JP6480850B2 - Heat exchanger, secondary heat exchanger and heat source machine - Google Patents

Heat exchanger, secondary heat exchanger and heat source machine Download PDF

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JP6480850B2
JP6480850B2 JP2015209910A JP2015209910A JP6480850B2 JP 6480850 B2 JP6480850 B2 JP 6480850B2 JP 2015209910 A JP2015209910 A JP 2015209910A JP 2015209910 A JP2015209910 A JP 2015209910A JP 6480850 B2 JP6480850 B2 JP 6480850B2
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heat exchange
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combustion exhaust
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哲也 栗田
哲也 栗田
小林 雅彦
雅彦 小林
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Purpose Co Ltd
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Description

本発明はたとえば、燃料排気の潜熱などを熱交換に用いる熱交換技術に関する。
The present invention relates to a heat exchange technique that uses, for example, latent heat of fuel exhaust for heat exchange.

給湯装置には燃料ガスの燃焼排気の熱を熱交換する熱交換器が備えられる。この熱交換器には、燃焼排気の顕熱を熱交換する一次熱交換器と、この一次熱交換器で熱交換後の燃焼排気の潜熱を熱交換する二次熱交換器が含まれる。二次熱交換器は、燃焼排気から潜熱を回収するので、熱交換器全体の熱交換効率を高めることができる上、外気に放出する燃焼排気を低温化できるなどの利点がある。   The hot water supply device is provided with a heat exchanger for exchanging heat of the combustion exhaust gas of the fuel gas. The heat exchanger includes a primary heat exchanger that exchanges sensible heat of the combustion exhaust and a secondary heat exchanger that exchanges latent heat of the combustion exhaust after heat exchange by the primary heat exchanger. Since the secondary heat exchanger recovers latent heat from the combustion exhaust, there are advantages such that the heat exchange efficiency of the entire heat exchanger can be improved and the combustion exhaust discharged to the outside air can be cooled.

二次熱交換器には、一次熱交換器での熱交換前の給水を燃焼排気の潜熱による予備加熱や、熱源として用いられる熱媒を一次熱交換前に燃焼排気の潜熱で予備加熱するなどの利用形態がある。   For secondary heat exchangers, preheat the water before heat exchange in the primary heat exchanger with the latent heat of the combustion exhaust, or preheat the heat medium used as the heat source with the latent heat of the combustion exhaust before the primary heat exchange, etc. There are usage forms.

このような熱交換の熱効率改善に関し、燃焼排気を流す通路空間の天井部に燃焼排気の流れを乱す凸壁を備える構成が知られている(たとえば、特許文献1)。さらに、複数の熱交換管を備えた熱交換器において、整流板によって熱交換管を仕切り、ドレン排出側を下方向に傾斜させたものが知られている(たとえば、特許文献2)。
With respect to improving the heat efficiency of such heat exchange, a configuration is known in which a ceiling wall of a passage space through which combustion exhaust flows is provided with a convex wall that disturbs the flow of combustion exhaust (for example, Patent Document 1). Furthermore, in a heat exchanger provided with a plurality of heat exchange tubes, one in which the heat exchange tubes are partitioned by a rectifying plate and the drain discharge side is inclined downward is known (for example, Patent Document 2).

特開2014−70800号公報JP 2014-70800 A 特開2014−119225号公報JP 2014-119225 A

ところで、二次熱交換器では、燃焼室側で一次熱交換後の燃焼排気が導かれ、この燃焼排気の熱を二次熱交換管に絡ませて熱交換を行い、効率的な熱交換の実現を想定している。   By the way, in the secondary heat exchanger, the combustion exhaust after the primary heat exchange is guided on the combustion chamber side, and the heat of this combustion exhaust is entangled in the secondary heat exchange pipe to perform heat exchange, thereby realizing efficient heat exchange Is assumed.

しかしながら、燃焼排気は、熱交換管が密集していない筐体天井側の流路抵抗の低い側に流れるため、高温の排気流が下流側に流れ、排気温度分布が不均一になるという課題がある。排気通路を流れる排気流の上部ほど排気熱量が高くなる傾向がある。排気通路を通過する排気流が不均一になると、熱交換管毎の熱交換にばらつきを生じ、ひとつの熱交換管であっても幅内で温度分布に偏差を持つ熱交換となる。この結果、熱交換にばらつきを生じ、期待する熱交換効率が得られないという課題がある。   However, since the combustion exhaust flows to the low-flow-path side of the casing ceiling side where the heat exchange pipes are not dense, there is a problem that the high-temperature exhaust flow flows downstream and the exhaust temperature distribution becomes uneven. is there. There is a tendency that the amount of exhaust heat becomes higher at the upper part of the exhaust flow through the exhaust passage. If the exhaust flow passing through the exhaust passage becomes non-uniform, the heat exchange between the heat exchange pipes varies, and even a single heat exchange pipe has a heat exchange having a deviation in temperature distribution within the width. As a result, there is a problem that the heat exchange varies and the expected heat exchange efficiency cannot be obtained.

下流側に高温の排気流が流れ、下流側に給水などの加熱に用いる熱交換管を備えていると、非給水時、残留水などの被加熱流体を過熱し、部分沸騰を生じるなどの課題もある。   When a high-temperature exhaust flow flows downstream and a heat exchange pipe used for heating water supply or the like is provided on the downstream side, the heated fluid such as residual water is overheated during non-water supply, causing partial boiling. There is also.

このような排気流を放置すれば、二次熱交換器による熱交換効率が低く、燃焼排気からの熱回収が不充分であり、排気温度を低温化できないという課題もある。   If such an exhaust flow is left unattended, there is a problem that the heat exchange efficiency by the secondary heat exchanger is low, the heat recovery from the combustion exhaust is insufficient, and the exhaust temperature cannot be lowered.

そこで、本発明の目的は上記課題に鑑み、燃焼排気の熱交換効率を高め、燃焼排気の熱回収率を向上させることにある。
In view of the above problems, an object of the present invention is to increase the heat exchange efficiency of combustion exhaust and improve the heat recovery rate of combustion exhaust.

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、燃焼排気を流す筐体と、前記筐体内で前記燃焼排気と被加熱流体を熱交換する複数の熱交換管が配置され、前記燃焼排気の上流側に第1の被加熱流体を通流させる第1の熱交換部と、前記燃焼排気の下流側に前記第1の被加熱流体と循環路が異なる第2の被加熱流体を通流させる第2の熱交換部とを含む熱交換部と、前記第2の熱交換部に流れた前記燃焼排気を前記第2の熱交換部から前記第1の熱交換部側に方向転換させる変流片であり、前記筐体に通流させた前記燃焼排気を変流することにより前記熱交換管に集合または分散させ、前記熱交換管と前記燃焼排気の熱交換を行わせる1または2以上の変流部材を備えればよい。 In order to achieve the above object, according to one aspect of the heat exchanger of the present invention, a casing for flowing combustion exhaust, and a plurality of heat exchange tubes for exchanging heat between the combustion exhaust and the fluid to be heated are disposed in the casing. A first heat exchange section for flowing a first heated fluid upstream of the combustion exhaust gas, and a second heat receiving section having a circulation path different from that of the first heated fluid downstream of the combustion exhaust gas. A heat exchanging part including a second heat exchanging part through which the heating fluid flows, and the combustion exhaust gas flowing to the second heat exchanging part from the second heat exchanging part to the first heat exchanging part side. A flow-changing piece that changes the direction of the heat-exhaust gas. The heat-exhaust gas flowed through the casing is collected or dispersed in the heat-exchange pipe to exchange heat between the heat-exchange pipe and the combustion exhaust gas. What is necessary is just to provide the 1 or 2 or more current transformation member to make.

