperature in a state in which hot water is continuously sent from the hot water storage tank to the hot water supply passage is executed. In other words, even during the water quality maintenance operation, if there is a demand for hot water supply, the hot water in the hot water storage tank will be sent through the hot water supply passage, and accordingly, the hot water storage tank will be supplied through the water supply passage. There has been a problem that the water quality maintenance operation cannot be performed properly, such as being unable to quickly heat the hot water in the hot water storage tank to the water quality maintenance temperature.

本発明は、かかる実情に鑑みてなされたものであり、その目的は、貯湯タンクの湯水の水質を維持するための水質維持運転を適切に実行し得る貯湯式の給湯熱源装置を提供することにある。   The present invention has been made in view of such circumstances, and an object of the present invention is to provide a hot water storage type hot water supply heat source device capable of appropriately performing a water quality maintenance operation for maintaining the quality of hot water in a hot water storage tank. is there.

本願発明の貯湯式の給湯熱源装置は、給水路を通して給水され且つ給湯路を通して湯水が送出される貯湯タンクと、
その貯湯タンクの湯水を加熱する加熱手段と、
前記給湯路を通流する湯水を目標給湯温度に加熱する補助加熱手段と、
前記貯湯タンクに目標貯湯温度で貯湯されるように前記加熱手段の作動を制御する制御手段とが設けられたものであって、
第1特徴構成は、放熱用端末器が設けられた熱媒循環路を循環する熱媒を加熱する暖房用補助加熱手段と、
前記加熱手段から前記貯湯タンクに供給される湯水と前記熱媒循環路を循環する熱媒との熱交換を行う加熱用熱交換器とが設けられ、
前記制御手段が、前記貯湯タンクの湯水の水質を維持するための水質維持運転として、前記貯湯タンク全体の湯水が設定水質維持温度以上である状態を設定水質維持時間継続させるように前記加熱手段を作動させる運転を実行すると共に、前記水質維持運転の実行中における、少なくとも前記貯湯タンク全体の湯水が前記設定水質維持温度以上になるまでの間、前記熱媒循環路に熱媒を循環させる状態で前記暖房用補助加熱手段を作動させる補助昇温運転を実行するように構成されている点を特徴とする。
A hot water storage type hot water supply heat source device of the present invention includes a hot water storage tank that is supplied with water through a water supply channel and to which hot water is sent through the water supply channel,
Heating means for heating the hot water in the hot water storage tank;
Auxiliary heating means for heating hot water flowing through the hot water supply path to a target hot water temperature;
Control means for controlling the operation of the heating means so that hot water is stored in the hot water storage tank at a target hot water temperature,
The first characteristic configuration is an auxiliary heating means for heating that heats the heat medium circulating in the heat medium circuit provided with the terminal for heat dissipation,
A heating heat exchanger for exchanging heat between hot water supplied from the heating means to the hot water storage tank and a heat medium circulating in the heat medium circulation path is provided;
As the water quality maintenance operation for maintaining the quality of the hot water in the hot water storage tank, the control means controls the heating means so as to continue the state in which the hot water in the entire hot water storage tank is equal to or higher than the preset water quality maintenance temperature. While performing the operation to be operated, in a state in which the heat medium is circulated through the heat medium circulation path at least until the hot water in the entire hot water storage tank becomes equal to or higher than the set water quality maintenance temperature during the water quality maintenance operation. It is characterized by the point comprised so that the auxiliary | assistant temperature rising operation which operates the said auxiliary heating means for heating may be performed.

即ち、前記水質維持運転は、前記貯湯タンク全体の湯水が設定水質維持温度以上である状態を設定水質維持時間継続させるように前記加熱手段を作動させる水質維持運転の実行中における、少なくとも貯湯タンク全体の湯水が設定水質維持温度以上になるまでの間は、上記補助昇温運転を実行することで、上記加熱用熱交換器において、加熱手段から貯湯タンクに供給される水が、熱媒循環路において暖房用補助加熱手段により加熱された熱媒により一層加熱されることになる。
つまり、前記水質維持運転の実行中は、少なくとも貯湯タンク全体の湯水が設定水質維持温度以上になるまでの間、貯湯タンクの湯水を、加熱手段による加熱に合わせて、上記暖房用補助加熱手段により加熱された熱媒を用いて加熱するので、貯湯タンク全体の湯水が設定水質維持温度以上になるまでの時間を短縮することが可能となり、前記水質維持運転の所要時間を短縮することが可能になる。
That is, the water quality maintenance operation is at least the entire hot water storage tank during execution of the water quality maintenance operation for operating the heating means so that the hot water in the entire hot water storage tank is at or above the set water quality maintenance temperature for a set water quality maintenance time. In the heating heat exchanger, the water supplied from the heating means to the hot water storage tank is transferred to the heating medium circulation path by performing the auxiliary heating operation until the hot water of the hot water reaches or exceeds the set water quality maintenance temperature. Then, the heating medium is further heated by the heating medium heated by the auxiliary heating means for heating.
That is, during the execution of the water quality maintenance operation, the hot water in the hot water storage tank is heated by the heating auxiliary heating means in accordance with the heating by the heating means until at least the hot water in the entire hot water storage tank reaches the set water quality maintenance temperature. Since heating is performed using a heated heating medium, it is possible to shorten the time until the hot water in the entire hot water storage tank reaches the set water quality maintenance temperature or more, and the time required for the water quality maintenance operation can be shortened. Become.

第2特徴構成は、上記第1特徴構成に加えて、前記熱媒循環路にて循環する熱媒を、前記端末器迂回路を通して前記放熱用端末器を迂回させる端末器迂回状態に切り換え自在な熱媒循環状態切換手段が設けられ、
前記運転制御手段が、前記水質維持運転の実行中において、前記熱媒循環状態切換手段を前記端末機器迂回状態に切り換えるように構成されている点を特徴とする。
In addition to the first feature configuration described above, the second feature configuration can freely switch the heating medium circulating in the heating medium circulation path to a terminal bypassing state in which the heat dissipation terminal is bypassed through the terminal bypass. Heat medium circulation state switching means is provided,
The operation control means is configured to switch the heat medium circulation state switching means to the terminal device bypass state during execution of the water quality maintenance operation.

即ち、上記運転制御手段が、前記補助昇温運転の実行中において、上記熱媒循環状態切換手段を上記端末機器迂回状態に切り換えることで、熱媒循環路において暖房用補助加熱手段により加熱された熱媒が暖房用端末器に供給され、不意に暖房用端末器において暖房が行われてしまうことを防止することができる。また、上記熱媒循環状態切換手段を上記端末機器迂回状態に切り換えることで、熱媒の暖房用端末器での放熱が無くなるので、上記加熱用熱交換器において、高温の熱媒により効率良く加熱手段から貯湯タンクに供給される水を加熱することができる。   That is, the operation control means is heated by the auxiliary heating means for heating in the heat medium circulation path by switching the heat medium circulation state switching means to the terminal device bypass state during execution of the auxiliary temperature raising operation. It is possible to prevent the heating medium from being supplied to the heating terminal device and unexpectedly performing heating in the heating terminal device. Further, since the heat medium circulation state switching means is switched to the terminal device detour state, the heat medium is not radiated from the heating terminal, so that the heating heat exchanger can be efficiently heated by the high-temperature heat medium. The water supplied from the means to the hot water storage tank can be heated.

第3特徴構成は、上記第1又は第2特徴構成に加えて、前記給水路にて供給される水をタンク迂回給水路を通して前記貯湯タンクを迂回して前記給湯路における前記補助加熱手段よりも上流側に供給し且つ前記貯湯タンクから前記給湯路への湯水の送出を停止するタンク迂回給水状態に切り換え自在な給水状態切換手段が設けられ、
前記制御手段が、前記水質維持運転を実行する必要がある水質維持運転タイミングであるか否かを判別して、その水質維持運転タイミングになると、前記水質維持運転として、前記給水状態切換手段を前記タンク迂回給水状態に切り換え、且つ、前記貯湯タンク全体の湯水が設定水質維持温度以上である状態を設定水質維持時間継続させるように前記加熱手段を作動させる運転を実行するように構成されている点を特徴とする。
In addition to the first or second characteristic configuration described above, the third characteristic configuration is more than the auxiliary heating means in the hot water supply path, with the water supplied in the water supply path bypassing the hot water storage tank through the tank bypass water supply path. A water supply state switching means is provided that can be switched to a tank bypass water supply state that supplies the upstream side and stops sending hot water from the hot water storage tank to the hot water supply path,
The control means determines whether or not it is the water quality maintenance operation timing that needs to perform the water quality maintenance operation, and when the water quality maintenance operation timing is reached, the water supply state switching means is set as the water quality maintenance operation. It is configured to switch to a tank bypass water supply state, and to perform an operation for operating the heating means so as to continue a state in which the hot water in the entire hot water storage tank is equal to or higher than a set water quality maintenance temperature for a set water quality maintenance time. It is characterized by.

即ち、前記制御手段は、前記水質維持運転タイミングであるか否かを判別して、その水質維持運転タイミングになると、前記給水状態切換手段を前記タンク迂回給水状態に切り換え、且つ、前記貯湯タンク全体の湯水が設定水質維持温度以上である状態を設定水質維持時間継続させるように前記加熱手段を作動させる水質維持運転を実行する。   That is, the control means determines whether or not it is the water quality maintenance operation timing, and when the water quality maintenance operation timing is reached, the water supply state switching means is switched to the tank bypass water supply state, and the entire hot water storage tank A water quality maintenance operation is performed to operate the heating means so that the hot water is at or above the set water quality maintenance temperature for a set water quality maintenance time.

つまり、前記水質維持運転は、前記給水路にて供給される水を前記タンク迂回給水路を通して前記貯湯タンクを迂回して前記給湯路における前記補助加熱手段よりも上流側に供給し且つ前記貯湯タンクから前記給湯路への湯水の送出を停止した状態で、前記貯湯タンク全体の湯水が設定水質維持温度以上である状態を設定水質維持時間継続させるように前記加熱手段を作動させるものであることから、その水質維持運転の実行中に、給湯需要があっても、前記貯湯タンクから前記給湯路への湯水の送出が停止された状態で、前記給水路にて供給される水が前記貯湯タンクを迂回して前記給湯路における前記補助加熱手段よりも上流側に供給されることになるので、貯湯タンクへの給水を停止した状態で、加熱手段により貯湯タンクの湯水を加熱することになって、貯湯タンクの湯水を迅速に水質維持温度にまで加熱することが可能になり、しかも、給水路を通して供給される水質の良い水を補助加熱手段にて目標給湯温度に加熱して給湯箇所に供給することが可能になる。   That is, in the water quality maintenance operation, the water supplied in the water supply path is supplied to the upstream side of the hot water storage tank by bypassing the hot water storage tank through the tank bypass water supply path and the hot water storage tank. The heating means is operated so that the state in which the hot water in the entire hot water storage tank is equal to or higher than the set water quality maintenance temperature is continued for the set water quality maintenance time in a state where the supply of hot water to the hot water supply channel is stopped. Even when there is a demand for hot water supply during the water quality maintenance operation, water supplied from the hot water storage tank to the hot water supply path is stopped and water supplied from the hot water supply path is not supplied to the hot water storage tank. Since it is detoured and supplied to the upstream side of the auxiliary heating means in the hot water supply passage, hot water in the hot water storage tank is added by the heating means with the water supply to the hot water storage tank stopped. Therefore, the hot water in the hot water storage tank can be quickly heated to the water quality maintenance temperature, and the water of good quality supplied through the water supply channel is heated to the target hot water supply temperature by the auxiliary heating means. Can be supplied to hot water supply points.

又、前記加熱手段としては、バーナや電気ヒータ等の専用の熱源を備えて構成する場合の他、例えば、燃料電池や、発電機をエンジンにて駆動するようにした回転式の発電装置等の排熱発生式の処理装置の排熱を熱源とするように構成して、省エネ性を向上するように構成する場合がある。
このような排熱発生式の処理装置は、前記給湯熱源装置とは無関係に独立して運転が停止されたり、出力が変更調節されたりして、運転状態が変更されることになって、そのような運転状態の変動により、排熱が発生しなくなったり排熱の発生量が変動したりすることになるので、前記貯湯タンクの湯水の温度が低くなって水質が低下する虞がある状態が比較的起こり易くなるが、前記貯湯タンクの湯水の温度が低くなって水質が低下する虞がある状態となるとき等、水質維持運転タイミングになると、上述のように水質維持運転を実行することにより、貯湯タンクの水質を維持することが可能となるのである。
In addition to the case where the heating means is configured with a dedicated heat source such as a burner or an electric heater, for example, a fuel cell, a rotary power generation device in which a generator is driven by an engine, etc. In some cases, the exhaust heat of the exhaust heat generation type processing device is used as a heat source so as to improve energy saving.
Such a waste heat generation type processing device is not operated independently of the hot water supply heat source device, the operation is stopped independently, the output is changed and adjusted, and the operation state is changed. Such a change in the operation state causes no exhaust heat or the amount of generated exhaust heat fluctuates. Therefore, there is a possibility that the temperature of the hot water in the hot water storage tank becomes low and the water quality may deteriorate. Although it is relatively easy to occur, when the water quality maintenance operation timing comes, such as when the temperature of the hot water in the hot water storage tank becomes low and there is a possibility that the water quality may deteriorate, by performing the water quality maintenance operation as described above, This makes it possible to maintain the water quality of the hot water storage tank.

要するに、水質維持運転の実行中に給湯需要があっても、水質の良い水を目標給湯温度に加熱した状態での適切な給湯を可能にしながら、貯湯タンクの湯水を迅速に水質維持温度にまで加熱することが可能になるので、水質維持運転を適切に実行し得る貯湯式の給湯熱源装置を提供することができるようになった。   In short, even if there is a demand for hot water supply during the water quality maintenance operation, the hot water in the hot water storage tank can be quickly brought to the water quality maintenance temperature while enabling appropriate hot water supply in a state where high-quality water is heated to the target hot water temperature. Since it becomes possible to heat, it has become possible to provide a hot water storage type hot water supply heat source device capable of appropriately performing the water quality maintenance operation.

第4特徴構成は、上記第3特徴構成に加えて、
前記制御手段は、前記給水路を通して前記貯湯タンクに給水され且つ前記貯湯タンクの湯水が前記給湯路を通して送出される形態にて前記貯湯タンクの湯水が入れ替わる湯水入れ替わり状態を判別するように構成され、且つ、前記貯湯タンクの湯水の温度が前記設定水質維持温度よりも低く且つ前記湯水入れ替わり状態を判別しない状態がタイミング判別用設定時間継続すると前記水質維持運転タイミングになると判別するように構成されている点を特徴とする。
In addition to the third feature configuration, the fourth feature configuration is
The control means is configured to determine a hot water replacement state in which hot water in the hot water storage tank is replaced in a form in which water is supplied to the hot water storage tank through the water supply passage and hot water in the hot water storage tank is sent out through the hot water supply passage. The hot water storage tank is configured such that the temperature of the hot water is lower than the set water quality maintenance temperature and the state in which the hot water replacement state is not discriminated continues for the set time for timing discrimination and the water quality maintenance operation timing is determined. Features a point.

即ち、前記制御手段は、前記貯湯タンクの湯水の温度が前記設定水質維持温度よりも低く且つ前記湯水入れ替わり状態を判別しない状態が継続する時間を監視して、その継続時間が前記タイミング判別用設定時間に達すると、前記水質維持運転タイミングになると判別する。   That is, the control means monitors the time during which the temperature of the hot water in the hot water storage tank is lower than the set water quality maintenance temperature and does not determine the hot water replacement state, and the duration is set for the timing determination. When the time is reached, it is determined that the water quality maintenance operation timing is reached.

つまり、前記貯湯タンクの湯水の温度が前記設定水質維持温度よりも低い状態で、貯湯タンクの湯水が入れ替えられない状態が長く続くと、水質が低下する虞がある。
そこで、前記タイミング判別用設定時間として、前記貯湯タンクの湯水の温度が前記設定水質維持温度よりも低い状態で貯湯タンクの湯水が入れ替えられない状態が続いて、貯湯タンクの湯水の水質が低下する虞がある状態となると水質維持運転が実行される時間でありながらも、極力短い時間に設定する。そして、前記貯湯タンクの湯水の温度が前記設定水質維持温度よりも低く且つ前記湯水入れ替わり状態を判別しない状態が前記タイミング判定設定時間継続すると、前記水質維持運転タイミングになったと判別して、前記水質維持運転を実行するようにすることにより、その水質維持運転が頻繁に実行されるのを回避しながら、貯湯タンクの湯水の水質が低下する虞がある状態となる水質維持運転の実行が必要な時期になると水質維持運転を実行することが可能になる。
In other words, if the hot water temperature in the hot water storage tank is lower than the set water quality maintenance temperature and the hot water in the hot water storage tank is not replaced for a long time, the water quality may deteriorate.
Therefore, as the set time for timing determination, the hot water in the hot water storage tank continues to be in a state where the hot water in the hot water storage tank is not replaced when the temperature of the hot water in the hot water storage tank is lower than the set water quality maintenance temperature. When there is a fear, it is set to a time as short as possible while it is the time for the water quality maintenance operation to be executed. When the state in which the temperature of the hot water in the hot water storage tank is lower than the set water quality maintenance temperature and the hot water replacement state is not determined continues for the timing determination set time, it is determined that the water quality maintenance operation timing has been reached, and the water quality is determined. By performing the maintenance operation, it is necessary to execute the water quality maintenance operation in which the water quality of the hot water storage tank may be deteriorated while avoiding frequent execution of the water quality maintenance operation. It is possible to carry out water quality maintenance operation at the right time.

