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JP6837589B2 - Heat exchanger and heat source machine - Google Patents
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JP6837589B2 - Heat exchanger and heat source machine - Google Patents

Heat exchanger and heat source machine Download PDF

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JP6837589B2
JP6837589B2 JP2020065715A JP2020065715A JP6837589B2 JP 6837589 B2 JP6837589 B2 JP 6837589B2 JP 2020065715 A JP2020065715 A JP 2020065715A JP 2020065715 A JP2020065715 A JP 2020065715A JP 6837589 B2 JP6837589 B2 JP 6837589B2
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heat
heat exchange
water supply
housing portion
combustion exhaust
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JP2020101363A (en
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克巳 内藤
克巳 内藤
貴也 太田
貴也 太田
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Purpose Co Ltd
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Description

本発明はたとえば、一缶三水型熱源機などに用いられる熱交換技術に関する。
The present invention relates to, for example, a heat exchange technique used in a one-can, three-water heat source machine or the like.

給湯、浴槽水追焚、温水暖房などの複数の機能を持ついわゆる暖房機能付き給湯器には、熱源に一缶三水型熱源機が用いられる。一缶三水型熱源機では熱源にひとつのバーナーが用いられ、バーナーの燃焼排気で複数系統からなる給湯加熱、追焚加熱および暖房水加熱を行う。 A one-can, three-water type heat source machine is used as a heat source for a so-called water heater with a heating function, which has multiple functions such as hot water supply, bathtub water reheating, and hot water heating. In a one-can, three-water type heat source machine, one burner is used as a heat source, and the combustion exhaust of the burner performs hot water supply heating, reheating heating, and heating water heating consisting of a plurality of systems.

バーナーの燃焼排気を給水、浴槽水または暖房水に熱交換する場合、燃焼排気の顕熱を回収する一次熱交換と、一次熱交換後の燃焼排気の潜熱を熱交換する二次熱交換を併用し、熱交換の高効率化を図ることが知られている。 When exchanging heat from the combustion exhaust of the burner with water supply, bath water or heating water, both primary heat exchange that recovers the actual heat of the combustion exhaust and secondary heat exchange that exchanges heat with the latent heat of the combustion exhaust after the primary heat exchange are used together. However, it is known to improve the efficiency of heat exchange.

この種の熱源機に関し、追焚回路や暖房回路のような循環回路と給湯回路の双方を加熱する二次熱交換器を含む熱交換器や該熱交換器を用いた給湯器が知られている(たとえば、特許文献1、特許文献2)。
Regarding this type of heat source machine, heat exchangers including a secondary heat exchanger that heats both a circulation circuit such as a reheating circuit and a heating circuit and a hot water supply circuit, and a water heater using the heat exchanger are known. (For example, Patent Document 1, Patent Document 2).

特開2004−28446号公報Japanese Unexamined Patent Publication No. 2004-28446 特開2004−28447号公報Japanese Unexamined Patent Publication No. 2004-28447

ところで、一次および二次の熱交換器を備える熱源機では、低温度の給水を二次熱交換で予備加熱を行った後、一次熱交換を行えば、燃焼排気が持つ熱を一次および二次の熱交換で究極的な高効率の熱交換を行って加熱できる。この熱交換の高効率化は、給水が低温度であるほど、有効である。 By the way, in a heat source machine equipped with primary and secondary heat exchangers, if low-temperature water supply is preheated by secondary heat exchange and then primary heat exchange is performed, the heat of the combustion exhaust is transferred to the primary and secondary. The ultimate high-efficiency heat exchange can be performed and heated. This high efficiency of heat exchange is more effective as the temperature of the water supply is lower.

しかし、暖房水などの熱媒では、放熱量が小さく、給水のように低温化していない場合がある。つまり、熱交換器に帰還する熱媒の温度が高い場合では、給水のような二次熱交換を行っても、燃焼排気から潜熱までは回収できないため、給水のような高効率の熱交換を実現することができない。また、熱媒の予備加熱を二次熱交換で実現しようとすれば、既述のように二次熱交換が予定している潜熱回収を行えないばかりか、熱媒の循環による循環抵抗を増大させるという課題がある。 However, with a heat medium such as heating water, the amount of heat dissipated is small, and the temperature may not be lowered as in the case of water supply. In other words, when the temperature of the heat medium returning to the heat exchanger is high, even if secondary heat exchange such as water supply is performed, the heat exchange from the combustion exhaust to the latent heat cannot be recovered, so high-efficiency heat exchange such as water supply is performed. It cannot be realized. Further, if the preheating of the heat medium is to be realized by the secondary heat exchange, not only the latent heat recovery planned for the secondary heat exchange cannot be performed as described above, but also the circulation resistance due to the circulation of the heat medium is increased. There is a problem to make it.

そこで、本発明の目的は上記課題に鑑み、燃焼排気から暖房水などに用いられる熱媒への究極的な熱回収を図り、効率的な熱交換を実現することにある。 Therefore, in view of the above problems, an object of the present invention is to achieve ultimate heat recovery from combustion exhaust gas to a heat medium used for heating water or the like, and to realize efficient heat exchange.

本発明の他の目的は上記課題に鑑み、燃焼排気から暖房水などに用いられる熱媒への究極的な熱回収に一次熱交換の多重化によって実現し、熱交換の高効率化を実現することにある。
In view of the above problems, another object of the present invention realizes ultimate heat recovery from combustion exhaust to a heat medium used for heating water or the like by multiplexing primary heat exchange, and realizes high efficiency of heat exchange. There is.

上記目的を達成するため、本発明の熱交換器の一側面によれば、燃焼排気と熱媒を熱交換させる第一熱交換部(6−1)を収納する第1の筐体部と、前記第1の筐体部に隣接し、前記第1の筐体部から流入する前記燃焼排気と前記熱媒を熱交換する第二熱交換部(6−2)と、前記燃焼排気と給水を熱交換する第三熱交換部(6−3)とを収納する第二筐体部と、前記第1の筐体部の天井部と前記第2の筐体部の底部との間に設けられ、前記第2の筐体部の前記底部を傾斜させる傾斜板と、前記傾斜板に形成され、前記第1の筐体部からの前記燃焼排気を前記第2の筐体部の内部に導く通気窓部と、前記傾斜板から前記通気窓部に張り出して設けられ、前記傾斜板よりも傾斜を大きくした遮蔽板とを備える。 In order to achieve the above object, according to one aspect of the heat exchanger of the present invention, a first housing portion for accommodating a first heat exchange portion (6-1) for heat exchange between combustion exhaust and a heat medium, and a first housing portion. A second heat exchange unit (6-2) adjacent to the first housing portion and exchanging heat between the combustion exhaust and the heat medium flowing in from the first housing portion, and the combustion exhaust and water supply. A second housing portion for accommodating a third heat exchange portion (6-3) for heat exchange is provided between the ceiling portion of the first housing portion and the bottom portion of the second housing portion. , An inclined plate that inclines the bottom portion of the second housing portion, and ventilation formed on the inclined plate to guide the combustion exhaust from the first housing portion to the inside of the second housing portion. It includes a window portion and a shielding plate which is provided so as to project from the inclined plate to the ventilation window portion and has a larger inclination than the inclined plate.

上記熱交換器において、前記遮蔽板は、前記通気窓部側に張り出した前記第二熱交換部(6−2)または前記第三熱交換部(6−3)の底部を覆ってよい。 In the heat exchanger, the shielding plate may cover the bottom of the second heat exchange section (6-2) or the third heat exchange section (6-3) protruding toward the ventilation window portion.

上記熱交換器において、前記第2の筐体部は、前記第1の筐体部の側面側に突出したドレン受けを有し、前記第二熱交換部(6−2)と前記第三熱交換部(6−3)のいずれかまたは双方から発生したドレンを、前記遮蔽板および前記傾斜板に沿って流して前記ドレン受けに導入してよい。 In the heat exchanger, the second housing portion has a drain receiver protruding from the side surface side of the first housing portion, and the second heat exchange portion (6-2) and the third heat. Drain generated from either or both of the exchange portions (6-3) may be flowed along the shielding plate and the inclined plate to be introduced into the drain receiver.

上記熱交換器において、前記第二熱交換部(6−2)と前記第三熱交換部(6−3)は、前記第2の筐体部内において、前記燃焼排気の流れ方向と平行に隣接または前記燃焼排気に対して垂直方向に隣接して配置されてよい。 In the heat exchanger, the second heat exchange section (6-2) and the third heat exchange section (6-3) are adjacent to each other in the second housing section in parallel with the flow direction of the combustion exhaust. Alternatively, it may be arranged adjacent to the combustion exhaust in the vertical direction.

上記目的を達成するため、本発明の熱源機の一側面によれば、熱媒回路に循環する熱媒、または追焚回路に循環する浴槽水と燃焼排気とを熱交換させる第一熱交換部(6−1)を収納する第1の筐体部と、前記第1の筐体部に隣接し、前記第1の筐体部から流入する前記燃焼排気と前記熱媒回路に循環する前記熱媒を熱交換する第二熱交換部(6−2)と、給湯回路に備えられて、この給湯回路に流れる給水と前記燃焼排気を熱交換する第三熱交換部(6−3)とを収納する第2の筐体部と、前記第1の筐体部の天井部と前記第2の筐体部の底部との間に設けられ、前記第2の筐体部の前記底部を傾斜させる傾斜板と、前記傾斜板に形成され、前記第1の筐体部からの前記燃焼排気を前記第2の筐体部の内部に導く通気窓部と、前記傾斜板から前記通気窓部に張り出して設けられ、前記傾斜板よりも傾斜を大きくした遮蔽板とを備える。
In order to achieve the above object, according to one aspect of the heat source machine of the present invention, the first heat exchange unit that exchanges heat between the heat medium circulating in the heat medium circuit or the bath water circulating in the reheating circuit and the combustion exhaust. The first housing portion that houses (6-1), the combustion exhaust that is adjacent to the first housing portion, flows in from the first housing portion, and the heat that circulates in the heat medium circuit. A second heat exchange unit (6-2) that exchanges heat with the medium, and a third heat exchange unit (6-3) that is provided in the hot water supply circuit and exchanges heat between the water supply flowing through the hot water supply circuit and the combustion exhaust. It is provided between the second housing portion to be stored, the ceiling portion of the first housing portion, and the bottom portion of the second housing portion, and the bottom portion of the second housing portion is inclined. An inclined plate, a ventilation window portion formed on the inclined plate and guiding the combustion exhaust from the first housing portion to the inside of the second housing portion, and a ventilation window portion extending from the inclined plate to the ventilation window portion. It is provided with a shielding plate having a larger inclination than the inclined plate.