上記熱交換器において、前記変流部材は、前記燃焼排気を衝突させて前記燃焼排気の流れ方向を変更する衝突部材、前記燃焼排気を一方向に流れ方向を変更させる流れ方向変更部材、前記熱交換管の一部を包囲する包囲部材の何れかまたはこれらの組合せを含んでよい。   In the heat exchanger, the current changing member includes a collision member that collides the combustion exhaust to change a flow direction of the combustion exhaust, a flow direction changing member that changes the flow direction of the combustion exhaust in one direction, and the heat Any of the surrounding members surrounding a portion of the exchange tube or a combination thereof may be included.

上記熱交換器において、前記変流部材は、前記第2の熱交換部に流れた前記燃焼排気を前記第2の熱交換部から前記第の熱交換部側に方向転換させる第1の変流片と、
前記第1の熱交換部に流れた前記燃焼排気を前記第1の熱交換部から前記第2の熱交換部側に方向転換させる第2の変流片とを含んでよい。
In the heat exchanger, the current transformation member may change the direction of the combustion exhaust gas that has flowed to the second heat exchange section from the second heat exchange section to the first heat exchange section. With flakes,
And a second current changing piece for changing the direction of the combustion exhaust gas flowing to the first heat exchange section from the first heat exchange section to the second heat exchange section.

上記目的を達成するため、本発明の二次熱交換器の一側面によれば、一次熱交換後の燃焼排気を流す筐体部と、前記筐体部で前記燃焼排気と被加熱流体を熱交換する複数の熱交換管が配置され、前記燃焼排気の上流側に第1の被加熱流体を通流させる第1の熱交換部と、前記燃焼排気の下流側に前記第1の被加熱流体と循環路が異なる第2の被加熱流体を通流させる第2の熱交換部とを含む熱交換部と、前記第2の熱交換部に流れた前記燃焼排気を前記第2の熱交換部から前記第1の熱交換部側に方向転換させる変流片であり、前記筐体に通流させた前記燃焼排気を変流することにより前記熱交換管に集合または分散させ、前記熱交換管と前記燃焼排気の熱交換を行わせる1または2以上の変流部材とを備えてよい。
In order to achieve the above object, according to one aspect of the secondary heat exchanger of the present invention, a casing portion for flowing combustion exhaust after primary heat exchange, and the combustion exhaust and the fluid to be heated are heated in the casing portion. A plurality of heat exchange tubes to be exchanged are arranged, and a first heat exchange section that allows the first heated fluid to flow upstream of the combustion exhaust, and the first heated fluid downstream of the combustion exhaust And a second heat exchanging part that allows a second heated fluid having a different circulation path to flow therethrough, and the second heat exchanging part that converts the combustion exhaust gas flowing through the second heat exchanging part to the second heat exchanging part From the first heat exchanging portion to the first heat exchanging portion, and the combustion exhaust gas flowing through the housing portion is diverted to gather or disperse in the heat exchanging pipe, thereby exchanging the heat. You may provide a pipe | tube and the 1 or 2 or more current transformation member which performs the heat exchange of the said combustion exhaust gas.

上記二次熱交換器において、既述の筐体部に上記熱交換器を備えてよい。   In the secondary heat exchanger, the above-described heat exchanger may be provided in the above-described casing portion.

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、上記熱交換器を備え、または上記二次熱交換器を備えて被加熱流体を加熱し、該被加熱流体を用いて給湯または暖房を行ってもよい。
In order to achieve the above object, according to one aspect of the heat source apparatus of the present invention, the fluid to be heated is provided with the heat exchanger or the secondary heat exchanger, and the heated fluid is used. Hot water supply or heating may be performed.

本発明によれば、次のような効果が得られる。   According to the present invention, the following effects can be obtained.

(1) 変流部材によって筐体内の燃焼排気を集合させまたは複数の排気流に分流させることにより排気流の均一化を図ることができ、排気流毎の燃焼排気と被加熱流体との熱交換を行わせることができる。   (1) Combustion exhaust in the housing is gathered by a current transformation member or divided into multiple exhaust flows to make the exhaust flow uniform, and heat exchange between the combustion exhaust and the fluid to be heated for each exhaust flow Can be performed.

(2) 燃焼排気と被加熱流体を熱交換する複数の熱交換管を備える筐体に変流部材を備えることにより、燃焼排気を変流して熱交換管と燃焼排気の熱交換を行わせるので、燃焼排気を均一化して熱交換が可能となり、燃焼排気の熱回収が良好になり、熱交換効率が高められる。   (2) Since a current transformation member is provided in a housing having a plurality of heat exchange tubes for exchanging heat between the combustion exhaust and the fluid to be heated, the combustion exhaust is transformed and heat exchange between the heat exchange tube and the combustion exhaust is performed. The combustion exhaust can be made uniform to exchange heat, the heat recovery of the combustion exhaust becomes good, and the heat exchange efficiency is improved.

(3) 上流側で熱交換を経ていない排気流が下流側に流れるのを防止でき、下流側の熱交換管での被加熱流体の部分沸騰を回避できる。
(3) It is possible to prevent the exhaust flow that has not undergone heat exchange on the upstream side from flowing downstream, and to avoid partial boiling of the heated fluid in the downstream heat exchange pipe.

本発明の第1の実施の形態に係る二次熱交換ユニットを示す図である。It is a figure which shows the secondary heat exchange unit which concerns on the 1st Embodiment of this invention. 二次熱交換ユニットの変形例を示す図である。It is a figure which shows the modification of a secondary heat exchange unit. 本発明の第2の実施の形態に係る二次熱交換ユニットを示す図である。It is a figure which shows the secondary heat exchange unit which concerns on the 2nd Embodiment of this invention. 本発明の第3の実施の形態に係る二次熱交換ユニットを示す図である。It is a figure which shows the secondary heat exchange unit which concerns on the 3rd Embodiment of this invention. 本発明の第4の実施の形態に係る二次熱交換ユニットを示す図である。It is a figure which shows the secondary heat exchange unit which concerns on the 4th Embodiment of this invention. 本発明の第5の実施の形態に係る二次熱交換ユニットを示す図である。It is a figure which shows the secondary heat exchange unit which concerns on the 5th Embodiment of this invention. 本発明の第6の実施の形態に係る二次熱交換ユニットを示す図である。It is a figure which shows the secondary heat exchange unit which concerns on the 6th Embodiment of this invention. 本発明の第7の実施の形態に係る二次熱交換ユニットを示す図である。It is a figure which shows the secondary heat exchange unit which concerns on the 7th Embodiment of this invention. 本発明の第8の実施の形態に係る熱源機を示す図である。It is a figure which shows the heat-source equipment which concerns on the 8th Embodiment of this invention. 本発明の第1の実施例に係る熱交換器を示す断面図である。It is sectional drawing which shows the heat exchanger which concerns on the 1st Example of this invention. 本発明の第2の実施例に係る熱源機を示す断面図である。It is sectional drawing which shows the heat source machine which concerns on the 2nd Example of this invention. 本発明の第3の実施例に係る給湯装置を示す図である。It is a figure which shows the hot water supply apparatus which concerns on the 3rd Example of this invention.

