JP2011127804A - Latent heat recovery unit - Google Patents

Latent heat recovery unit Download PDF

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JP2011127804A
JP2011127804A JP2009284933A JP2009284933A JP2011127804A JP 2011127804 A JP2011127804 A JP 2011127804A JP 2009284933 A JP2009284933 A JP 2009284933A JP 2009284933 A JP2009284933 A JP 2009284933A JP 2011127804 A JP2011127804 A JP 2011127804A
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latent heat
heat recovery
side circulation
heat
hot water
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JP5406001B2 (en
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Mitsuharu Onishi
満春 大西
Takeaki Tara
武晃 多良
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Showa Manufacturing Co Ltd
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Showa Manufacturing Co Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a hot-water generator capable of efficiently recovering heat of high-temperature exhaust gas by a heat exchanger for latent heat recovery by installing a latent heat recovery unit including the heat exchanger for latent heat recovery. <P>SOLUTION: The latent heat recovery unit can be mounted to a water heater including a hot-water generator body storing heating medium water, a combustion chamber warming the heating medium water within the hot-water generator body and a secondary side circulation passage circulating secondary hot water which has undergone heat exchange with the heating medium water stored in the hot-water generator body. A flue construct enabling connection and communication with the combustion chamber and discharging exhaust gas discharged from the combustion chamber to outside, a primary side circulation passage constituted independently of the secondary side circulation passage and circulating the heating medium water, the heat exchanger for latent heat recovery exchanging heat between the exhaust gas discharged from the combustion chamber and made to pass through inside of the flue construct and the heating medium water in the primary side circulation passage to recover latent heat of the exhaust gas and an indirect heat exchanger exchanging heat between the heating medium water circulated in the primary side circulation passage and the secondary hot water circulated in the secondary side circulation passage are stored and arranged in a predetermined casing. <P>COPYRIGHT: (C)2011,JPO&INPIT

Description

本発明は、温水発生機に関し、詳しくは燃焼装置の排気ガスの潜熱を回収して2次側の湯水を予熱可能とした潜熱回収用熱交換器を備えた温水発生機に関する。   The present invention relates to a hot water generator, and more particularly to a hot water generator equipped with a latent heat recovery heat exchanger that recovers the latent heat of exhaust gas from a combustion device and enables preheating of secondary hot water.

従来、温水発生機では、燃費の向上を図るために、バーナを燃焼室で燃焼させてその燃焼熱により熱媒水や2次側の湯水を加温するだけではなく、バーナを燃焼させた後に発生する排気ガスの熱を利用して、熱媒水や2次側の湯水を予熱する方法があった。   Conventionally, in a hot water generator, in order to improve fuel efficiency, not only does the burner burn in the combustion chamber and the heat of combustion heats the heat transfer water and hot water on the secondary side, but also burns the burner. There has been a method of preheating the heat transfer water or the secondary hot water using the heat of the generated exhaust gas.

例えば、ボイラ等から排出される燃焼排気ガスの熱を有効活用するために、燃焼排気ガスの顕熱だけではなく潜熱をも最大限吸収して熱吸収量を増大させた潜熱回収用熱交換器(エコノマイザ)が提案されている(例えば、特許文献1を参照。)。   For example, in order to effectively use the heat of combustion exhaust gas discharged from boilers, etc., a heat exchanger for recovering latent heat that absorbs not only sensible heat of combustion exhaust gas but also latent heat to increase the amount of heat absorption (Economizer) has been proposed (see, for example, Patent Document 1).

かかる潜熱回収用熱交換器を利用した従来の温水器を、例えば銭湯などのような施設で給湯用に用いる場合、図2に示すような構成が採用されることが多い。   When a conventional water heater using such a heat exchanger for collecting latent heat is used for hot water supply in a facility such as a public bath, for example, the configuration shown in FIG. 2 is often adopted.

図2に示すように、従来の温水発生機は、バーナ110が設けられた燃焼室120を備え、熱媒水200を収容可能とした温水発生機本体100と、温水発生機本体100に収容された熱媒水200を循環させる1次側循環路300と、給湯のために設けられたカラン410に2次湯水500を循環させる2次側循環路400と、1次側循環路300を循環する高温の熱媒水200と2次側循環路400を循環する低温の2次湯水500との熱交換を行う間接熱交換器600と、バーナ110の燃焼により発生した排気ガス130の熱(顕熱、潜熱)を回収する潜熱回収用熱交換器700と、により構成されている。図中、符号310で示したものは1次側循環路300に設けられた熱媒循環ポンプ、符号420で示したものは2次側循環路400に設けられた循環ポンプ、また、符号800で示したものは、潜熱回収用熱交換器700を介して燃焼室120に連通連結した煙道を示す。   As shown in FIG. 2, the conventional hot water generator includes a combustion chamber 120 provided with a burner 110 and can accommodate a heat transfer water 200, and is accommodated in the hot water generator main body 100. The primary side circulation path 300 that circulates the heat transfer water 200, the secondary side circulation path 400 that circulates the secondary hot water 500 in the currant 410 provided for hot water supply, and the primary side circulation path 300 are circulated. The heat (sensible heat) of the exhaust gas 130 generated by the combustion of the indirect heat exchanger 600 that exchanges heat between the high-temperature heat transfer water 200 and the low-temperature secondary hot water 500 that circulates in the secondary-side circulation path 400 and the burner 110. , Latent heat recovery heat exchanger 700 for recovering latent heat). In the figure, the reference numeral 310 indicates a heat medium circulation pump provided in the primary side circulation path 300, the reference numeral 420 indicates a circulation pump provided in the secondary side circulation path 400, and a reference numeral 800. Shown is a flue that is communicatively coupled to the combustion chamber 120 via a latent heat recovery heat exchanger 700.

上記構成の温水発生機は、ガス・油等の燃料をバーナ110により燃焼室120で燃焼して、その燃焼熱により温水発生機本体100に収容した熱媒水200を加温する。そして、熱媒循環ポンプ310により高温の熱媒水200を1次側循環路300に循環させ、同様に、循環ポンプ420により低温の2次湯水500を2次側循環路400に循環させて、間接熱交換器600により熱交換して2次側循環路400を循環する2次湯水500を加温している。   The hot water generator configured as described above burns fuel such as gas and oil in the combustion chamber 120 by the burner 110 and heats the heat transfer water 200 accommodated in the hot water generator main body 100 by the combustion heat. Then, the high-temperature heat medium water 200 is circulated to the primary-side circulation path 300 by the heat-medium circulation pump 310, and similarly, the low-temperature secondary hot water 500 is circulated to the secondary-side circulation path 400 by the circulation pump 420. The secondary hot water 500 circulating through the secondary side circulation path 400 is heated by exchanging heat with the indirect heat exchanger 600.

さらに、図示するように、2次側循環路400を循環する2次湯水500は、間接熱交換器600に供給されて加温される前に、潜熱回収用熱交換器700と熱交換することにより予熱されるようになっている。すなわち、従来の温水器においては、2次側循環路400を循環する2次湯水500を予熱するために潜熱回収用熱交換器700が用いられていた。   Further, as shown in the figure, the secondary hot water 500 circulating in the secondary side circulation path 400 is heat-exchanged with the latent heat recovery heat exchanger 700 before being supplied to the indirect heat exchanger 600 and heated. Is preheated. That is, in the conventional water heater, the latent heat recovery heat exchanger 700 is used to preheat the secondary hot water 500 circulating in the secondary side circulation path 400.

また、図2に示す温水発生機は、複数の1次側循環路300とそれに応じた複数の間接熱交換器600及び複数の2次側循環路400を備えることにより、給湯のみならず、例えば、暖房、循環加熱などを同時に行うことができる構成としている。   Moreover, the hot water generator shown in FIG. 2 includes not only hot water supply but also a plurality of primary side circulation paths 300 and a plurality of indirect heat exchangers 600 and a plurality of secondary side circulation paths 400 corresponding thereto, for example, , Heating, circulation heating and the like can be performed simultaneously.