本発明によれば、次のいずれかの効果が得られる。 According to the present invention, any of the following effects can be obtained.

(1) 第一熱交換部では燃焼排気と熱媒を熱交換でき、第二熱交換部では第一熱交換部を通過させた燃焼排気と第一熱交換部の通過前の熱媒とを熱交換できるので、第一熱交換部および第二熱交換部で燃焼排気の顕熱を熱媒に回収でき、熱変換効率を高めることができる。 (1) The first heat exchange section can exchange heat between the combustion exhaust and the heat medium, and the second heat exchange section exchanges the combustion exhaust that has passed through the first heat exchange section with the heat medium before passing through the first heat exchange section. Since heat can be exchanged, the apparent heat of the combustion exhaust can be recovered in the heat medium at the first heat exchange section and the second heat exchange section, and the heat conversion efficiency can be improved.

(2) 熱媒がたとえば、暖房水のように、高温状態で第二熱交換部から第一熱交換部に循環する場合にあっても、第二熱交換部では燃焼排気の顕熱を熱媒に熱交換でき、第二熱交換部を通過した熱媒に第一熱交換部で燃焼排気の顕熱を回収できるので、燃焼排気の顕熱の熱変換効率を高め、熱効率を向上させることができる。 (2) Even when the heat medium circulates from the second heat exchange section to the first heat exchange section in a high temperature state, such as heating water, the second heat exchange section heats the apparent heat of the combustion exhaust. Since heat can be exchanged with the medium and the apparent heat of the combustion exhaust can be recovered by the first heat exchange section with the heat medium that has passed through the second heat exchange section, the heat conversion efficiency of the visible heat of the combustion exhaust can be improved and the heat efficiency can be improved. Can be done.

(3) 第一熱交換部および第二熱交換部で顕熱が回収された燃焼排気をたとえば、低温の給水に熱交換でき、給水に対する熱交換効率を高めることができる。給水加熱側の部分沸騰を防止でき、燃焼停止の頻発を防止でき、加熱制御が容易になる。 (3) For example, the combustion exhaust whose sensible heat is recovered in the first heat exchange section and the second heat exchange section can be heat-exchanged for low-temperature water supply, and the heat exchange efficiency for the water supply can be improved. Partial boiling on the water supply heating side can be prevented, combustion stoppage can be prevented frequently, and heating control becomes easy.

(4) 燃焼排気から暖房水などに用いられる熱媒への究極的な熱回収に一次熱交換の多重化によって実現でき、熱交換の高効率化を図ることができる。
(4) The ultimate heat recovery from combustion exhaust to a heat medium used for heating water, etc. can be realized by multiplexing primary heat exchange, and high efficiency of heat exchange can be achieved.

一実施の形態に係る熱交換器の一例を示す図である。It is a figure which shows an example of the heat exchanger which concerns on one Embodiment. 一実施の形態に係る熱交換器の変形例を示す図である。It is a figure which shows the modification of the heat exchanger which concerns on one Embodiment. 実施例1に係る熱源機の一部を示す斜視図である。It is a perspective view which shows a part of the heat source machine which concerns on Example 1. FIG. Aは排気筒部を省略した図3のIVA −IVA 線断面図であり、BはAのIVB −IVB 線断面図である。A is a sectional view taken along line IVA-IVA of FIG. 3 in which the exhaust stack portion is omitted, and B is a sectional view taken along line IVB-IVB of A. 熱源機から取り出した熱交換器を示す斜視図である。It is a perspective view which shows the heat exchanger taken out from a heat source machine. 熱交換器の背面側から示す斜視図である。It is a perspective view which shows from the back side of a heat exchanger. 実施例2に係る給湯器の一例を示す図である。It is a figure which shows an example of the water heater which concerns on Example 2. FIG. 制御系統を示す図である。It is a figure which shows the control system. 駆動制御の処理手順の一例を示すフローチャートである。It is a flowchart which shows an example of the processing procedure of a drive control. 駆動制御の処理手順の一例を示すフローチャートである。It is a flowchart which shows an example of the processing procedure of a drive control. 他の実施の形態に係る熱交換器を示す図である。It is a figure which shows the heat exchanger which concerns on other embodiment.

図1は、一実施の形態に係る熱交換器を示している。図1に示す構成は一例であり、係る構成に本発明が限定されるものではない。 FIG. 1 shows a heat exchanger according to an embodiment. The configuration shown in FIG. 1 is an example, and the present invention is not limited to such a configuration.

この熱交換器2の下側には筐体4が備えられ、この筐体4の上側に第一熱交換部6−1、第二熱交換部6−2および第三熱交換部6−3が備えられている。筐体4はたとえば、燃料ガスGを燃焼させるバーナー8が備えられた燃焼室であり、燃料ガスGの燃焼で生じた燃焼排気EGが第一熱交換部6−1に流れ、この第一熱交換部6−1を通過した後、第二熱交換部6−2および第三熱交換部6−3に流れ、その後、排気部10から外気に排出される。 A housing 4 is provided on the lower side of the heat exchanger 2, and the first heat exchange unit 6-1, the second heat exchange unit 6-2, and the third heat exchange unit 6-3 are provided on the upper side of the housing 4. Is provided. The housing 4 is, for example, a combustion chamber provided with a burner 8 for burning the fuel gas G, and the combustion exhaust EG generated by the combustion of the fuel gas G flows to the first heat exchange section 6-1 and the first heat. After passing through the exchange section 6-1 it flows to the second heat exchange section 6-2 and the third heat exchange section 6-3, and then is discharged from the exhaust section 10 to the outside air.

第一熱交換部6−1には第1の熱交換パイプとしてたとえば、熱媒熱交換パイプ12−1、第2の熱交換パイプとしてたとえば、浴槽水熱交換パイプ14が備えられる。熱媒熱交換パイプ12−1では燃焼排気EGと熱媒Mの一次熱交換、浴槽水熱交換パイプ14では燃焼排気EGと浴槽水BWとの一次熱交換が行われる。ここで、一次熱交換は、燃焼排気EGの顕熱と熱媒Mや浴槽水BWの被加熱流体との熱交換である。被加熱流体には給水を含んでもよい。 The first heat exchange section 6-1 is provided with, for example, a heat medium heat exchange pipe 12-1 as a first heat exchange pipe, and, for example, a bath water heat exchange pipe 14 as a second heat exchange pipe. In the heat medium heat exchange pipe 12-1, the primary heat exchange between the combustion exhaust EG and the heat medium M is performed, and in the bath water heat exchange pipe 14, the primary heat exchange between the combustion exhaust EG and the bath water BW is performed. Here, the primary heat exchange is the heat exchange between the sensible heat of the combustion exhaust EG and the heated fluid of the heat medium M and the bath water BW. The fluid to be heated may include water supply.

第二熱交換部6−2には第3の熱交換パイプとしてたとえば、熱媒熱交換パイプ12−2が備えられる。この熱媒熱交換パイプ12−2は熱媒熱交換パイプ12−1と共通の熱媒循環路を構成しており、図示していないが、熱媒熱交換パイプ12−1に接続されている。この熱媒熱交換パイプ12−2には暖房負荷または熱源機内の熱媒循環路を循環した熱媒Mを流し、熱媒熱交換パイプ12−1の熱交換前の熱媒Mの予備加熱が行われる。 The second heat exchange section 6-2 is provided with, for example, a heat medium heat exchange pipe 12-2 as a third heat exchange pipe. This heat medium heat exchange pipe 12-2 constitutes a common heat medium circulation path with the heat medium heat exchange pipe 12-1, and is connected to the heat medium heat exchange pipe 12-1 although not shown. .. A heat medium M circulated through a heating load or a heat medium circulation path in the heat source machine is passed through the heat medium heat exchange pipe 12-2, and preheating of the heat medium M before heat exchange of the heat medium heat exchange pipe 12-1 is performed. Will be done.

第三熱交換部6−3には熱媒Mの循環系統と異なる給水系統のたとえば、給水熱交換パイプ16が備えられる。この給水熱交換パイプ16は、第4の熱交換パイプの一例である。この給水熱交換パイプ16では給湯時、給水Wの予備加熱が行われる。 The third heat exchange unit 6-3 is provided with, for example, a water supply heat exchange pipe 16 having a water supply system different from the circulation system of the heat medium M. The water supply heat exchange pipe 16 is an example of a fourth heat exchange pipe. In the water supply heat exchange pipe 16, the water supply W is preheated at the time of hot water supply.

この熱交換器2の熱交換は以下の通りである。 The heat exchange of the heat exchanger 2 is as follows.

第一熱交換部6−1を通過した燃焼排気EGは、筐体4から第一熱交換部6−1の下流側にある第二熱交換部6−2および第三熱交換部6−3に流れる。 The combustion exhaust EG that has passed through the first heat exchange section 6-1 is the second heat exchange section 6-2 and the third heat exchange section 6-3 located on the downstream side of the first heat exchange section 6-1 from the housing 4. Flow to.

熱媒Mは、第二熱交換部6−2の熱媒熱交換パイプ12−2を経て熱媒熱交換パイプ12−1に流れる。これに対し、燃焼排気EGは、第一熱交換部6−1を経て第二熱交換部6−2に流れる。つまり、バーナー8から生じた燃焼排気EGについて、バーナー8に近い側を上流側、バーナー8から遠い側を下流側とすれば、第一熱交換部6−1では上流側の燃焼排気EGで熱交換が行われ、第二熱交換部6−2では下流側の燃焼排気EGで熱交換が行われることになる。 The heat medium M flows through the heat medium heat exchange pipe 12-2 of the second heat exchange section 6-2 to the heat medium heat exchange pipe 12-1. On the other hand, the combustion exhaust EG flows to the second heat exchange section 6-2 via the first heat exchange section 6-1. That is, with respect to the combustion exhaust EG generated from the burner 8, if the side closer to the burner 8 is the upstream side and the side far from the burner 8 is the downstream side, the first heat exchange section 6-1 heats up with the combustion exhaust EG on the upstream side. The exchange is performed, and in the second heat exchange unit 6-2, heat exchange is performed at the combustion exhaust EG on the downstream side.