従って、水質維持運転が頻繁に行われるのを回避しながら、貯湯タンクに水質維持温度よりも低い温度の湯水が入れ替わりが無い状態で継続して貯留される状態となっても、その貯湯タンクの湯水の水質が低下する虞がある状態となると適切に水質維持運転を実行して、貯湯タンクの湯水の水質を維持することができるようになった。   Therefore, even if hot water having a temperature lower than the water quality maintenance temperature is continuously stored in the hot water storage tank without being replaced while avoiding frequent water quality maintenance operation, When there is a possibility that the quality of the hot water will deteriorate, the water quality maintenance operation can be appropriately executed to maintain the quality of the hot water in the hot water storage tank.

第5特徴構成は、上記第1〜第4特徴構成のいずれかに加えて、
前記加熱手段が、熱電併給装置から発生する熱にて前記貯湯タンクの湯水を加熱するように構成され、
前記制御手段が、通常運転の実行中は電力負荷に応じた電力を発電し、前記水質維持運転の実行中は余剰電力を生じさせるべく前記電力負荷よりも大きい電力を発電するように、前記熱電併給装置の運転を制御するように構成され、
前記水質維持運転の実行中における、少なくとも前記貯湯タンク全体の湯水が前記設定水質維持温度以上になるまでの間、前記余剰電力を前記貯湯タンクに貯湯するための熱に変換する電気ヒータが設けられている点を特徴とする。
In addition to any of the first to fourth feature configurations described above, the fifth feature configuration is
The heating means is configured to heat the hot water in the hot water storage tank with heat generated from the combined heat and power supply device;
The control means generates electric power according to the electric power load during execution of normal operation, and generates electric power larger than the electric power load to generate surplus electric power during execution of the water quality maintenance operation. Configured to control the operation of the co-feeder;
An electric heater for converting the surplus power into heat for storing hot water in the hot water storage tank is provided at least until the hot water in the entire hot water storage tank reaches the set water quality maintenance temperature or higher during execution of the water quality maintenance operation. It is characterized by that.

即ち、前記制御手段は、通常運転の実行中は電力負荷に応じた電力を発電し、前記水質維持運転の実行中は余剰電力を生じさせるべく前記電力負荷よりも大きい電力を発電するように、前記熱電併給装置の運転を制御する。
そして、前記通常運転の実行中は、前記加熱手段により、前記熱電併給装置から発生する熱にて前記貯湯タンクの湯水が加熱され、前記水質維持運転の実行中における、少なくとも貯湯タンク全体の湯水が設定水質維持温度以上になるまでの間は、加熱手段により、熱電併給装置から発生する熱にて貯湯タンクの湯水が加熱され、並びに、前記電気ヒータにより、熱電併給装置の余剰電力にて前記貯湯タンクの湯水が加熱される。
つまり、前記水質維持運転の実行中は、少なくとも貯湯タンク全体の湯水が設定水質維持温度以上になるまでの間、貯湯タンクの湯水を、加熱手段による加熱に合わせて、電気ヒータにて熱電併給装置の余剰電力を用いて加熱するので、貯湯タンク全体の湯水が設定水質維持温度以上になるまでの時間を短縮することが可能となり、前記水質維持運転の所要時間を短縮することが可能になる。
又、貯湯タンクの湯水を、加熱手段による加熱に合わせて、電気ヒータにて熱電併給装置の余剰電力を用いて加熱するようにすることにより、前記貯湯タンク全体の湯水を前記設定水質維持温度よりも高い温度に加熱することが可能となり、そして、そのように貯湯タンク全体の湯水を前記設定水質維持温度よりも高い温度に加熱することにより、前記設定水質維持時間を短く設定することが可能となり、延いては、前記水質維持運転の所要時間を短縮することが可能になる。
従って、水質維持運転を適切に実行しながらも、その所要時間を短縮することができるようになった。
That is, the control means generates electric power according to the electric power load during execution of normal operation, and generates electric power larger than the electric power load to generate surplus electric power during execution of the water quality maintenance operation. Controls the operation of the cogeneration device.
During the execution of the normal operation, the heating means heats the hot water in the hot water storage tank with heat generated from the combined heat and power supply device, and at least the hot water in the entire hot water storage tank during the water quality maintenance operation is performed. The hot water in the hot water storage tank is heated by the heat generated from the combined heat and power supply device by the heating means until the temperature reaches the set water quality maintenance temperature or higher, and the hot water storage device uses the electric heater to generate excess power from the combined heat and power supply device The hot water in the tank is heated.
That is, during the execution of the water quality maintenance operation, the hot water in the hot water storage tank is combined with the heating by the heating means until the hot water in the entire hot water storage tank reaches or exceeds the set water quality maintenance temperature, and the combined heat and power supply device with the electric heater is used. Therefore, it is possible to shorten the time required for the hot water in the entire hot water storage tank to reach the set water quality maintenance temperature or more, and the time required for the water quality maintenance operation can be shortened.
In addition, the hot water in the hot water storage tank is heated by using the surplus power of the combined heat and power device with an electric heater in accordance with the heating by the heating means. It is possible to heat the hot water in the entire hot water storage tank to a temperature higher than the set water quality maintenance temperature, and thus the set water quality maintenance time can be set short. As a result, the time required for the water quality maintenance operation can be shortened.
Accordingly, it is possible to shorten the required time while appropriately executing the water quality maintenance operation.

第6特徴構成は、上記第1〜第5特徴構成のいずれかに加えて、
前記貯湯タンクが密閉式に構成されて、前記給水路がタンク底部に接続され、且つ、前記給湯路がタンク上部に接続され、
前記加熱手段が、タンク底部から取り出した湯水を加熱作用部を経由してタンク上部に戻す形態で貯湯用循環路を通じて前記貯湯タンクの湯水を循環させるように構成されている点を特徴とする。
In addition to any of the first to fifth feature configurations described above, the sixth feature configuration is
The hot water storage tank is configured in a sealed manner, the water supply path is connected to a tank bottom, and the hot water supply path is connected to an upper part of the tank;
The heating means is configured to circulate the hot water in the hot water storage tank through the hot water storage circulation path in such a manner that the hot water taken out from the bottom of the tank is returned to the upper portion of the tank via the heating action portion.

即ち、前記貯湯タンクの湯水が、タンク底部から取り出され、前記加熱作用部にて加熱された後、タンク上部に戻される形態で、貯湯用循環路を通じて循環されることにより、前記貯湯タンクに温度成層を形成する状態で湯水が貯留される。
そして、給湯需要があると、上層の温度の高い湯水が前記給湯路を通して送出されると共に、前記貯湯タンクの底部に前記給水路を通して給水されることになり、温度成層の乱れを抑制しながら、温度の高い湯水を給湯箇所に供給することが可能になる。
That is, the hot water in the hot water storage tank is taken out from the bottom of the tank, heated by the heating action part, and then returned to the upper part of the tank, and is circulated through the hot water storage circulation path so that the temperature of the hot water storage tank is increased. Hot water is stored in a state of forming a stratification.
And when there is a demand for hot water supply, hot water with a high temperature in the upper layer is sent through the hot water supply channel, and water is supplied to the bottom of the hot water storage tank through the water supply channel, while suppressing disturbance of temperature stratification, Hot water with high temperature can be supplied to the hot water supply location.

つまり、貯湯タンクに温度成層を形成する状態で貯湯して、上層の温度の高い湯水を給湯路を通して送出することにより、目標給湯温度の湯水を給湯箇所に供給するようにするに当たって、前記補助加熱手段による加熱を不要にするか、あるいは、その加熱量を低減して、その補助加熱手段のエネルギー消費量を低減することが可能になり、省エネ性を向上することが可能になる。   That is, when the hot water is stored in a state where temperature stratification is formed in the hot water storage tank, hot water having a high temperature in the upper layer is sent out through the hot water supply passage so that hot water at the target hot water temperature is supplied to the hot water supply location. It is possible to eliminate the heating by the means, or to reduce the amount of heating, and to reduce the energy consumption of the auxiliary heating means, thereby improving the energy saving performance.

従って、省エネ性に優れながらも、水質維持運転を適切に実行し得る貯湯式の給湯熱源装置を提供することができるようになった。   Therefore, it has become possible to provide a hot water storage type hot water supply heat source device that can appropriately execute the water quality maintenance operation while being excellent in energy saving.

〔第1実施形態〕
以下、図面に基づいて、本発明にかかる給湯熱源装置をコージェネレーションシステムに適用した場合の第1実施形態を説明する。
図1は、本発明にかかる給湯熱源装置Aを備えたコージェネレーションシステムを示し、このコージェネレーションシステムは、前記給湯熱源装置Aの他に、熱電併給装置の一例としての燃料電池G、及び、その燃料電池Gを商用電源1に系統連系するインバータ2等を備え、前記給湯熱源装置Aは、前記燃料電池Gにて発生する熱を用いて、給水路4を通して給水され且つ給湯路3を通して湯水が送出される貯湯タンク5内に貯湯するように構成してある。
[First Embodiment]
Hereinafter, based on drawing, 1st Embodiment at the time of applying the hot-water supply heat source apparatus concerning this invention to a cogeneration system is described.
FIG. 1 shows a cogeneration system provided with a hot water supply heat source device A according to the present invention. This cogeneration system includes, in addition to the hot water supply heat source device A, a fuel cell G as an example of a combined heat and power supply device, and its An inverter 2 or the like that interconnects the fuel cell G to the commercial power source 1 is provided, and the hot water supply source A is supplied with water through the water supply channel 4 and hot water through the hot water supply channel 3 using heat generated in the fuel cell G. Is configured to store hot water in the hot water storage tank 5 to which the water is discharged.

前記商用電源1は、商用電力供給ライン7を介して、テレビ、冷蔵庫、洗濯機等の電力消費機器8に接続してある。
前記インバータ2は、前記燃料電池Gの出力電力を商用電源1から供給される電力と同じ電圧および同じ周波数に変換するように構成してあり、コージェネ用供給ライン9を介して前記商用電力供給ライン7に電気的に接続して、前記燃料電池Gの発電電力が前記インバータ2にて交流に変換されて、前記コージェネ用供給ライン9、前記商用電力供給ライン7を介して前記電力消費機器8に供給されるように構成してある。
The commercial power source 1 is connected to a power consuming device 8 such as a television, a refrigerator, or a washing machine via a commercial power supply line 7.
The inverter 2 is configured to convert the output power of the fuel cell G into the same voltage and the same frequency as the power supplied from the commercial power source 1, and the commercial power supply line via the cogeneration supply line 9. 7, the power generated by the fuel cell G is converted into alternating current by the inverter 2, and is supplied to the power consuming device 8 via the cogeneration supply line 9 and the commercial power supply line 7. It is configured to be supplied.

図1に基づいて、前記給湯熱源装置Aについて説明を加える。
前記給湯熱源装置Aは、前記貯湯タンク5と、前記貯湯タンク5の湯水を加熱する加熱手段としての加熱部Hと、前記給湯路3を通流する湯水を目標給湯温度に加熱する補助加熱手段としてのガス燃焼式の補助加熱器19と、前記給水路4を通して前記貯湯タンク5に給水し且つ前記貯湯タンク5から前記給湯路3への湯水の送出を許容する通常給水状態と前記給水路4にて供給される水をタンク迂回給水路24を通して前記貯湯タンク5を迂回して前記給湯路3における前記補助加熱器19よりも上流側に供給し且つ前記貯湯タンク5から前記給湯路3への湯水の送出を停止するタンク迂回給水状態に切り換え自在な給水状態切換手段としての給水切換三方弁25と、前記給湯熱源装置Aの各種制御を司る熱源制御部20等を備えて構成してある。
Based on FIG. 1, the hot water supply heat source apparatus A will be described.
The hot water supply heat source device A includes the hot water storage tank 5, a heating unit H as a heating means for heating hot water in the hot water storage tank 5, and auxiliary heating means for heating hot water flowing through the hot water supply passage 3 to a target hot water temperature. A normal water supply state in which water is supplied to the hot water storage tank 5 through the water supply passage 4 and the hot water supply from the hot water storage tank 5 to the hot water supply passage 3 is allowed. Is supplied to the upstream side of the auxiliary heater 19 in the hot water supply path 3, bypassing the hot water storage tank 5 through the tank bypass water supply path 24, and from the hot water storage tank 5 to the hot water supply path 3. A water supply switching three-way valve 25 as a water supply state switching means that can be switched to a tank bypass water supply state that stops the delivery of hot water, a heat source control unit 20 that performs various controls of the hot water supply source A, and the like. A.

本実施形態においては、前記貯湯タンク5を密閉式に構成して、そのタンク底部に水道水を給水する前記給水路4を接続し、タンク上部に前記給湯路3を接続して、図示しない給湯栓の開栓等により前記給湯路3を通じて前記貯湯タンク5の上部から前記給湯路3に湯水が送出されるのに伴って、前記給水路4を通じて前記貯湯タンク5の底部に給水されるようになっていて、前記貯湯タンク5には満杯状態に湯水が貯留されるように構成してある。
前記加熱部Hは、タンク底部から取り出した湯水をタンク上部に戻す形態で貯湯用循環路12を通じて前記貯湯タンク5の湯水を循環させる貯湯用循環ポンプ13、及び、前記貯湯用循環路12を通流する湯水を前記燃料電池Gから発生する熱にて加熱する加熱作用部としての排熱熱源熱交換器14を備えて構成して、前記貯湯タンク5に温度成層が形成される状態で貯湯するように構成してある。
In the present embodiment, the hot water storage tank 5 is configured in a sealed manner, the water supply path 4 for supplying tap water is connected to the bottom of the tank, the hot water supply path 3 is connected to the upper part of the tank, and hot water supply (not shown) As hot water is sent from the upper part of the hot water storage tank 5 to the hot water supply path 3 through the hot water supply path 3 by opening the stopper, the water is supplied to the bottom of the hot water storage tank 5 through the water supply path 4. The hot water storage tank 5 is configured to store hot water in a full state.
The heating unit H is configured to circulate hot water in the hot water storage tank 5 through the hot water storage circulation path 12 and return the hot water taken out from the tank bottom to the upper part of the tank, and the hot water storage circulation path 12. An exhaust heat source heat exchanger 14 is provided as a heating portion for heating the flowing hot water with heat generated from the fuel cell G, and hot water is stored in a state where temperature stratification is formed in the hot water storage tank 5. It is constituted as follows.

更に、前記給湯熱源装置Aには、加熱用熱交換器11と放熱用端末器6とにわたって熱媒循環路21を通じて熱媒循環ポンプ22にて熱媒を循環させて、前記放熱用端末器6にて加熱対象を加熱する放熱運転を実行する放熱部Wと、前記排熱熱源熱交換器14にて加熱されて前記貯湯用循環路12を通流する湯水を前記加熱用熱交換器11を通過させた後、前記貯湯タンク5のタンク上部に供給する加熱用流路15と、前記排熱熱源熱交換器14にて加熱された湯水を前記加熱用流路15に通流させる加熱状態と通流させない非加熱状態とに切り換え自在な加熱切換三方弁16とを設け、前記補助加熱器19は、前記熱媒循環路21を循環する熱媒を目標熱媒温度に加熱するようにも構成してある。ちなみに、前記放熱用端末器6としては、例えば床暖房パネル等があり、その場合は、前記床暖房パネルにて加熱対象としての暖房対象域を暖房することになる。   Further, in the hot water supply heat source apparatus A, a heat medium is circulated by the heat medium circulation pump 22 through the heat medium circulation path 21 over the heat exchanger 11 for heating and the terminal device 6 for heat radiation, and the terminal device 6 for heat radiation. The heat-dissipating part W for performing the heat-dissipating operation for heating the object to be heated and the heating heat exchanger 11 for the hot water heated by the exhaust heat source heat exchanger 14 and flowing through the hot-water storage circulation path 12 A heating flow path 15 that is supplied to the upper part of the hot water storage tank 5 after passing through, and a heating state in which hot water heated by the exhaust heat source heat exchanger 14 is passed through the heating flow path 15; A heating switching three-way valve 16 that can be switched to a non-heating state that does not flow is provided, and the auxiliary heater 19 is also configured to heat the heat medium circulating in the heat medium circulation path 21 to a target heat medium temperature. It is. Incidentally, as the heat radiating terminal 6, for example, there is a floor heating panel or the like, and in that case, a heating target area as a heating target is heated by the floor heating panel.

また、上記熱媒循環路21には、熱媒を放熱用端末器6を迂回させ流通させる端末器迂回路50が設けられ、更に、熱媒を端末器迂回路50を通して放熱用端末器6を迂回させる端末器迂回状態に切り換え自在な熱媒循環状態切換手段として、熱媒循環路21と端末器迂回路50との接続部に、熱媒循環状態切換三方弁51が設けられている。   Further, the heat medium circulation path 21 is provided with a terminal bypass circuit 50 for circulating the heat medium by bypassing the heat dissipation terminal 6, and further, the heat dissipation terminal 6 is connected to the heat medium through the terminal bypass circuit 50. A heat medium circulation state switching three-way valve 51 is provided at a connection portion between the heat medium circulation path 21 and the terminal device bypass circuit 50 as a heat medium circulation state switching means that can be switched to a terminal device bypass state to be bypassed.