特開平11−248105JP 11-248105 A

上述したような、潜熱回収用熱交換器を備えた従来の温水発生機は、元来捨てていた燃焼排気ガスの熱を有効活用できるために極めて好ましい構成といえるが、潜熱回収用熱交換器を備えていない温水発生機を用いている施設の方がまだまだ多い。   The above-mentioned conventional hot water generator equipped with a heat exchanger for recovering latent heat can be said to be a very preferable configuration because it can effectively use the heat of combustion exhaust gas that was originally discarded, but the heat exchanger for recovering latent heat There are still many facilities that use hot water generators that do not have a.

そして、潜熱回収用熱交換器を配設して省エネを図りたくとも、温水発生機本体100などの燃焼装置を含む装置全体を再構築するとなると、大がかりな配管、煙道の改造が必要になってコストが嵩むため簡単ではない。   Even if it is desired to save energy by installing a heat exchanger for recovering latent heat, if the entire apparatus including the combustion device such as the hot water generator main body 100 is reconstructed, large-scale piping and flue modification are required. It is not easy because of the high cost.

しかも、例えば、銭湯などのような施設の場合、常時所定温度の湯水を提供する必要があるため、図2に示すように、2次側循環路400を循環する2次湯水500を予熱して、常に2次湯水500を2次側循環路400内で循環させている。   In addition, for example, in the case of a facility such as a public bath, it is necessary to always provide hot water at a predetermined temperature. Therefore, as shown in FIG. 2, the secondary hot water 500 circulating in the secondary side circulation path 400 is preheated. The secondary hot water 500 is always circulated in the secondary side circulation path 400.

このため、カラン410から供給される2次湯水500の使用頻度が低下すると、2次側循環路400の内部を循環する2次湯水500の温度が必要以上に上昇してしまい、潜熱回収用熱交換器700へ高温の2次湯水500が入水されることになる。一般に、潜熱回収用熱交換器700に入水する2次湯水500の温度が高くなると、潜熱回収用熱交換器700の特性上、排気ガス130中の水分凝縮が生起されにくくなり、結果として潜熱回収用熱交換器700内における熱交換の効率が低下する虞があった。   For this reason, when the usage frequency of the secondary hot water 500 supplied from the currant 410 decreases, the temperature of the secondary hot water 500 circulating in the secondary side circulation path 400 rises more than necessary, and the heat for latent heat recovery is increased. The high-temperature secondary hot water 500 enters the exchanger 700. In general, when the temperature of the secondary hot water 500 entering the latent heat recovery heat exchanger 700 becomes high, moisture condensation in the exhaust gas 130 is less likely to occur due to the characteristics of the latent heat recovery heat exchanger 700, resulting in latent heat recovery. There is a possibility that the efficiency of heat exchange in the heat exchanger 700 for use may decrease.

また、給湯のための温水発生機においては、カラン410の開閉頻度、つまり、給湯頻度により、潜熱回収用熱交換器700へ入水する2次湯水500の量や温度にばらつきが生じ、結果的に潜熱回収用熱交換器700内における熱交換の効率もばらついてしまう。さらに、潜熱回収用熱交換器700の熱交換能力は、2次側循環路400を循環する2次湯水500の量や温度に依存するため、例えば、循環する2次湯水500の量が少ないときや循環ポンプ420の発停制御を行っている場合、熱の受け渡しが十分でなければ、排気ガス130の熱により潜熱回収用熱交換器700の内部が過熱状態や圧力上昇する危険性がある。   Further, in the hot water generator for hot water supply, the amount and temperature of the secondary hot water 500 entering the latent heat recovery heat exchanger 700 vary depending on the frequency of opening and closing of the currant 410, that is, the hot water supply frequency. The efficiency of heat exchange in the latent heat recovery heat exchanger 700 also varies. Furthermore, since the heat exchange capacity of the latent heat recovery heat exchanger 700 depends on the amount and temperature of the secondary hot water 500 circulating in the secondary side circulation path 400, for example, when the amount of the secondary hot water 500 circulating is small. When the start / stop control of the circulation pump 420 is performed, if the heat transfer is not sufficient, the heat of the exhaust gas 130 may cause the inside of the latent heat recovery heat exchanger 700 to be overheated or the pressure may increase.

本発明は、上述した課題を解決し、潜熱回収用熱交換器のヒータ効率の低下や過熱状態が発生することを防止し、かつ、既設の給湯装置に潜熱回収用熱交換器を簡単に後付け可能とした技術を提供することを目的としている。   The present invention solves the above-described problems, prevents the heater efficiency of the latent heat recovery heat exchanger from being lowered and prevents an overheating state, and easily installs the latent heat recovery heat exchanger in an existing hot water supply device. It aims to provide the technology that has been made possible.

本発明においては上記課題を解決するために以下の手段を講じた。   In the present invention, the following means have been taken in order to solve the above problems.

(1)熱媒水を収容する温水発生機本体と、前記温水発生機本体内の熱媒水を加温する燃焼室と、前記温水発生機本体に収容された熱媒水と熱交換された2次湯水を循環させる2次側循環路と、を備える温水発生機に取付可能とした潜熱回収ユニットであって、前記燃焼室と連通連結可能であり、当該燃焼室より排出される排気ガスを外部に排出する煙道構成体と、前記2次側循環路とは独立して構成され、熱媒水を循環させる1次側循環路と、前記燃焼室より排出され、前記煙道構成体内を通過する排気ガスと前記1次側循環路中の熱媒水とを熱交換して当該排気ガスの潜熱を回収する潜熱回収用熱交換器と、前記1次側循環路を循環する熱媒水と前記2次側循環路を循環する2次湯水との熱交換を行う間接熱交換器と、が所定のケーシングに収納配設されていることとした。   (1) The hot water generator main body that stores the heat transfer water, the combustion chamber that heats the heat transfer medium in the hot water generator main body, and the heat transfer water stored in the hot water generator main body are heat-exchanged. A latent heat recovery unit that can be attached to a hot water generator that circulates secondary hot water, and that can be connected to the combustion chamber and exhaust gas discharged from the combustion chamber. The flue structure to be discharged to the outside and the secondary side circulation path are configured independently, and the primary side circulation path for circulating the heat transfer water and the combustion chamber are discharged from the flue structure. A heat exchanger for latent heat recovery that recovers the latent heat of the exhaust gas by exchanging heat between the passing exhaust gas and the heat transfer water in the primary side circulation path, and the heat transfer water circulating through the primary side circulation path And an indirect heat exchanger for exchanging heat between the secondary hot water circulating in the secondary side circulation path and a predetermined case It was that are housed disposed.

(2)上記(1)の潜熱回収ユニットにおいて、前記2次側循環路を複数路具備する温水発生機に取付可能な潜熱回収ユニットであって、前記ケーシング内に、前記2次側循環路の数と同数の間接熱交換器を収納配設したことを特徴とする。   (2) The latent heat recovery unit according to (1), wherein the latent heat recovery unit can be attached to a hot water generator having a plurality of the secondary side circulation paths, and the secondary side circulation path is disposed in the casing. The same number of indirect heat exchangers are accommodated and arranged.

(3)上記(1)又は(2)の潜熱回収ユニットにおいて、前記1次側循環路を循環する熱媒水の温度変化による膨張及び収縮を吸収する開放筒を具備することを特徴とする。   (3) The latent heat recovery unit according to (1) or (2) is characterized by comprising an open cylinder that absorbs expansion and contraction due to a temperature change of the heat transfer medium circulating in the primary side circulation path.