このような第一熱交換部6−1および第二熱交換部6−2では、一次熱交換の多重化により、燃焼排気EGの顕熱と熱媒Mとの熱交換を行う。第一熱交換部6−1を通過した燃焼排気EGが持つ熱は一次熱交換に適した高温排気である。しかも、熱媒Mはたとえば、暖房水などでは低温化していない場合も想定される。そこで、第二熱交換部6−2では熱媒Mと燃焼排気EGの顕熱との熱交換を行い、これにより加熱された熱媒Mが第一熱交換部6−1に流れる。これにより、熱媒Mと燃焼排気EGとの究極的な一次熱交換が行われ、熱媒Mが高温化される。この場合、暖房負荷や熱源機内から帰還する熱媒Mが低温化していない場合にもこれらの一次熱交換によって加熱することができる。一次熱交換を多重化して究極的な顕熱の熱回収を実現できる。 In such a first heat exchange unit 6-1 and a second heat exchange unit 6-2, the sensible heat of the combustion exhaust EG and the heat exchange with the heat medium M are performed by multiplexing the primary heat exchange. The heat contained in the combustion exhaust EG that has passed through the first heat exchange section 6-1 is high temperature exhaust suitable for primary heat exchange. Moreover, it is assumed that the heat medium M is not lowered in temperature with, for example, heating water. Therefore, the second heat exchange unit 6-2 exchanges heat between the heat medium M and the sensible heat of the combustion exhaust EG, and the heat medium M heated by this exchanges heat with the first heat exchange unit 6-1. As a result, the ultimate primary heat exchange between the heat medium M and the combustion exhaust EG is performed, and the temperature of the heat medium M is raised. In this case, even when the heat medium M returning from the heating load or the heat source machine is not cooled down, it can be heated by these primary heat exchanges. The ultimate sensible heat recovery can be achieved by multiplexing the primary heat exchange.

既述の一次熱交換は二次熱交換を排除する意味ではない。熱媒Mが低温化されている場合には、第二熱交換部6−2で燃焼排気EGの顕熱だけでなく、潜熱との熱交換を行えることは言うまでもない。 The primary heat exchange described above does not mean to exclude the secondary heat exchange. Needless to say, when the heat medium M is lowered in temperature, not only the sensible heat of the combustion exhaust EG but also the heat exchange with the latent heat can be performed by the second heat exchange unit 6-2.

そして、第三熱交換部6−3では給湯時、給水熱交換パイプ16に給水Wを循環させ、下流側の燃焼排気EGと給水Wの二次熱交換が行われる。 Then, in the third heat exchange unit 6-3, at the time of hot water supply, the water supply W is circulated in the water supply heat exchange pipe 16, and the secondary heat exchange between the combustion exhaust EG on the downstream side and the water supply W is performed.

<一実施の形態の効果> <Effect of one embodiment>

(1) 一次熱交換の多重化によって究極的な熱交換つまり、燃焼排気EGから顕熱を回収し、熱媒Mなどの被加熱媒体の加熱を実現でき、熱変換効率が高められる。 (1) Ultimate heat exchange by multiplexing primary heat exchange, that is, sensible heat can be recovered from the combustion exhaust EG to realize heating of a medium to be heated such as heat medium M, and heat conversion efficiency is enhanced.

(2) 給水などの低温被加熱流体に比較し、暖房水などの熱媒Mの他、低温化していない被加熱媒体の顕熱による加熱を実現できる。 (2) Compared with a low-temperature heated fluid such as water supply, it is possible to realize heating by sensible heat of a heated medium that has not been cooled in addition to the heat medium M such as heating water.

(3) 低温化した熱媒Mでは燃焼排気EGから潜熱までも熱媒Mに吸収し、熱変換効率が高められる。 (3) In the low-temperature heat medium M, even the latent heat from the combustion exhaust EG is absorbed by the heat medium M, and the heat conversion efficiency is enhanced.

(4) 給湯時、給水熱交換パイプ16に給水Wを循環させ、下流側の燃焼排気EGと給水Wの二次熱交換が行われ、給水Wの主たる熱交換前の予備加熱を行うことができる。この場合、給水Wには燃焼排気EGの潜熱を回収させるので、給湯を停止している際にも、給水熱交換パイプ16の残留水の部分沸騰を回避できる。 (4) At the time of hot water supply, the water supply W is circulated through the water supply heat exchange pipe 16 to exchange the secondary heat between the combustion exhaust EG on the downstream side and the water supply W, and preheating before the main heat exchange of the water supply W is performed. it can. In this case, since the latent heat of the combustion exhaust EG is recovered by the water supply W, partial boiling of the residual water of the water supply heat exchange pipe 16 can be avoided even when the hot water supply is stopped.

図1に示す実施の形態では、第二熱交換部6−2の上側に第三熱交換部6−3を延長してその一部を設置しているが、これに限定されない。たとえば、図2に示すように、第二熱交換部6−2の下側に第三熱交換部6−3を延長させて設置してもよい。
In the embodiment shown in FIG. 1, the third heat exchange section 6-3 is extended above the second heat exchange section 6-2 and a part thereof is installed, but the present invention is not limited to this. For example, as shown in FIG. 2, the third heat exchange unit 6-3 may be extended and installed below the second heat exchange unit 6-2.

図3は、実施例1に係る熱源機の一例を示している。この熱源機において、図1または図2と同一部分には同一符号を付してある。 FIG. 3 shows an example of the heat source machine according to the first embodiment. In this heat source machine, the same parts as those in FIG. 1 or 2 are designated by the same reference numerals.

この熱源機20には、図中前側に熱交換器22が配置され、この熱交換器22の後部側にプレート熱交換器24が配置されている。このプレート熱交換器24は、第四熱交換部の一例である。熱交換器22は、既述の熱交換器2の一例である。プレート熱交換器24は、熱交換器22で加熱された熱媒Mと給水Wとの熱交換を行う。この例では、給水Wは、熱交換器22に含まれる第三熱交換部6−3で予備加熱が施される。 In the heat source machine 20, a heat exchanger 22 is arranged on the front side in the drawing, and a plate heat exchanger 24 is arranged on the rear side of the heat exchanger 22. The plate heat exchanger 24 is an example of a fourth heat exchanger. The heat exchanger 22 is an example of the heat exchanger 2 described above. The plate heat exchanger 24 exchanges heat between the heat medium M heated by the heat exchanger 22 and the water supply W. In this example, the water supply W is preheated by the third heat exchange section 6-3 included in the heat exchanger 22.

この熱源機20には破線で示すように、熱源機筐体として角筒状のカバー部26−1が備えられ、この本体カバー部26−1の上部に上側カバー部26−2が備えられる。熱交換器22には、第一筐体部28−1、第二筐体部28−2および第三筐体部28−3が備えられる。第一筐体部28−1は既述の筐体4の一例である。 As shown by the broken line, the heat source machine 20 is provided with a square tubular cover portion 26-1 as a heat source machine housing, and an upper cover portion 26-2 is provided above the main body cover portion 26-1. The heat exchanger 22 is provided with a first housing portion 28-1, a second housing portion 28-2, and a third housing portion 28-3. The first housing portion 28-1 is an example of the housing 4 described above.

この第一筐体部28−1の下側にはファン30が設置され、このファン30はファンモータ32によって回転し、燃焼用空気を第一筐体部28−1内に通流させる。この第一筐体部28−1の上側には第二筐体部28−2が設置され、この第二筐体部28−2には既述の第一熱交換部6−1が設置される。この第二筐体部28−2の上側には第三筐体部28−3が設置されている。この第三筐体部28−3には第二熱交換部6−2および第三熱交換部6−3が設置される。第三筐体部28−3の前面側に排気筒部34が備えられ、熱交換後の燃焼排気EGが外気に放出される。 A fan 30 is installed under the first housing portion 28-1, and the fan 30 is rotated by a fan motor 32 to allow combustion air to flow into the first housing portion 28-1. The second housing portion 28-2 is installed on the upper side of the first housing portion 28-1, and the first heat exchange portion 6-1 described above is installed on the second housing portion 28-2. To. A third housing portion 28-3 is installed above the second housing portion 28-2. A second heat exchange unit 6-2 and a third heat exchange unit 6-3 are installed in the third housing unit 28-3. An exhaust pipe portion 34 is provided on the front side of the third housing portion 28-3, and the combustion exhaust EG after heat exchange is released to the outside air.

図4のAは、図3のIVA −IVA 線断面から熱源機20の排気筒部34を省略して示している。この熱源機20では、筐体4の底部に設置されたバーナー8に対し、燃料ガスGの混合気噴出部36が備えられる。この混合気噴出部36の混合気噴出ノズル38−1、38−2より、混合気がバーナー8の混合気導入部40−1、40−2に導入される。バーナー8の上側にはイグナイタ42およびフレームロッド44が備えられ、イグナイタ42は、バーナー8から噴き出される混合気に着火する。 FIG. 4A shows the exhaust stack portion 34 of the heat source machine 20 omitted from the IVA-IVA line cross section of FIG. In the heat source machine 20, the fuel gas G air-fuel mixture ejection portion 36 is provided with respect to the burner 8 installed at the bottom of the housing 4. The air-fuel mixture is introduced into the air-fuel mixture introduction parts 40-1 and 40-2 of the burner 8 from the air-fuel mixture ejection nozzles 38-1 and 38-2 of the air-fuel mixture ejection portion 36. An igniter 42 and a frame rod 44 are provided on the upper side of the burner 8, and the igniter 42 ignites the air-fuel mixture ejected from the burner 8.