以下、前記給湯熱源装置Aの各部について説明を加える。
前記貯湯タンク5の上部には、その貯湯タンク5内の圧力が設定タンク内圧力以下になると開いて、貯湯タンク5内の圧力低下を防止するバキュームブレーカー26を設けてある。
又、前記貯湯タンク5には、その貯湯タンク5の湯水の温度を検出する4個の貯湯温度センサTtを上下方向の略全長にわたって分散した状態で設けて、貯湯タンク5の上下方向の各部における湯水の温度を検出するようにしてある。
Hereinafter, each part of the hot water supply heat source apparatus A will be described.
A vacuum breaker 26 is provided above the hot water storage tank 5 to open when the pressure in the hot water storage tank 5 becomes equal to or lower than the set tank internal pressure to prevent a decrease in the pressure in the hot water storage tank 5.
The hot water storage tank 5 is provided with four hot water storage temperature sensors Tt for detecting the temperature of the hot water in the hot water storage tank 5 in a state of being distributed over substantially the entire length in the vertical direction. The temperature of hot water is detected.

又、前記給水路4には、その給水圧を検出する給水圧センサ27を設けてある。ちなみに、水道が断水して、前記給水路4による前記貯湯タンク5への給水が停止すると、前記バキュームブレーカー26が作動して、前記貯湯タンク5内に外気が侵入する場合があるが、そのように前記バキュームブレーカー26が作動して前記貯湯タンク5内に外気が侵入する外気侵入状態が発生したことを、前記給水圧センサ27の検出圧力が所定の設定タンク給水圧よりも低くなることに基づいて判別することができる。   The water supply path 4 is provided with a water supply pressure sensor 27 for detecting the water supply pressure. Incidentally, when the water supply is cut off and the water supply to the hot water storage tank 5 by the water supply channel 4 is stopped, the vacuum breaker 26 is activated, and external air may enter the hot water storage tank 5. The fact that the vacuum breaker 26 is activated and the outside air intrusion state in which the outside air enters the hot water storage tank 5 has occurred is based on the fact that the detected pressure of the feed water pressure sensor 27 is lower than a predetermined set tank feed water pressure. Can be determined.

前記放熱部Wについて説明を加えると、その放熱部Wは、前記熱媒循環ポンプ22を作動させることにより、前述のように、前記加熱用熱交換器11と前記放熱用端末器6とにわたって前記熱媒循環路21を通じて熱媒を循環させて、前記放熱用端末器6にて熱媒から放熱させることにより、加熱対象を加熱する前記放熱運転を実行するように構成してある。そして、放熱部Wには、前記放熱運転の開始及び停止を指令する放熱運転操作部23を設けてあり、その放熱運転操作部23から運転開始が指令されると、前記熱媒循環ポンプ22を作動させて前記放熱運転を開始し、前記放熱運転操作部23から運転停止が指令されると、前記熱媒循環ポンプ22を停止させて前記放熱運転を停止するように構成してある。
又、前記放熱用端末器6から流出して前記加熱用熱交換器11に戻す熱媒戻し温度を検出する熱媒戻し温度センサTmを設けてある。
When the heat radiating portion W is described, the heat radiating portion W operates over the heating heat exchanger 11 and the heat radiating terminal 6 as described above by operating the heat medium circulation pump 22. The heat medium is circulated through the heat medium circulation path 21 and is radiated from the heat medium by the heat radiating terminal 6 so that the heat radiation operation for heating the heating target is performed. The heat dissipating part W is provided with a heat dissipating operation part 23 for instructing start and stop of the heat dissipating operation. When the start of operation is instructed from the heat dissipating operation part 23, the heat medium circulation pump 22 is The heat radiation operation is started by operating, and when the operation stop is commanded from the heat radiation operation operation unit 23, the heat medium circulation pump 22 is stopped and the heat radiation operation is stopped.
Further, a heat medium return temperature sensor Tm for detecting a heat medium return temperature that flows out from the heat radiating terminal 6 and returns to the heating heat exchanger 11 is provided.

前記補助加熱器19について説明を加えると、この補助加熱器19には、前記給湯路3を通流する湯水を加熱するための給湯用補助加熱部19sと、前記熱媒循環路21を循環する熱媒を加熱するための暖房用補助加熱部19w(暖房用補助加熱手段)とを備えてある。これら給湯用補助加熱部19sと暖房用補助加熱部19wは、加熱対象の湯水又は熱媒を通流させる熱交換器h、その熱交換器hを加熱するガスバーナb、そのガスバーナbに燃焼用空気を供給する送風機f、前記熱交換器hに流入する湯水又は熱媒の流入温度を検出する流入温度センサ(図示省略)、前記熱交換器hから流出する湯水又は熱媒の流出温度を検出する流出温度センサ(図示省略)、前記熱交換器hに流入する湯水又は熱媒の流量を検出する流量センサ(図示省略)、燃焼制御部(図示省略)等を備えて、同様に構成してあり、又、前記各燃焼制御部により互いに独立して制御されるようになっている。   When the auxiliary heater 19 is described further, the auxiliary heater 19 circulates through the hot water supply auxiliary heating portion 19 s for heating the hot water flowing through the hot water supply passage 3 and the heating medium circulation passage 21. A heating auxiliary heating unit 19w (heating auxiliary heating means) for heating the heat medium is provided. The hot water supply auxiliary heating unit 19s and the heating auxiliary heating unit 19w include a heat exchanger h that allows hot water or a heating medium to flow through, a gas burner b that heats the heat exchanger h, and combustion air to the gas burner b. , An inflow temperature sensor (not shown) for detecting the inflow temperature of hot water or heat medium flowing into the heat exchanger h, and detecting the outflow temperature of hot water or heat medium flowing out of the heat exchanger h. An outflow temperature sensor (not shown), a flow rate sensor (not shown) for detecting the flow rate of hot water or heat medium flowing into the heat exchanger h, a combustion control unit (not shown), and the like are configured similarly. In addition, the combustion control units are controlled independently of each other.

前記給湯用補助加熱部19sの前記燃焼制御部の制御動作について簡単に説明すると、前記流量センサが設定流量以上の流量を検出している状態で、前記流入温度センサ及び前記流出温度センサの検出情報に基づいて、流入温度が目標給湯温度未満になると、前記バーナbを燃焼させて、前記流出温度が前記目標給湯温度になるように前記バーナbの燃焼量を調節し、前記燃焼量を設定最少燃焼量に調節しても前記流出温度が前記目標給湯温度以上になるときは前記バーナbを消火させる。又、前記バーナbの燃焼中に、前記流量センサの検出流量が前記設定流量未満になると、前記バーナbを消火させる。
前記暖房用補助加熱部19wの前記燃焼制御部の制御動作は、前記バーナbにて加熱するための目標温度が前記給湯用補助加熱部19sにおける前記目標給湯温度から目標熱媒温度に変わる点が異なる以外は、前記給湯用補助加熱部19sの前記燃焼制御部の制御動作と同様であるので、説明を省略する。
The control operation of the combustion control unit of the hot water supply auxiliary heating unit 19s will be briefly described. The detection information of the inflow temperature sensor and the outflow temperature sensor in a state where the flow rate sensor detects a flow rate higher than a set flow rate. When the inflow temperature becomes lower than the target hot water supply temperature, the burner b is combusted, and the combustion amount of the burner b is adjusted so that the outflow temperature becomes the target hot water supply temperature. Even if the combustion amount is adjusted, the burner b is extinguished when the outflow temperature becomes equal to or higher than the target hot water supply temperature. Further, if the flow rate detected by the flow sensor becomes less than the set flow rate during combustion of the burner b, the burner b is extinguished.
The control operation of the combustion control unit of the heating auxiliary heating unit 19w is that the target temperature for heating by the burner b changes from the target hot water supply temperature in the hot water supply auxiliary heating unit 19s to the target heat medium temperature. Except for the difference, the operation is the same as the control operation of the combustion control unit of the hot water supply auxiliary heating unit 19 s, and the description thereof will be omitted.

前記タンク迂回給水路24は、前記給水路4と前記給湯路3における前記補助加熱器19よりも上流側の箇所とに接続し、前記給水切換三方弁25は、前記タンク迂回給水路24と前記給湯路3との接続部分に、前記給湯路3における前記貯湯タンク5側の部分と前記補助加熱器19側の部分とを連通する給湯路連通流路状態と、前記タンク迂回給水路24と前記給湯路3における前記補助加熱器19側の部分とを連通するタンク迂回路連通流路状態とに切換自在なように設けてある。
つまり、前記給水切換三方弁25を前記給湯路連通流路状態に切り換えることが、前記通常給水状態に切り換えることに相当し、前記給水切換三方弁25を前記タンク迂回路連通流路状態に切り換えることが、前記タンク迂回給水状態に切り換えることに相当する。
The tank bypass water supply path 24 is connected to the water supply path 4 and a location upstream of the auxiliary heater 19 in the hot water supply path 3, and the water supply switching three-way valve 25 is connected to the tank bypass water supply path 24 and the A hot water path communication flow path state in which the hot water storage tank 5 side portion and the auxiliary heater 19 side portion of the hot water supply path 3 are connected to the connecting portion with the hot water supply path 3, the tank bypass water supply path 24 and the It is provided so as to be switchable to a tank bypass circuit communication flow path state that communicates with the auxiliary heater 19 side portion in the hot water supply path 3.
That is, switching the water supply switching three-way valve 25 to the hot water supply channel communication channel state corresponds to switching to the normal water supply state, and switching the water supply switching three-way valve 25 to the tank bypass circuit communication channel state. This corresponds to switching to the tank bypass water supply state.

そして、前記給水切換三方弁25を前記通常給水状態に切り換えた状態では、図1に太実線で示すように、前記給湯栓が開栓されるに伴って、前記貯湯タンク5の上部から湯水が前記給湯路3を通して送出されると共に、前記給水路4を通して前記貯湯タンク5の底部に給水される。その場合、前記貯湯タンク5の上部からの湯水の温度が前記目標給湯温度よりも低いときは、前記補助加熱器19の給湯用補助加熱部19sにより前記目標給湯温度になるように加熱されることになる。
又、前記給水切換三方弁25を前記タンク迂回給水状態に切り換えた状態では、前記給湯栓が開栓されるに伴って、図2に太実線で示すように、前記給水路4からの水が前記タンク迂回給水路24を通じて前記貯湯タンク5を迂回して前記給湯路3に供給されて、その水が、前記補助加熱器19の前記給湯用補助加熱部19sにて前記目標給湯温度になるように加熱されることになる。
In the state where the water supply switching three-way valve 25 is switched to the normal water supply state, as shown by the thick solid line in FIG. 1, hot water is supplied from the upper part of the hot water storage tank 5 as the hot water tap is opened. While being sent out through the hot water supply path 3, water is supplied to the bottom of the hot water storage tank 5 through the water supply path 4. In that case, when the temperature of the hot water from the upper part of the hot water storage tank 5 is lower than the target hot water supply temperature, the hot water is heated to the target hot water temperature by the hot water auxiliary heating unit 19 s of the auxiliary heater 19. become.
Further, in the state where the water supply switching three-way valve 25 is switched to the tank bypass water supply state, as the hot water tap is opened, the water from the water supply path 4 flows as shown by a thick solid line in FIG. The hot water storage tank 5 is bypassed through the tank bypass water supply passage 24 and supplied to the hot water supply passage 3 so that the water reaches the target hot water supply temperature in the auxiliary heating section 19s for hot water supply of the auxiliary heater 19. Will be heated.

尚、上記給水切換三方弁25の代わりに、前記タンク迂回給水路24を開閉可能な開閉弁、及び、前記給湯路3のタンク迂回給水路24との接続部よりも上流側を開閉可能な開閉弁を設け、それら開閉弁の一方を開状態とし他方を閉状態とすることで、上記給湯路連通流路状態と上記タンク迂回路連通流路状態とを切り換える給水状態切換手段を構成しても構わない。   Instead of the water supply switching three-way valve 25, an opening / closing valve capable of opening / closing the tank bypass water supply passage 24 and an opening / closing capable of opening / closing the upstream side of the connecting portion of the hot water supply passage 3 with the tank bypass water supply passage 24. A water supply state switching means for switching between the hot water supply channel communication channel state and the tank bypass circuit communication channel state by providing a valve and opening one of the on-off valves and closing the other valve; I do not care.

前記貯湯用循環路12は、その両端を前記貯湯タンク5の底部と上部とに接続し、その貯湯用循環路12には、前記貯湯用循環ポンプ13を前記貯湯タンク5の底部に対して吸引作用するように設け、更に、前記排熱熱源熱交換器14を設けてある。
一つの流入口と二つの流出口とを備えた前記加熱切換三方弁16を、前記流入口と前記二つの流出口の一方とを用いて、前記貯湯用循環路12における前記排熱熱源熱交換器14よりも下流側で且つ前記貯湯タンク5よりも上流側の部分に介装し、前記加熱用流路15は、その一端を前記加熱切換三方弁16の残りの流出口に接続し、且つ、他端を貯湯用循環路12における前記加熱切換三方弁16の介装箇所よりも下流側に接続して設け、前記加熱用流路15の途中に、前記加熱用熱交換器11を設けてある。
Both ends of the hot water storage circulation path 12 are connected to the bottom and top of the hot water storage tank 5, and the hot water storage circulation path 12 sucks the hot water storage circulation pump 13 against the bottom of the hot water storage tank 5. In addition, the exhaust heat source heat exchanger 14 is provided.
The heat-switching three-way valve 16 having one inlet and two outlets is used to exchange the exhaust heat source heat in the hot water storage circuit 12 using the inlet and one of the two outlets. The heating channel 15 is connected at one end to the remaining outlet of the heating switching three-way valve 16, and is interposed in a portion downstream of the vessel 14 and upstream of the hot water storage tank 5. The other end is connected to the downstream side of the heating switching three-way valve 16 in the hot water storage circulation path 12 and the heating heat exchanger 11 is provided in the middle of the heating flow path 15. is there.

前記加熱切換三方弁16は、前記流入口に流入する湯水の全量を前記加熱用流路15が接続された前記流出口から流出させて前記加熱用流路15に通流させる前記加熱状態と、前記流入口に流入する湯水の全量を前記貯湯用循環路12が接続された前記流出口から流出させて前記加熱用流路15には通流させない前記非加熱状態とに切り換え自在なように構成してある。   The heating switching three-way valve 16 has the heating state in which the entire amount of hot water flowing into the inflow port is caused to flow out of the outflow port to which the heating flow channel 15 is connected and passed through the heating flow channel 15; The entire amount of hot water flowing into the inlet is made to flow out of the outlet to which the hot water storage circulation path 12 is connected and can be switched to the non-heated state where it is not passed through the heating passage 15. It is.

つまり、前記加熱切換三方弁16を前記非加熱状態に切り換えると、前記排熱熱源熱交換器14にて加熱された湯水の全量を前記貯湯タンク5に貯湯する貯湯単独運転モードを実行することができる。
その貯湯単独運転モードでは、図1に太実線にて示すように、貯湯タンク5の底部から取り出された湯水が、前記排熱熱源熱交換器14にて加熱された後、その全量が前記貯湯タンク5の上部に戻される形態で、前記貯湯タンク5の湯水が貯湯用循環路12を通じて循環されることになり、貯湯タンク5に貯湯される。
That is, when the heating switching three-way valve 16 is switched to the non-heating state, a hot water storage independent operation mode in which the entire amount of hot water heated by the exhaust heat source heat exchanger 14 is stored in the hot water storage tank 5 is executed. it can.
In the hot water storage single operation mode, as shown by a thick solid line in FIG. 1, hot water taken out from the bottom of the hot water storage tank 5 is heated by the exhaust heat source heat exchanger 14, and then the entire amount is stored in the hot water storage. The hot water in the hot water storage tank 5 is circulated through the hot water storage circulation path 12 in a form returned to the upper part of the tank 5, and is stored in the hot water storage tank 5.

又、前記加熱切換三方弁16を前記加熱状態に切り換えると、前記排熱熱源熱交換器14にて加熱された湯水の全量を前記加熱用流路15に通流させて、前記加熱用熱交換器11にて前記熱媒循環路21を循環する熱媒を加熱し、並びに、前記排熱熱源熱交換器14を通過した湯水を前記貯湯タンク5に供給して貯湯する並行運転モードを実行することができる。
その並行運転モードでは、図示は省略するが、貯湯タンク5の底部から取り出された湯水が、前記排熱熱源熱交換器14にて加熱され、その全量が前記加熱用熱交換器11を通過して前記熱媒と熱交換した後、貯湯タンク5の上部に戻される形態で、前記貯湯タンク5の湯水が貯湯用循環路12と加熱用流路15とを通じて循環されることになり、前記熱媒循環路21を循環する熱媒が加熱されると共に、貯湯タンク5に貯湯される。
Further, when the heating switching three-way valve 16 is switched to the heating state, the entire amount of hot water heated by the exhaust heat source heat exchanger 14 is passed through the heating flow path 15 and the heat exchange for heating. A parallel operation mode is performed in which the heat medium circulating in the heat medium circulation path 21 is heated in the vessel 11 and hot water that has passed through the exhaust heat source heat exchanger 14 is supplied to the hot water storage tank 5 to store hot water. be able to.
In the parallel operation mode, although not shown, the hot water taken out from the bottom of the hot water storage tank 5 is heated by the exhaust heat source heat exchanger 14, and the entire amount passes through the heating heat exchanger 11. After exchanging heat with the heat medium, the hot water in the hot water storage tank 5 is circulated through the hot water storage circulation path 12 and the heating flow path 15 in a form that is returned to the upper part of the hot water storage tank 5. The heat medium circulating in the medium circulation path 21 is heated and stored in the hot water storage tank 5.