〔第1の実施の形態〕 [First Embodiment]

図1のAは、第1の実施の形態に係る二次熱交換ユニットを示している。図に示す構成例は本発明の熱交換器または二次熱交換器の一例であり、係る構成に本発明は限定されない。以下、各実施の形態においても同様である。   FIG. 1A shows a secondary heat exchange unit according to the first embodiment. The configuration example shown in the figure is an example of the heat exchanger or the secondary heat exchanger of the present invention, and the present invention is not limited to such a configuration. The same applies to each embodiment below.

二次熱交換ユニット2にはたとえば、一次熱交換後の燃焼排気EGの排気空間として筒状の筐体4が備えられる。筐体4には底面側に排気導入部6、この排気導入部6から離間した側面部に排出部8が備えられる。排気導入部6から導入された燃焼排気EGは、筐体4内を通過し、排出部8から外気に放出される。   For example, the secondary heat exchange unit 2 includes a cylindrical housing 4 as an exhaust space for the combustion exhaust EG after the primary heat exchange. The housing 4 is provided with an exhaust introduction portion 6 on the bottom surface side, and a discharge portion 8 on a side surface spaced from the exhaust introduction portion 6. The combustion exhaust EG introduced from the exhaust introduction part 6 passes through the housing 4 and is released from the exhaust part 8 to the outside air.

筐体4にはたとえば、一系統の熱交換部10が備えられ、この熱交換部10に含まれる複数の熱交換管12が配置されている。これら熱交換管12は連続した循環路を構成し、一系統の被加熱流体Mを通流させる。この被加熱流体Mは給湯に供される給水Wでもよいし、熱媒の一例として暖房に供される暖房水hWでもよい。   For example, the housing 4 is provided with a single heat exchange unit 10, and a plurality of heat exchange tubes 12 included in the heat exchange unit 10 are arranged. These heat exchange pipes 12 constitute a continuous circulation path, and allow one system of heated fluid M to flow. This heated fluid M may be water supply W provided for hot water supply, or may be heating water hW provided for heating as an example of a heat medium.

筐体4の内壁部には1または2以上の変流部材の一例として邪魔板14−1、14−2、14−3が備えられる。邪魔板14−1、14−2は筐体4の天井板16に配置され、邪魔板14−3は底面板18に配置されている。邪魔板14−1、14−2は天井板16から底面板18に向かって垂下させた垂直板であり、邪魔板14−3は底面板18から天井板16に向かって立設させた垂直板である。邪魔板14−1、14−2は燃焼排気EGの流れ方向に向かってたとえば、等間隔で配置され、邪魔板14−3は邪魔板14−1、14−2の間隔内に配置されている。邪魔板14−1の高さをh1、邪魔板14−2の高さをh2、邪魔板14−3の高さをh3とすれば、これらはh1=h2=h3でもよく、h1≠h2≠h3でもよく、h1<h2としてもよく、h1>h2としてもよい。この例では、h1、h2をたとえば、最上部側の熱交換管12の管径内に到達する大きさとし、h3をたとえば、最下部側の熱交換管12の管径内に到達する大きさとしている。   The inner wall of the housing 4 is provided with baffle plates 14-1, 14-2, 14-3 as an example of one or more current transformation members. The baffle plates 14-1 and 14-2 are disposed on the ceiling plate 16 of the housing 4, and the baffle plate 14-3 is disposed on the bottom plate 18. The baffle plates 14-1 and 14-2 are vertical plates suspended from the ceiling plate 16 toward the bottom plate 18, and the baffle plates 14-3 are vertical plates erected from the bottom plate 18 toward the ceiling plate 16. It is. The baffle plates 14-1 and 14-2 are arranged, for example, at equal intervals in the flow direction of the combustion exhaust EG, and the baffle plate 14-3 is arranged within the interval between the baffle plates 14-1 and 14-2. . If the height of the baffle plate 14-1 is h1, the height of the baffle plate 14-2 is h2, and the height of the baffle plate 14-3 is h3, these may be h1 = h2 = h3, and h1 ≠ h2 ≠. It may be h3, h1 <h2, or h1> h2. In this example, h1 and h2 are, for example, large enough to reach the tube diameter of the uppermost heat exchange tube 12, and h3 is large enough to reach the tube diameter of the lowermost heat exchange tube 12, for example. Yes.

このような二次熱交換ユニット2では、図1のBに示すように、排気導入部6から侵入した燃焼排気EGは層流を成しており、天井板16側から底面板18側に向かって層流を成しており、たとえば、上層側に排気流EG1、中層側に排気流EG2、下層側に排気流EG3を定義することができる。これら層流は燃焼排気EGの流速の影響を受け、流速が速い場合には排気流EG1側が支配的である。   In such a secondary heat exchange unit 2, as shown in FIG. 1B, the combustion exhaust EG that has entered from the exhaust introduction portion 6 forms a laminar flow, and moves from the ceiling plate 16 side toward the bottom plate 18 side. For example, an exhaust flow EG1 can be defined on the upper layer side, an exhaust flow EG2 on the middle layer side, and an exhaust flow EG3 on the lower layer side. These laminar flows are affected by the flow velocity of the combustion exhaust EG, and when the flow velocity is high, the exhaust flow EG1 side is dominant.

過渡的な層流変化を概観すれば、排気流EG1は各邪魔板14−1、14−2に衝突して反転し、排気流EG2と交差して層流を変化させる。つまり、排気流EG1と排気流EG2、排気流EG1と排気流EG3を攪拌させる。また、排気流EG3は邪魔板14−3に衝突して反転し、排気流EG1、EG2と交差して層流を変化させる。これにより、排気流EG3と排気流EG2、排気流EG3と排気流EG1を攪拌させる。   If the transitional laminar flow change is overviewed, the exhaust flow EG1 collides with the baffle plates 14-1 and 14-2 and reverses, and intersects the exhaust flow EG2 to change the laminar flow. That is, the exhaust flow EG1 and the exhaust flow EG2, and the exhaust flow EG1 and the exhaust flow EG3 are agitated. Further, the exhaust flow EG3 collides with the baffle plate 14-3 and reverses, and intersects the exhaust flows EG1 and EG2 to change the laminar flow. As a result, the exhaust flow EG3 and the exhaust flow EG2, and the exhaust flow EG3 and the exhaust flow EG1 are agitated.

このような攪拌により燃焼排気EGの排気流EG1、EG2、EG3は、層流方向、層流速度などの要素が絡み、各層流が乱される結果、燃焼排気EGは層流に偏りを生ずることなく、各熱交換管12に広く行き渡るので、筐体4に流入した燃焼排気EGが被加熱流体Mの熱交換に供される。   Due to such agitation, the exhaust flow EG1, EG2, EG3 of the combustion exhaust EG is entangled with elements such as the laminar flow direction and the laminar flow speed, and each laminar flow is disturbed. As a result, the combustion exhaust EG is biased in the laminar flow. However, the exhaust gas EG that has flowed into the housing 4 is used for heat exchange of the fluid M to be heated.