(4)上記(1)〜(3)の潜熱回収ユニットにおいて、前記潜熱回収用熱交換器による排気ガスの潜熱回収により発生する酸性のドレンを中和する中和装置を具備することを特徴とする。   (4) The latent heat recovery unit according to any one of (1) to (3) above, further comprising a neutralizing device for neutralizing acidic drain generated by the latent heat recovery of exhaust gas by the latent heat recovery heat exchanger. To do.

(5)上記(1)〜(4)の潜熱回収ユニットにおいて、前記潜熱回収用熱交換器を通過する前と通過した後の排気ガスの温度を測定する複数の温度センサを前記煙道構成体に設けたことを特徴とする。   (5) In the latent heat recovery unit of (1) to (4) above, a plurality of temperature sensors for measuring the temperature of the exhaust gas before and after passing through the latent heat recovery heat exchanger include the flue structure. It is characterized by being provided in.

本発明によれば、潜熱回収用熱交換器が設けられていない既設の温水発生機に、潜熱回収用熱交換器を含む潜熱回収ユニットを後付けすることを可能とするとともに、潜熱回収ユニットは、潜熱回収用熱交換器に供給される熱媒水の温度を、比較的低温度とすることができるので熱交換効率を高くすることができ、さらに、開放筒を設け潜熱回収用熱交換器の過熱や圧力上昇を防止することができるので、安全性に優れた潜熱回収ユニットを具備する温水発生機とすることができる。   According to the present invention, it is possible to add a latent heat recovery unit including a latent heat recovery heat exchanger to an existing hot water generator that is not provided with a latent heat recovery heat exchanger, and the latent heat recovery unit includes: Since the temperature of the heat transfer water supplied to the latent heat recovery heat exchanger can be set to a relatively low temperature, the heat exchange efficiency can be increased, and an open cylinder is provided for the latent heat recovery heat exchanger. Since overheating and pressure rise can be prevented, a hot water generator including a latent heat recovery unit with excellent safety can be obtained.

本発明の一実施形態の温水発生機を示す概略構成図である。It is a schematic block diagram which shows the warm water generator of one Embodiment of this invention. 潜熱回収用熱交換器を備えた従来の温水発生機を示す概略構成図である。It is a schematic block diagram which shows the conventional warm water generator provided with the heat exchanger for latent heat collection | recovery.

以下、本発明の一実施形態に係る潜熱回収ユニットについて、図面を参照しながら具体的に説明する。図1は本実施形態に係る温水発生機10を示す概略構成図である。   Hereinafter, a latent heat recovery unit according to an embodiment of the present invention will be specifically described with reference to the drawings. FIG. 1 is a schematic configuration diagram showing a hot water generator 10 according to the present embodiment.

なお、この潜熱回収ユニットを備えた本実施形態における温水発生機10は、例えば、ビルや工場、あるいは銭湯施設などでの給湯や暖房などに好適に使用できるものであるが、給湯や暖房が必要な場所であれば如何なる場所にも設置できる。   In addition, the hot water generator 10 in this embodiment provided with this latent heat recovery unit can be suitably used for hot water supply and heating in a building, a factory, or a public bath facility, for example, but hot water supply and heating are required. It can be installed anywhere.

図1に示すように、本実施形態に係る温水発生機10は、バーナ装置12が設けられた燃焼室13と温水発生機付属熱交換器16とを備えるとともに、減圧蒸気室11aと熱媒水を収容可能とした熱媒水貯留室11bで構成される温水発生機本体11と、燃焼室13より排出される排気ガスを外部に排出する煙道15と、給湯のために設けられた出湯端末である複数のカラン32を備え、各カラン32から出湯される2次湯水を循環させる複数の2次側循環路30と、本実施形態の要部をなし、後に詳述する潜熱回収ユニット90とを具備する構成としている。   As shown in FIG. 1, the hot water generator 10 according to the present embodiment includes a combustion chamber 13 provided with a burner device 12 and a heat exchanger 16 attached to the hot water generator, and a decompression steam chamber 11a and a heat transfer water. The hot water generator main body 11 composed of the heat transfer water storage chamber 11b that can accommodate the hot water, the flue 15 for exhausting the exhaust gas discharged from the combustion chamber 13 to the outside, and the hot water terminal provided for hot water supply A plurality of secondary circulation paths 30 that circulate the secondary hot water discharged from each of the currans 32, a latent heat recovery unit 90 that is a main part of the present embodiment and will be described in detail later. It is set as the structure which comprises.

潜熱回収ユニット90は、上記2次側循環路30とは独立して構成される1次側循環路20と、この1次側循環路20を循環する熱媒水と2次側循環路30を循環する2次湯水との熱交換を行う間接熱交換器50と、既設の煙道15と接続可能に設けられ、バーナ装置12の燃焼により発生した排気ガスを、ケーシング91内を支障なく通過させて既設の煙道15に導出するための煙道構成体70と、この煙道構成体70を通過する排気ガスの熱(顕熱、潜熱)を回収する潜熱回収用熱交換器40とを、所定形状のケーシング91に収納配設した構成としている。   The latent heat recovery unit 90 includes a primary side circulation path 20 configured independently of the secondary side circulation path 30, a heat transfer water circulating through the primary side circulation path 20, and the secondary side circulation path 30. An indirect heat exchanger 50 for exchanging heat with the circulating secondary hot water and an existing flue 15 are provided so that exhaust gas generated by the combustion of the burner device 12 can pass through the casing 91 without hindrance. A flue structure 70 for leading to the existing flue 15 and a latent heat recovery heat exchanger 40 for recovering the heat (sensible heat, latent heat) of the exhaust gas passing through the flue structure 70, The casing 91 is housed and arranged in a predetermined shape.

また、潜熱回収ユニット90は、1次側循環路20を循環する熱媒水の温度変化による膨張及び収縮を吸収する開放筒22と、潜熱回収用熱交換器40による排気ガスの潜熱回収により発生する酸性のドレンを中和する中和装置23と、煙道構成体70を通過する排気ガスが潜熱回収用熱交換器を通過する前と通過した後の排気ガスの温度を測定する2個の温度センサ41,41と、を具備している。   The latent heat recovery unit 90 is generated by the recovery of the latent heat of the exhaust gas by the open cylinder 22 that absorbs expansion and contraction due to the temperature change of the heat transfer water circulating in the primary-side circulation path 20 and the latent heat recovery heat exchanger 40. Neutralizing device 23 for neutralizing acidic drain, and two exhaust gas temperatures for measuring the exhaust gas temperature before and after the exhaust gas passing through the flue structure 70 passes through the latent heat recovery heat exchanger. Temperature sensors 41, 41.

つまり、本実施形態の温水発生機10は、潜熱回収用熱交換器40を具備した潜熱回収ユニット90を備え、この潜熱回収ユニット90により、燃焼室13から排出される排気ガスの熱(潜熱及び顕熱)を効率よく回収して、2次側循環路30を循環する2次湯水を予熱することで、煙道15より排出される熱量を回収して燃料の削減を図っている。   That is, the hot water generator 10 according to the present embodiment includes a latent heat recovery unit 90 including a heat exchanger 40 for recovering latent heat, and the heat of exhaust gas discharged from the combustion chamber 13 by the latent heat recovery unit 90 (latent heat and By efficiently recovering the sensible heat) and preheating the secondary hot water circulating through the secondary side circulation path 30, the amount of heat discharged from the flue 15 is recovered to reduce fuel.

また、潜熱回収ユニット90は、煙道構成体70を通過する排気ガスの潜熱を潜熱回収用熱交換器40により、潜熱回収ユニット90に設けられた1次側循環路20を循環する熱媒水に回収し、1次側循環路20を循環する熱媒水と2次側循環路30を循環する2次湯水とを間接熱交換器50により熱交換させて2次側循環路30を循環する2次湯水を加温する1次循環方式を用いている。   Further, the latent heat recovery unit 90 is a heat transfer water that circulates the latent heat of the exhaust gas passing through the flue structure 70 through the primary side circulation path 20 provided in the latent heat recovery unit 90 by the latent heat recovery heat exchanger 40. The heat transfer water circulating in the primary side circulation path 20 and the secondary hot water circulating in the secondary side circulation path 30 are heat-exchanged by the indirect heat exchanger 50 and circulated in the secondary side circulation path 30. A primary circulation system for heating secondary hot water is used.