バーナー8の上側には空間部46を介在して第一熱交換部6−1の複数の熱媒熱交換パイプ12−1および浴槽水熱交換パイプ14が併設されるとともに、複数の吸熱フィン48が設置されている。熱媒熱交換パイプ12−1および浴槽水熱交換パイプ14は、燃焼排気EGの流れ方向と交差方向に設置されているのに対し、各吸熱フィン48は燃焼排気EGの流れ方向と平行方向に設置されている。熱媒熱交換パイプ12−1および浴槽水熱交換パイプ14は、燃焼排気EGから吸熱する吸熱管であり、吸熱フィン48は燃焼排気EGから吸熱し、熱媒熱交換パイプ12−1および浴槽水熱交換パイプ14に伝導させる吸熱部材および熱伝導部材を構成する。図4のBは図4のAのIVB −IVB 線断面を示している。 A plurality of heat medium heat exchange pipes 12-1 and bath water heat exchange pipes 14 of the first heat exchange section 6-1 are provided on the upper side of the burner 8 with a space portion 46 interposed therebetween, and a plurality of endothermic fins 48. Is installed. The heat medium heat exchange pipe 12-1 and the bath water heat exchange pipe 14 are installed in a direction intersecting the flow direction of the combustion exhaust EG, whereas each endothermic fin 48 is in a direction parallel to the flow direction of the combustion exhaust EG. is set up. The heat medium heat exchange pipe 12-1 and the bath water heat exchange pipe 14 are heat absorbing tubes that absorb heat from the combustion exhaust EG, and the heat absorbing fins 48 absorb heat from the combustion exhaust EG, and the heat medium heat exchange pipe 12-1 and the bath water. It constitutes a heat absorbing member and a heat conducting member that conduct heat to the heat exchange pipe 14. B in FIG. 4 shows the IVB-IVB line cross section of A in FIG.

この例では、複数の熱媒熱交換パイプ12−1の二段のパイプ列を図中X軸方向に配列させ、熱媒熱交換パイプ12−1のパイプ列間にX軸方向に向かって浴槽水熱交換パイプ14のパイプ列が配置されている。つまり、Y軸方向における、熱媒熱交換パイプ12−1の間に浴槽水熱交換パイプ14が挟持されており、熱媒熱交換パイプ12−1および浴槽水熱交換パイプ14のパイプ壁面を密着させ、両者間の熱伝導を可能にしている。そして、これら熱媒熱交換パイプ12−1および浴槽水熱交換パイプ14は吸熱フィン48と一体化されており、X軸方向およびY軸方向の熱伝導が可能となっている。 In this example, a two-stage pipe row of a plurality of heat medium heat exchange pipes 12-1 is arranged in the X-axis direction in the drawing, and a bathtub is provided between the pipe rows of the heat medium heat exchange pipes 12-1 in the X-axis direction. A row of pipes of the water heat exchange pipe 14 is arranged. That is, the bath water heat exchange pipe 14 is sandwiched between the heat medium heat exchange pipes 12-1 in the Y-axis direction, and the pipe wall surfaces of the heat medium heat exchange pipe 12-1 and the bath water heat exchange pipe 14 are in close contact with each other. It enables heat conduction between the two. The heat medium heat exchange pipe 12-1 and the bath water heat exchange pipe 14 are integrated with the heat absorbing fins 48, and heat conduction in the X-axis direction and the Y-axis direction is possible.

第二筐体部28−2の天井部と第三筐体部28−3の底部との間には傾斜板50が設置されており、第三筐体部28−3の底面板52を傾斜させている。この例では、底面板52が図中左側に傾斜板50の持つ傾斜角度θに応じて傾斜している。この傾斜角度θの設定は、熱交換で生じたドレンDを底面板52に沿って流し、ドレン受け54に導入できる程度の角度であればよい。 An inclined plate 50 is installed between the ceiling portion of the second housing portion 28-2 and the bottom portion of the third housing portion 28-3, and the bottom plate 52 of the third housing portion 28-3 is inclined. I'm letting you. In this example, the bottom plate 52 is inclined to the left side in the drawing according to the inclination angle θ of the inclined plate 50. The inclination angle θ may be set so as to allow the drain D generated by heat exchange to flow along the bottom plate 52 and be introduced into the drain receiver 54.

傾斜板50および底面板52には通気窓部56が備えられる。この通気窓部56を通して、燃焼排気EGが第二筐体部28−2から第三筐体部28−3に導かれる。この通気窓部56には、燃焼排気EGを通過させ、ドレンDの第二筐体部28−2側への落下を回避するため、遮蔽板58が備えられている。このような遮蔽板58を備えれば、第三筐体部28−3側でドレンDが生じたとしても、このドレンDの第二筐体部28−2側への落下を防止できる。 The inclined plate 50 and the bottom plate 52 are provided with a ventilation window portion 56. The combustion exhaust EG is guided from the second housing portion 28-2 to the third housing portion 28-3 through the ventilation window portion 56. The ventilation window portion 56 is provided with a shielding plate 58 in order to allow the combustion exhaust EG to pass through and prevent the drain D from falling to the second housing portion 28-2 side. If such a shielding plate 58 is provided, even if a drain D occurs on the third housing portion 28-3 side, it is possible to prevent the drain D from falling to the second housing portion 28-2 side.

第三筐体部28−3には第二熱交換部6−2の熱媒熱交換パイプ12−2、第三熱交換部6−3の給水熱交換パイプ16が設置されている。この第三筐体部28−3には、第二筐体部28−2の側面側に突出したドレン受け54が備えられる。このドレン受け54は第三筐体部28−3を形成する金属材料によって第三筐体部28−3と一体にたとえば、プレス加工によって形成すればよい。傾斜板50に沿って流動したドレンDは、ドレン受け54に集められて溜められる。 The heat medium heat exchange pipe 12-2 of the second heat exchange unit 6-2 and the water supply heat exchange pipe 16 of the third heat exchange unit 6-3 are installed in the third housing portion 28-3. The third housing portion 28-3 is provided with a drain receiver 54 projecting from the side surface side of the second housing portion 28-2. The drain receiver 54 may be formed integrally with the third housing portion 28-3 by, for example, press working, with the metal material forming the third housing portion 28-3. The drain D that has flowed along the inclined plate 50 is collected and stored in the drain receiver 54.

図5は、熱交換器22を排気部側から示している。第一熱交換部6−1の熱媒熱交換パイプ12−1には熱媒管路66を介して第二熱交換部6−2の熱媒熱交換パイプ12−2が接続されている。熱媒熱交換パイプ12−1の出側ポート64−2には加熱後の高温の熱媒Mが取り出される。 FIG. 5 shows the heat exchanger 22 from the exhaust unit side. The heat medium heat exchange pipe 12-2 of the second heat exchange unit 6-2 is connected to the heat medium heat exchange pipe 12-1 of the first heat exchange unit 6-1 via a heat medium pipe line 66. The high-temperature heat medium M after heating is taken out from the outlet port 64-2 of the heat medium heat exchange pipe 12-1.

浴槽水熱交換パイプ14の入側ポート68−1(図6)に流入させた浴槽水BWが加熱された後、出側ポート68−2から浴槽に戻される。 After the bathtub water BW flowing into the inlet side port 68-1 (FIG. 6) of the bathtub water heat exchange pipe 14 is heated, it is returned to the bathtub from the outlet side port 68-2.

給水熱交換パイプ16の入側ポート70−1に流入させた給水Wが加熱された後、出側ポート70−2からプレート熱交換器24に循環される。 After the water supply W flowing into the inlet port 70-1 of the water supply heat exchange pipe 16 is heated, it is circulated from the outlet port 70-2 to the plate heat exchanger 24.

第三筐体部28−3の前面側には排気口部72が備えられ、この排気口部72には既述の排気筒部34(図3)が取り付けられる。 An exhaust port portion 72 is provided on the front surface side of the third housing portion 28-3, and the exhaust pipe portion 34 (FIG. 3) described above is attached to the exhaust port portion 72.

図6は、熱交換器22の背面側から示している。熱媒熱交換パイプ12−2の入側ポート74−1には暖房負荷などを循環したたとえば、放熱後の低温の熱媒Mが流入し、この熱媒熱交換パイプ12−2の出側ポート74−2には熱媒管路66が接続されており、この熱媒管路66から加熱した熱媒Mが分配弁62の入側ポート64−1に流れる(図5)。 FIG. 6 is shown from the back side of the heat exchanger 22. For example, a low-temperature heat medium M after heat dissipation flows into the inlet port 74-1 of the heat medium heat exchange pipe 12-2, and a heating load or the like is circulated, and the outlet port of the heat medium heat exchange pipe 12-2. A heat medium line 66 is connected to 74-2, and the heat medium M heated from the heat medium line 66 flows to the inlet port 64-1 of the distribution valve 62 (FIG. 5).

<実施例1の効果> <Effect of Example 1>

この実施例1によれば、次のような効果が得られる。 According to the first embodiment, the following effects can be obtained.

(1) この実施例1によれば、既述した一実施の形態と同様の効果が得られる。 (1) According to the first embodiment, the same effect as that of the above-described embodiment can be obtained.

(2) 熱媒熱交換パイプ12−1のパイプ列との間に浴槽水熱交換パイプ14が挟み込まれて密着しているので、両者間の熱伝導が良好となり、熱の回収率が高められる。 (2) Since the bath water heat exchange pipe 14 is sandwiched and adhered to the pipe row of the heat medium heat exchange pipe 12-1, the heat conduction between the two is improved and the heat recovery rate is improved. ..

(3) 熱媒熱交換パイプ12−1のパイプ列との間に浴槽水熱交換パイプ14が挟み込まれて密着しているので、第一熱交換部6−1のコンパクト化を図ることができる。
(3) Since the bathtub water heat exchange pipe 14 is sandwiched and adhered to the pipe row of the heat medium heat exchange pipe 12-1, the first heat exchange section 6-1 can be made compact. ..

図7は、実施例2に係る熱源機の一例として給湯・追焚き・暖房装置80を示している。この給湯・追焚き・暖房装置80において、図3と同一部分には同一符号を付してある。この給湯・追焚き・暖房装置80では、本発明の熱交換器を用いて、給湯機能、暖房機能および追焚機能を実現している。 FIG. 7 shows a hot water supply / reheating / heating device 80 as an example of the heat source machine according to the second embodiment. In the hot water supply / reheating / heating device 80, the same parts as those in FIG. 3 are designated by the same reference numerals. In this hot water supply / reheating / heating device 80, the hot water supply function, the heating function, and the reheating function are realized by using the heat exchanger of the present invention.