このような層流変化を生じさせるための邪魔板14−1、14−2、14−3は、熱交換管12の受熱部幅(燃焼排気EGと交差方向の幅)に跨がる単一板としてもよいが、幅内の一部の幅を持つものであってもよい。たとえば、図2に示すように、ヘッダ20−1、20−2に跨がる熱交換管12と平行に、その幅内でたとえば、邪魔板14−1を分断させて複数の変流片14−11、14−12としてもよい。この形態は邪魔板14−2、14−3でも同様である。各変流片14−11、14−12など複数の変流片を備えれば、これら変流片は、天井板16と底面板18で位置を異ならせ、たとえば、千鳥状など交互に配置してもよく、燃焼排気EGの層流に複雑な変化を生じさせる形態であればよい。また、各邪魔板14−1、14−2、14−3は陰になる熱交換管12に接触させ、排気流の熱を熱交換管12に伝熱するように構成しても良い。   The baffle plates 14-1, 14-2 and 14-3 for causing such laminar flow changes are a single straddle across the heat receiving portion width of the heat exchange pipe 12 (width in the direction crossing the combustion exhaust EG). Although it may be a plate, it may have a partial width within the width. For example, as shown in FIG. 2, the baffle plate 14-1 is divided within the width in parallel with the heat exchange pipe 12 straddling the headers 20-1 and 20-2, and the plurality of current-transforming pieces 14. -11, 14-12 may be used. This configuration is the same for the baffle plates 14-2 and 14-3. If a plurality of current transformation pieces such as each of the current transformation pieces 14-11 and 14-12 are provided, the positions of the current transformation pieces are different between the ceiling plate 16 and the bottom plate 18, and are alternately arranged, for example, in a staggered manner. It may be a form that causes a complicated change in the laminar flow of the combustion exhaust gas EG. Further, the baffle plates 14-1, 14-2, 14-3 may be configured to contact the heat exchange pipe 12 which is shaded to transfer the heat of the exhaust flow to the heat exchange pipe 12.

なお、邪魔板14−1、14−2の高さh1、h2をh1<h2とすれば、邪魔板14−1をすり抜けた排気流EG1を邪魔板14−2に衝突させ、層流変化を促進させることができる。   If the heights h1 and h2 of the baffle plates 14-1 and 14-2 are set to h1 <h2, the exhaust flow EG1 that has passed through the baffle plate 14-1 collides with the baffle plate 14-2, and the laminar flow change is caused. Can be promoted.

<第1の実施の形態の効果> <Effect of the first embodiment>

(1) 第1の実施の形態の二次熱交換ユニット2によれば、給湯単能機、ふろ給湯機などの二次熱交換器として用いることができる。   (1) According to the secondary heat exchange unit 2 of the first embodiment, it can be used as a secondary heat exchanger such as a single hot water supply machine or a bath water heater.

(2) 熱交換部10の熱交換管12は一系統の被加熱流体Mの加熱に用いることができる。   (2) The heat exchange pipe 12 of the heat exchange unit 10 can be used for heating the heated fluid M of one system.

(3) 筐体4で構成される排気路に備えた単一または複数の変流部材としてたとえば、邪魔板14−1、14−2、14−3が設けられ、排気流EG1、EG3の流路が上下方向に変更され、特に、最上部や最下部を流れる排気流が熱交換に供されることなく、排出部8側に抜け出るのを防止できる。   (3) For example, baffle plates 14-1, 14-2, 14-3 are provided as single or plural current transformation members provided in the exhaust path constituted by the casing 4, and the flow of the exhaust flows EG1, EG3 The path is changed in the vertical direction, and in particular, the exhaust flow flowing through the uppermost part and the lowermost part can be prevented from coming out to the discharge part 8 side without being subjected to heat exchange.

(4) 筐体4の排気空間に流れる燃焼排気EGの層流が乱される結果、燃焼排気EGのすり抜けや偏りを防止でき、筐体4内に流入する燃焼排気EGを筐体4内の全ての熱交換管12に絡ませて熱交換に供することができ、熱交換効率を高めることができる。   (4) As a result of the laminar flow of the combustion exhaust EG flowing in the exhaust space of the casing 4 being disturbed, it is possible to prevent the combustion exhaust EG from slipping through and being biased, and the combustion exhaust EG flowing into the casing 4 All the heat exchange tubes 12 can be entangled and used for heat exchange, and the heat exchange efficiency can be improved.

(5) 熱交換部10をたとえば、ヘッダ20−1、20−2および複数の熱交換管12からなるユニットとし、このユニットを筐体4と別部材とし、邪魔板14−1、14−2、14−3は筐体4側の部材として構成すれば、熱交換部10の構造の複雑化を防止でき、製造工程を分離し、二次熱交換ユニット2の効率的な製造工程を実現できる。   (5) The heat exchanging unit 10 is, for example, a unit composed of headers 20-1, 20-2 and a plurality of heat exchanging pipes 12, and this unit is a separate member from the casing 4, and the baffle plates 14-1, 14-2 , 14-3 can be configured as a member on the housing 4 side, so that the structure of the heat exchanging unit 10 can be prevented from being complicated, the manufacturing process can be separated, and an efficient manufacturing process of the secondary heat exchange unit 2 can be realized. .

〔第2の実施の形態〕 [Second Embodiment]

図3のAは、第2の実施の形態に係る二次熱交換ユニットを示している。第2の実施の形態に係る二次熱交換ユニット2では、第1の実施の形態と同様に単一または複数の変流部材としてたとえば、複数の邪魔板24−1、24−2、24−3が備えられる。第1の実施の形態の邪魔板14−1、14−2、14−3は垂直板であったのに対し、邪魔板24−1、24−2、24−3は上流から下流方向に角度θ1、θ2、θ3で傾斜する傾斜板である。各邪魔板24−1、24−2は筐体4の天井板16に配置され、邪魔板24−3は底面板18に配置されている。   FIG. 3A shows a secondary heat exchange unit according to the second embodiment. In the secondary heat exchange unit 2 according to the second embodiment, for example, a plurality of baffle plates 24-1, 24-2, 24- 3 is provided. The baffle plates 14-1, 14-2, 14-3 of the first embodiment are vertical plates, whereas the baffle plates 24-1, 24-2, 24-3 are angled from upstream to downstream. It is an inclined plate inclined at θ1, θ2, and θ3. The baffle plates 24-1 and 24-2 are disposed on the ceiling plate 16 of the housing 4, and the baffle plate 24-3 is disposed on the bottom plate 18.

邪魔板24−1は天井板16から排出部8の方向に向かって角度θ1の勾配を持たせた傾斜板、邪魔板24−2も天井板16から排出部8の方向に向かって角度θ2の勾配を持たせた傾斜板、邪魔板24−3は底面板18から排出部8の方向に向かって角度θ3の勾配を持たせた傾斜板である。邪魔板24−1、24−2は燃焼排気EGの流れ方向に向かってたとえば、等間隔で配置され、邪魔板24−3は邪魔板24−1、24−2の間隔内に配置されている。角度θ1、θ2、θ3は、θ1=θ2=θ3でもよく、θ1≠θ2≠θ3でもよく、θ1<θ2としてもよく、θ1>θ2としてもよい。   The baffle plate 24-1 is an inclined plate having an inclination of the angle θ1 from the ceiling plate 16 toward the discharge portion 8, and the baffle plate 24-2 is also inclined at the angle θ2 from the ceiling plate 16 toward the discharge portion 8. The inclined plate and baffle plate 24-3 having a gradient are inclined plates having a gradient of an angle θ3 from the bottom plate 18 toward the discharge unit 8. The baffle plates 24-1 and 24-2 are arranged, for example, at equal intervals in the flow direction of the combustion exhaust EG, and the baffle plate 24-3 is arranged within the interval between the baffle plates 24-1 and 24-2. . The angles θ1, θ2, and θ3 may be θ1 = θ2 = θ3, θ1 ≠ θ2 ≠ θ3, θ1 <θ2, or θ1> θ2.