つまり、カラン32から出湯される2次湯水は、図示しない水源(上水など)から2次側循環路30に供給された常温の2次湯水(つまり、比較的低温の水である)を、1次側循環路20を循環する高温の熱媒水と間接熱交換器50により熱交換して予熱した後に、さらに、温水発生機本体11に収納されている熱媒水を熱源とした温水発生機付属熱交換器16で加温して、所定温度の2次湯水として供給する。   That is, the secondary hot water discharged from the currant 32 is a secondary hot water having a normal temperature (that is, a relatively low-temperature water) supplied from a water source (not shown) to the secondary side circulation path 30. Hot water generation using heat transfer water stored in the hot water generator body 11 as a heat source after heat exchange with the high-temperature heat transfer water circulating through the primary side circulation path 20 by the indirect heat exchanger 50 and preheating. Heated by the machine-attached heat exchanger 16 and supplied as secondary hot water at a predetermined temperature.

また、図示するように、潜熱回収ユニット90は、排気ガスが通過する煙道構成体70と、この煙道構成体70に設けられた潜熱回収用熱交換器40と、潜熱回収ユニット90の内部で熱媒水を循環させる複数の1次側循環路20と、複数の間接熱交換器50と、外部からの2次湯水を間接熱交換器50へ供給および外部へ排出する複数の2次側循環路30とをケーシング91に収納してユニット化した構成としている。   Further, as shown in the drawing, the latent heat recovery unit 90 includes a flue structure 70 through which exhaust gas passes, a latent heat recovery heat exchanger 40 provided in the flue structure 70, and the interior of the latent heat recovery unit 90. A plurality of primary circulation paths 20 for circulating the heat transfer water, a plurality of indirect heat exchangers 50, and a plurality of secondary sides for supplying secondary hot water from the outside to the indirect heat exchanger 50 and discharging to the outside The circulation path 30 is housed in a casing 91 to form a unit.

このため、ケーシング91には、複数の2次側循環路30を循環する2次湯水を潜熱回収ユニット90の内部の複数の2次側循環路30に供給し、複数の間接熱交換器50により熱交換されて予熱された後の2次湯水を、潜熱回収ユニット90の外部の複数の2次側循環路30に排出する2次側接続部30aが設けられている。   For this reason, the secondary hot water circulating through the plurality of secondary circulation paths 30 is supplied to the casing 91 to the plurality of secondary circulation paths 30 inside the latent heat recovery unit 90, and is supplied by the plurality of indirect heat exchangers 50. Secondary side connection portions 30 a are provided for discharging the secondary hot water after heat exchange and preheating to a plurality of secondary side circulation paths 30 outside the latent heat recovery unit 90.

また、ケーシング91には、温水発生機本体11の燃焼室13及び既設の煙道15、あるいは潜熱回収ユニット90を配設するために用意した煙道15と、ケーシング91の内部の煙道構成体70とを接続する煙道接続部15aが設けられている。かかる煙道接続部15aを介して、温水発生機本体11の燃焼室13から排出される排気ガスはケーシング91内の煙道構成体70に供給され、煙道構成体70を通過して潜熱回収用熱交換器40により熱を回収された後の排気ガスは、ケーシング91の外部に設置された煙道15に排出することができる。   The casing 91 has a flue 15 prepared for disposing the combustion chamber 13 and the existing flue 15 of the hot water generator main body 11 or the latent heat recovery unit 90, and a flue structure inside the casing 91. A flue connection portion 15 a for connecting to 70 is provided. Exhaust gas discharged from the combustion chamber 13 of the hot water generator main body 11 is supplied to the flue structure 70 in the casing 91 through the flue connection portion 15a and passes through the flue structure 70 to recover latent heat. The exhaust gas after the heat is recovered by the heat exchanger 40 can be exhausted to the flue 15 installed outside the casing 91.

なお、潜熱回収ユニット90のケーシング91に設けられた2次側接続部30aは、外部の2次側循環路30を構成する配管等と簡易に接続できる接続機器を採用し、煙道接続部15aも同様に、燃焼室13から排出される排気ガスの煙道15と簡易に接続できる接続機器を採用することが望ましい。これにより、潜熱回収用熱交換器40を有しない既存の温水発生機10等に対する潜熱回収ユニット90の後付け作業を簡易とすることができる。   In addition, the secondary side connection part 30a provided in the casing 91 of the latent heat recovery unit 90 employs a connection device that can be easily connected to piping or the like constituting the external secondary side circulation path 30, and the flue connection part 15a. Similarly, it is desirable to employ a connecting device that can be easily connected to the flue 15 of the exhaust gas discharged from the combustion chamber 13. Thereby, the retrofitting operation | work of the latent heat recovery unit 90 with respect to the existing hot water generator 10 etc. which does not have the heat exchanger 40 for latent heat recovery can be simplified.

また、本実施形態においては、1次側循環路20、間接熱交換器50及び2次側循環路30により構成される回路を、例えば、給湯や暖房のための目的の異なる複数組の回路(例えば、給湯回路、暖房回路など)を備えた構成としている。各回路は基本的に同じ構成となるため、以下の説明では、一組の1次側循環路20、間接熱交換器50及びカラン32を備えた2次側循環路30からなる給湯回路について説明する。   Moreover, in this embodiment, the circuit comprised by the primary side circulation path 20, the indirect heat exchanger 50, and the secondary side circulation path 30 is, for example, a plurality of sets of circuits having different purposes for hot water supply and heating ( For example, it is configured to include a hot water supply circuit, a heating circuit, and the like. Since each circuit has basically the same configuration, in the following description, a hot water supply circuit composed of a secondary side circulation path 30 having a set of primary side circulation path 20, indirect heat exchanger 50 and currant 32 will be described. To do.

温水発生機本体11内の熱媒水貯留室11bには、燃焼室13が設けられており、この燃焼室13の一端側にバーナ装置12を取付けてバーナ口を燃焼室13内に臨ませる一方、他端側には、潜熱回収ユニット90の煙道構成体70と接続されて煙道15の一部となる筒体の基端を連通連結している。なお、筒体としては、潜熱回収ユニット90を後付けする前に配設されていた煙道の一部であってもよい。そして、燃焼室13内での所定の燃料(例えば、ガス・油等)をバーナ装置12により燃焼させた燃焼熱により、温水発生機本体11内の熱媒水貯留室11bに収容されている熱媒水を加温する。   A combustion chamber 13 is provided in the heat medium water storage chamber 11 b in the hot water generator main body 11, and a burner device 12 is attached to one end side of the combustion chamber 13 so that the burner port faces the combustion chamber 13. The other end side is connected to the base end of the cylinder that is connected to the flue structure 70 of the latent heat recovery unit 90 and forms a part of the flue 15. Note that the cylinder may be a part of a flue disposed before the latent heat recovery unit 90 is retrofitted. Then, heat stored in the heat transfer water storage chamber 11b in the hot water generator main body 11 by the combustion heat obtained by burning the predetermined fuel (for example, gas, oil, etc.) in the combustion chamber 13 by the burner device 12. Warm water.