この給湯・追焚き・暖房装置80は装置筐体82を備え、この装置筐体82が家屋の壁部材などに取り付けられる。 The hot water supply / reheating / heating device 80 includes a device housing 82, and the device housing 82 is attached to a wall member or the like of a house.

この給湯・追焚き・暖房装置80には熱交換器22、プレート熱交換器24、熱媒タンク84、熱媒Mの循環路88−1、88−2、浴槽水BWの循環路88−3、給水路88−4および給湯路88−5などが備えられる。熱交換器22では、浴槽水BWの加熱および給水Wの予備加熱を行い、プレート熱交換器24は予備加熱後の給水Wの給湯加熱を行う。 The hot water supply / reheating / heating device 80 includes a heat exchanger 22, a plate heat exchanger 24, a heat medium tank 84, circulation paths 88-1 and 88-2 of the heat medium M, and circulation paths 88-3 of the bath water BW. , Water supply channel 88-4, hot water supply channel 88-5, and the like are provided. The heat exchanger 22 heats the bathtub water BW and preheats the water supply W, and the plate heat exchanger 24 heats the water supply W after the preheating.

熱媒タンク84は、循環路88−1、88−2を循環する熱媒Mが溜められる。循環路88−1は、循環ポンプ90−1を備えて高温の熱媒Mを高温暖房負荷92−1に循環させる。この循環路88−1には分岐部94−1が設けられ、この分岐部94−1から循環路88−13を通して低温の熱媒Mを低温暖房負荷92−2に循環させる。この循環路88−1には熱交換器22の第一熱交換部6−1の熱媒熱交換パイプ12−1、第二熱交換部6−2の熱媒熱交換パイプ12−2、熱媒タンク84とともに、高温暖房負荷92−1または低温暖房負荷92−2が含まれる。 The heat medium tank 84 stores the heat medium M that circulates in the circulation paths 88-1 and 88-2. The circulation path 88-1 includes a circulation pump 90-1 to circulate the high-temperature heat medium M to the high-temperature heating load 92-1. A branching portion 94-1 is provided in the circulation passage 88-1, and a low-temperature heat medium M is circulated from the branching portion 94-1 through the circulation passage 88-13 to the low-temperature heating load 92-2. In this circulation path 88-1, the heat medium heat exchange pipe 12-1 of the first heat exchange section 6-1 of the heat exchanger 22, the heat medium heat exchange pipe 12-2 of the second heat exchange section 6-2, and heat Along with the medium tank 84, a high temperature heating load 92-1 or a low temperature heating load 92-2 is included.

循環路88−2は装置筐体82内に配置されて循環路88−1の一部から高温暖房負荷92−1および低温暖房負荷92−2側の循環路をバイパスして熱媒Mを循環させる。したがって、この循環路88−2には熱交換器22の第一熱交換部6−1の熱媒熱交換パイプ12−1、第二熱交換部6−2の熱媒熱交換パイプ12−2および熱媒タンク84が含まれる。 The circulation path 88-2 is arranged in the apparatus housing 82 and circulates the heat medium M from a part of the circulation path 88-1 by bypassing the circulation path on the high temperature heating load 92-1 and the low temperature heating load 92-2 side. Let me. Therefore, in this circulation path 88-2, the heat medium heat exchange pipe 12-1 of the first heat exchange section 6-1 of the heat exchanger 22 and the heat medium heat exchange pipe 12-2 of the second heat exchange section 6-2 And the heat medium tank 84 is included.

この実施例では、熱媒熱交換パイプ12−1に循環路88−11を形成し、この循環路88−11に熱媒熱交換パイプ12−2が接続されている。循環路88−11には温度センサ98−1、分配弁96−1および混合弁96−2が備えられている。分配弁96−1から循環路88−12を介して高温の熱媒Mがプレート熱交換器24に循環し、熱媒タンク84に帰還する。温度センサ98−1では、熱媒熱交換パイプ12−1の出口側の熱媒Mの温度が検出される。また、混合弁96−2から循環路88−13を介して低温の熱媒Mが低温暖房負荷92−2に循環し、熱媒タンク84に帰還する。分配弁96−1と混合弁96−2の間の循環路88−11に分岐部94−2が形成されている。この分岐部94−2から高温の熱媒Mが循環路88−14により高温暖房負荷92−1に循環する。 In this embodiment, a circulation path 88-11 is formed in the heat medium heat exchange pipe 12-1, and the heat medium heat exchange pipe 12-2 is connected to the circulation path 88-11. The circulation path 88-11 is provided with a temperature sensor 98-1, a distribution valve 96-1 and a mixing valve 96-2. The high-temperature heat medium M circulates from the distribution valve 96-1 through the circulation path 88-12 to the plate heat exchanger 24 and returns to the heat medium tank 84. The temperature sensor 98-1 detects the temperature of the heat medium M on the outlet side of the heat medium heat exchange pipe 12-1. Further, the low-temperature heat medium M circulates from the mixing valve 96-2 through the circulation path 88-13 to the low-temperature heating load 92-2 and returns to the heat medium tank 84. A branch 94-2 is formed in the circulation path 88-11 between the distribution valve 96-1 and the mixing valve 96-2. A high-temperature heat medium M circulates from the branch portion 94-2 to the high-temperature heating load 92-1 through the circulation path 88-14.

浴槽水循環路88−3には往き管88−31および戻り管88−32が備えられ、循環ポンプ90−2の駆動により、浴槽89の浴槽水BWを第一熱交換部6−1の浴槽水熱交換パイプ14に循環させる。 The bathtub water circulation path 88-3 is provided with an forward pipe 88-31 and a return pipe 88-32, and the bathtub water BW of the bathtub 89 is converted into the bathtub water of the first heat exchange section 6-1 by driving the circulation pump 90-2. It is circulated in the heat exchange pipe 14.

給水路88−4には第三熱交換部6−3の給水熱交換パイプ16が接続され、予備加熱された給水Wが管路88−41を通してプレート熱交換器24に通流し、このプレート熱交換器24で熱媒Mと熱交換の後、給湯路88−5から出湯する。給水路88−4と給湯路88−5の間にはバイパス路88−6が混合弁96−3を介して分岐されている。この混合弁96−3の開度により給水Wが温水HWに混合される。給水Wの温度は温度センサ98−2により検出され、プレート熱交換器24の出側温度は温度センサ98−3により検出され、出湯温度は温度センサ98−4により検出される。給水Wの給水量は給水量センサ98−5で検出される。給湯を開始する際、給水量、給水温度、熱交換直後の温水温度を参照し、給湯を開始した後は、出湯温度を参照し、混合弁96−3が制御され、熱交換直後の温水HWに給水Wの混合比率が調整される。これにより、設定温度に制御された温水HWを出湯することができる。 The water supply heat exchange pipe 16 of the third heat exchange section 6-3 is connected to the water supply channel 88-4, and the preheated water supply W flows through the pipeline 88-41 to the plate heat exchanger 24, and the plate heat is generated. After exchanging heat with the heat medium M in the exchanger 24, hot water is discharged from the hot water supply passage 88-5. A bypass passage 88-6 is branched between the water supply passage 88-4 and the hot water supply passage 88-5 via a mixing valve 96-3. The water supply W is mixed with the hot water HW by the opening degree of the mixing valve 96-3. The temperature of the water supply W is detected by the temperature sensor 98-2, the outlet temperature of the plate heat exchanger 24 is detected by the temperature sensor 98-3, and the hot water temperature is detected by the temperature sensor 98-4. The amount of water supplied by the water supply W is detected by the water supply amount sensor 98-5. When starting hot water supply, refer to the amount of water supply, water supply temperature, and hot water temperature immediately after heat exchange, and after starting hot water supply, refer to the hot water discharge temperature, and the mixing valve 96-3 is controlled, and the hot water HW immediately after heat exchange. The mixing ratio of the water supply W is adjusted. As a result, hot water HW controlled to a set temperature can be discharged.

給湯路88−5には分岐部94−3を設けて給湯路88−5と循環路88−3の戻り管88−32との間に注湯管88−8が連結され、この注湯管88−8から温水HWが注湯電磁弁96−5を介して循環路88−3の戻り管88−32に注湯される。つまり、浴槽注湯時、注湯電磁弁96−5が開かれ、熱媒Mで加熱された温水HWが浴槽89に注湯される。この温水HWの注湯量は注湯量センサ98−6で検出される。 A branch portion 94-3 is provided in the hot water supply passage 88-5, and a hot water injection pipe 88-8 is connected between the hot water supply passage 88-5 and the return pipe 88-32 of the circulation passage 88-3. From 88-8, hot water HW is poured into the return pipe 88-32 of the circulation path 88-3 via the hot water pouring solenoid valve 96-5. That is, at the time of pouring the bathtub, the pouring solenoid valve 96-5 is opened, and the hot water HW heated by the heat medium M is poured into the bathtub 89. The pouring amount of this hot water HW is detected by the pouring amount sensor 98-6.

バーナー8には燃料ガスGが燃料供給管43から供給される。このバーナー8に対する燃料ガスGの供給や供給量が燃料制御弁96−4により制御される。 Fuel gas G is supplied to the burner 8 from the fuel supply pipe 43. The supply and amount of fuel gas G to the burner 8 are controlled by the fuel control valve 96-4.

第二熱交換部6−2や第三熱交換部6−3で生じたドレンDはドレン受け54で受け、ドレンパイプ88−7を通してドレンタンク97に導かれて溜められ、その貯留量に応じて排出管88−9から放出される。 The drain D generated in the second heat exchange section 6-2 and the third heat exchange section 6-3 is received by the drain receiver 54, guided to the drain tank 97 through the drain pipe 88-7, and stored according to the stored amount. Is discharged from the discharge pipe 88-9.