邪魔板24−1の長さをL1、その高さをh1、邪魔板24−2の長さをL2、その高さをh2、邪魔板24−3の長さをL3、その高さをh3とすれば、これらはL1=L2=L3でもよく、L1≠L2≠L3でもよく、L1<L2としてもよく、L1>L2としてもよい。また、第1の実施の形態と同様に、h1=h2=h3でもよく、h1≠h2≠h3でもよく、h1<h2としてもよく、h1>h2としてもよい。この例では、h1、h2をたとえば、最上部側の熱交換管12を超える高さとし、h3をたとえば、最下部側の熱交換管12を超える高さとしている。θ1、θ2およびθ3はたとえば、45度である。   The length of the baffle plate 24-1 is L1, its height is h1, the length of the baffle plate 24-2 is L2, its height is h2, the length of the baffle plate 24-3 is L3, and its height is h3 Then, these may be L1 = L2 = L3, L1 ≠ L2 ≠ L3, L1 <L2, or L1> L2. Similarly to the first embodiment, h1 = h2 = h3, h1 ≠ h2 ≠ h3, h1 <h2, or h1> h2. In this example, h1 and h2 are, for example, higher than the uppermost heat exchange pipe 12, and h3 is, for example, higher than the lowermost heat exchange pipe 12. θ1, θ2, and θ3 are, for example, 45 degrees.

このような二次熱交換ユニット2では、図3のBに示すように、排気導入部6から侵入した燃焼排気EGは層流を成しており、天井板16側から底面板18側に向かって排気流EG1、EG2、EG3が含まれる。これら層流は燃焼排気EGの流速の影響を受け、排気流EG1側が支配的であることは第1の実施の形態と同様である。   In such a secondary heat exchange unit 2, as shown in FIG. 3B, the combustion exhaust EG that has entered from the exhaust introduction portion 6 forms a laminar flow, and moves from the ceiling plate 16 side toward the bottom plate 18 side. The exhaust flows EG1, EG2, and EG3 are included. These laminar flows are affected by the flow velocity of the combustion exhaust EG, and the exhaust flow EG1 side is dominant as in the first embodiment.

過渡的な層流変化を概観すれば、排気流EG1が各邪魔板24−1、24−2に衝突して反転し、排気流EG2と交差して層流を変化させ、また、排気流EG3が邪魔板24−3に衝突して反転し、排気流EG1、EG2と交差して層流を変化させることは既述の通りである。これにより、排気流EG3と排気流EG2、排気流EG3と排気流EG1を攪拌させる。   If an overview of the transient laminar flow change is given, the exhaust flow EG1 collides with the baffle plates 24-1 and 24-2 and reverses, crosses the exhaust flow EG2, changes the laminar flow, and the exhaust flow EG3. Has collided with the baffle plate 24-3 and reversed to change the laminar flow by crossing the exhaust flows EG1 and EG2. As a result, the exhaust flow EG3 and the exhaust flow EG2, and the exhaust flow EG3 and the exhaust flow EG1 are agitated.

この層流拡散において、各邪魔板24−1、24−2、24−3が角度θ1、θ2、θ3の勾配を持つため、各層流に対する抵抗機能が緩和され、層流の方向を緩やかに変更させ、層流間の攪拌を行うことができる。   In this laminar flow diffusion, the baffle plates 24-1, 24-2, and 24-3 have gradients of angles θ1, θ2, and θ3, so that the resistance function to each laminar flow is relaxed and the direction of the laminar flow is changed gently. And stirring between laminar flows can be performed.

そして、斯かる攪拌により燃焼排気EGの排気流EG1、EG2、EG3は、層流方向、層流速度などの要素が絡み、各層流が乱される結果、燃焼排気EGは層流に偏りを生ずることなく、各熱交換管12に広く行き渡り、筐体4に流入した燃焼排気EGが被加熱流体Mの熱交換に供される。   As a result of such agitation, the exhaust flow EG1, EG2, EG3 of the combustion exhaust EG is entangled with elements such as the laminar flow direction and the laminar flow velocity, and each laminar flow is disturbed. The combustion exhaust gas EG that has spread widely to the heat exchange pipes 12 and has flowed into the housing 4 is used for heat exchange of the heated fluid M.

この実施の形態においても、邪魔板24−1、24−2、24−3は、熱交換管12の受熱部幅(燃焼排気EGと交差方向の幅)に跨がる単一板とする構成だけではなく、ヘッダ20−1、20−2に跨がる熱交換管12と平行に、その幅内でたとえば、既述の図2に示すように、邪魔板24−1を分断させ、複数の変流片にしてもよい。また、複数の変流片を備えた場合、各変流片は、天井板16と底面板18で位置を異ならせ、たとえば、千鳥状など交互に配置してもよく、燃焼排気EGの層流に複雑な変化を生じさせることができる。   Also in this embodiment, the baffle plates 24-1, 24-2, and 24-3 are configured as a single plate that spans the heat receiving portion width of the heat exchange pipe 12 (width in the direction intersecting with the combustion exhaust EG). In addition, the baffle plate 24-1 is divided in parallel with the heat exchange pipe 12 extending over the headers 20-1 and 20-2, for example, as shown in FIG. It may be a current piece. When a plurality of current transformation pieces are provided, the positions of the current transformation pieces are different between the ceiling plate 16 and the bottom plate 18 and may be alternately arranged, for example, in a staggered manner, or the laminar flow of the combustion exhaust EG. Can cause complex changes.

なお、邪魔板24−1、24−2の高さh1、h2をh1<h2とすれば、邪魔板24−1をすり抜けた排気流EG1を邪魔板24−2に衝突させ、層流変化を促進させることができることはこの実施の形態においても同様である。   If the heights h1 and h2 of the baffle plates 24-1 and 24-2 are h1 <h2, the exhaust flow EG1 that has passed through the baffle plate 24-1 collides with the baffle plate 24-2, and the laminar flow change is caused. The same can be said for this embodiment.

<第2の実施の形態の効果> <Effects of Second Embodiment>

(1) 第2の実施の形態に係る二次熱交換ユニット2によれば、給湯単能機、ふろ給湯機などの二次熱交換器で利用できる。   (1) According to the secondary heat exchange unit 2 according to the second embodiment, it can be used in a secondary heat exchanger such as a single hot water supply machine or a bath water heater.

(2) この実施の形態においても、熱交換管12に一系統の被加熱流体Mを流し、燃焼排気EGの持つ顕熱や潜熱の熱交換に利用できる。   (2) In this embodiment as well, a system of heated fluid M is allowed to flow through the heat exchange pipe 12 and can be used for heat exchange of sensible heat and latent heat of the combustion exhaust EG.

(3) この実施の形態の邪魔板24−1、24−2、24−3は燃焼排気EGの上流側から下流側に向かって傾斜しているので、排気流EG1、EG2、EG3に対して排気抵抗を下げることができ、排気効率の低下を防止できる。   (3) Since the baffle plates 24-1, 24-2, and 24-3 of this embodiment are inclined from the upstream side to the downstream side of the combustion exhaust EG, the baffle plates 24-1, 24-2, and 24-3 are inclined with respect to the exhaust flows EG1, EG2, and EG3. Exhaust resistance can be lowered, and a reduction in exhaust efficiency can be prevented.

(4) 邪魔板24−1、24−2、24−3で覆われる熱交換管12は、邪魔板24−1、24−2、24−3を伝熱フィンとして機能させることができ、受熱効率を高めることができる。   (4) The heat exchange pipe 12 covered with the baffle plates 24-1, 24-2 and 24-3 can cause the baffle plates 24-1, 24-2 and 24-3 to function as heat transfer fins and receive heat. Efficiency can be increased.