前記燃料電池Gについて説明を加える。
図3に示すように、前記燃料電池Gは、水素を含有する燃料ガス及び酸素含有ガスが供給されて発電するセルスタック30、そのセルスタック30に供給する燃料ガスを生成する燃料ガス生成部R、前記セルスタック30に酸素含有ガスとして空気を供給するブロア31、前記セルスタック30を冷却する冷却水を冷却水循環路32を通じて循環させる冷却水循環ポンプ33、前記セルスタック30から排出される燃料極側排ガスの保有熱を前記冷却水循環路32を通流する冷却水に回収する第1排熱回収用熱交換器34、前記セルスタック30から排出される酸素極側排ガスの保有熱と前記燃料ガス生成部Rから排出される燃焼排ガスの保有熱とを前記冷却水循環路32を通流する冷却水に回収する第2排熱回収用熱交換器35、及び、前記燃料電池Gの各種制御を司る燃料電池制御部36等を備えて構成してある。
The fuel cell G will be further described.
As shown in FIG. 3, the fuel cell G includes a cell stack 30 that generates power by supplying a fuel gas containing hydrogen and an oxygen-containing gas, and a fuel gas generator R that generates fuel gas to be supplied to the cell stack 30. A blower 31 for supplying air as an oxygen-containing gas to the cell stack 30; a cooling water circulation pump 33 for circulating cooling water for cooling the cell stack 30 through a cooling water circulation path 32; and a fuel electrode side discharged from the cell stack 30 The first heat exchanger 34 for recovering exhaust heat that recovers the retained heat of the exhaust gas into the cooling water flowing through the cooling water circulation path 32, the retained heat of the oxygen electrode side exhaust gas discharged from the cell stack 30, and the generation of the fuel gas A second heat recovery heat exchanger 35 for recovering the retained heat of the combustion exhaust gas discharged from the part R into the cooling water flowing through the cooling water circulation path 32, and the front It includes a fuel cell controller 36 or the like that governs various controls of the fuel cell G are constituted.

以下、燃料電池Gを構成する各部について説明を加える。
前記セルスタック30は周知であるので、詳細な説明及び図示は省略して、簡単に説明すると、前記セルスタック30は、電解質層としての高分子膜の両側に酸素極と燃料極を振り分けて配置した固体高分子型のセルの複数を積層状態に設けて構成し、並びに、供給される燃料ガスが各セルの燃料極に分配供給され且つ供給される反応用空気が各セルの酸素極に分配供給されるように構成して、各セルにて水素と酸素との電気化学的な反応により発電を行うように構成してある。
Hereinafter, each part constituting the fuel cell G will be described.
Since the cell stack 30 is well known, detailed description and illustration are omitted, and briefly described. The cell stack 30 is arranged by distributing an oxygen electrode and a fuel electrode on both sides of a polymer film as an electrolyte layer. A plurality of solid polymer cells are provided in a stacked state, and the supplied fuel gas is distributed and supplied to the fuel electrode of each cell, and the supplied reaction air is distributed to the oxygen electrode of each cell. In this configuration, power is generated by an electrochemical reaction between hydrogen and oxygen in each cell.

前記燃料ガス生成部Rは、供給される都市ガス(例えば、天然ガスベースの都市ガス)等の炭化水素系の原燃料ガスを脱硫処理する脱硫器37、その脱硫器37から供給される脱硫原燃料ガスと水蒸気生成器(図示省略)から供給される水蒸気とを改質用バーナ38bの加熱により改質反応させて、水素を主成分とする改質ガスを生成する改質器38、その改質器38から供給される改質ガス中の一酸化炭素を水蒸気にて二酸化炭素に変成処理する変成器39、その変成器39から供給される改質ガス中の一酸化炭素を別途供給される選択酸化用空気にて選択酸化する一酸化炭素除去器40等を備えて構成して、改質ガス中の一酸化炭素を変成処理及び選択酸化処理により低減した一酸化炭素濃度の低い(例えば10ppm以下)改質ガスを生成するように構成してある。
そして、一酸化炭素を変成処理及び選択酸化処理により低減した改質ガスを、前記燃料ガスとして前記セルスタック30に供給するようにしてある。
前記脱硫器37への原燃料ガスの供給を断続し、更に、その供給量を調節する原料ガス調節弁43を設けてあり、この原料ガス調節弁43により原燃料ガスの供給量を調節することにより、前記セルスタック30への燃料ガスの供給量を調節して、前記セルスタック30の出力電力を調節する。
The fuel gas generation unit R includes a desulfurizer 37 that desulfurizes a hydrocarbon-based raw fuel gas such as a supplied city gas (for example, a natural gas-based city gas), and a desulfurization source that is supplied from the desulfurizer 37. A reformer 38 for generating a reformed gas mainly composed of hydrogen by reforming the fuel gas and steam supplied from a steam generator (not shown) by heating the reforming burner 38b. The carbon monoxide in the reformed gas supplied from the reformer 38 is converted to carbon dioxide with steam, and the carbon monoxide in the reformed gas supplied from the shifter 39 is supplied separately. A carbon monoxide remover 40 that selectively oxidizes with selective oxidization air is provided, and the carbon monoxide in the reformed gas is reduced by the conversion treatment and the selective oxidation treatment. Below) reformed gas It is arranged to formed.
Then, the reformed gas obtained by reducing carbon monoxide by the modification process and the selective oxidation process is supplied to the cell stack 30 as the fuel gas.
The supply of the raw fuel gas to the desulfurizer 37 is interrupted, and a raw material gas control valve 43 for adjusting the supply amount is provided, and the supply amount of the raw fuel gas is adjusted by the raw material gas control valve 43. Thus, the amount of fuel gas supplied to the cell stack 30 is adjusted to adjust the output power of the cell stack 30.

前記セルスタック30の各セルの前記燃料極から排出される燃料極側排ガスを、燃料極側排ガス路41を通じて、前記第1排熱回収用熱交換器34を通過させた後、前記改質用バーナ38bに供給し、又、前記ブロア31にて燃焼用空気を前記改質用バーナ38bに供給して、その改質用バーナ38bにて燃料極側排ガスを燃焼させて、改質器38を改質反応が可能なように加熱するようにしてある。
前記セルスタック30の各セルの酸素極から排出される酸素極排ガスと前記改質用バーナ38bから排出される燃焼排ガスとを混合させて、その混合排ガスを前記第2排熱回収用熱交換器35を通過させた後、装置外部に排出するように、混合排ガス路42を前記改質用バーナ38b、前記セルスタック30及び前記第2排熱回収用熱交換器35に接続してある。
After the fuel electrode side exhaust gas discharged from the fuel electrode of each cell of the cell stack 30 passes through the first exhaust heat recovery heat exchanger 34 through the fuel electrode side exhaust gas passage 41, the reforming The combustion air is supplied to the burner 38b, the combustion air is supplied to the reforming burner 38b by the blower 31, and the fuel electrode side exhaust gas is burned by the reforming burner 38b. Heating is performed so that the reforming reaction is possible.
The oxygen electrode exhaust gas discharged from the oxygen electrode of each cell of the cell stack 30 is mixed with the combustion exhaust gas discharged from the reforming burner 38b, and the mixed exhaust gas is mixed with the second exhaust heat recovery heat exchanger. The mixed exhaust gas passage 42 is connected to the reforming burner 38b, the cell stack 30, and the second exhaust heat recovery heat exchanger 35 so as to be discharged outside the apparatus after passing through the apparatus 35.

そして、図1にも示すように、前記冷却水循環路32は、前記セルスタック30を冷却して前記セルスタック30から排出される冷却水を、前記排熱熱源熱交換器14、前記第2排熱回収用熱交換器35、前記第1排熱回収用熱交換器34の順に通流させて、前記セルスタック30に戻すように設け、前記燃料電池Gから発生する熱として、前記燃焼排ガス、前記酸素極側排ガス及び前記燃料極側排ガス夫々の保有熱、並びに、前記セルスタック30から発生する発電反応熱を冷却水に回収させ、その冷却水を前記排熱熱源熱交換器14に通流させて、その排熱熱源熱交換器14において、前記燃料電池Gから発生する熱を回収した冷却水と前記貯湯用循環路12を通流する湯水とを熱交換させて、前記冷却水を冷却すると共に前記湯水を加熱するように構成してある。   As shown in FIG. 1, the cooling water circulation path 32 cools the cell stack 30 and discharges the cooling water discharged from the cell stack 30 to the exhaust heat source heat exchanger 14 and the second exhaust. The heat recovery heat exchanger 35 and the first exhaust heat recovery heat exchanger 34 are passed through in this order to be returned to the cell stack 30, and as the heat generated from the fuel cell G, the combustion exhaust gas, The retained heat of each of the oxygen electrode side exhaust gas and the fuel electrode side exhaust gas and the power generation reaction heat generated from the cell stack 30 are recovered in cooling water, and the cooling water is passed to the exhaust heat source heat exchanger 14. In the exhaust heat source heat exchanger 14, the cooling water recovered from the heat generated from the fuel cell G and the hot water flowing through the hot water storage circuit 12 are heat-exchanged to cool the cooling water. And add the hot water It is arranged to.

又、前記冷却水循環路32において、前記排熱熱源熱交換器14よりも下流側で前記第2排熱回収熱交換器35よりも上流側の箇所には、通流する冷却水を冷却するラジエータ44を設けてある。
更に、前記セルスタック30から排出されて前記冷却水循環路32を通流する冷却水の温度を検出する冷却水温度センサTw、及び、前記排熱熱源熱交換器14にて加熱されて前記貯湯用循環路12を通流する湯水の温度を検出するタンク供給温度センサTeを設けてある。
Further, in the cooling water circulation path 32, a radiator that cools the flowing cooling water at a location downstream of the exhaust heat source heat exchanger 14 and upstream of the second exhaust heat recovery heat exchanger 35. 44 is provided.
Furthermore, it is heated by the cooling water temperature sensor Tw for detecting the temperature of the cooling water discharged from the cell stack 30 and flowing through the cooling water circulation path 32, and the exhaust heat source heat exchanger 14 for the hot water storage. A tank supply temperature sensor Te for detecting the temperature of hot water flowing through the circulation path 12 is provided.

次に、前記燃料電池制御部36について説明を加える。
前記燃料電池制御部36は、図示しない燃料電池操作部から運転開始が指令されると、前記原燃料ガス調節弁43を開弁して前記燃料ガス生成部Rへ原燃料ガスを供給し、且つ、前記ブロア31を作動させて、前記燃料電池Gの運転を開始し、前記燃料電池操作部から運転の停止が指令されると、前記原燃料ガス調節弁43を閉弁して前記燃料ガス生成部Rへの原燃料ガスの供給を停止し、且つ、前記ブロア31を停止させて、前記燃料電池Gの運転を停止する。
そして、前記燃料電池制御部36は、前記燃料電池Gの運転中は、前記電力消費機器8の消費電力、即ち、電力負荷に応じて出力電力を変更調節する電力負荷追従運転を実行するように構成してある。その電力負荷追従運転では、前記燃料電池制御部36は、前記原燃料ガスの供給量が、前記コージェネ用供給ライン9を通じて出力される電力を計測する電力計測部(図示省略)の検出電力に応じた設定供給量になるように、前記原燃料ガス調節弁43の開度を調節し、前記冷却水温度センサTwの検出温度が設定冷却水温度になるように冷却水循環量を調節すべく前記冷却水循環ポンプ33の作動を制御し、且つ、前記タンク供給温度センサTeの検出温度が予め設定した目標貯湯温度になるように湯水循環量を調節すべく前記貯湯用循環ポンプ13を制御するように構成してある。ちなみに、前記目標貯湯温度としては、例えば65°Cに設定する。
又、前記燃料電池制御部36は、前記冷却水循環流量を設定最大流量に調節した状態で、前記冷却水温度センサTwの検出温度が前記設定冷却水温度を越えるときは、前記ラジエータ44のラジエータファン44fを作動させて前記ラジエータ44を放熱作動させ、前記検出温度が前記設定冷却水温度になるように、前記ラジエータファン44fの作動を制御するように構成してある。
Next, the fuel cell control unit 36 will be described.
When the start of operation is commanded from a fuel cell operation unit (not shown), the fuel cell control unit 36 opens the raw fuel gas control valve 43 to supply the raw fuel gas to the fuel gas generation unit R, and The blower 31 is operated to start the operation of the fuel cell G. When the stop of the operation is instructed from the fuel cell operation unit, the raw fuel gas control valve 43 is closed to generate the fuel gas. The supply of the raw fuel gas to the part R is stopped, and the blower 31 is stopped to stop the operation of the fuel cell G.
The fuel cell control unit 36 performs a power load following operation that changes and adjusts the output power according to the power consumption of the power consuming device 8, that is, the power load, during the operation of the fuel cell G. It is configured. In the power load following operation, the fuel cell control unit 36 determines that the supply amount of the raw fuel gas corresponds to the detected power of a power measurement unit (not shown) that measures the power output through the cogeneration supply line 9. In order to adjust the cooling water circulation amount so that the detected temperature of the cooling water temperature sensor Tw becomes the set cooling water temperature, the opening degree of the raw fuel gas control valve 43 is adjusted so that the set supply amount becomes equal. The operation of the water circulation pump 33 is controlled, and the hot water circulation pump 13 is controlled to adjust the hot water circulation amount so that the temperature detected by the tank supply temperature sensor Te becomes a preset target hot water storage temperature. It is. Incidentally, the target hot water storage temperature is set to 65 ° C., for example.
The fuel cell control unit 36 adjusts the radiator fan of the radiator 44 when the detected temperature of the cooling water temperature sensor Tw exceeds the set cooling water temperature with the cooling water circulation flow rate adjusted to the set maximum flow rate. The radiator 44 is operated to dissipate heat, and the operation of the radiator fan 44f is controlled so that the detected temperature becomes the set coolant temperature.

以下、前記熱源制御部20について説明する。
前記熱源制御部20は、前記貯湯タンク5の湯水の水質を維持するための水質維持運転を実行するように構成してある。更に、熱源制御部20は、水質維持運転を実行する必要がある水質維持運転タイミングであるか否かを判別して、前記水質維持運転タイミングにならない間は、通常運転を実行し、前記水質維持運転タイミングになると、水質維持運転を実行するように構成してある。
Hereinafter, the heat source control unit 20 will be described.
The heat source control unit 20 is configured to perform a water quality maintenance operation for maintaining the quality of the hot water in the hot water storage tank 5. Furthermore, the heat source control unit 20 determines whether or not it is a water quality maintenance operation timing at which it is necessary to perform a water quality maintenance operation, and performs a normal operation until the water quality maintenance operation timing is reached. At the operation timing, the water quality maintenance operation is executed.

前記熱源制御部20は、前記通常運転では、前記給水切換三方弁25を前記通常給水状態に維持して、前記給水路4を通じて前記貯湯タンク5の底部に給水する状態に維持した状態で、前記放熱部Wの停止中は前記加熱切換三方弁16を前記非加熱状態にして、前記貯湯単独運転モードにて運転し、前記放熱部Wの運転中は、前記加熱切換三方弁16を前記加熱状態にして、並行運転モードにて運転するように構成してある。
図1に太実線で示すように、その通常運転中に、前記給湯栓が開栓されると、前記貯湯タンク5の上部から湯水が前記給湯路3を通して送出されると共に、前記給水路4を通して前記貯湯タンク5の底部に給水されることになる。
In the normal operation, the heat source control unit 20 maintains the water supply switching three-way valve 25 in the normal water supply state and supplies water to the bottom of the hot water storage tank 5 through the water supply path 4. While the heat dissipating part W is stopped, the heating switching three-way valve 16 is set in the non-heated state and operated in the hot water storage single operation mode. During operation of the heat dissipating part W, the heating switching three-way valve 16 is operated in the heated state. Thus, it is configured to operate in the parallel operation mode.
As shown by a thick solid line in FIG. 1, when the hot water tap is opened during the normal operation, hot water is sent from the upper part of the hot water storage tank 5 through the hot water supply passage 3 and through the water supply passage 4. Water is supplied to the bottom of the hot water storage tank 5.

又、前記熱源制御部20は、前記水質維持運転では、例えば前記給水切換三方弁25を前記タンク迂回給水状態に切り換えた状態で、前記貯湯タンク5全体の湯水が設定水質維持温度以上である状態を設定水質維持時間継続させるように前記加熱部Hを作動させる運転を実行するように構成してある。   Further, in the water quality maintenance operation, the heat source control unit 20 is in a state where the hot water in the entire hot water storage tank 5 is equal to or higher than the set water quality maintenance temperature in a state where the water supply switching three-way valve 25 is switched to the tank bypass water supply state, for example. Is operated to operate the heating unit H so as to continue the set water quality maintenance time.