本実施形態に係る潜熱回収ユニット90は、潜熱回収用熱交換器40を、燃焼室13と連通連結された煙道構成体70の燃焼室側に配設し、高温の排気ガスが潜熱回収用熱交換器40を通過するようにしている。そして、潜熱回収用熱交換器40により熱を回収された排気ガスは、煙道構成体70と連通連結された煙道15から外部へ排出される。すなわち、この潜熱回収用熱交換器40は、1次側循環路20を循環する熱媒水を、燃焼室13で所定の燃料(例えば、ガス・油等)を燃焼させた後の排気ガスと熱交換して、1次側循環路20を循環する熱媒水を加温するものであり、1次側循環方式の温水発生機10を実現している。   In the latent heat recovery unit 90 according to the present embodiment, the latent heat recovery heat exchanger 40 is disposed on the combustion chamber side of the flue structure 70 connected to the combustion chamber 13 so that the high-temperature exhaust gas is used for recovering latent heat. It passes through the heat exchanger 40. The exhaust gas whose heat has been recovered by the latent heat recovery heat exchanger 40 is discharged to the outside from the flue 15 connected to the flue structure 70 in communication. That is, the latent heat recovery heat exchanger 40 is configured such that the heat transfer water circulating in the primary-side circulation path 20 and the exhaust gas after burning a predetermined fuel (for example, gas or oil) in the combustion chamber 13 The heat transfer water circulating through the primary-side circulation path 20 is heated by heat exchange, and the primary-side circulation-type hot water generator 10 is realized.

なお、上述した熱交換を行う潜熱回収用熱交換器40及び間接熱交換器50については周知のものであるので説明は省略する。なお、潜熱回収用熱交換器40を用いて行われる熱交換の結果、排気ガスの中の水分が凝縮して酸性のドレンが発生するが、潜熱回収ユニット90には中和装置23が付設されており、潜熱回収用熱交換器40から排出される酸性のドレンはこの中和装置23により処理された後に、温水発生機10の外部へ排水される。   The latent heat recovery heat exchanger 40 and the indirect heat exchanger 50 that perform the heat exchange described above are well known and will not be described. As a result of the heat exchange performed using the latent heat recovery heat exchanger 40, moisture in the exhaust gas is condensed and acidic drain is generated. However, the latent heat recovery unit 90 is provided with a neutralizer 23. The acidic drain discharged from the latent heat recovery heat exchanger 40 is treated by the neutralizing device 23 and then discharged to the outside of the hot water generator 10.

潜熱回収ユニット90の内部の1次側循環路20には、1次側循環ポンプ21が配設されている。この1次側循環ポンプ21は、潜熱回収用熱交換器40と熱交換して加温された比較的高温の熱媒水を間接熱交換器50に供給して、熱媒水と2次側循環路30を循環する2次湯水との熱交換を行うために1次側循環路20の内部の熱媒体を循環させるためのものである。   A primary side circulation pump 21 is disposed in the primary side circulation path 20 inside the latent heat recovery unit 90. The primary-side circulation pump 21 supplies a relatively high-temperature heat transfer water heated by exchanging heat with the latent heat recovery heat exchanger 40 to the indirect heat exchanger 50, so that the heat transfer water and the secondary side In order to perform heat exchange with the secondary hot water circulating in the circulation path 30, the heat medium in the primary side circulation path 20 is circulated.

1次側循環路20には、開放筒22が設けられている。この開放筒22は、1次側循環路20を循環する熱媒水の温度変化による膨張及び収縮を吸収する機器としての機能を有し、このように開放式の開放筒22を用いることで、潜熱回収用熱交換器40を含む潜熱回収ユニット90が第一種圧力容器に該当しないため、本実施形態における温水発生機10の取り扱いが専用の有資格者に限定されることがない。   An open cylinder 22 is provided in the primary side circulation path 20. The open cylinder 22 has a function as a device that absorbs expansion and contraction due to a temperature change of the heat transfer water circulating through the primary side circulation path 20, and by using the open type open cylinder 22 in this way, Since the latent heat recovery unit 90 including the latent heat recovery heat exchanger 40 does not correspond to the first type pressure vessel, the handling of the hot water generator 10 in this embodiment is not limited to a dedicated qualified person.

1次側循環路20を循環する熱媒水は、潜熱回収用熱交換器40で高温の排気ガスの熱を回収して加温され、間接熱交換器50で2次側循環路30を循環する2次湯水と熱交換する。そして、2次湯水と熱交換して温度が低下した熱媒水は、再び潜熱回収用熱交換器40で熱交換して加温されて再び間接熱交換器50に供給される。つまり、潜熱回収ユニット90の内部で1次側循環路20を循環する熱媒水は、潜熱回収用熱交換器40における排気ガスとの熱交換による温度の上昇と、間接熱交換器50における2次側循環ポンプ31を循環する2次湯水との熱交換による温度の低下とを繰り返しながら1次側循環路20を循環する。   The heat transfer water circulating in the primary side circulation path 20 is heated by collecting the heat of the high-temperature exhaust gas in the latent heat recovery heat exchanger 40, and circulates in the secondary side circulation path 30 in the indirect heat exchanger 50. Exchange heat with secondary hot water. Then, the heat transfer water whose temperature has been reduced by exchanging heat with the secondary hot water is again heated by the heat exchanger 40 for recovering latent heat and then supplied to the indirect heat exchanger 50 again. That is, the heat transfer water circulating in the primary side circulation path 20 inside the latent heat recovery unit 90 increases in temperature due to heat exchange with the exhaust gas in the latent heat recovery heat exchanger 40, and 2 in the indirect heat exchanger 50. The primary side circulation path 20 is circulated while repeating a decrease in temperature due to heat exchange with the secondary hot water circulating in the secondary circulation pump 31.

1次側循環路20には給水弁61が設けられた給水管60が接続されている。これは、1次側循環路20内を循環する熱媒水を自動的に補給するためのものである。つまり、潜熱回収ユニット90内の複数の回路において、自然蒸発等により1次側循環路20を循環する熱媒水の量が減少した場合は、給水管60の給水弁61開放して、給水管60から熱媒水を1次側循環路20に補給することで、1次側循環路20内を循環する熱媒水の量を一定に保っている。   A water supply pipe 60 provided with a water supply valve 61 is connected to the primary side circulation path 20. This is for automatically replenishing the heat transfer water circulating in the primary side circulation path 20. That is, in the plurality of circuits in the latent heat recovery unit 90, when the amount of the heat transfer water circulating through the primary side circulation path 20 decreases due to natural evaporation or the like, the water supply valve 61 of the water supply pipe 60 is opened and the water supply pipe is opened. The amount of heat transfer water circulating in the primary side circulation path 20 is kept constant by replenishing the heat transfer medium water from 60 to the primary side circulation path 20.

潜熱回収ユニット90の煙道構成体70には、排気ガスが潜熱回収用熱交換器40を通過する前と通過した後に、当該排気ガスの温度を測定する2個の温度センサ41,41が設けられている。そして、温度センサ41,41で測定した排気ガスの温度が所定の温度より上昇したことを検出することにより、潜熱回収用熱交換器40の清掃時期を予測することができる。   The flue structure 70 of the latent heat recovery unit 90 is provided with two temperature sensors 41, 41 for measuring the temperature of the exhaust gas before and after passing through the latent heat recovery heat exchanger 40. It has been. Then, by detecting that the temperature of the exhaust gas measured by the temperature sensors 41, 41 has risen above a predetermined temperature, the cleaning time of the latent heat recovery heat exchanger 40 can be predicted.

一方、2次側循環路30には、2次湯水を循環させる2次側循環ポンプ31が配設されている。2次側循環ポンプ31により2次側循環路30内を循環する2次湯水は、潜熱回収ユニット90内の間接熱交換器50に供給され、1次側循環路20を循環する熱媒水と熱交換して予熱された後、潜熱回収ユニット90から排出される。   On the other hand, the secondary side circulation path 30 is provided with a secondary side circulation pump 31 for circulating the secondary hot water. The secondary hot water circulated in the secondary side circulation path 30 by the secondary side circulation pump 31 is supplied to the indirect heat exchanger 50 in the latent heat recovery unit 90, and the heat transfer water circulating in the primary side circulation path 20 After being preheated by heat exchange, the heat is discharged from the latent heat recovery unit 90.