(5) 邪魔板24−1、24−2、24−3に角度θ1、θ2、θ3を設定したことにより、角度θ1、θ2、θ3に応じたなだらかな反射流を生じさせ、これら層流を排気流EG2に交差させて層流を攪乱させ、燃焼排気EGのすり抜けや偏りを防止することができる。   (5) By setting the angles θ1, θ2, and θ3 to the baffle plates 24-1, 24-2, and 24-3, a gentle reflected flow corresponding to the angles θ1, θ2, and θ3 is generated, and these laminar flows are By crossing the exhaust flow EG2, the laminar flow can be disturbed to prevent the combustion exhaust EG from slipping through and being biased.

(6) 筐体4内に流入する燃焼排気EGを筐体4内の全ての熱交換管12に絡ませて熱交換に供することができ、熱交換効率を高めることができる。   (6) The combustion exhaust EG flowing into the housing 4 can be entangled with all the heat exchange pipes 12 in the housing 4 for heat exchange, and the heat exchange efficiency can be improved.

〔第3の実施の形態〕 [Third Embodiment]

図4のAは、第3の実施の形態に係る二次熱交換ユニットの一例である。この二次熱交換ユニット2では第1または第2の実施の形態の邪魔板に代え、変流部材として複数の邪魔板34−1、34−2、34−3、34−4が備えられる。各邪魔板34−1、34−2、34−3、34−4は筐体4の排気導入部6から排出部8に向かって一定の間隔で配置され、邪魔板34−1、34−3が底面板18側、邪魔板34−2、34−4が天井板16側に配置されている。   FIG. 4A is an example of a secondary heat exchange unit according to the third embodiment. In this secondary heat exchange unit 2, instead of the baffle plate of the first or second embodiment, a plurality of baffle plates 34-1 34-2, 34-3 and 34-4 are provided as current transformation members. The baffle plates 34-1, 34-2, 34-3, and 34-4 are arranged at regular intervals from the exhaust introduction part 6 of the housing 4 toward the discharge part 8, and the baffle plates 34-1 and 34-3 are arranged. Are arranged on the bottom plate 18 side, and the baffle plates 34-2 and 34-4 are arranged on the ceiling plate 16 side.

邪魔板34−1は、底面板18側で高さ方向の位置が異なるとともに、排出部8に向かって前後する一対の熱交換管12に被せられており、天井板16に対して角度θ1の傾斜面を成している。   The baffle plate 34-1 has a position in the height direction that is different on the bottom plate 18 side, and is covered with a pair of heat exchange pipes 12 that move back and forth toward the discharge portion 8, and has an angle θ1 with respect to the ceiling plate 16. It has an inclined surface.

邪魔板34−2は、邪魔板34−1より排出部8側の天井板16側で高さ方向の位置が異なるとともに、排出部8に向かって前後する一対の熱交換管12に被せられており、底面板18に対して角度θ2の傾斜面を成している。   The baffle plate 34-2 is covered with a pair of heat exchange pipes 12 that are different from each other in the height direction on the ceiling plate 16 side on the discharge unit 8 side than the baffle plate 34-1 and back and forth toward the discharge unit 8. The bottom plate 18 is inclined with an angle θ2.

邪魔板34−3は、邪魔板34−2より排出部8側の底面板18側で高さ方向の位置が異なるとともに、排出部8に向かって前後する一対の熱交換管12に被せられており、天井板16に対して角度θ3の傾斜面を成している。   The baffle plate 34-3 is covered with a pair of heat exchange tubes 12 that are different from each other in the height direction on the bottom plate 18 side on the discharge unit 8 side than the baffle plate 34-2 and back and forth toward the discharge unit 8. It forms an inclined surface with respect to the ceiling plate 16 at an angle θ3.

邪魔板34−4は、邪魔板34−3より排出部8側の天井板16側で高さ方向の位置が異なるとともに、排出部8に向かって前後する一対の熱交換管12に被せられており、底面板18に対して角度θ4の傾斜面を成している。   The baffle plate 34-4 has a different position in the height direction on the ceiling plate 16 side on the discharge unit 8 side than the baffle plate 34-3, and is covered with a pair of heat exchange tubes 12 back and forth toward the discharge unit 8. The bottom plate 18 is inclined with an angle θ4.

これら角度θ1、θ2、θ3、θ4は、θ1=θ2=θ3=θ4でもよく、θ1≠θ2≠θ3≠θ4でもよい。   These angles θ1, θ2, θ3, and θ4 may be θ1 = θ2 = θ3 = θ4, or may be θ1 ≠ θ2 ≠ θ3 ≠ θ4.

各邪魔板34−1、34−2、34−3、34−4の幅Lxは、取り付けられる熱交換管12の直径および間隔に依存する。幅Lxは邪魔板34−1、34−2、34−3、34−4毎に異ならせてもよいし、一致させてもよい。   The width Lx of each baffle plate 34-1, 34-2, 34-3, 34-4 depends on the diameter and interval of the heat exchange pipe 12 to be attached. The width Lx may be different for each baffle plate 34-1, 34-2, 34-3, 34-4, or may be matched.

このような邪魔板34−1、34−2、34−3、34−4を備えれば、第1または第2の実施の形態と同様に、燃焼排気EGが排気流EG1、EG2、EG3を成し、これらに層流変化をもたらし、第1または第2の実施の形態の熱交換を行うことができる。   If such baffle plates 34-1, 34-2, 34-3, and 34-4 are provided, the combustion exhaust gas EG converts the exhaust flows EG1, EG2, and EG3, as in the first or second embodiment. Thus, laminar flow changes can be brought about, and the heat exchange of the first or second embodiment can be performed.

図4のBに示すように、排気流EG1が各邪魔板34−1、34−2に衝突して反転し、排気流EG2と交差して層流を変化させ、また、排気流EG3が邪魔板34−3に衝突して反転し、排気流EG1、EG2と交差して層流を変化させることは既述の通りである。これにより、排気流EG3と排気流EG2、排気流EG3と排気流EG1を攪拌させる。   As shown in FIG. 4B, the exhaust flow EG1 collides with the baffle plates 34-1 and 34-2 and reverses, crosses the exhaust flow EG2, changes the laminar flow, and the exhaust flow EG3 interferes. As described above, the plate 34-3 collides with the plate 34-3, reverses, and crosses the exhaust flows EG1 and EG2 to change the laminar flow. As a result, the exhaust flow EG3 and the exhaust flow EG2, and the exhaust flow EG3 and the exhaust flow EG1 are agitated.

この層流拡散において、各邪魔板34−1、34−2、34−3、34−4が角度θ1、θ2、θ3、θ4の勾配を持つため、各層流に対する抵抗機能が緩和され、層流の方向を緩やかに変更させ、層流間の攪拌を行うことができる。   In this laminar flow diffusion, the baffle plates 34-1, 34-2, 34-3, and 34-4 have gradients of angles θ1, θ2, θ3, and θ4. It is possible to gently change between the directions of the laminar flows.

そして、斯かる攪拌により燃焼排気EGの排気流EG1、EG2、EG3は、層流方向、層流速度などの要素が絡み、各層流が乱される結果、燃焼排気EGは層流に偏りを生ずることなく、各熱交換管12に広く行き渡り、筐体4に流入した燃焼排気EGが被加熱流体Mの熱交換に供される。   As a result of such agitation, the exhaust flow EG1, EG2, EG3 of the combustion exhaust EG is entangled with elements such as the laminar flow direction and the laminar flow velocity, and each laminar flow is disturbed. The combustion exhaust gas EG that has spread widely to the heat exchange pipes 12 and has flowed into the housing 4 is used for heat exchange of the heated fluid M.