電装基板100が備えられ、この電装基板100には商用交流電源を電源部102で受け、電源出力が供給される。この電装基板100には給湯・追焚き・暖房制御部104(図8)が備えられ、リモコン装置106−1、106−2、106−3が接続されている。 An electrical board 100 is provided, and the electrical board 100 receives a commercial AC power supply at the power supply unit 102, and a power output is supplied to the electrical board 100. The electrical board 100 is provided with a hot water supply / reheating / heating control unit 104 (FIG. 8), and remote controller devices 106-1, 106-2, and 106-3 are connected to the electrical board 100.

<制御系統> <Control system>

図8は、給湯・追焚き・暖房制御部104の一例を示している。図8に示す構成では、実施の形態としての機能を説明するために必要な機能部を記載しており、斯かる機能部に限定されるものではない。 FIG. 8 shows an example of the hot water supply / reheating / heating control unit 104. In the configuration shown in FIG. 8, a functional unit necessary for explaining the function as the embodiment is described, and the present invention is not limited to such a functional unit.

給湯・追焚き・暖房制御部104やリモコン装置106−1、106−2、106−3は、コンピュータで構成され、情報処理によって後述の制御態様を実現している。プロセッサ108ではメモリ部110にあるプログラムを実行し、給湯・追焚き・暖房の制御に必要な情報処理や、データの記憶などを実行する。 The hot water supply / reheating / heating control unit 104 and the remote controller devices 106-1, 106-2, 106-3 are composed of a computer, and realize the control mode described later by information processing. The processor 108 executes a program in the memory unit 110 to execute information processing and data storage necessary for controlling hot water supply, reheating, and heating.

メモリ部110にはROM(Read-Only Memory)、RAM(Random-Access Memory)などの記録媒体を備え、制御に必要な情報処理を実行するためのプログラムが格納される。ROMの他、EEPROM(Electrically Erasable Programmable Read-Only Memory )などの不揮発性記録媒体を用いてもよい。RAMは情報処理のワークエリアを構成している。 The memory unit 110 includes a recording medium such as a ROM (Read-Only Memory) and a RAM (Random-Access Memory), and stores a program for executing information processing necessary for control. In addition to ROM, a non-volatile recording medium such as EEPROM (Electrically Erasable Programmable Read-Only Memory) may be used. RAM constitutes an information processing work area.

システム通信部112はプロセッサ108によって制御され、有線または無線によってリモコン装置106−1、106−2、106−3と連係し、これらとの情報の授受を実行する。 The system communication unit 112 is controlled by the processor 108, cooperates with the remote controller devices 106-1, 106-2, and 106-3 by wire or wirelessly, and executes information exchange with these remote controllers 106-1, 106-2, and 106-3.

入出力部(I/O)114は、プロセッサ108の情報処理に供する入力情報や、処理結果である制御出力を取り出す。このI/O114には循環ポンプ90−1、90−2、分配弁96−1、混合弁96−2、96−3、温度センサ98−1、98−2、98−3、98−4、給水量センサ98−5、燃料制御弁96−4、注湯電磁弁96−5などが接続されている。 The input / output unit (I / O) 114 takes out input information to be used for information processing of the processor 108 and control output which is a processing result. The I / O 114 includes circulation pumps 90-1, 90-2, distribution valve 96-1, mixing valves 96-2, 96-3, temperature sensors 98-1, 98-2, 98-3, 98-4, A water supply amount sensor 98-5, a fuel control valve 96-4, a hot water pouring solenoid valve 96-5, and the like are connected.

<給湯・追焚き・暖房装置80の駆動制御> <Drive control of hot water supply / reheating / heating device 80>

給湯・追焚き・暖房装置80には、給湯運転、追焚き運転、暖房運転などが含まれ、これらの運転にはポンプ回転数制御、バーナー燃焼制御、給湯制御、浴槽注湯制御などが含まれる。 The hot water supply / reheating / heating device 80 includes hot water supply operation, reheating operation, heating operation, etc., and these operations include pump rotation speed control, burner combustion control, hot water supply control, bath water pouring control, and the like. ..

図9および図10は、給湯・追焚き・暖房装置80の駆動制御の処理手順の一例を示している。図9および図10において、共通符号a、bはフローチャート間の連結子を示している。 9 and 10 show an example of a processing procedure for driving control of the hot water supply / reheating / heating device 80. In FIGS. 9 and 10, common reference numerals a and b indicate connectors between flowcharts.

この処理手順では、いずれかの機能がON状態か否かを判定する。いずれの機能もON状態でなければ(S101のNO)、待機状態を維持する。 In this processing procedure, it is determined whether or not any of the functions is in the ON state. If none of the functions is in the ON state (NO in S101), the standby state is maintained.

いずれかの機能がON状態であれば(S101のYES)、追焚き単独運転であるかを判定する(S102)。追焚き単独運転であれば(S102のYES)、循環ポンプ90−1の回転数制御として、追焚きに必要な所定回転数で循環ポンプ90−1を駆動し(S103)、S107に移行する。 If any of the functions is in the ON state (YES in S101), it is determined whether the reheating independent operation is performed (S102). If the reheating alone operation is performed (YES in S102), the circulation pump 90-1 is driven at a predetermined rotation speed required for reheating as the rotation speed control of the circulation pump 90-1 (S103), and the process proceeds to S107.

いずれかの機能がON状態であっても(S101のYES)、追焚き単独運転でなければ(S102のNO)、給湯単独運転または、給湯および追焚き運転かを判定する(S104)。給湯単独運転または、給湯および追焚き運転であれば(S104のYES)、必要号数に見合った所定温度たとえば、80〔℃〕の熱媒Mの流量を確保する回転数に循環ポンプ90−1を駆動し(S105)、S107に移行する。 Even if any of the functions is in the ON state (YES in S101), if it is not the reheating independent operation (NO in S102), it is determined whether the hot water supply alone operation or the hot water supply and reheating operation is performed (S104). In the case of hot water supply independent operation or hot water supply and reheating operation (YES in S104), the circulation pump 90-1 is set to a rotation speed that secures the flow rate of the heat medium M at a predetermined temperature, for example, 80 [° C.], which matches the required number. (S105) and shift to S107.

給湯単独運転または、給湯および追焚き運転でなければ(S104のNO)、使用する機能の組合せに応じた回転数に循環ポンプ90−1を駆動し(S106)、S107に移行する。 Unless it is a hot water supply independent operation or a hot water supply and reheating operation (NO in S104), the circulation pump 90-1 is driven to a rotation speed according to the combination of functions to be used (S106), and the process proceeds to S107.

S107では、温度センサ98−1による熱媒Mの検出温度が所定温度たとえば、80〔℃〕にバーナー8の燃焼制御を行う。 In S107, the combustion control of the burner 8 is performed so that the temperature detected by the heat medium M by the temperature sensor 98-1 is a predetermined temperature, for example, 80 [° C.].

浴槽注湯または給湯では、S107の後、浴槽注湯または給湯ありかを判定する(S108)。浴槽注湯または給湯ありの場合には(S108のYES)、浴槽注湯単独かを判定する(S109)。浴槽注湯単独であれば(S109のYES)、温度センサ98−4の検出温度がたとえば、浴槽設定温度−追焚き熱交換での加熱量になるように混合弁96−3の制御を行い(S110)、S114に移行する。 In the bathtub pouring or hot water supply, after S107, it is determined whether or not there is bathtub pouring or hot water supply (S108). When there is bathtub pouring or hot water supply (YES in S108), it is determined whether bathtub pouring alone or not (S109). If the bathtub pouring alone is used (YES in S109), the mixing valve 96-3 is controlled so that the detection temperature of the temperature sensor 98-4 is, for example, the set temperature of the bathtub-the amount of heat generated by the reheating heat exchange (YES in S109). S110), shift to S114.

S109において、浴槽注湯の単独でなければ(S109のNO)、給湯単独かを判定する(S111)。給湯単独であれば(S111のYES)、出湯温度が給湯設定温度になるように、つまり、温度センサ98−4の検出温度が給湯設定温度になるように混合弁96−3の制御を行う(S112)。 In S109, if it is not the bathtub pouring alone (NO in S109), it is determined whether the hot water is supplied alone (S111). If the hot water supply is independent (YES in S111), the mixing valve 96-3 is controlled so that the hot water outlet temperature becomes the hot water supply set temperature, that is, the detection temperature of the temperature sensor 98-4 becomes the hot water supply set temperature (YES). S112).

S111において、給湯単独でなければ(S111のNO)、浴槽注湯および給湯に対応した制御を行う(S113)。 In S111, if hot water supply alone is not performed (NO in S111), control corresponding to bathtub pouring and hot water supply is performed (S113).

追焚運転(図10)では、追焚運転ありかを判定し(S114)、追焚運転であれば(S114のYES)、追焚側循環ポンプ90−2を駆動する(S115)。追焚運転でなければ(S114のNO)、追焚側循環ポンプ90−2の駆動(S115)をスキップする。 In the reheating operation (FIG. 10), it is determined whether or not there is a reheating operation (S114), and if it is a reheating operation (YES in S114), the reheating side circulation pump 90-2 is driven (S115). If it is not a reheating operation (NO in S114), the drive of the reheating side circulation pump 90-2 (S115) is skipped.

高温暖房運転では、高温暖房運転ありかを判定し(S116)、高温暖房運転であれば(S116のYES)、高温暖房運転を行う(S117)。高温暖房運転でなければ(S116のNO)、高温暖房運転(S117)をスキップする。 In the high-temperature heating operation, it is determined whether or not there is a high-temperature heating operation (S116), and if it is a high-temperature heating operation (YES in S116), the high-temperature heating operation is performed (S117). If it is not the high temperature heating operation (NO in S116), the high temperature heating operation (S117) is skipped.

低温暖房運転では、低温暖房運転ありかを判定し(S118)、低温暖房運転であれば(S118のYES)、低温暖房運転を行う(S119)。低温暖房運転でなければ(S118のNO)、低温暖房運転(S119)をスキップし、この処理を終了する。 In the low-temperature heating operation, it is determined whether or not there is a low-temperature heating operation (S118), and if it is a low-temperature heating operation (YES in S118), the low-temperature heating operation is performed (S119). If it is not the low-temperature heating operation (NO in S118), the low-temperature heating operation (S119) is skipped and this process ends.