そして、潜熱回収ユニット90内の間接熱交換器50により予熱された後の2次湯水は、2次側循環路30を循環して温水発生機本体11に付設された温水発生機付属熱交換器16と熱交換してさらに加温される。   The secondary hot water after being preheated by the indirect heat exchanger 50 in the latent heat recovery unit 90 circulates through the secondary side circulation path 30 and is attached to the hot water generator main body 11 and attached to the hot water generator main body 11. Heat exchange with 16 and further heating.

本実施形態における温水発生機本体11は、内部圧を大気圧以下とした缶体に熱媒水を封入して減圧蒸気室11aと熱媒水貯留室11bを形成すると共に、同熱媒水を加熱するバーナ装置12を燃焼室13に連設し、さらに、熱を取り出すための温水発生機付属熱交換器16を減圧蒸気室11a内に配設して、缶体内に発生する蒸気により2次側循環路30内を循環する2次湯水を加温する。   The hot water generator main body 11 in this embodiment forms a decompression steam chamber 11a and a heat medium water storage chamber 11b by enclosing the heat medium water in a can body having an internal pressure equal to or lower than atmospheric pressure, and also uses the heat medium water. A heating burner device 12 is connected to the combustion chamber 13, and a heat exchanger 16 attached to the hot water generator for taking out heat is disposed in the decompression steam chamber 11 a, and secondary by steam generated in the can body. The secondary hot water circulating in the side circulation path 30 is heated.

つまり、2次側循環路30を循環する2次湯水は、潜熱回収ユニット90の間接熱交換器50により、1次側循環路20を循環する熱媒水と熱交換して予熱され、その後さらに、温水発生機本体11に付設された温水発生機付属熱交換器16と熱交換してさらに加温されて、2次側循環路30に配設されているカラン32から給湯される。   That is, the secondary hot water circulating in the secondary side circulation path 30 is preheated by exchanging heat with the heat transfer medium circulating in the primary side circulation path 20 by the indirect heat exchanger 50 of the latent heat recovery unit 90, and then further heated. Then, heat is exchanged with the heat exchanger 16 attached to the hot water generator main body 11 and further heated, and hot water is supplied from a currant 32 disposed in the secondary side circulation path 30.

また、2次側循環路30には、カラン32から給湯された分の2次湯水を補給する給水口(図示せず)が設けられており、常に2次側循環路30内を所定量の2次湯水が循環するようにしている。   Further, the secondary side circulation path 30 is provided with a water supply port (not shown) for replenishing secondary hot water supplied from the currant 32, and always has a predetermined amount of water in the secondary side circulation path 30. Secondary hot water is circulated.

上述したように、本実施形態においては、潜熱回収ユニット90の潜熱回収用熱交換器40で加温された比較的高温の熱媒水は、複数の1次側循環路20を循環させて複数の間接熱交換器50に供給される。一方、給湯のための比較的低温の2次湯水は、潜熱回収ユニット90内の1次側循環路20とは独立して配管されている複数の2次側循環路30を循環させて複数の間接熱交換器50に供給される。そして、それぞれの間接熱交換器50において熱交換して、複数の2次側循環路30を循環する2次湯水を予熱する構成としている。   As described above, in the present embodiment, the relatively high-temperature heat transfer water heated by the latent heat recovery heat exchanger 40 of the latent heat recovery unit 90 is circulated through the plurality of primary-side circulation paths 20. The indirect heat exchanger 50 is supplied. On the other hand, the relatively low temperature secondary hot water for hot water supply is circulated through a plurality of secondary side circulation paths 30 that are piped independently from the primary side circulation path 20 in the latent heat recovery unit 90. It is supplied to the indirect heat exchanger 50. And it is set as the structure which heat-exchanges in each indirect heat exchanger 50, and preheats the secondary hot water which circulates through the some secondary side circulation path 30. FIG.

そして、2次側循環路30の2次湯水と熱交換して、温度の低下した1次側循環路20の熱媒水は、潜熱回収用熱交換器40において、排気ガスと熱交換して再度加温される。このように、本実施形態に係る温水発生機10は、1次側循環路20を循環する熱媒水を加温するために潜熱回収用熱交換器40を用いている。   Then, the heat transfer water of the primary side circulation path 20, whose temperature has been reduced by exchanging heat with the secondary hot water in the secondary side circulation path 30, exchanges heat with the exhaust gas in the latent heat recovery heat exchanger 40. It is warmed again. As described above, the hot water generator 10 according to the present embodiment uses the latent heat recovery heat exchanger 40 in order to heat the heat transfer water circulating through the primary side circulation path 20.

以上、上述した実施形態によれば、潜熱回収ユニット90は、内部に複数の間接熱交換器50、複数の1次側循環路20、複数の2次側循環路30、潜熱回収用熱交換器40が配置された煙道構成体70などをケーシング91に収納した独立した回路となっているため、潜熱回収用熱交換器40が設置されていない既存の温水発生機にも、最小の配管工事や煙道15の改造により、潜熱回収ユニット90を後付けすることが可能であり、今まで捨てていた高温の排気ガスの熱を有効に回収して、燃費等の向上を図ることができる潜熱回収ユニット90を具備する温水発生機10とすることができる。   As described above, according to the above-described embodiment, the latent heat recovery unit 90 includes the plurality of indirect heat exchangers 50, the plurality of primary circulation paths 20, the plurality of secondary circulation paths 30, and the latent heat recovery heat exchanger. 40 is arranged in an independent circuit in which casings 91 and the like are housed in a casing 91. Therefore, even in an existing hot water generator in which no latent heat recovery heat exchanger 40 is installed, the minimum piping work is performed. The latent heat recovery unit 90 can be retrofitted by remodeling the flue 15 or the flue 15, and the latent heat recovery can effectively improve the fuel consumption by recovering the heat of the high-temperature exhaust gas that has been thrown away until now. It can be set as the warm water generator 10 which comprises the unit 90. FIG.

また、潜熱回収ユニット90の内部で1次側循環路20を循環する熱媒水は、複数の2次側循環路30を循環する2次湯水と複数の間接熱交換器50で熱交換されて温度が低下するため、比較的安定した低温の熱媒水を潜熱回収用熱交換器40に提供することができる。これにより、潜熱回収用熱交換器40の内部の過熱状態や圧力上昇を防ぐとともに、潜熱回収用熱交換器40により効率の高い熱交換を行うことができる。   In addition, the heat transfer water circulating in the primary side circulation path 20 in the latent heat recovery unit 90 is heat-exchanged by the secondary hot water circulating in the plurality of secondary side circulation paths 30 by the plurality of indirect heat exchangers 50. Since the temperature is lowered, a relatively stable low-temperature heat transfer water can be provided to the latent heat recovery heat exchanger 40. Thereby, while preventing the overheat state and pressure rise inside the latent heat recovery heat exchanger 40, the latent heat recovery heat exchanger 40 can perform efficient heat exchange.

また、潜熱回収ユニット90では、1次側循環路20と2次側循環路30とは、間接熱交換器50の内部で切り離されているため、2次側循環路30を循環する2次湯水のスケール成分等が1次側循環路20を循環する熱媒水に侵入することはない。このため、潜熱回収用熱交換器40の内部において、スケール成分等の付着による過熱が起こることはなく、また、腐食等も発生することがない。   Further, in the latent heat recovery unit 90, the primary side circulation path 20 and the secondary side circulation path 30 are separated inside the indirect heat exchanger 50, and therefore, the secondary hot water circulating through the secondary side circulation path 30. The scale component or the like does not enter the heat transfer water circulating through the primary side circulation path 20. For this reason, overheating due to adhesion of scale components and the like does not occur inside the latent heat recovery heat exchanger 40, and corrosion and the like do not occur.