この実施の形態においても、邪魔板34−1、34−2、34−3、34−4は、熱交換管12の受熱部幅(燃焼排気EGと交差方向の幅)に跨がる単一板とする構成だけではなく、ヘッダ20−1、20−2に跨がる熱交換管12と平行に、その幅内でたとえば、既述の図2に示すように、邪魔板34−1を分断させ、複数の変流片14−11、14−12としてもよい。また、複数の変流片を備えた場合、各変流片は、天井板16と底面板18で位置を異ならせ、たとえば、千鳥状など交互に配置してもよく、燃焼排気EGの層流に複雑な変化を生じさせることができる。   Also in this embodiment, the baffle plates 34-1, 34-2, 34-3, and 34-4 are single over the heat receiving portion width of the heat exchange pipe 12 (width in the direction crossing the combustion exhaust EG). In addition to the configuration of the plate, the baffle plate 34-1 is disposed within the width in parallel with the heat exchange pipe 12 extending over the headers 20-1 and 20-2, for example, as shown in FIG. It may be divided into a plurality of current-transforming pieces 14-11 and 14-12. When a plurality of current transformation pieces are provided, the positions of the current transformation pieces are different between the ceiling plate 16 and the bottom plate 18 and may be alternately arranged, for example, in a staggered manner, or the laminar flow of the combustion exhaust EG. Can cause complex changes.

なお、邪魔板34−1、34−2の高さh1、h2をh1<h2とすれば、邪魔板34−1をすり抜けた排気流EG1を邪魔板34−2に衝突させ、層流変化を促進させることができることはこの実施の形態においても同様である。   If the heights h1 and h2 of the baffle plates 34-1 and 34-2 are set to h1 <h2, the exhaust flow EG1 that has passed through the baffle plate 34-1 collides with the baffle plate 34-2, and the laminar flow change is caused. The same can be said for this embodiment.

<第3の実施の形態の効果> <Effect of the third embodiment>

(1) この実施の形態に係る二次熱交換ユニット2についても、給湯単能機、ふろ給湯機などの二次熱交換器で利用できる。   (1) The secondary heat exchange unit 2 according to this embodiment can also be used in a secondary heat exchanger such as a single hot water supply machine or a bath water heater.

(2) この実施の形態においても、第1または第2の実施の形態と同様に、熱交換管12に一系統の被加熱流体Mを流し、燃焼排気EGの持つ顕熱や潜熱の熱交換を行うことができる。   (2) In this embodiment as well, as in the first or second embodiment, a single heated fluid M is caused to flow through the heat exchange pipe 12 to exchange heat of sensible heat or latent heat of the combustion exhaust EG. It can be performed.

(3) 邪魔板34−1、34−2、34−3、34−4は、燃焼排気EGの上流側から下流側に向かって橋絡する平板部を備えて縁部を湾曲して熱交換管12に取り付けられている。このため、各邪魔板34−1、34−2、34−3、34−4の組み付けが容易である。   (3) The baffle plates 34-1, 34-2, 34-3, 34-4 are provided with a flat plate portion that bridges from the upstream side to the downstream side of the combustion exhaust EG, and the edges are curved to exchange heat. Attached to the tube 12. For this reason, the assembly of each baffle plate 34-1, 34-2, 34-3, 34-4 is easy.

(4) 各邪魔板34−1、34−2、34−3、34−4では、橋絡部分を媒介として排気流の燃焼排気EGの流路を変更させることができ、複数の熱交換管12の表面に密着させているので、伝熱フィンとして機能させることができ、熱交換効率を向上させることができる。つまり、邪魔板34−1、34−2、34−3、34−4が熱交換管12に密着しているので、伝熱性が高められる。   (4) In each baffle plate 34-1, 34-2, 34-3, 34-4, the flow path of the combustion exhaust EG of the exhaust flow can be changed through the bridge portion, and a plurality of heat exchange tubes Since it adheres to the surface of 12, it can be made to function as a heat-transfer fin, and heat exchange efficiency can be improved. That is, since the baffle plates 34-1, 34-2, 34-3, and 34-4 are in close contact with the heat exchange tube 12, the heat transfer is improved.

(5) 傾斜角度θ1、θ2、θ3を設定したことにより、角度θ1、θ2、θ3に応じたなだらかな反射流を生じさせ、これら層流を排気流に交差させて層流を乱すことができ、燃焼排気EGのすり抜けや偏りを防止できるとともに、その傾斜面に衝突した排気流を反射させて層流に絡ませることができ、燃焼排気EGを層流速度に応じて拡散させることができる。この拡散により、熱交換効率を向上させることができる。   (5) By setting the inclination angles θ1, θ2, and θ3, it is possible to generate a gentle reflected flow according to the angles θ1, θ2, and θ3, and to disrupt the laminar flow by crossing these laminar flows with the exhaust flow. Further, the exhaust gas EG can be prevented from slipping through and being biased, and the exhaust flow colliding with the inclined surface can be reflected and entangled with the laminar flow, and the combustion exhaust EG can be diffused according to the laminar flow velocity. This diffusion can improve the heat exchange efficiency.

(6) 筐体4内に流入する燃焼排気EGを筐体4内の全ての熱交換管12に絡ませて熱交換に供することができる。   (6) The combustion exhaust EG flowing into the housing 4 can be entangled with all the heat exchange tubes 12 in the housing 4 to be used for heat exchange.

(7) 熱交換管12に邪魔板34−1、34−2、34−3、34−4を取り付けて配置しているので、邪魔板34−1、34−2、34−3、34−4を熱交換管12に支持させることができ、邪魔板34−1、34−2、34−3、34−4の支持強度を高めることができる。邪魔板34−1、34−2、34−3、34−4はたとえば、肉厚の薄い軽量部材で形成でき、軽量化を図ることができる。   (7) Since the baffle plates 34-1, 34-2, 34-3, 34-4 are attached to the heat exchange pipe 12, the baffle plates 34-1, 34-2, 34-3, 34- 4 can be supported by the heat exchange pipe 12, and the support strength of the baffle plates 34-1, 34-2, 34-3, 34-4 can be increased. The baffle plates 34-1, 34-2, 34-3, and 34-4 can be formed of, for example, a thin member having a small thickness, and the weight can be reduced.

(8) 邪魔板34−1、34−2、34−3、34−4の二次熱交換ユニット2に占める割合を低減でき、邪魔板による容積専有率を低減できる。   (8) The ratio of the baffle plates 34-1, 34-2, 34-3, 34-4 to the secondary heat exchange unit 2 can be reduced, and the volume occupation rate by the baffle plates can be reduced.

(9) 邪魔板34−1、34−2、34−3、34−4のエッジ側を熱交換管12の外周と同心円面に形成すれば、流体抵抗を低減できる。   (9) If the edge sides of the baffle plates 34-1, 34-2, 34-3, 34-4 are formed concentrically with the outer periphery of the heat exchange tube 12, the fluid resistance can be reduced.

〔第4の実施の形態〕 [Fourth Embodiment]

図5のAは、第4の実施の形態に係る二次熱交換ユニットを示している。第1ないし第3の実施の形態では単一系統の熱交換部のみであったのに対し、筐体4に燃焼排気EGの上流側に第1系統の熱交換部10−1、その下流側に第2系統の熱交換部10−2を備えている。熱交換部10−1には第1の被加熱流体M1を通流する複数の熱交換管12−1、熱交換部10−2には第2の被加熱流体M2を通流する複数の熱交換管12−2が備えられる。   FIG. 5A shows a secondary heat exchange unit according to the fourth embodiment. In the first to third embodiments, there is only a single system heat exchanging section, whereas the casing 4 has a first system heat exchanging section 10-1 upstream of the combustion exhaust EG, and its downstream side. Is provided with a second system heat exchange section 10-2. A plurality of heat exchange pipes 12-1 that flow through the first heated fluid M1 through the heat exchange unit 10-1, and a plurality of heats through the second heated fluid M2 through the heat exchange unit 10-2. An exchange tube 12-2 is provided.