前記水質維持運転について説明を加える。
設定保持温度として、前記設定水質維持温度と同温度、又は、その設定水質維持温度よりも高い温度に設定する。そして、水質維持運転では、前記給水切換三方弁25を前記タンク迂回給水状態に切り換えた状態で、前記排熱熱源熱交換器14にて前記目標貯湯温度に加熱された湯の全量を前記貯湯タンク5に供給する状態にし、前記4個の貯湯温度センサTtの全てが前記設定保持温度以上の温度を検出している状態になると、前記貯湯タンク5全体の湯水が設定水質維持温度以上である状態になったとして、そのように前記4個の貯湯温度センサTtの全てが前記設定保持温度以上の温度を検出している状態が前記設定水質維持時間継続するまで、前記給水切換三方弁25を前記タンク迂回給水状態にする状態を維持することになる。ちなみに、前記設定水質維持温度としては、例えば60°Cに設定し、本実施形態においては、前記設定保持温度を設定水質維持温度と同温度の60°Cに設定し、そのように設定保持温度を60°Cに設定しているときは、前記設定水質維持時間としては例えば5分間程度に設定する。
The water quality maintenance operation will be explained.
The set holding temperature is set to the same temperature as the set water quality maintenance temperature or a temperature higher than the set water quality maintenance temperature. In the water quality maintenance operation, the hot water heated to the target hot water storage temperature in the exhaust heat source heat exchanger 14 in the state where the water supply switching three-way valve 25 is switched to the tank bypass water supply state, the hot water storage tank 5, and when all of the four hot water storage temperature sensors Tt detect a temperature not lower than the set holding temperature, the hot water in the entire hot water storage tank 5 is not lower than the set water quality maintenance temperature. As described above, the water supply switching three-way valve 25 is turned on until the state where all of the four hot water storage temperature sensors Tt detect the temperature equal to or higher than the set holding temperature continues for the set water quality maintenance time. The state where the tank bypass water supply state is maintained. Incidentally, the set water quality maintenance temperature is set to 60 ° C., for example, and in this embodiment, the set retention temperature is set to 60 ° C. which is the same temperature as the set water quality maintenance temperature. Is set to 60 ° C., the set water quality maintenance time is set to about 5 minutes, for example.

つまり、前記水質維持運転中は、図2に太実線にて示すように、貯湯タンク5の底部から取り出された湯水が、前記排熱熱源熱交換器14にて加熱された後、その全量が前記貯湯タンク5の上部に戻される形態で、前記貯湯タンク5の湯水が貯湯用循環路12を通じて循環されることになり、前記目標貯湯温度に加熱された湯が貯湯タンク5に貯湯される。その水質維持運転中に、前記給湯栓が開栓されると、前記給水路4からの水が前記タンク迂回給水路24を通じて前記貯湯タンク5を迂回して前記給湯路3に供給されて、その水が、前記補助加熱器19の前記給湯用補助加熱部19sにて前記目標給湯温度になるように加熱されることになる。   That is, during the water quality maintenance operation, as shown by a thick solid line in FIG. 2, the hot water taken out from the bottom of the hot water storage tank 5 is heated by the exhaust heat source heat exchanger 14, and then the total amount is The hot water in the hot water storage tank 5 is circulated through the hot water storage circulation path 12 in a form returned to the upper part of the hot water storage tank 5, and hot water heated to the target hot water storage temperature is stored in the hot water storage tank 5. When the hot water tap is opened during the water quality maintenance operation, the water from the water supply channel 4 is supplied to the hot water supply channel 3 by bypassing the hot water storage tank 5 through the tank bypass water supply channel 24, and Water is heated so as to reach the target hot water supply temperature in the hot water supply auxiliary heating section 19 s of the auxiliary heater 19.

熱源制御部20は、水質維持運転の実行中における、少なくとも貯湯タンク5全体の湯水が上記設定水質維持温度以上になるまでの間、熱媒循環路21に熱媒を循環させる状態で暖房用補助加熱部19wを作動させる補助昇温運転を実行するように構成してある。
即ち、前記補助昇温運転では、貯湯用循環路12において前記加熱切換三方弁16を前記加熱状態として、加熱部Hにより加熱された湯水が加熱用熱交換器11を通って貯湯タンク5に供給されるようにし、一方、熱媒循環路21において熱媒循環ポンプ22により熱媒循環路21に循環する熱媒が暖房用補助加熱部19wにより加熱されて加熱用熱交換器11に供給されるようにする。
The heat source control unit 20 assists heating in a state in which the heat medium is circulated through the heat medium circulation path 21 at least until the hot water in the entire hot water storage tank 5 reaches or exceeds the set water quality maintenance temperature during execution of the water quality maintenance operation. The auxiliary heating operation for operating the heating unit 19w is performed.
That is, in the auxiliary temperature raising operation, the heating switching three-way valve 16 is set in the heating state in the hot water storage circuit 12, and hot water heated by the heating unit H is supplied to the hot water storage tank 5 through the heating heat exchanger 11. On the other hand, the heating medium circulating in the heating medium circulation path 21 by the heating medium circulation pump 22 in the heating medium circulation path 21 is heated by the heating auxiliary heating unit 19w and supplied to the heating heat exchanger 11. Like that.

従って、補助昇温運転では、加熱用熱交換器11において、貯湯用循環路12を循環する湯水が、熱媒循環路21を循環する高温の熱媒との熱交換により加熱され、その目標貯湯温度に加熱された湯が貯湯タンク5に貯湯される。   Therefore, in the auxiliary heating operation, in the heating heat exchanger 11, the hot water circulating in the hot water storage circuit 12 is heated by heat exchange with the high-temperature heat medium circulating in the heat medium circuit 21, and the target hot water storage is performed. Hot water heated to the temperature is stored in the hot water storage tank 5.

また、前記熱源制御部20は、前記水質維持運転の実行中に常時上記補助昇温運転を実行するように構成しても構わないが、前記タンク供給温度センサTeの検出温度が水質維持温度未満である間のみ上記補助昇温運転を実行し、前記タンク供給温度センサTeの検出温度が水質維持温度以上である間には、貯湯用循環路12において前記加熱切換三方弁16を前記非加熱状態として、前記排熱熱源熱交換器14にて前記目標貯湯温度に加熱された湯をそのまま前記貯湯タンク5に供給する状態にしても構わない。   Further, the heat source control unit 20 may be configured to always perform the auxiliary temperature raising operation during the water quality maintenance operation, but the temperature detected by the tank supply temperature sensor Te is less than the water quality maintenance temperature. The auxiliary heating operation is executed only during the period of time, and while the temperature detected by the tank supply temperature sensor Te is equal to or higher than the water quality maintenance temperature, the heating switching three-way valve 16 is set in the non-heated state in the hot water storage circuit 12 As described above, the hot water heated to the target hot water storage temperature by the exhaust heat source heat exchanger 14 may be supplied to the hot water storage tank 5 as it is.

更に、熱媒運転制御部20は、上記補助昇温運転の実行中において、熱媒循環状態切換三方弁51を端末機器迂回状態に切り換えるように構成されている。よって、補助昇温運転の実行中は、熱媒循環路21において暖房用補助加熱部19wにより加熱された熱媒が暖房用端末器6に供給されることがないので、暖房用端末器6において不意に暖房が行われてしまうことがない。   Furthermore, the heat medium operation control unit 20 is configured to switch the heat medium circulation state switching three-way valve 51 to the terminal device bypass state during the execution of the auxiliary temperature raising operation. Therefore, during the execution of the auxiliary heating operation, the heating medium heated by the auxiliary heating unit 19w for heating in the heating medium circulation path 21 is not supplied to the heating terminal 6. There is no unexpected heating.

以下、前記熱源制御部20が前記水質維持運転タイミングであるか否かを判別するための構成について、説明を加える。
即ち、前記熱源制御部20は、前記給水路4を通して前記貯湯タンク5に給水され且つ前記貯湯タンク5の湯水が前記給湯路3を通して送出される形態にて前記貯湯タンク5の湯水が入れ替わる湯水入れ替わり状態を判別するように構成してある。
そして、前記熱源制御部20は、前記貯湯タンク5の湯水の温度が前記設定水質維持温度よりも低く且つ前記湯水入れ替わり状態を判別しない状態がタイミング判別用設定時間継続すると前記水質維持運転タイミングになると判別するように構成してある。
Hereinafter, the structure for discriminating whether or not the heat source control unit 20 is the water quality maintenance operation timing will be described.
That is, the heat source control unit 20 supplies hot water to the hot water storage tank 5 through the water supply passage 4 and hot water in the hot water storage tank 5 is replaced with hot water from the hot water storage tank 5 in a form in which hot water from the hot water storage tank 5 is sent out through the hot water supply passage 3. It is configured to determine the state.
And when the state where the temperature of the hot water in the hot water storage tank 5 is lower than the set water quality maintenance temperature and the hot water replacement state is not discriminated continues for the set time for timing judgment, the heat source control unit 20 becomes the water quality maintenance operation timing. It is configured to discriminate.

ちなみに、前記給水切換三方弁25が前記通常給水状態になっている状態での前記補助加熱器19の給湯用補助加熱部19sの流量センサの検出流量を積算し、その積算流量が、予め前記貯湯タンク5の総容量に設定してある設定タンク容量に達しない間は、前記湯水入れ替わり状態でないと判別し、前記積算流量が前記設定タンク容量に達すると前記湯水入れ替わり状態であると判別するように構成してある。
又、前記4個の貯湯温度センサTtの検出情報に基づいて、少なくとも1個の貯湯温度センサTtの検出温度が前記設定水質維持温度よりも低いときは、前記貯湯タンク5の湯水の温度が前記設定水質維持温度よりも低い低貯湯温状態であると判別するように構成してある。
そして、前記低貯湯温状態になると、前記流量センサの検出流量の積算を開始すると共に、同時に、その低貯湯温状態が継続する低貯湯温状態継続時間の計測を開始し、その計測時間が前記タイミング判別用設定時間に達するまでに、前記積算流量が前記設定タンク容量に達すると積算検出流量及び計測時間をリセットして、新たに検出流量の積算及び低貯湯温状態継続時間の計測を開始する、又は、前記4個の貯湯温度センサTtの検出温度の全てが前記設定水質維持温度以上になると積算検出流量及び計測時間をリセットして、前記低貯湯温状態になると新たに検出流量の積算及び低貯湯温状態継続時間の計測を開始する形態で、検出流量の積算及び低貯湯温状態継続時間の計測を繰り返す。そして、低貯湯温状態継続時間の計測時間を前記タイミング判別用設定時間に達するまでにリセットするときは、前記貯湯タンク5の湯水の温度が前記設定水質維持温度よりも低く且つ前記湯水入れ替わり状態を判別しない状態が前記タイミング判別用設定時間継続しないとして、前記水質維持運転タイミングではないと判別し、低貯湯温状態継続時間の計測時間が前記タイミング判別用設定時間に達すると、前記貯湯タンク5の湯水の温度が前記設定水質維持温度よりも低く且つ前記湯水入れ替わり状態を判別しない状態が前記タイミング判別用設定時間継続したとして、前記水質維持運転タイミングになると判別するのである。
Incidentally, the detected flow rate of the flow rate sensor of the hot water supply auxiliary heating portion 19s of the auxiliary heater 19 in a state where the water supply switching three-way valve 25 is in the normal water supply state is integrated, and the integrated flow rate is previously stored in the hot water storage. While the set tank capacity set as the total capacity of the tank 5 is not reached, it is determined that the hot water is not changed, and when the integrated flow rate reaches the set tank capacity, it is determined that the hot water is changed. It is configured.
On the basis of the detection information of the four hot water storage temperature sensors Tt, when the temperature detected by at least one hot water storage temperature sensor Tt is lower than the set water quality maintenance temperature, the temperature of the hot water in the hot water storage tank 5 is It is comprised so that it may discriminate | determine that it is the low hot water storage temperature state lower than preset water quality maintenance temperature.
Then, when the low hot water storage temperature state is reached, the integration of the detected flow rate of the flow sensor is started, and simultaneously, the measurement of the low hot water storage temperature state duration in which the low hot water storage temperature state continues is started, and the measurement time is If the integrated flow rate reaches the set tank capacity before reaching the timing determination set time, the integrated detection flow rate and measurement time are reset, and the detection flow rate integration and measurement of the low hot water storage temperature state duration time are newly started. Alternatively, when all the detected temperatures of the four hot water storage temperature sensors Tt are equal to or higher than the set water quality maintenance temperature, the integrated detection flow rate and measurement time are reset, and when the low hot water storage temperature state is reached, the detection flow rate is newly integrated and Accumulation of the detected flow rate and measurement of the low hot water temperature state duration are repeated in the form of starting the measurement of the low hot water temperature state duration. And when resetting the measurement time of the low hot water storage temperature state time until the timing determination set time is reached, the hot water temperature in the hot water storage tank 5 is lower than the set water quality maintenance temperature and the hot water replacement state is set. If the state not determined does not continue for the timing determination set time, it is determined that it is not the water quality maintenance operation timing, and when the measurement time of the low hot water storage temperature state duration reaches the timing determination set time, the hot water storage tank 5 If the hot water temperature is lower than the set water quality maintenance temperature and the state in which the hot water replacement state is not discriminated continues for the set time for timing discrimination, it is discriminated that the water quality maintenance operation timing is reached.

ちなみに、前記タイミング判別用設定時間としては、前記貯湯タンク5に前記設定水質維持温度よりも低い温度の湯水が入れ替えられない状態で貯留されることにより水質が低下すると考えられる最も短い時間の半分程度の時間に設定する。このように前記タイミング判別用設定時間を設定することにより、前記水質維持運転が頻繁に実行されるのを回避しながら、貯湯タンク5の湯水の水質が低下する虞がある状態となる水質維持運転の実行が必要な時期になると水質維持運転を実行するようにすることが可能になる。   By the way, the set time for the timing determination is about half of the shortest time that the water quality is considered to be deteriorated by storing the hot water at a temperature lower than the set water quality maintenance temperature in the hot water storage tank 5 without being replaced. Set the time. By setting the timing determination setting time in this manner, the water quality maintenance operation in which the quality of the hot water in the hot water storage tank 5 may be lowered while avoiding frequent execution of the water quality maintenance operation. It is possible to perform water quality maintenance operation when it is necessary to perform the operation.

つまり、例えば、旅行等により、前記燃料電池G及び前記給湯熱源装置Aの運転が停止されて、前記貯湯タンク5の湯水が加熱されず且つ前記貯湯タンク5から前記給湯路3を通じて湯水が送出されない状態が継続すると、前記水質維持運転タイミングになると判別される場合がある。
又、前記並行運転モードにて前記通常運転が実行されると、前記設定水質維持温度よりも低い温度の湯が前記貯湯タンク5に供給される場合があるので、前記並行運転モードにて前記通常運転が実行され且つ前記貯湯タンク5から前記給湯路3を通じて湯水が送出されない状態が継続すると、前記水質維持運転タイミングになると判別される場合がある。
又、前記燃料電池Gが出力電力の小さい低負荷運転されるときは、発生熱量が少なくて、前記排熱熱源熱交換器14にて湯水が前記目標貯湯温度にまで加熱されない場合があり、このように前記燃料電池Gが低負荷運転され且つ前記貯湯タンク5から前記給湯路3を通じて湯水が送出されない状態が継続すると、前記水質維持運転タイミングになると判別される場合がある。
That is, for example, due to travel or the like, the operation of the fuel cell G and the hot water supply heat source device A is stopped, the hot water in the hot water storage tank 5 is not heated, and hot water is not sent from the hot water storage tank 5 through the hot water supply passage 3. If the state continues, it may be determined that the water quality maintenance operation timing is reached.
Further, when the normal operation is executed in the parallel operation mode, hot water having a temperature lower than the set water quality maintenance temperature may be supplied to the hot water storage tank 5, so the normal operation is performed in the parallel operation mode. If the operation is executed and the state where hot water is not sent from the hot water storage tank 5 through the hot water supply passage 3 continues, it may be determined that the water quality maintenance operation timing is reached.
In addition, when the fuel cell G is operated at a low load with a small output power, the amount of generated heat is small and the hot water may not be heated to the target hot water temperature in the exhaust heat source heat exchanger 14. As described above, when the fuel cell G is operated at a low load and no hot water is sent from the hot water storage tank 5 through the hot water supply passage 3, it may be determined that the water quality maintenance operation timing is reached.

又、水道の断水に伴って前記バキュームブレーカー26が作動して、前記貯湯タンク5内に外気が侵入する外気侵入状態が発生すると、前記貯湯タンク5内の湯水の水質が低下する虞がある。
そこで、前記熱源制御部20を、前記給水圧センサ27の検出圧力が前記設定タンク給水圧よりも低くなることに基づいて前記外気侵入状態が発生したと判別して、前記水質維持運転タイミングになると判別するように構成してある。
In addition, when the vacuum breaker 26 is actuated in response to the water cut off and an outside air intrusion state occurs in which the outside air enters the hot water storage tank 5, the quality of the hot water in the hot water storage tank 5 may be deteriorated.
Therefore, when the heat source control unit 20 determines that the outside air intrusion state has occurred based on the detected pressure of the feed water pressure sensor 27 being lower than the set tank feed water pressure, the water quality maintenance operation timing is reached. It is configured to discriminate.

又、前記給湯熱源装置Aが設置されて、前記貯湯タンク5に初めて水が充填されたときや、メンテナンス等により、前記貯湯タンク5の水を入れ替えたとき等は、貯湯タンク5の湯水の温度が低く水質が低下する虞がある。
そこで、前記水質維持運転の実行を指令する水質維持運転指令スイッチ(図示省略)を設けてあり、前記熱源制御部20を、前記水質維持運転指令スイッチにて前記水質維持運転の実行が指令されると、前記水質維持運転タイミングになると判別するように構成してある。
When the hot water supply heat source device A is installed and the hot water storage tank 5 is filled with water for the first time, or when the water in the hot water storage tank 5 is replaced by maintenance or the like, the temperature of the hot water in the hot water storage tank 5 is changed. The water quality is likely to be low.
Therefore, a water quality maintenance operation command switch (not shown) for commanding execution of the water quality maintenance operation is provided, and the heat source control unit 20 is commanded to execute the water quality maintenance operation by the water quality maintenance operation command switch. And the water quality maintenance operation timing is determined.