また、潜熱回収ユニット90は、開放筒22を備えているため、1次側循環路20を循環する熱媒水の温度変化による膨張及び収縮を吸収する。このように、開放式の開放筒22を用いることで、潜熱回収用熱交換器40が第一種圧力容器に該当することはない。   Further, since the latent heat recovery unit 90 includes the open cylinder 22, the latent heat recovery unit 90 absorbs expansion and contraction due to a temperature change of the heat transfer water circulating through the primary side circulation path 20. Thus, by using the open type open cylinder 22, the latent heat recovery heat exchanger 40 does not correspond to the first type pressure vessel.

また、潜熱回収ユニット90は、中和装置23を備えているため、潜熱回収用熱交換器40から排出される酸性のドレンを、中和装置23により処理した後に温水発生機10の外部へ排水する。これにより、酸性のドレンによる下水や河川の汚染を防止している。   Further, since the latent heat recovery unit 90 includes the neutralization device 23, the acidic drain discharged from the latent heat recovery heat exchanger 40 is treated by the neutralization device 23 and then discharged to the outside of the hot water generator 10. To do. This prevents sewage and rivers from being contaminated by acidic drainage.

なお、潜熱回収ユニット90を既存の温水発生機に新しく付設すると、潜熱回収用熱交換器40による熱交換により排気ガスの温度が低下するため、煙道構成体70のドラフトが不足して、排気ガスの排出が滞る場合がある。この場合は、煙道構成体70に排気ガスの誘引ファンなどを設けて、煙道構成体70から煙道15へ排気ガスを強制的に排出することで、排気ガスの排出を促進することができる。   Note that if the latent heat recovery unit 90 is newly attached to an existing hot water generator, the temperature of the exhaust gas decreases due to heat exchange by the latent heat recovery heat exchanger 40, so that the draft of the flue structure 70 is insufficient and the exhaust gas is exhausted. Gas emissions may stagnate. In this case, exhaust gas exhaust fan is forcibly discharged from the flue structure 70 to the flue 15 by providing an exhaust fan for the flue structure 70, etc. it can.

また、新規に温水発生機10を設置する場合でも、潜熱回収ユニット90を独立させているため、例えば、潜熱回収ユニット90を構成する要素の故障時の対応や部品の交換などが容易である。   Further, even when the hot water generator 10 is newly installed, since the latent heat recovery unit 90 is made independent, for example, it is easy to cope with a failure of an element constituting the latent heat recovery unit 90 or to replace parts.

上述してきた実施形態より、以下の潜熱回収ユニット90を具備した温水発生機10が実現できる。   From the embodiment described above, the hot water generator 10 including the following latent heat recovery unit 90 can be realized.

(1)熱媒水を収容する温水発生機本体11と、温水発生機本体11内の熱媒水を加温する燃焼室13と、温水発生機本体11に収容された熱媒水と熱交換された2次湯水を循環させる2次側循環路30と、を備える温水発生機10に取付可能とした潜熱回収ユニット90であって、燃焼室13と連通連結可能であり、当該燃焼室13より排出される排気ガスを外部に排出する煙道構成体70と、2次側循環路30とは独立して構成され、熱媒水を循環させる1次側循環路20と、燃焼室13より排出され、煙道構成体70を通過する排気ガスと1次側循環路20中の熱媒水とを熱交換して当該排気ガスの潜熱を回収する潜熱回収用熱交換器40と、1次側循環路20を循環する熱媒水と2次側循環路30を循環する2次湯水との熱交換を行う間接熱交換器50と、が所定のケーシングに収納配設されている潜熱回収ユニット90。 (1) Hot water generator main body 11 that stores the heat transfer water, the combustion chamber 13 that heats the heat transfer medium in the hot water generator main body 11, and heat exchange with the heat transfer water stored in the hot water generator main body 11. A latent heat recovery unit 90 that can be attached to a hot water generator 10 that circulates the secondary hot water that has been circulated, can be connected to the combustion chamber 13, and can be connected to the combustion chamber 13. The flue structure 70 that discharges exhaust gas to the outside and the secondary side circulation path 30 are configured independently, and are discharged from the primary side circulation path 20 that circulates heat transfer water and the combustion chamber 13. The heat exchanger 40 for recovering latent heat that recovers the latent heat of the exhaust gas by exchanging heat between the exhaust gas passing through the flue structure 70 and the heat transfer water in the primary circulation path 20 and the primary side Heat exchange between the heat transfer water circulating in the circulation path 20 and the secondary hot water circulating in the secondary circulation path 30 is performed. Latent heat recovery unit 90 and the indirect heat exchanger 50, but are housed arranged in a predetermined casing.

かかる構成により、例えば、潜熱回収用熱交換器40を備えていない既設の温水発生機10に対して、最小の配管工事や煙道15の改造で、排気ガスの高温の熱を効率よく回収することができる潜熱回収ユニット90を設置することができ、排気ガスの熱を有効に活用して、燃費の向上を図るとともに、二酸化炭素の削減、温室効果の防止等環境に配慮した温水発生機10とすることができる。   With this configuration, for example, with respect to the existing hot water generator 10 that does not include the latent heat recovery heat exchanger 40, the high-temperature heat of the exhaust gas can be efficiently recovered with the minimum piping work and the modification of the flue 15. The latent heat recovery unit 90 can be installed, and the heat from the exhaust gas is effectively used to improve the fuel consumption, and reduce the carbon dioxide and prevent the greenhouse effect. It can be.

(2)2次側循環路30を複数路具備する温水発生機10に取付可能な潜熱回収ユニット90であって、潜熱回収ユニット90を構成するケーシング内に、2次側循環路の数と同数の間接熱交換器50を収納配設した潜熱回収ユニット90。 (2) A latent heat recovery unit 90 which can be attached to the hot water generator 10 having a plurality of secondary side circulation paths 30, and the same number as the number of secondary side circulation paths in the casing constituting the latent heat recovery unit 90. A latent heat recovery unit 90 in which the indirect heat exchanger 50 is accommodated.

かかる構成により、1次側循環路20を循環する熱媒水を、複数の間接熱交換器50により複数路の2次側循環路30を循環する2次湯水と効率よく熱交換して、1次側循環路20を循環して潜熱回収用熱交換器40に供給される熱媒水の温度を低下させることができるため、潜熱回収用熱交換器40内部での熱交換の効率を向上させることができる。   With this configuration, the heat transfer water circulating through the primary circulation path 20 is efficiently heat-exchanged with the secondary hot water circulating through the plurality of secondary circulation paths 30 by the plurality of indirect heat exchangers 50, and 1 Since the temperature of the heat transfer water supplied to the latent heat recovery heat exchanger 40 through the secondary side circulation path 20 can be lowered, the efficiency of heat exchange within the latent heat recovery heat exchanger 40 is improved. be able to.

(3)1次側循環路20を循環する熱媒水の温度変化による膨張及び収縮を吸収する開放筒22を具備する潜熱回収ユニット90。   (3) The latent heat recovery unit 90 including the open cylinder 22 that absorbs expansion and contraction due to temperature change of the heat transfer water circulating in the primary side circulation path 20.

かかる構成により、1次側循環路20を循環する熱媒水の温度変化による膨張及び収縮を吸収する機器として開放式の開放筒22を用いたため、第一種圧力容器に該当しない潜熱回収ユニット90を具備した温水発生機10とすることができる。   With this configuration, since the open-type open cylinder 22 is used as a device that absorbs expansion and contraction due to temperature change of the heat transfer water circulating in the primary-side circulation path 20, the latent heat recovery unit 90 that does not correspond to the first type pressure vessel is used. It can be set as the warm water generator 10 comprised.

(4)潜熱回収用熱交換器40による排気ガスの潜熱回収により発生する酸性のドレンを中和する中和装置23を具備する潜熱回収ユニット90。   (4) A latent heat recovery unit 90 including a neutralizing device 23 for neutralizing acidic drain generated by the latent heat recovery of exhaust gas by the latent heat recovery heat exchanger 40.