<実施例2の効果> <Effect of Example 2>

この実施例2によれば、次のような効果が得られる。 According to the second embodiment, the following effects can be obtained.

循環ポンプ90−1の回転数制御では、ポンプ回転数に応じて熱媒Mの流量が変化する。このポンプ制御は、基本的にFF(フィードフォワード)制御であり、給湯量、高温暖房または低温暖房、さらには暖房端末の接続数に応じた回転数に制御できる。追焚単独運転では、熱媒Mの沸騰防止のために所定回転数で熱媒Mを循環させる。この場合、熱媒Mはプレート熱交換器24を経由し、循環路88−2を通して装置内循環とする。追焚単独運転でなければ、他の機能にあわせたポンプ回転数に依存させる。追焚側の循環ポンプ90−2の回転数はバーナー8の燃焼量により制御してもよい。 In the rotation speed control of the circulation pump 90-1, the flow rate of the heat medium M changes according to the rotation speed of the pump. This pump control is basically FF (feedforward) control, and can be controlled to a hot water supply amount, high temperature heating or low temperature heating, and a rotation speed according to the number of connected heating terminals. In the reheating independent operation, the heat medium M is circulated at a predetermined rotation speed in order to prevent the heat medium M from boiling. In this case, the heat medium M is circulated in the device through the circulation path 88-2 via the plate heat exchanger 24. If it is not a reheating independent operation, it depends on the pump rotation speed according to other functions. The rotation speed of the circulation pump 90-2 on the reheating side may be controlled by the amount of combustion of the burner 8.

給湯(注湯も含む)単独運転や給湯と同時に行う追焚運転では、温度センサ98−2の給水Wの検出温度、給水量センサ98−5の検出値、および給湯または注湯の設定温度により加熱に必要な燃焼号数(燃焼量)を算出し、この号数に応じて設定温度たとえば、80〔℃〕の熱媒Mの流量より循環ポンプ90−1の回転数を求め、循環ポンプ90−1の制御をする。これにより、必要以上に熱媒Mを加熱しなくてよいので、燃焼の一時停止などの不都合を防止できる。 In the hot water supply (including hot water injection) independent operation or the reheating operation performed at the same time as the hot water supply, the detection temperature of the water supply W of the temperature sensor 98-2, the detection value of the water supply amount sensor 98-5, and the set temperature of the hot water supply or the hot water injection are used. The number of combustions (combustion amount) required for heating is calculated, and the number of rotations of the circulation pump 90-1 is obtained from the flow rate of the heat medium M at a set temperature, for example, 80 [° C.] according to this number, and the circulation pump 90 Control -1. As a result, it is not necessary to heat the heat medium M more than necessary, so that inconveniences such as suspension of combustion can be prevented.

燃焼制御では、循環ポンプ90−1が駆動している間、熱媒Mが所定温度たとえば、80〔℃〕になるようにバーナー8の燃焼量を制御する。この場合、ポンプ駆動を制御条件とすればよく、熱媒回路内に流量センサを必要としない。 In the combustion control, the combustion amount of the burner 8 is controlled so that the heat medium M reaches a predetermined temperature, for example, 80 [° C.] while the circulation pump 90-1 is being driven. In this case, the pump drive may be a control condition, and a flow rate sensor is not required in the heat medium circuit.

熱交換器22を流れる熱媒Mの流量にかかわらず、温度センサ98−1の検出温度が所定温度たとえば、80〔℃〕になるようにガス量を調整すればよい。この場合、熱媒タンク84の出側温度が熱媒Mの所定温度に近ければ、バーナー燃焼を停止してもよい。 Regardless of the flow rate of the heat medium M flowing through the heat exchanger 22, the amount of gas may be adjusted so that the detection temperature of the temperature sensor 98-1 becomes a predetermined temperature, for example, 80 [° C.]. In this case, if the temperature on the outlet side of the heat medium tank 84 is close to the predetermined temperature of the heat medium M, the burner combustion may be stopped.

浴槽注湯または給湯では、給湯の有無を給水量センサ98−5により検出することができる。浴槽注湯が単独であるか否かは、給水量センサ98−5と、注湯量センサ98−6との検出値を比較して判断すればよい。この検出値に差があれば給湯と注湯の同時使用であることが判る。 In bathtub pouring or hot water supply, the presence or absence of hot water supply can be detected by the water supply amount sensor 98-5. Whether or not the bathtub pouring is independent may be determined by comparing the detected values of the water supply amount sensor 98-5 and the pouring amount sensor 98-6. If there is a difference in this detected value, it can be seen that hot water supply and hot water pouring are used at the same time.

注湯単独では、温度センサ98−4で温度を検出された温水HWが注湯管88−8から循環路88−3に流れ、往き管88−31および戻り管88−32により浴槽89に注湯される。この場合、往き管88−31を経由する際、浴槽水熱交換パイプ14で加熱されるので、この加熱分を考慮し、温度センサ98−4の検出温度を参照し、浴槽89の設定湯温より低い所定温度になるように混合弁96−3を制御する。 In the pouring alone, the hot water HW whose temperature was detected by the temperature sensor 98-4 flows from the pouring pipe 88-8 to the circulation path 88-3, and is poured into the bathtub 89 by the outbound pipe 88-31 and the return pipe 88-32. It is hot water. In this case, when passing through the going pipe 88-31, it is heated by the bathtub water heat exchange pipe 14, so in consideration of this heating amount, refer to the detection temperature of the temperature sensor 98-4, and set the hot water temperature of the bathtub 89. The mixing valve 96-3 is controlled so as to have a lower predetermined temperature.

給湯単独では、温度センサ98−4の検出温度を監視し、出湯温度が給湯設定温度になるように混合弁96−3を制御する。 In the hot water supply alone, the detection temperature of the temperature sensor 98-4 is monitored, and the mixing valve 96-3 is controlled so that the hot water discharge temperature becomes the hot water supply set temperature.

注湯および給湯を同時に生じる場合には、同時使用に対応した制御を行い、少なくとも温度センサ98−4の検出温度を監視し、温水HWに必要な温度が得られるように混合弁96−3を制御すればよい。 When hot water pouring and hot water supply occur at the same time, control for simultaneous use is performed, at least the detection temperature of the temperature sensor 98-4 is monitored, and the mixing valve 96-3 is used so that the temperature required for the hot water HW can be obtained. You just have to control it.

追焚運転では、追焚側の循環ポンプ90−2を駆動するとともに循環ポンプ90−1を駆動し熱媒熱交換パイプ12−1の熱媒Mが高温にならないように制御することができる。 In the reheating operation, the circulation pump 90-2 on the reheating side is driven and the circulation pump 90-1 is driven so that the heat medium M of the heat medium heat exchange pipe 12-1 can be controlled so as not to become hot.

高温暖房運転では、分配弁96−1を制御し、高温暖房負荷92−1に高温の熱媒Mを循環させることができる。 In the high-temperature heating operation, the distribution valve 96-1 can be controlled to circulate the high-temperature heat medium M through the high-temperature heating load 92-1.

低温暖房運転では、混合弁96−2を制御して低温暖房負荷92−2に循環する熱媒Mの温度を適正値に制御することができる。 In the low-temperature heating operation, the mixing valve 96-2 can be controlled to control the temperature of the heat medium M circulating in the low-temperature heating load 92-2 to an appropriate value.

〔他の実施の形態〕 [Other Embodiments]

A)上記実施の形態または実施例1、2では、第二熱交換部6−2側に第三熱交換部6−3の給水熱交換パイプ16を張り出させて配置した例を示したが、図11に示すように、第一熱交換部6−1を通過した燃焼排気EGから顕熱を回収する熱媒熱交換パイプ12−2のみを第二熱交換部6−2に設置し、第三熱交換部6−3に給水熱交換パイプ16のみを設置してもよい。斯かる構成によっても熱交換効率を高めることができる。 A) In the above-described embodiment or Examples 1 and 2, an example is shown in which the water supply heat exchange pipe 16 of the third heat exchange unit 6-3 is arranged so as to project on the second heat exchange unit 6-2 side. As shown in FIG. 11, only the heat medium heat exchange pipe 12-2 that recovers the apparent heat from the combustion exhaust EG that has passed through the first heat exchange section 6-1 is installed in the second heat exchange section 6-2. Only the water supply heat exchange pipe 16 may be installed in the third heat exchange section 6-3. The heat exchange efficiency can also be improved by such a configuration.

B)上記実施の形態では、熱源機として給湯器を例示して説明したが、本発明は給湯器に限定されるものではない。給排気を伴うガス燃焼の他、液体燃料の燃焼制御についても本発明は同様に適用できる。 B) In the above embodiment, the water heater has been illustrated as a heat source machine, but the present invention is not limited to the water heater. In addition to gas combustion accompanied by air supply and exhaust, the present invention can be similarly applied to combustion control of liquid fuel.

C)上記実施の形態において、第二熱交換部6−2および第三熱交換部6−3を単一の熱交換ユニットとして独立した構成とし、この熱交換ユニットを第一筐体部28−1と着脱可能に構成してもよい。 C) In the above embodiment, the second heat exchange unit 6-2 and the third heat exchange unit 6-3 are independently configured as a single heat exchange unit, and this heat exchange unit is used as the first housing unit 28-. It may be configured to be detachable from 1.

D)第二熱交換部側に燃焼排気EGを第三熱交換部6−3に先行的に流す通気部を備えてもよい。 D) A ventilation unit may be provided on the side of the second heat exchange unit to allow the combustion exhaust EG to flow in advance to the third heat exchange unit 6-3.

以上説明したように、本発明の技術の最も好ましい実施の形態等について説明した。本発明は、上記記載に限定されるものではない。特許請求の範囲に記載され、または発明を実施するための形態に開示された発明の要旨に基づき、当業者において様々な変形や変更が可能である。斯かる変形や変更が、本発明の範囲に含まれることは言うまでもない。
As described above, the most preferable embodiment of the technique of the present invention has been described. The present invention is not limited to the above description. Various modifications and modifications can be made by those skilled in the art based on the gist of the invention described in the claims or disclosed in the form for carrying out the invention. Needless to say, such modifications and modifications are included in the scope of the present invention.