次に、前記熱源制御部20により、前記貯湯単独モードでの通常運転、前記並行運転モードでの通常運転、前記水質維持運転に運転状態を切り換えて運転する制御動作について説明を加える。
前記熱源制御部20は、前記熱媒戻し温度センサTmにて検出される熱媒戻し温度に基づいて、その熱媒戻し温度が設定熱媒戻し温度以下のときは前記放熱部Wが停止中であると判別し、前記熱媒戻し温度が前記設定熱媒戻し温度よりも高くなると前記放熱部Wが放熱運転中であると判別するように構成してある。
つまり、前記放熱運転操作部23から運転開始が指令されて、前記熱媒循環ポンプ22が作動して前記熱媒循環路21を熱媒が循環すると、その熱媒の温度が前記目標熱媒温度よりも低いときは、熱媒が前記補助加熱器19の前記暖房用補助加熱部19wにて前記目標熱媒温度に加熱されて、前記熱媒戻し温度センサTmの検出温度が前記設定熱媒戻し温度よりも高くなり、前記放熱部Wの運転が開始されたことが判別される。又、前記放熱運転操作部23から運転停止が指令されて、前記熱媒循環ポンプ22が停止して前記熱媒循環路21の熱媒の循環が停止すると、熱媒の温度が低下して、前記熱媒戻し温度センサTmの検出温度が前記設定熱媒戻し温度以下となり、前記放熱部Wの運転が停止されたことが判別される。
Next, a description will be given of a control operation in which the heat source control unit 20 operates by switching the operation state to the normal operation in the hot water storage single mode, the normal operation in the parallel operation mode, and the water quality maintenance operation.
The heat source control unit 20 is based on the heat medium return temperature detected by the heat medium return temperature sensor Tm, and when the heat medium return temperature is equal to or lower than the set heat medium return temperature, the heat radiating unit W is stopped. When it is determined that there is a heat medium return temperature higher than the set heat medium return temperature, it is determined that the heat dissipating part W is in a heat dissipating operation.
That is, when an operation start is instructed from the heat radiation operation operation unit 23 and the heat medium circulation pump 22 is operated and the heat medium circulates in the heat medium circulation path 21, the temperature of the heat medium becomes the target heat medium temperature. Is lower than the heating medium, the heating medium is heated to the target heating medium temperature in the heating auxiliary heating unit 19w of the auxiliary heater 19, and the detected temperature of the heating medium return temperature sensor Tm is set to the set heating medium return. It becomes higher than temperature and it is discriminate | determined that the driving | operation of the said thermal radiation part W was started. Further, when the operation stop is instructed from the heat radiation operation operation unit 23 and the heat medium circulation pump 22 is stopped and the circulation of the heat medium in the heat medium circulation path 21 is stopped, the temperature of the heat medium is decreased, It is determined that the detected temperature of the heat medium return temperature sensor Tm is equal to or lower than the set heat medium return temperature and the operation of the heat radiating unit W is stopped.

そして、前記熱源制御部20は、前記水質維持運転タイミングでないと判別している状態においては、前記熱媒戻し温度センサTmにて検出される熱媒戻し温度が前記設定熱媒戻し温度以下で前記放熱部Wが停止中であると判別している間は、前記給水切換三方弁25を前記通常給水状態にし且つ前記加熱切換三方弁16を前記非加熱状態にする貯湯単独運転モードにて通常運転を実行し、その貯湯単独運転モードでの通常運転の実行中に、前記熱媒戻し温度センサTmにて検出される熱媒戻し温度が前記設定熱媒戻し温度よりも高くなって、前記放熱部Wの放熱運転が開始されたと判別すると、前記加熱切換三方弁16を前記加熱状態に切り換えて、前記貯湯単独運転モードから前記並行運転モードに切り換え、その並行運転モードでの通常運転を実行中に、前記熱媒戻し温度センサTmにて検出される熱媒戻し温度が前記設定熱媒戻し温度以下になって、前記放熱部Wの放熱運転が停止されたと判別すると、前記加熱切換三方弁16を前記非加熱状態に切り換えて、並行運転モードから前記貯湯単独運転モードに切り換える。   Then, in a state where the heat source control unit 20 determines that it is not the water quality maintenance operation timing, the heat medium return temperature detected by the heat medium return temperature sensor Tm is equal to or lower than the set heat medium return temperature. While it is determined that the heat dissipating part W is stopped, the normal operation is performed in the hot water storage single operation mode in which the water supply switching three-way valve 25 is in the normal water supply state and the heating switching three-way valve 16 is in the non-heating state. And during the normal operation in the hot water storage single operation mode, the heat medium return temperature detected by the heat medium return temperature sensor Tm becomes higher than the set heat medium return temperature, and the heat radiating unit When it is determined that the heat release operation of W has been started, the heating switching three-way valve 16 is switched to the heating state, the hot water storage single operation mode is switched to the parallel operation mode, and the communication in the parallel operation mode is performed. If it is determined that the heat medium return temperature detected by the heat medium return temperature sensor Tm is equal to or lower than the set heat medium return temperature and the heat release operation of the heat radiating unit W is stopped during the operation, the heating The switching three-way valve 16 is switched to the non-heating state to switch from the parallel operation mode to the hot water storage single operation mode.

前記熱源制御部20は、前記水質維持運転タイミングに達したと判別すると、前記給水切換三方弁25を前記タンク迂回給水状態に切り換え、前記加熱切換三方弁16が前記非加熱状態の時はその状態を継続し、前記加熱切換三方弁16が前記加熱状態のときは前記非加熱状態に切り換えて、前記4個の貯湯温度センサTtの全てが前記設定保持温度以上の温度を検出している状態となり、更にその状態が設定水質維持時間継続されるまで前記加熱切換三方弁16が前記非加熱状態である状態を維持し、前記設定水質維持時間が経過すると、前記給水切換三方弁25を前記通常給水状態に切り換え、前記放熱部Wが放熱運転中か否かに応じて、前記加熱切換三方弁16が前記非加熱状態である状態を継続するか前記加熱切換三方弁16を前記加熱状態に切り換える。
尚、前記燃料電池Gの停止中に前記水質維持運転タイミングになると、前記燃料電池Gの運転が開始されて、前記貯湯用循環ポンプ13が運転されるのに伴って、前記貯湯タンク5への貯湯が開始されることになる。
When determining that the water quality maintenance operation timing has been reached, the heat source control unit 20 switches the water supply switching three-way valve 25 to the tank bypass water supply state, and when the heating switching three-way valve 16 is in the non-heating state, When the heating switching three-way valve 16 is in the heating state, the heating switching three-way valve 16 is switched to the non-heating state, and all the four hot water storage temperature sensors Tt detect a temperature equal to or higher than the set holding temperature. Further, the heating switching three-way valve 16 is maintained in the non-heated state until the state continues for the set water quality maintenance time, and when the set water quality maintenance time has elapsed, the water supply switching three-way valve 25 is switched to the normal water supply. Depending on whether or not the heat dissipating part W is in a heat dissipating operation, the heating switching three-way valve 16 continues to be in the non-heating state or the heating switching three-way valve 16 is It switched to the heat state.
When the water quality maintenance operation timing is reached while the fuel cell G is stopped, the operation of the fuel cell G is started and the hot water storage circulation pump 13 is operated. Hot water storage will be started.

このように水質維持運転が実行されると、前記貯湯タンク5内並びに前記貯湯用循環路12内の湯水の全てが前記設定水質維持温度(例えば60°C)以上の温度にて前記設定水質維持時間(例えば5分間)保持されることになるので、湯水の水質を維持することが可能になる。   When the water quality maintenance operation is executed in this way, all the hot water in the hot water storage tank 5 and the hot water storage circuit 12 is maintained at the set water quality at a temperature equal to or higher than the set water quality maintenance temperature (for example, 60 ° C.). Since the time is maintained (for example, 5 minutes), the quality of the hot water can be maintained.

つまり、図1に示すように、前記熱源制御部20及び前記燃料電池制御部36により、制御手段Cを構成してあり、その制御手段Cは、前記貯湯タンク5に目標貯湯温度で貯湯されるように前記加熱部Hの作動を制御する制御、前記給水切換三方弁25の作動の制御、前記水質維持運転タイミングであるか否かの判別、水質維持運転を実行させるように前記加熱部Hを作動させる制御、及び、前記湯水入れ替わり状態であるか否かの判別等を実行する。   That is, as shown in FIG. 1, the heat source control unit 20 and the fuel cell control unit 36 constitute a control means C, and the control means C stores hot water in the hot water storage tank 5 at a target hot water storage temperature. Control for controlling the operation of the heating unit H, control of the operation of the water supply switching three-way valve 25, determination of whether or not it is the water quality maintenance operation timing, and the heating unit H to execute the water quality maintenance operation Control to be operated, determination of whether or not the hot water is changed, and the like are executed.

貯湯用循環路12内の湯水を設定水質維持温度以上に保持する水質維持運転中において、燃料電池Gの運転を継続させるためには、ラジエータ44を運転して、冷却水循環路32を通流する冷却水を十分に冷却する必要がある。   In order to continue the operation of the fuel cell G during the water quality maintenance operation in which the hot water in the hot water storage circuit 12 is maintained at the set water quality maintenance temperature or higher, the radiator 44 is operated and the cooling water circuit 32 is caused to flow. It is necessary to cool the cooling water sufficiently.

更に、上記実施の形態では、ラジエータ44は、燃料電池G側の冷却水循環路32に設けたが、別に、このラジエータ44を、貯湯用循環路12において、前記排熱熱源熱交換器14よりも上流側で前記貯湯タンク5よりも下流側の箇所に設けても構わない。
そして、このように貯湯用循環路12にラジエータ44を設ける場合には、水質維持運転中において、燃料電池Gの運転を継続させるためには、貯湯用循環路12内の全ての湯水を設定水質維持温度以上に保持することができないが、このような場合には、水質維持運転中において、燃料電池G及びラジエータ44の運転を停止して、貯湯用循環路12内の全ての湯水を設定水質維持温度以上に保持するように構成しても構わない。
Furthermore, in the above-described embodiment, the radiator 44 is provided in the cooling water circulation path 32 on the fuel cell G side. Separately, the radiator 44 is provided in the hot water storage circulation path 12 more than the exhaust heat source heat exchanger 14. You may provide in the location downstream from the said hot water storage tank 5 in the upstream.
When the radiator 44 is provided in the hot water storage circuit 12 as described above, in order to continue the operation of the fuel cell G during the water quality maintenance operation, all the hot water in the hot water storage circuit 12 is set to the set water quality. In such a case, during the water quality maintenance operation, the operation of the fuel cell G and the radiator 44 is stopped and all the hot water in the hot water storage circuit 12 is set to the set water quality. You may comprise so that it may hold | maintain above maintenance temperature.

〔第2実施形態〕
以下、図面に基づいて、本発明にかかる給湯熱源装置をコージェネレーションシステムに適用した場合の第2実施形態を説明する。
この第2実施形態においては、第1実施形態と同じ構成要素や同じ作用を有する構成要素については、重複説明を避けるために、同じ符号を付すことにより説明を省略し、主として、第1実施形態と異なる構成を説明する。
図4に示すように、この第2実施形態においては、第1実施形態に加えて、水質維持運転の実行中における、少なくとも前記貯湯タンク5全体の湯水が前記設定水質維持温度以上になるまでの間、前記燃料電池Gの後述する余剰電力を前記貯湯タンク5に貯湯するための熱に変換する電気ヒータ28を設けてある。
[Second Embodiment]
Hereinafter, based on drawing, 2nd Embodiment at the time of applying the hot-water supply heat source apparatus concerning this invention to a cogeneration system is described.
In the second embodiment, the same components as those in the first embodiment and the components having the same functions are denoted by the same reference numerals in order to avoid redundant description, and the description thereof is mainly omitted. A different configuration will be described.
As shown in FIG. 4, in the second embodiment, in addition to the first embodiment, during the execution of the water quality maintenance operation, at least the hot water in the entire hot water storage tank 5 is equal to or higher than the set water quality maintenance temperature. In the meantime, an electric heater 28 is provided for converting surplus electric power, which will be described later, of the fuel cell G into heat for storing hot water in the hot water storage tank 5.

前記電気ヒータ28について説明を加える。
前記電気ヒータ28は、複数の電気ヒータから構成し、前記冷却水循環路32における前記燃料電池G(具体的には前記セルスタック30)よりも下流側で且つ前記排熱熱源熱交換器14よりも上流側の部分を通流する前記燃料電池Gの冷却水を加熱するように設けると共に、各電気ヒータに対応する作動スイッチ29を介して前記コージェネ用供給ライン9に接続してある。
そして、オン状態にする前記作動スイッチ29の個数の調節により、電気ヒータ28の消費電力を調整するように構成してある。
The electric heater 28 will be further described.
The electric heater 28 is composed of a plurality of electric heaters, and is downstream of the fuel cell G (specifically, the cell stack 30) in the cooling water circulation path 32 and more than the exhaust heat source heat exchanger 14. The cooling water of the fuel cell G flowing through the upstream portion is provided to be heated, and is connected to the cogeneration supply line 9 via an operation switch 29 corresponding to each electric heater.
The power consumption of the electric heater 28 is adjusted by adjusting the number of the operation switches 29 to be turned on.

次に、前記熱源制御部20及び前記燃料電池制御部36について説明を加える。
前記熱源制御部20及び前記燃料電池制御部36は、互いに制御情報の通信が可能なように構成してあり、燃料電池制御部36には、熱源制御部20から前記通常運転の実行中か、前記水質維持運転の実行中かを示す情報が通信されるようになっている。尚、前記目標貯湯温度、前記設定水質維持温度、前記設定保持温度及び前記設定水質維持時間は、上記の第1実施形態と同様に設定してある。
Next, the heat source control unit 20 and the fuel cell control unit 36 will be described.
The heat source control unit 20 and the fuel cell control unit 36 are configured to be able to communicate control information with each other, and the fuel cell control unit 36 is performing the normal operation from the heat source control unit 20 or Information indicating whether the water quality maintenance operation is being performed is communicated. The target hot water storage temperature, the set water quality maintenance temperature, the set holding temperature, and the set water quality maintenance time are set in the same manner as in the first embodiment.

前記熱源制御部20は、第1実施形態における加熱切換三方弁16の切り換え制御を省略した以外は、第1実施形態と同様に構成してある。
つまり、前記熱源制御部20は、前記貯湯タンク5の湯水の水質を維持するために水質維持運転を実行する必要がある水質維持運転タイミングであるか否かを判別して、前記水質維持運転タイミングにならない間は、通常運転を実行し、前記水質維持運転タイミングになると、水質維持運転を実行するように構成してある。
The heat source control unit 20 is configured in the same manner as in the first embodiment except that the switching control of the heat switching three-way valve 16 in the first embodiment is omitted.
That is, the heat source control unit 20 determines whether or not it is a water quality maintenance operation timing at which it is necessary to perform a water quality maintenance operation in order to maintain the quality of the hot water in the hot water storage tank 5, and the water quality maintenance operation timing is determined. During this period, normal operation is performed, and when the water quality maintenance operation timing comes, the water quality maintenance operation is executed.

前記熱源制御部20の制御動作について説明を加えると、前記熱源制御部20は、前記通常運転では、前記給水切換三方弁25を前記通常給水状態に維持し、前記水質維持運転タイミングになると、前記給水切換三方弁25を前記タンク迂回給水状態に切り換え、前記4個の貯湯温度センサTtの全てが前記設定保持温度以上の温度を検出している状態になり、更に、その状態が前記設定水質維持時間継続すると、前記給水切換三方弁25を前記通常給水状態に切り換えるように構成してある。   When the control operation of the heat source control unit 20 is described, the heat source control unit 20 maintains the water supply switching three-way valve 25 in the normal water supply state in the normal operation, and when the water quality maintenance operation timing is reached, The water supply switching three-way valve 25 is switched to the tank bypass water supply state, and all of the four hot water storage temperature sensors Tt are in a state of detecting a temperature equal to or higher than the set holding temperature. When the time continues, the water supply switching three-way valve 25 is configured to switch to the normal water supply state.

尚、前記熱源制御部20が前記水質維持運転タイミングであるか否かを判別するための構成は、上記の第1実施形態と同様であるので、その説明を省略する。
つまり、この第2実施形態では、旅行等により、前記燃料電池G及び前記給湯熱源装置Aの運転が停止されて、前記貯湯タンク5の湯水が加熱されず且つ前記貯湯タンク5から前記給湯路3を通じて湯水が送出されない状態が継続したり、前記燃料電池Gが出力電力の小さい低負荷運転され且つ前記貯湯タンク5から前記給湯路3を通じて湯水が送出されない状態が継続したりすると、前記水質維持運転タイミングになると判別される場合がある。
又、前記給水圧センサ27の検出圧力が前記設定タンク給水圧よりも低くなることに基づいて前記外気侵入状態が発生したと判別して、前記水質維持運転タイミングになると判別し、又、前記水質維持運転指令スイッチにて前記水質維持運転の実行が指令されると、前記水質維持運転タイミングになると判別することになる。
In addition, since the structure for discriminating whether the said heat source control part 20 is the said water quality maintenance operation timing is the same as that of said 1st Embodiment, the description is abbreviate | omitted.
That is, in the second embodiment, the operation of the fuel cell G and the hot water supply heat source device A is stopped due to travel or the like, the hot water in the hot water storage tank 5 is not heated, and the hot water supply path 3 is connected to the hot water supply path 3. When the state where hot water is not sent through continues or when the fuel cell G is operated at a low load with low output power and the state where hot water is not sent from the hot water storage tank 5 through the hot water supply passage 3 continues, the water quality maintenance operation is performed. It may be determined that it is time.
Further, it is determined that the outside air intrusion state has occurred based on the detected pressure of the water supply pressure sensor 27 being lower than the set tank water supply pressure, and it is determined that the water quality maintenance operation timing is reached. When execution of the water quality maintenance operation is commanded by the maintenance operation command switch, it is determined that the water quality maintenance operation timing is reached.