かかる構成により、潜熱回収用熱交換器40により生じる酸性のドレンを中和処理した後に排出することができるので、自然環境を破壊することのない環境に優しい潜熱回収ユニット90を具備した温水発生機10とすることができる。   With this configuration, since the acidic drain generated by the latent heat recovery heat exchanger 40 can be discharged after being neutralized, the hot water generator provided with the environmentally friendly latent heat recovery unit 90 that does not destroy the natural environment. 10 can be used.

(5)潜熱回収用熱交換器40を通過する前と通過した後の排気ガスの温度を測定する複数の温度センサ41,41を煙道構成体70に設けた潜熱回収ユニット90。   (5) A latent heat recovery unit 90 provided with a plurality of temperature sensors 41 and 41 in the flue structure 70 for measuring the temperature of exhaust gas before and after passing through the latent heat recovery heat exchanger 40.

かかる構成により、潜熱回収用熱交換器40による熱交換の効率の低下を知ることができるため、潜熱回収ユニット90に具備されている潜熱回収用熱交換器40の清掃時期の予測を容易に行うことができる。   With this configuration, since it is possible to know a decrease in the efficiency of heat exchange by the latent heat recovery heat exchanger 40, it is easy to predict the cleaning time of the latent heat recovery heat exchanger 40 provided in the latent heat recovery unit 90. be able to.

なお、本実施形態においては、熱媒水として水(熱媒水)を加熱する潜熱回収ユニット90を具備する温水発生機10を用いて説明したが、本発明はこれに限定されるものではなく、例えば、ガスエンジンの排熱回収、その他高温の排気ガスが発生する機器に適用することも可能である。   In addition, in this embodiment, although demonstrated using the warm water generator 10 which comprises the latent heat recovery unit 90 which heats water (heat-medium water) as heat-medium water, this invention is not limited to this. For example, the present invention can be applied to exhaust heat recovery of a gas engine and other devices that generate high-temperature exhaust gas.

以上、実施例を説明したが、本発明の具体的な構成は前記実施例に限定されるものではなく、発明の要旨を逸脱しない範囲の設計変更等があっても本発明に含まれる。   Although the embodiments have been described above, the specific configuration of the present invention is not limited to the above-described embodiments, and design changes and the like within a scope not departing from the gist of the invention are included in the present invention.

10 温水発生機
11 温水発生機本体
12 バーナ装置
13 燃焼室
15 煙道
16 温水発生機付属熱交換器
20 1次側循環路
21 1次側循環ポンプ
22 開放筒
23 中和装置
30 2次側循環路
31 2次側循環ポンプ
32 カラン
40 潜熱回収用熱交換器
41 温度センサ
50 間接熱交換器
60 給水管
61 給水弁
70 煙道構成体
90 潜熱回収ユニット
91 ケーシング
DESCRIPTION OF SYMBOLS 10 Hot water generator 11 Hot water generator main body 12 Burner apparatus 13 Combustion chamber 15 Flue 16 Heat exchanger attached to hot water generator 20 Primary side circulation path 21 Primary side circulation pump 22 Open cylinder 23 Neutralizer 30 Secondary side circulation Path 31 Secondary circulation pump 32 Curan 40 Heat exchanger for latent heat recovery 41 Temperature sensor 50 Indirect heat exchanger 60 Water supply pipe 61 Water supply valve 70 Flue structure 90 Latent heat recovery unit 91 Casing

Claims (5)

熱媒水を収容する温水発生機本体と、
前記温水発生機本体内の熱媒水を加温する燃焼室と、
前記温水発生機本体に収容された熱媒水と熱交換された2次湯水を循環させる2次側循環路と、を備える温水器に取付可能とした潜熱回収ユニットであって、
前記燃焼室と連通連結可能であり、当該燃焼室より排出される排気ガスを外部に排出する煙道構成体と、
前記2次側循環路とは独立して構成され、熱媒水を循環させる1次側循環路と、
前記燃焼室より排出され、前記煙道構成体内を通過する排気ガスと前記1次側循環路中の熱媒水とを熱交換して当該排気ガスの潜熱を回収する潜熱回収用熱交換器と、
前記1次側循環路を循環する熱媒水と前記2次側循環路を循環する2次湯水との熱交換を行う間接熱交換器と、
が所定のケーシングに収納配設されていることを特徴とする潜熱回収ユニット。
A hot water generator main body for storing heat transfer water,
A combustion chamber for heating the heat transfer water in the hot water generator body;
A latent heat recovery unit that can be attached to a water heater comprising a secondary side circulation path that circulates secondary hot water that has been heat-exchanged with heat transfer water contained in the hot water generator body,
A flue structure that is communicably connected to the combustion chamber and exhausts exhaust gas discharged from the combustion chamber to the outside;
A primary side circulation path configured independently of the secondary side circulation path for circulating the heat transfer water;
A latent heat recovery heat exchanger for exchanging heat between the exhaust gas discharged from the combustion chamber and passing through the flue structure and the heat transfer water in the primary side circulation path to recover the latent heat of the exhaust gas; ,
An indirect heat exchanger that performs heat exchange between the heat transfer water circulating through the primary circuit and the secondary hot water circulating through the secondary circuit;
Is stored and arranged in a predetermined casing.
前記2次側循環路を複数路具備する温水器に取付可能な潜熱回収ユニットであって、
前記ケーシング内に、前記2次側循環路の数と同数の間接熱交換器を収納配設したことを特徴とする請求項1に記載の潜熱回収ユニット。
A latent heat recovery unit attachable to a water heater having a plurality of secondary side circulation paths,
The latent heat recovery unit according to claim 1, wherein the same number of indirect heat exchangers as the number of the secondary circulation paths are accommodated in the casing.
前記1次側循環路を循環する熱媒水の温度変化による膨張及び収縮を吸収する開放筒を具備することを特徴とする請求項1又は2に記載の潜熱回収ユニット。   The latent heat recovery unit according to claim 1, further comprising an open cylinder that absorbs expansion and contraction due to a temperature change of the heat transfer water circulating in the primary side circulation path. 前記潜熱回収用熱交換器による排気ガスの潜熱回収により発生する酸性のドレンを中和する中和装置を具備することを特徴とする請求項1〜3のいずれか1項に記載の潜熱回収ユニット。   The latent heat recovery unit according to any one of claims 1 to 3, further comprising a neutralizer that neutralizes acidic drain generated by the latent heat recovery of the exhaust gas by the latent heat recovery heat exchanger. . 前記潜熱回収用熱交換器を通過する前と通過した後の排気ガスの温度を測定する複数の温度センサを前記煙道構成体に設けたことを特徴とする請求項1〜4のいずれか1項に記載の潜熱回収ユニット。   5. The flue structure according to claim 1, wherein a plurality of temperature sensors for measuring the temperature of the exhaust gas before and after passing through the latent heat recovery heat exchanger are provided in the flue structure. The latent heat recovery unit according to Item.
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JP2013108727A (en) * 2011-11-24 2013-06-06 Nippon Thermoener Co Ltd Heat recovery device of vacuum type water heater exhaust gas and heat recovery method using the same
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JP2015200455A (en) * 2014-04-08 2015-11-12 株式会社日本サーモエナー Vacuum-type water heater
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JP2013108727A (en) * 2011-11-24 2013-06-06 Nippon Thermoener Co Ltd Heat recovery device of vacuum type water heater exhaust gas and heat recovery method using the same
JP2015183914A (en) * 2014-03-24 2015-10-22 株式会社日本サーモエナー Vacuum type water warmer
JP2015200455A (en) * 2014-04-08 2015-11-12 株式会社日本サーモエナー Vacuum-type water heater
CN114484575A (en) * 2021-12-28 2022-05-13 青海中控太阳能发电有限公司 Heat storage equipment matched with molten salt tank and using method thereof
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