本発明によれば、たとえば、熱媒を暖房および給湯の熱源に利用し、一次熱交換で浴槽水を加熱する一缶三水型熱源機などに利用でき、燃焼排気の熱を熱媒などの熱交換に利用し、熱交換効率を高めることができる。
According to the present invention, for example, a heat medium can be used as a heat source for heating and hot water supply, and can be used for a one-can, three-water type heat source machine that heats bath water by primary heat exchange, and the heat of combustion exhaust can be used as a heat medium or the like. It can be used for heat exchange to improve heat exchange efficiency.

2 熱交換器
4 筐体
6−1 第一熱交換部
6−2 第二熱交換部
6−3 第三熱交換部
8 バーナー
10 排気部
12−1 熱媒熱交換パイプ
12−2 熱媒熱交換パイプ
14 浴槽水熱交換パイプ
16 給水熱交換パイプ
20 熱源機
22 熱交換器
24 プレート熱交換器(第四熱交換部)
26 本体ケース部
26−1 本体カバー部
26−2 上側カバー部
28−1 第一筐体部
28−2 第二筐体部
28−3 第三筐体部
30 ファン
32 ファンモータ
34 排気筒部
36 混合気噴出部
38−1、38−2 混合気噴出ノズル
40−1、40−2 混合気導入部
42 イグナイタ
43 燃料供給管
44 フレームロッド
46 空間部
48 吸熱フィン
50 傾斜板
52 底面板
54 ドレン受け
56 通気窓部
58 遮蔽板
62 分配弁
64−1 入側ポート
64−2 出側ポート
66 熱媒管路
68−1 入側ポート
68−2 出側ポート
70−1 入側ポート
70−2 出側ポート
72 排気口部
74−1 入側ポート
74−2 出側ポート
80 給湯・追焚き・暖房装置
82 装置筐体
84 熱媒タンク
88−1、88−2、88−3、88−11、88−12、88−13、88−14 循環路
88−4 給水路
88−5 給湯路
88−6 バイパス路
88−7 ドレンパイプ
88−8 注湯管
88−9 排出管
88−31 往き管
88−32 戻り管
88−41 管路
89 浴槽
90−1、90−2 循環ポンプ
92−1 高温暖房負荷
92−2 低温暖房負荷
94−1 分岐部
94−2 分岐部
94−3 分岐部
96−1 分配弁
96−2 混合弁
96−3 混合弁
96−4 燃料制御弁
96−5 注湯電磁弁
97 ドレンタンク
98−1 温度センサ
98−2、98−3、98−4 温度センサ
98−5 給水量センサ
98−6 注湯量センサ
100 電装基板
102 電源部
104 給湯・追焚き・暖房制御部
106−1、106−2、106−3 リモコン装置
108 プロセッサ
110 メモリ部
112 システム通信部
114 入出力部
2 Heat exchanger 4 Housing 6-1 1st heat exchange part 6-2 2nd heat exchange part 6-3 3rd heat exchange part 8 Burner 10 Exhaust part 12-1 Heat medium heat exchange pipe 12-2 Heat medium heat Exchange pipe 14 Bath water heat exchange pipe 16 Water supply heat exchange pipe 20 Heat source machine 22 Heat exchanger 24 Plate heat exchanger (4th heat exchange section)
26 Main body case part 26-1 Main body cover part 26-2 Upper cover part 28-1 First housing part 28-2 Second housing part 28-3 Third housing part 30 Fan 32 Fan motor 34 Exhaust pipe part 36 Air-fuel mixture ejection part 38-1, 38-2 Air-fuel mixture ejection nozzle 40-1, 40-2 Air-fuel mixture introduction part 42 Ignite 43 Fuel supply pipe 44 Frame rod 46 Space part 48 Heat absorption fin 50 Inclined plate 52 Bottom plate 54 Drain receiver 56 Ventilation window 58 Shielding plate 62 Distribution valve 64-1 Entering port 64-2 Outer port 66 Heat medium line 68-1 Entering port 68-2 Outer port 70-1 Entering port 70-2 Outer side Port 72 Exhaust port 74-1 Inlet port 74-2 Outlet port 80 Hot water supply / reheating / heating device 82 Equipment housing 84 Heat medium tank 88-1, 88-2, 88-3, 88-11, 88 -12, 88-13, 88-14 Circulation route 88-4 Water supply route 88-5 Hot water supply route 88-6 Bypass route 88-7 Drain pipe 88-8 Pouring pipe 88-9 Discharge pipe 88-31 Outgoing pipe 88- 32 Return pipe 88-41 Pipe line 89 Bathtub 90-1, 90-2 Circulation pump 92-1 High temperature heating load 92-2 Low temperature heating load 94-1 Branch 94-2 Branch 94-3 Branch 96-1 Distribution Valve 96-2 Mixing valve 96-3 Mixing valve 96-4 Fuel control valve 96-5 Hot water pouring electromagnetic valve 97 Drain tank 98-1 Temperature sensor 98-2, 98-3, 98-4 Temperature sensor 98-5 Water supply amount Sensor 98-6 Hot water injection amount sensor 100 Electrical board 102 Power supply unit 104 Hot water supply / reheating / heating control unit 106-1, 106-2, 106-3 Remote control device 108 Processor 110 Memory unit 112 System communication unit 114 Input / output unit

Claims (5)

燃焼排気と熱媒を熱交換させる第一熱交換部を収納する第1の筐体部と、
前記第1の筐体部に隣接し、前記第1の筐体部から流入する前記燃焼排気と前記熱媒を熱交換する第二熱交換部と、前記燃焼排気と給水を熱交換する第三熱交換部とを収納する第2の筐体部と、
前記第1の筐体部の天井部と前記第2の筐体部の底部との間に設けられ、前記第2の筐体部の前記底部を傾斜させる傾斜板と、
前記傾斜板に形成され、前記第1の筐体部からの前記燃焼排気を前記第2の筐体部の内部に導く通気窓部と、
前記傾斜板から前記通気窓部に張り出して設けられ、前記傾斜板よりも傾斜を大きくした遮蔽板と、
を備えることを特徴とする熱交換器。
A first housing unit that houses the first heat exchange unit that exchanges heat between the combustion exhaust and the heat medium, and
A second heat exchange unit that is adjacent to the first housing portion and exchanges heat between the combustion exhaust and the heat medium flowing in from the first housing portion, and a third that exchanges heat between the combustion exhaust and the water supply. A second housing that houses the heat exchange and
An inclined plate provided between the ceiling portion of the first housing portion and the bottom portion of the second housing portion and inclining the bottom portion of the second housing portion.
A ventilation window portion formed on the inclined plate and guiding the combustion exhaust gas from the first housing portion to the inside of the second housing portion.
A shielding plate that is provided so as to project from the inclined plate to the ventilation window portion and has a larger inclination than the inclined plate.
A heat exchanger characterized by being equipped with.
前記遮蔽板は、前記通気窓部側に張り出した前記第二熱交換部または前記第三熱交換部の底部を覆うことを特徴とする請求項1に記載の熱交換器。 The heat exchanger according to claim 1, wherein the shielding plate covers the bottom of the second heat exchange section or the third heat exchange section that projects toward the ventilation window portion. 前記第2の筐体部は、前記第1の筐体部の側面側に突出したドレン受けを有し、前記第二熱交換部と前記第三熱交換部のいずれかまたは双方から発生したドレンを、前記遮蔽板および前記傾斜板に沿って流して前記ドレン受けに導入することを特徴とする請求項1または請求項2に記載の熱交換器。 The second housing portion has a drain receiver protruding from the side surface side of the first housing portion, and drains generated from either or both of the second heat exchange portion and the third heat exchange portion. The heat exchanger according to claim 1 or 2, wherein the heat exchanger is introduced into the drain receiver by flowing along the shielding plate and the inclined plate. 前記第二熱交換部と前記第三熱交換部は、前記第2の筐体部内において、前記燃焼排気の流れ方向と平行に隣接または前記燃焼排気に対して垂直方向に隣接して配置されることを特徴とする請求項1ないし請求項3のいずれかに記載の熱交換器。 The second heat exchange unit and the third heat exchange unit are arranged in the second housing portion in parallel with the flow direction of the combustion exhaust or adjacent in the direction perpendicular to the combustion exhaust. The heat exchanger according to any one of claims 1 to 3, wherein the heat exchanger is characterized in that. 熱媒回路に循環する熱媒、または追焚回路に循環する浴槽水と燃焼排気とを熱交換させる第一熱交換部を収納する第1の筐体部と、
前記第1の筐体部に隣接し、前記第1の筐体部から流入する前記燃焼排気と前記熱媒回路に循環する前記熱媒を熱交換する第二熱交換部と、給湯回路に備えられて、この給湯回路に流れる給水と前記燃焼排気を熱交換する第三熱交換部とを収納する第2の筐体部と、
前記第1の筐体部の天井部と前記第2の筐体部の底部との間に設けられ、前記第2の筐体部の前記底部を傾斜させる傾斜板と、
前記傾斜板に形成され、前記第1の筐体部からの前記燃焼排気を前記第2の筐体部の内部に導く通気窓部と、
前記傾斜板から前記通気窓部に張り出して設けられ、前記傾斜板よりも傾斜を大きくした遮蔽板と、
を備えることを特徴とする熱源機。

A first housing unit that houses a first heat exchange unit that exchanges heat between the heat medium that circulates in the heat medium circuit or the bathtub water that circulates in the reheating circuit and the combustion exhaust gas.
A second heat exchange unit that is adjacent to the first housing portion and exchanges heat between the combustion exhaust that flows in from the first housing portion and the heat medium that circulates in the heat medium circuit, and a hot water supply circuit are provided. A second housing unit that houses the water supply flowing through the hot water supply circuit and the third heat exchange unit that exchanges heat with the combustion exhaust.
An inclined plate provided between the ceiling portion of the first housing portion and the bottom portion of the second housing portion and inclining the bottom portion of the second housing portion.
A ventilation window portion formed on the inclined plate and guiding the combustion exhaust gas from the first housing portion to the inside of the second housing portion.
A shielding plate that is provided so as to project from the inclined plate to the ventilation window portion and has a larger inclination than the inclined plate.
A heat source machine characterized by being equipped with.

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