前記燃料電池制御部36は、前記熱源制御部20から前記通常運転の実行中であることを示す情報が通信されている間は、電力負荷に応じて出力電力を変更調節する電力負荷追従運転を実行し、前記熱源制御部20から前記水質維持運転の実行中であることを示す情報が通信されている間は、前記燃料電池Gの出力電力をその調節範囲における最大値に設定された設定最大出力電力に調節し且つ前記燃料電池Gの余剰電力を前記電気ヒータ28にて消費するように前記スイッチ29の作動を制御する最大出力運転を実行するように構成してある。   While the information indicating that the normal operation is being performed is communicated from the heat source control unit 20, the fuel cell control unit 36 performs a power load following operation for changing and adjusting the output power according to the power load. While the information indicating that the water quality maintenance operation is being performed is communicated from the heat source control unit 20, the output power of the fuel cell G is set to the maximum value in the adjustment range. A maximum output operation for controlling the operation of the switch 29 is executed so as to adjust the output power and to consume the surplus power of the fuel cell G by the electric heater 28.

ちなみに、前記負荷追従運転において、前記電力負荷が前記設定最大出力電力を越えるときは、前記燃料電池Gの出力電力が前記設定最大出力電力に調節され、前記電力負荷のうち、前記燃料電池Gの出力電力では不足する分が、前記商用電源1から供給されることになり、前記最大出力運転の実行中は、前記電力負荷が前記設定最大出力電力よりも小さいときは、余剰電力が生じることになる。
つまり、前記燃料電池制御部36は、前記水質維持運転の実行中は余剰電力を生じさせるべく前記電力負荷よりも大きい電力を発電するように、前記燃料電池Gの運転を制御するように構成してある。
Incidentally, in the load following operation, when the power load exceeds the set maximum output power, the output power of the fuel cell G is adjusted to the set maximum output power, and the fuel cell G of the power load is out of the power load. Insufficient output power will be supplied from the commercial power source 1, and during execution of the maximum output operation, if the power load is smaller than the set maximum output power, surplus power will be generated. Become.
That is, the fuel cell control unit 36 is configured to control the operation of the fuel cell G so as to generate electric power larger than the electric power load so as to generate surplus electric power during the execution of the water quality maintenance operation. It is.

前記燃料電池制御部36の制御動作について説明を加える。
前記熱源制御部20から前記通常運転の実行中であることを示す情報が通信されている間は、前記原燃料ガスの供給量が前記電力計測部の検出電力に応じた設定供給量になるように前記原燃料ガス調節弁43を制御して、前記電力負荷追従運転を実行する。
その電力負荷追従運転の実行中に、前記熱源制御部20から前記水質維持運転の実行中であることを示す情報が通信されてくると、前記原燃料ガスの供給量が前記設定最大出力電力に応じた設定供給量になるように前記原燃料供給量調節弁43を制御し、且つ、前記燃料電池Gの余剰電力を前記電気ヒータ28にて消費するように前記スイッチ29の作動を制御して、前記最大出力運転を開始し、その最大出力運転の実行中に、前記熱源制御部20から前記通常運転の実行中であることを示す情報が通信されてくると、前記電力負荷追従運転に切り換える。尚、前記冷却水循環ポンプ33及び前記貯湯用循環ポンプ13は、上記の第1実施形態と同様に制御するので、その説明を省略する。
The control operation of the fuel cell control unit 36 will be described.
While the information indicating that the normal operation is being performed is communicated from the heat source control unit 20, the supply amount of the raw fuel gas becomes a set supply amount corresponding to the detected power of the power measurement unit. The raw fuel gas control valve 43 is controlled to execute the power load following operation.
When information indicating that the water quality maintenance operation is being performed is communicated from the heat source control unit 20 during the power load following operation, the supply amount of the raw fuel gas is set to the set maximum output power. The raw fuel supply amount adjustment valve 43 is controlled so as to obtain a set supply amount according to the control, and the operation of the switch 29 is controlled so that surplus power of the fuel cell G is consumed by the electric heater 28. When the information indicating that the normal operation is being executed is transmitted from the heat source control unit 20 during the execution of the maximum output operation, the operation is switched to the power load following operation. . The cooling water circulation pump 33 and the hot water circulation pump 13 are controlled in the same manner as in the first embodiment, and the description thereof is omitted.

つまり、図4に示すように、前記水質維持運転では、前記燃料電池Gの冷却水が、燃料電池Gの発生熱により加熱され且つ前記電気ヒータ28により燃料電池Gの余剰電力を用いて加熱されながら、前記排熱熱源熱交換器14を通過して前記冷却水循環路32を循環され、並びに、貯湯タンク5の底部から取り出された湯水が、前記排熱熱源熱交換器14にて加熱された後、前記貯湯タンク5の上部に戻される形態で、前記貯湯タンク5の湯水が貯湯用循環路12を通じて循環されることになり、前記目標貯湯温度に加熱された湯が貯湯タンク5に貯湯される。その水質維持運転中に、前記給湯栓が開栓されると、前記給水路4からの水が前記タンク迂回給水路24を通じて前記貯湯タンク5を迂回して前記給湯路3に供給されて、その水が、前記補助加熱器19の前記給湯用補助加熱部19sにて前記目標給湯温度になるように加熱されることになる。   That is, as shown in FIG. 4, in the water quality maintenance operation, the cooling water of the fuel cell G is heated by the heat generated by the fuel cell G and is heated by the electric heater 28 using the surplus power of the fuel cell G. However, the hot water that was passed through the exhaust heat source heat exchanger 14 and circulated through the cooling water circulation path 32 and was taken out from the bottom of the hot water storage tank 5 was heated by the exhaust heat source heat exchanger 14. Thereafter, the hot water in the hot water storage tank 5 is circulated through the hot water storage circulation path 12 in a form returned to the upper part of the hot water storage tank 5, and the hot water heated to the target hot water storage temperature is stored in the hot water storage tank 5. The When the hot water tap is opened during the water quality maintenance operation, the water from the water supply channel 4 is supplied to the hot water supply channel 3 by bypassing the hot water storage tank 5 through the tank bypass water supply channel 24, and Water is heated so as to reach the target hot water supply temperature in the hot water supply auxiliary heating section 19 s of the auxiliary heater 19.

この第2実施形態においては、水質維持運転では、第1実施形態におけるよりも、前記燃料電池Gの冷却水により多い熱量を与えることが可能になるので、貯湯タンク5全体の湯水が前記設定保持温度以上になるまで、つまり、前記設定水質維持温度以上になるまでの時間を短縮することが可能となり、前記水質維持運転の所要時間を短縮することが可能になる。   In the second embodiment, in the water quality maintenance operation, it becomes possible to give a larger amount of heat to the cooling water of the fuel cell G than in the first embodiment. It becomes possible to shorten the time until the temperature is higher than the temperature, that is, the time until the temperature is higher than the set water quality maintenance temperature, and the time required for the water quality maintenance operation can be shortened.

図4に示すように、この第2実施形態においても、前記熱源制御部20及び前記燃料電池制御部36により、制御手段Cを構成してあり、その制御手段Cは、前記貯湯タンク5に目標貯湯温度で貯湯されるように前記加熱部Hの作動を制御する制御、前記給水切換三方弁25の作動の制御、前記水質維持運転タイミングであるか否かの判別、水質維持運転を実行させるように前記加熱部Hを作動させる制御、前記湯水入れ替わり状態であるか否かの判別、及び、通常運転の実行中は電力負荷に応じた電力を発電し、前記水質維持運転の実行中は余剰電力を生じさせるべく前記電力負荷よりも大きい電力を発電するように燃料電池Gの運転を制御する制御等を実行する。   As shown in FIG. 4, also in the second embodiment, the heat source control unit 20 and the fuel cell control unit 36 constitute a control means C, and the control means C is used as a target for the hot water storage tank 5. Control for controlling the operation of the heating unit H so as to store hot water at the hot water storage temperature, control of the operation of the water supply switching three-way valve 25, determination of whether or not it is the water quality maintenance operation timing, and water quality maintenance operation are executed. Control for operating the heating unit H, determining whether or not the hot water is switched, and generating electric power according to the power load during execution of normal operation, and surplus power during execution of the water quality maintenance operation Control for controlling the operation of the fuel cell G so as to generate electric power larger than the electric power load is performed.

〔別実施形態〕
次に別実施形態を説明する。
(イ) 上記の各実施形態においては、前記貯湯タンク5を密閉式に構成する場合について例示したが、貯湯タンク5を開放式にして、その貯湯タンク5内の湯水を前記給湯路3を通じて送出する給湯ポンプを設けても良い。この場合は、前記給水状態切換手段は、前記給水切換三方弁25に加えて前記給湯ポンプも備えて構成することになり、その給湯ポンプの運転と停止の切り換えにより、前記貯湯タンク5から前記給湯路3への湯水の送出を許容する状態と停止する状態とに切り換えることになる。
[Another embodiment]
Next, another embodiment will be described.
(A) In each of the above embodiments, the case where the hot water storage tank 5 is configured to be sealed is illustrated, but the hot water storage tank 5 is opened and the hot water in the hot water storage tank 5 is sent out through the hot water supply passage 3. A hot water supply pump may be provided. In this case, the water supply state switching means is configured to include the hot water supply pump in addition to the water supply switching three-way valve 25, and the hot water storage tank 5 can switch the hot water supply by switching the operation and stop of the hot water supply pump. The state is switched between a state in which hot water is allowed to be sent to the passage 3 and a state in which the hot water is stopped.

(ロ) 上記の第1実施形態においては、前記排熱熱源熱交換器14にて湯水を前記目標貯湯温度に加熱するように湯水循環量を調節するための前記貯湯用循環ポンプ13の制御、即ち、前記加熱部Hの作動の制御を、前記燃料電池制御部36に行わせるように構成したが、前記熱源制御部20に行わせるように構成しても良い。この場合は、前記制御手段Cを前記熱源制御部20のみにて構成することになる。
上記の第2実施形態において、前記給湯熱源装置Aの運転を制御する熱源制御部20と前記燃料電池Gの運転を制御する燃料電池制御部36とを各別に構成する場合について例示したが、前記給湯熱源装置A及び前記燃料電池G夫々の運転を制御する1個の制御部を設けても良い。この場合は、前記1個の制御部にて前記制御手段Cを構成することになる。
(B) In the first embodiment, the control of the hot water circulation pump 13 for adjusting the hot water circulation amount so as to heat the hot water to the target hot water temperature in the exhaust heat source heat exchanger 14; That is, the fuel cell control unit 36 is configured to control the operation of the heating unit H, but may be configured to be performed by the heat source control unit 20. In this case, the control means C is configured only by the heat source control unit 20.
In said 2nd Embodiment, although illustrated about the case where the heat source control part 20 which controls the driving | operation of the said hot water supply heat source apparatus A and the fuel cell control part 36 which controls the driving | operation of the said fuel cell G were each comprised separately, One controller for controlling the operation of each of the hot water supply heat source device A and the fuel cell G may be provided. In this case, the control means C is configured by the one control unit.

(ハ) 上記の第1実施形態において、前記補助加熱器19の前記給湯用補助加熱部19s及び暖房用補助加熱部19w夫々の燃焼制御部を省略して、それら各燃焼制御部にて行わせていた前記給湯用補助加熱部19s及び暖房用補助加熱部19w夫々の作動の制御を、前記制御手段Cに行わせるように構成しても良い。 (C) In the first embodiment described above, the combustion controller of each of the auxiliary hot water heater 19s and the auxiliary heater 19w for heating is omitted in each of the combustion controllers. The control means C may be configured to control the operations of the hot water supply auxiliary heating unit 19s and the heating auxiliary heating unit 19w.

(ニ) 上記の各実施形態において、前記給水切換三方弁25の設置箇所は、前記給水路4と前記タンク迂回給水路24との接続部分に変更可能である。 (D) In each of the above embodiments, the installation location of the water supply switching three-way valve 25 can be changed to a connection portion between the water supply channel 4 and the tank bypass water supply channel 24.

(ホ) 前記目標貯湯温度及び前記設定水質維持温度は、設定水質維持温度を目標貯湯温度以下に設定する条件で、上記の各実施形態において例示した以外に種々に変更可能である。
又、上記の各実施形態においては、前記設定保持温度を前記設定水質維持温度と同温度に設定する場合について例示したが、設定保持温度を設定水質維持温度よりも高い温度に設定しても良く、そして、設定保持温度を高く設定するほど、前記貯湯タンク5の水質を維持することができながらも、設定水質維持時間を短く設定することが可能となって、水質維持運転の所要時間を短縮することが可能になる。
設定保持温度を設定水質維持温度よりも高い温度に設定する場合は、水質維持運転時は通常運転時よりも高温の湯を貯湯タンク5に供給する必要があるので、前記目標貯湯温度として、通常運転時用の目標貯湯温度と水質維持運転時用の目標貯湯温度とを、水質維持運転時用の方が高くなる状態で設定することになる。
例えば、設定保持温度を70°Cに設定すると、通常運転時用の目標貯湯温度は、上記の各実施形態のように65°Cに設定し、水質維持運転時用の目標貯湯温度は、貯湯タンク5に70°C以上の湯を供給できるように、例えば、72°C程度に設定する。
ちなみに、設定保持温度を70°Cに設定する場合は、前記設定水質維持時間は例えば1分間程度の短い時間に設定することが可能になる。
尚、第2実施形態においては、水質維持運転では、第1実施形態におけるよりも、前記燃料電池Gの冷却水により多い熱量を与えることが可能になって、前記排熱熱源熱交換器14にて湯水をより高温に加熱することが可能になるので、設定保持温度を設定水質維持温度よりも高い温度に設定する実施形態は、第2実施形態において適用するのが好ましい。
(E) The target hot water storage temperature and the set water quality maintenance temperature can be changed in various ways other than those exemplified in the above embodiments under the condition that the set water quality maintenance temperature is set to be equal to or lower than the target hot water storage temperature.
Further, in each of the above embodiments, the case where the set holding temperature is set to the same temperature as the set water quality maintenance temperature is exemplified, but the set holding temperature may be set to a temperature higher than the set water quality maintenance temperature. And, as the set retention temperature is set higher, the water quality of the hot water storage tank 5 can be maintained, but the set water quality maintenance time can be set shorter and the time required for the water quality maintenance operation is shortened. It becomes possible to do.
When the set holding temperature is set to a temperature higher than the set water quality maintenance temperature, it is necessary to supply hot water to the hot water storage tank 5 during the water quality maintenance operation, which is higher than that during normal operation. The target hot water storage temperature for operation and the target hot water storage temperature for water quality maintenance operation are set in a state where the water temperature maintenance operation becomes higher.
For example, when the set holding temperature is set to 70 ° C., the target hot water storage temperature for normal operation is set to 65 ° C. as in the above embodiments, and the target hot water storage temperature for water quality maintenance operation is For example, the temperature is set to about 72 ° C. so that hot water of 70 ° C. or higher can be supplied to the tank 5.
Incidentally, when the set holding temperature is set to 70 ° C., the set water quality maintenance time can be set to a short time of about 1 minute, for example.
In the second embodiment, in the water quality maintenance operation, it becomes possible to give more heat to the cooling water of the fuel cell G than in the first embodiment. Therefore, the embodiment in which the set holding temperature is set to a temperature higher than the set water quality maintenance temperature is preferably applied in the second embodiment.

(ヘ) 前記水質維持運転タイミングの判別の仕方は、上記の実施形態において例示した以外にも種々可能である。
例えば、前記燃料電池Gの運転が停止される時間が所定の設定時間に達したり、燃料電池Gの出力電力が設定出力よりも小さい低出力運転状態が所定の設定時間継続すると、水質維持運転タイミングになると判別するようにしても良い。
あるいは、定期的に水質維持運転タイミングになると判別するようにしても良い。
(F) There are various ways of determining the water quality maintenance operation timing other than those exemplified in the above embodiment.
For example, when the time during which the operation of the fuel cell G is stopped reaches a predetermined set time, or the low output operation state in which the output power of the fuel cell G is lower than the set output continues for the predetermined set time, the water quality maintaining operation timing You may make it discriminate | determine.
Or you may make it discriminate | determine that it becomes a water quality maintenance driving | operation timing regularly.

(ト) 前記排熱熱源熱交換器14にて前記湯水に回収させる前記燃料電池Gの発生熱としては、上記の実施形態において例示した如き、前記燃焼排ガス、前記酸素極側排ガス及び前記燃料極側排ガス夫々の保有熱、並びに、前記セルスタック30から発生する発電反応熱に限定されるものではない。
例えば、前記燃焼排ガス、前記酸素極側排ガス及び前記燃料極側排ガス夫々の保有熱のうち、いずれか一つ、いずれか二つ、又は、全てを除いても良い。
又、前記変成器39から前記一酸化炭素除去器40に供給される変成処理後の改質ガスの保有熱や、前記燃料ガス生成部Rから前記セルスタッ30に供給される燃料ガスの保有熱を用いることが可能である。
(G) The generated heat of the fuel cell G to be recovered in the hot water by the exhaust heat source heat exchanger 14 is the combustion exhaust gas, the oxygen electrode side exhaust gas, and the fuel electrode as exemplified in the above embodiment. It is not limited to the retained heat of each side exhaust gas and the power generation reaction heat generated from the cell stack 30.
For example, any one, any two, or all of the retained heat of the combustion exhaust gas, the oxygen electrode side exhaust gas, and the fuel electrode side exhaust gas may be removed.
In addition, the retained heat of the reformed gas supplied from the transformer 39 to the carbon monoxide remover 40 and the retained heat of the fuel gas supplied from the fuel gas generation unit R to the cell stack 30 are also obtained. It is possible to use.

(チ) 上記の各実施形態において、前記燃料電池制御部36による燃料電池Gの運転形態を、実際の電力負荷を測定してその測定電力負荷に応じて出力電力を変更調節する電力負荷追従運転とするように構成する場合について例示したが、燃料電池Gの運転形態としては、上記電力負荷追従運転に限らず、例えば、実際の電力負荷の測定データに基づいて電力負荷を予測し、その予測電力負荷に応じて出力電力を変更調節するように構成しても良い。 (H) In each of the above embodiments, the operation mode of the fuel cell G by the fuel cell control unit 36 is the power load following operation in which the actual power load is measured and the output power is changed and adjusted according to the measured power load. However, the operation mode of the fuel cell G is not limited to the power load follow-up operation. For example, the power load is predicted based on the actual power load measurement data, and the prediction is performed. The output power may be changed and adjusted according to the power load.

(リ) 余剰電力を生じさせるべく前記電力負荷よりも大きい電力を発電するように前記燃料電池Gの運転を制御するように、前記燃料電池制御部36を構成するに、上記の第2実施形態における構成、即ち、前記燃料電池Gの出力電力を前記設定最大出力電力に調節する構成に限定されるものではなく、例えば、前記燃料電池Gの出力電力を前記電力負荷よりも設定電力大きい電力に調節する構成でも良い。 (I) In the second embodiment, the fuel cell control unit 36 is configured to control the operation of the fuel cell G so as to generate electric power larger than the electric power load so as to generate surplus electric power. Is not limited to the configuration in which the output power of the fuel cell G is adjusted to the set maximum output power. For example, the output power of the fuel cell G is set to a power that is larger than the power load. The structure to adjust may be sufficient.

(ヌ) 前記燃料電池Gの余剰電力を前記貯湯タンク5に貯湯するための熱に変換する前記電気ヒータ28の設置形態は、上記の第2実施形態において例示した形態、即ち、前記冷却水循環路32を通流する冷却水を加熱するように設ける形態に限定されるものではない。例えば、前記貯湯用循環路12におけるタンク供給温度センサTeの温度検出位置よりも上流側を通流する湯水を加熱するように設けても良い。 (Nu) The installation form of the electric heater 28 that converts surplus power of the fuel cell G into heat for storing hot water in the hot water storage tank 5 is the form illustrated in the second embodiment, that is, the cooling water circulation path. It is not limited to the form which provides so that the cooling water which flows through 32 may be heated. For example, the hot water flowing through the upstream side of the temperature detection position of the tank supply temperature sensor Te in the hot water storage circuit 12 may be provided so as to be heated.

(ル) 上記の第2実施形態においては、水質維持運転の実行中は、貯湯タンク5全体の湯水が設定水質維持温度以上になった以降も、前記最大出力運転を継続する場合について例示したが、貯湯タンク5全体の湯水が設定水質維持温度になると、前記最大出力運転を停止して、前記電力負荷追従運転に切り換えるように構成しても良い。 (L) In the second embodiment, the case where the maximum output operation is continued even after the hot water in the entire hot water storage tank 5 becomes equal to or higher than the set water quality maintenance temperature during the water quality maintenance operation is illustrated. When the hot water in the entire hot water storage tank 5 reaches the set water quality maintenance temperature, the maximum output operation may be stopped and switched to the power load following operation.

(ヲ) 上記の第1実施形態において、第2実施形態と同様に、前記電気ヒータ28を設けて、前記水質維持運転の実行中は、前記燃料電池Gの出力電力を前記設定最大出力電力に調節し且つ前記燃料電池Gの余剰電力を前記電気ヒータ28にて消費するように前記スイッチ29の作動を制御する最大出力運転を実行するように構成しても良い。 (W) In the first embodiment, as in the second embodiment, the electric heater 28 is provided, and the output power of the fuel cell G is set to the set maximum output power during the water quality maintenance operation. A maximum output operation for controlling the operation of the switch 29 so as to adjust and consume the surplus power of the fuel cell G by the electric heater 28 may be executed.

(ワ) 上記の第1実施形態においては、前記加熱用流路15を、前記加熱用熱交換器11を通過した湯水を前記貯湯タンク5に戻すように設ける場合について例示したが、前記加熱用熱交換器11を通過した湯水を、前記貯湯タンク5を迂回させて前記貯湯用循環路12における前記排熱熱源熱交換器14よりも上流側に戻すように設けても良い。 (W) In the first embodiment described above, the case where the heating flow path 15 is provided so as to return the hot water that has passed through the heating heat exchanger 11 to the hot water storage tank 5 is illustrated. The hot water having passed through the heat exchanger 11 may be provided so as to return to the upstream side of the exhaust heat source heat exchanger 14 in the hot water circulation circuit 12 by bypassing the hot water storage tank 5.

(カ) 上記の各実施形態においては、前記加熱部Hを、熱電併給装置から発生する熱を熱源とするように構成する場合について例示したが、ガスバーナや電気ヒータ等の専用の熱源を備えて構成したり、ガスエンジンやガソリンエンジン等によりコンプレッサを駆動するようにしたエンジン駆動式のヒートポンプ装置から発生する熱を熱源とするように構成することが可能である。エンジン駆動式のヒートポンプ装置から発生する熱を熱源とする場合は、ヒートポンプそのものから発生する熱や、エンジンの冷却水にて回収される排熱を熱源とすることになる。
又、前記熱電併給装置から発生する熱を熱源とするように構成する場合、熱電併給装置の具体例として、上記の実施形態のように燃料電池Gを適用する場合、その型式は上記の実施形態において例示した固体高分子型に限定されるものではなく、リン酸型や固体電解質型等の種々の型式のものを用いることが可能であり、又、前記燃料電池G以外に、ガスエンジンやガソリンエンジン等により発電機を駆動するように構成した回転式の発電装置を適用することが可能である。この場合は、エンジンの冷却水にて回収される排熱を熱源とすることになる。
(F) In each of the above embodiments, the case where the heating unit H is configured to use heat generated from the combined heat and power supply as a heat source has been described, but a dedicated heat source such as a gas burner or an electric heater is provided. It is possible to configure such that heat generated from an engine-driven heat pump device in which a compressor is driven by a gas engine, a gasoline engine, or the like is used as a heat source. When heat generated from an engine-driven heat pump device is used as a heat source, heat generated from the heat pump itself or exhaust heat recovered by engine cooling water is used as a heat source.
In the case where the heat generated from the combined heat and power unit is used as a heat source, as a specific example of the combined heat and power unit, when the fuel cell G is applied as in the above embodiment, the model is the above embodiment. It is not limited to the solid polymer type illustrated in FIG. 1, and various types such as a phosphoric acid type and a solid electrolyte type can be used. In addition to the fuel cell G, a gas engine or gasoline can be used. It is possible to apply a rotary power generator configured to drive a generator by an engine or the like. In this case, exhaust heat recovered by engine cooling water is used as a heat source.

第1実施形態にかかる貯湯式の給湯熱源装置を備えたコージェネレーションシステムの構成、及び、貯湯単独運転モードでの湯水の流れを示すブロック図The block diagram which shows the flow of the hot water in the structure of the cogeneration system provided with the hot water storage type hot-water supply heat source apparatus concerning 1st Embodiment, and hot water storage independent operation mode 第1実施形態にかかる貯湯式の給湯熱源装置を備えたコージェネレーションシステムの水質維持運転での湯水の流れを示すブロック図The block diagram which shows the flow of the hot water in the water quality maintenance operation | movement of the cogeneration system provided with the hot water storage type hot-water supply heat source apparatus concerning 1st Embodiment. 燃料電池の構成を示すブロック図Block diagram showing the configuration of the fuel cell 第2実施形態にかかる貯湯式の給湯熱源装置を備えたコージェネレーションシステムの構成、及び、水質維持運転での湯水の流れを示すブロック図The block diagram which shows the flow of the hot water in the structure of the cogeneration system provided with the hot water storage type hot-water supply heat source apparatus concerning 2nd Embodiment, and water quality maintenance operation | movement.

符号の説明Explanation of symbols

3 給湯路
4 給水路
5 貯湯タンク
12 貯湯用循環路
14 加熱作用部
19 補助加熱器(補助加熱手段)
19w 暖房用補助加熱部(暖房用補助加熱手段)
24 タンク迂回給水路
25 給水切換三方弁(給水状態切換手段)
28 電気ヒータ
50 端末器迂回路
51 熱媒循環状態切換三方弁(熱媒循環状態切換手段)
C 制御手段
H 加熱手段
G 熱電併給装置
3 Hot-water supply path 4 Hot-water supply path 5 Hot-water storage tank 12 Hot-water supply circulation path 14 Heating action part 19 Auxiliary heater (auxiliary heating means)
19w Auxiliary heating unit for heating (auxiliary heating means for heating)
24 Tank bypass water supply path 25 Water supply switching three-way valve (Water supply state switching means)
28 Electric heater 50 Terminal bypass circuit 51 Heat medium circulation state switching three-way valve (heat medium circulation state switching means)
C Control means H Heating means G Cogeneration device

Claims (6)

給水路を通して給水され且つ給湯路を通して湯水が送出される貯湯タンクと、
その貯湯タンクの湯水を加熱する加熱手段と、
前記給湯路を通流する湯水を目標給湯温度に加熱する補助加熱手段と、
前記貯湯タンクに目標貯湯温度で貯湯されるように前記加熱手段の作動を制御する制御手段とが設けられた貯湯式の給湯熱源装置であって、
放熱用端末器が設けられた熱媒循環路を循環する熱媒を加熱する暖房用補助加熱手段と、
前記加熱手段から前記貯湯タンクに供給される湯水と前記熱媒循環路を循環する熱媒との熱交換を行う加熱用熱交換器とが設けられ、
前記制御手段が、前記貯湯タンクの湯水の水質を維持するための水質維持運転として、前記貯湯タンク全体の湯水が設定水質維持温度以上である状態を設定水質維持時間継続させるように前記加熱手段を作動させる運転を実行すると共に、前記水質維持運転の実行中における、少なくとも前記貯湯タンク全体の湯水が前記設定水質維持温度以上になるまでの間、前記熱媒循環路に熱媒を循環させる状態で前記暖房用補助加熱手段を作動させる補助昇温運転を実行するように構成されている貯湯式の給湯熱源装置。
A hot water storage tank which is supplied with water through a water supply channel and to which hot water is sent out through the water supply channel;
Heating means for heating the hot water in the hot water storage tank;
Auxiliary heating means for heating hot water flowing through the hot water supply path to a target hot water temperature;
A hot water storage type hot water supply heat source device provided with control means for controlling the operation of the heating means so that hot water is stored in the hot water storage tank at a target hot water storage temperature,
An auxiliary heating means for heating that heats the heat medium circulating in the heat medium circuit provided with the terminal for heat dissipation;
A heating heat exchanger for exchanging heat between hot water supplied from the heating means to the hot water storage tank and a heat medium circulating in the heat medium circulation path is provided;
As the water quality maintenance operation for maintaining the quality of the hot water in the hot water storage tank, the control means controls the heating means so as to continue the state in which the hot water in the entire hot water storage tank is equal to or higher than the preset water quality maintenance temperature. While performing the operation to be operated, in a state in which the heat medium is circulated through the heat medium circulation path at least until the hot water in the entire hot water storage tank becomes equal to or higher than the set water quality maintenance temperature during the water quality maintenance operation. A hot water storage type hot water supply heat source apparatus configured to execute an auxiliary temperature raising operation for operating the auxiliary heating means for heating.
前記熱媒循環路にて循環する熱媒を、端末器迂回路を通して前記放熱用端末器を迂回させる端末器迂回状態に切り換え自在な熱媒循環状態切換手段が設けられ、
前記運転制御手段が、前記補助昇温運転の実行中において、前記熱媒循環状態切換手段を前記端末機器迂回状態に切り換えるように構成されている請求項1に記載の貯湯式の給湯熱源装置。
A heating medium circulating state switching means is provided that can freely switch the heating medium circulating in the heating medium circulation path to a terminal bypassing state that bypasses the heat radiating terminal through a terminal bypass.
The hot water storage hot water supply heat source apparatus according to claim 1, wherein the operation control means is configured to switch the heat medium circulation state switching means to the terminal device bypass state during execution of the auxiliary temperature raising operation.
前記給水路にて供給される水をタンク迂回給水路を通して前記貯湯タンクを迂回して前記給湯路における前記補助加熱手段よりも上流側に供給し且つ前記貯湯タンクから前記給湯路への湯水の送出を停止するタンク迂回給水状態に切り換え自在な給水状態切換手段が設けられ、
前記制御手段が、前記水質維持運転を実行する必要がある水質維持運転タイミングであるか否かを判別して、その水質維持運転タイミングになると、前記水質維持運転として、前記給水状態切換手段を前記タンク迂回給水状態に切り換え、且つ、前記貯湯タンク全体の湯水が設定水質維持温度以上である状態を設定水質維持時間継続させるように前記加熱手段を作動させる運転を実行するように構成されている請求項1又は2に記載の貯湯式の給湯熱源装置。
Water supplied from the hot water supply channel is supplied to the upstream side of the auxiliary heating means in the hot water supply channel, bypassing the hot water storage tank through the bypass water supply channel, and sent from the hot water storage tank to the hot water supply channel. A water supply state switching means is provided that can be switched to a tank bypass water supply state that stops the operation,
The control means determines whether or not it is the water quality maintenance operation timing that needs to perform the water quality maintenance operation, and when the water quality maintenance operation timing is reached, the water supply state switching means is set as the water quality maintenance operation. It is configured to switch to a tank detour water supply state, and to perform an operation for operating the heating means so as to continue a state in which the hot water in the entire hot water storage tank is equal to or higher than a set water quality maintenance temperature for a set water quality maintenance time. Item 3. A hot water storage heat source device according to item 1 or 2.
前記制御手段は、前記給水路を通して前記貯湯タンクに給水され且つ前記貯湯タンクの湯水が前記給湯路を通して送出される形態にて前記貯湯タンクの湯水が入れ替わる湯水入れ替わり状態を判別するように構成され、且つ、前記貯湯タンクの湯水の温度が前記設定水質維持温度よりも低く且つ前記湯水入れ替わり状態を判別しない状態がタイミング判別用設定時間継続すると前記水質維持運転タイミングになると判別するように構成されている請求項3記載の貯湯式の給湯熱源装置。   The control means is configured to determine a hot water replacement state in which hot water in the hot water storage tank is replaced in a form in which water is supplied to the hot water storage tank through the water supply passage and hot water in the hot water storage tank is sent out through the hot water supply passage. The hot water storage tank is configured such that the temperature of the hot water is lower than the set water quality maintenance temperature and the state in which the hot water replacement state is not discriminated continues for the set time for timing discrimination and the water quality maintenance operation timing is determined. The hot-water storage type hot water supply heat source device according to claim 3. 前記加熱手段が、熱電併給装置から発生する熱にて前記貯湯タンクの湯水を加熱するように構成され、
前記制御手段が、通常運転の実行中は電力負荷に応じた電力を発電し、前記水質維持運転の実行中は余剰電力を生じさせるべく前記電力負荷よりも大きい電力を発電するように、前記熱電併給装置の運転を制御するように構成され、
前記水質維持運転の実行中における、少なくとも前記貯湯タンク全体の湯水が前記設定水質維持温度以上になるまでの間、前記余剰電力を前記貯湯タンクに貯湯するための熱に変換する電気ヒータが設けられている請求項1〜4のいずれか1項に記載の貯湯式の給湯熱源装置。
The heating means is configured to heat the hot water in the hot water storage tank with heat generated from the combined heat and power supply device;
The control means generates electric power according to the electric power load during execution of normal operation, and generates electric power larger than the electric power load to generate surplus electric power during execution of the water quality maintenance operation. Configured to control the operation of the co-feeder;
An electric heater for converting the surplus power into heat for storing hot water in the hot water storage tank is provided at least until the hot water in the entire hot water storage tank reaches the set water quality maintenance temperature or higher during execution of the water quality maintenance operation. The hot water storage type hot water supply heat source device according to any one of claims 1 to 4.
前記貯湯タンクが密閉式に構成されて、前記給水路がタンク底部に接続され、且つ、前記給湯路がタンク上部に接続され、
前記加熱手段が、タンク底部から取り出した湯水を加熱作用部を経由してタンク上部に戻す形態で貯湯用循環路を通じて前記貯湯タンクの湯水を循環させるように構成されている請求項1〜5のいずれか1項に記載の貯湯式の給湯熱源装置。
The hot water storage tank is configured in a sealed manner, the water supply path is connected to a tank bottom, and the hot water supply path is connected to an upper part of the tank;
The said heating means is comprised so that the hot water of the said hot water storage tank may be circulated through the circulation path for hot water storage in the form which returns the hot water taken out from the tank bottom part to a tank upper part via a heating action part. The hot water storage type hot water supply heat source device according to any one of the preceding claims.
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