この実施の形態では、天井板16に単一の邪魔板44−1が備えられ、この邪魔板44−1が熱交換部10−1と熱交換部10−2の間に垂下状態で設置されている。   In this embodiment, the ceiling plate 16 is provided with a single baffle plate 44-1, and this baffle plate 44-1 is installed in a suspended state between the heat exchange unit 10-1 and the heat exchange unit 10-2. ing.

斯かる構成によれば、図5のBに示すように、燃焼排気EGの排気流EG1側に対し、邪魔板44−1が反射板として機能させる。邪魔板44−1に衝突した排気流EG1は邪魔板44−1で跳ね返り、排気流EG2または排気流EG3に衝突し、燃焼排気EGを拡散させる。   According to such a configuration, as shown in B of FIG. 5, the baffle plate 44-1 functions as a reflecting plate with respect to the exhaust flow EG1 side of the combustion exhaust EG. The exhaust flow EG1 colliding with the baffle plate 44-1 rebounds at the baffle plate 44-1, collides with the exhaust flow EG2 or the exhaust flow EG3, and diffuses the combustion exhaust EG.

<第4の実施の形態の効果> <Effect of the fourth embodiment>

(1) 第4の実施の形態の二次熱交換ユニット2によれば、一缶三水型の暖房給湯機などの二次熱交換器に利用できる。   (1) According to the secondary heat exchange unit 2 of the fourth embodiment, the secondary heat exchange unit 2 can be used for a secondary heat exchanger such as a single-can three-water type heating water heater.

(2) 熱交換部10−1の熱交換管12−1にはたとえば、暖房放熱用の熱媒M1を循環させ、熱交換部10−2の熱交換管12−2にはたとえば、給水Wを循環させ、給湯の予備加熱に利用することができる。   (2) For example, heating medium M1 for heating and radiating heat is circulated in the heat exchange pipe 12-1 of the heat exchange unit 10-1, and water supply W is provided in the heat exchange pipe 12-2 of the heat exchange unit 10-2. Can be circulated and used for preheating hot water.

(3) 熱交換部10−1と熱交換部10−2の間に邪魔板44−1を備えたことにより、燃焼排気EGの主として排気流EG1を衝突させ、この排気流EG1を排気流EG2または排気流EG3側に押し下げて交差させ、燃焼排気EGの拡散を促進させることができる。   (3) By providing the baffle plate 44-1 between the heat exchanging unit 10-1 and the heat exchanging unit 10-2, the exhaust flow EG1 of the combustion exhaust EG is collided mainly, and this exhaust flow EG1 is used as the exhaust flow EG2. Alternatively, the exhaust gas EG3 can be pushed down and intersected to promote the diffusion of the combustion exhaust gas EG.

(4) 燃焼排気EGの拡散により、燃焼排気EGが上流側にある熱交換部10−1の全体の熱交換管12−1に当たり、熱交換部10−1の全体で燃焼排気EGの熱交換を行うことができる。この熱交換は、燃焼排気EGの排気量にかかわらず行えるので、熱交換効率を高めることができる。   (4) Due to the diffusion of the combustion exhaust EG, the combustion exhaust EG hits the entire heat exchange pipe 12-1 of the heat exchange unit 10-1 on the upstream side, and the heat exchange of the combustion exhaust EG in the entire heat exchange unit 10-1. It can be performed. Since this heat exchange can be performed regardless of the displacement of the combustion exhaust EG, the heat exchange efficiency can be improved.

(5) 下流側の熱交換部10−2の熱交換管12−2には燃焼排気EGが拡散されて当たるので、熱交換部10−2においても熱交換効率を高めることができる。   (5) Since the combustion exhaust EG is diffused and hits the heat exchange pipe 12-2 of the heat exchange unit 10-2 on the downstream side, the heat exchange efficiency can be increased also in the heat exchange unit 10-2.

(6) 下流側の熱交換部10−2の熱交換管12−2に対して高温の燃焼排気EGの偏りを防止でき、熱交換部10−2の上流側にある熱交換管12−2に循環する被加熱流体の部分沸騰を防止できる。   (6) The bias of the high-temperature combustion exhaust EG can be prevented with respect to the heat exchange pipe 12-2 of the heat exchange section 10-2 on the downstream side, and the heat exchange pipe 12-2 on the upstream side of the heat exchange section 10-2 It is possible to prevent partial boiling of the heated fluid circulating in the tank.

〔第5の実施の形態〕 [Fifth Embodiment]

図6のAは、第5の実施の形態に係る二次熱交換ユニットを示している。この二次熱交換ユニット2では、第4の実施の形態に係る二次熱交換ユニット2にある邪魔板44−1に加え、熱交換部10−2側に邪魔板44−2、44−3が備えられる。   FIG. 6A shows a secondary heat exchange unit according to the fifth embodiment. In this secondary heat exchange unit 2, in addition to the baffle plate 44-1 in the secondary heat exchange unit 2 according to the fourth embodiment, the baffle plates 44-2, 44-3 on the heat exchange unit 10-2 side. Is provided.

邪魔板44−2は、筐体4の底面板18側に立設され、邪魔板44−3は、筐体4の天井板16側に垂下状態に立設されている。この例では、邪魔板44−1、44−3の中間位置に邪魔板44−2が配置されている。   The baffle plate 44-2 is erected on the bottom plate 18 side of the housing 4, and the baffle plate 44-3 is erected on the ceiling plate 16 side of the housing 4. In this example, the baffle plate 44-2 is disposed at an intermediate position between the baffle plates 44-1 and 44-3.

係る構成では、図6のBに示すように、邪魔板44−1に燃焼排気EGの主として排気流EG1が衝突し、流路が変更される。邪魔板44−2に燃焼排気EGの主として排気流EG3が衝突し、流路が変更される。邪魔板44−3に燃焼排気EGの主として排気流EG1が衝突し、流路が変更される。このような流路の変更により、排気流EG1が熱交換部10−1の熱交換管12−1に絡むことは第4の実施の形態と同様である。排気流EG2、EG3は熱交換部10−2の熱交換管12−2に絡む。また、流路を変更された各排気流EG1、EG2、EG3を拡散して各熱交換管12−1、12−2に絡み、被加熱流体との熱交換に寄与する。   In such a configuration, as shown in FIG. 6B, the exhaust flow EG1 of the combustion exhaust EG mainly collides with the baffle plate 44-1, and the flow path is changed. The exhaust flow EG3 of the combustion exhaust EG mainly collides with the baffle plate 44-2, and the flow path is changed. The exhaust flow EG1 of the combustion exhaust EG mainly collides with the baffle plate 44-3, and the flow path is changed. It is the same as in the fourth embodiment that the exhaust flow EG1 is entangled with the heat exchange pipe 12-1 of the heat exchange unit 10-1 by such a change in the flow path. The exhaust flows EG2 and EG3 are entangled with the heat exchange pipe 12-2 of the heat exchange unit 10-2. Further, the exhaust flows EG1, EG2, and EG3 whose flow paths are changed are diffused and entangled with the heat exchange tubes 12-1 and 12-2, thereby contributing to heat exchange with the heated fluid.

<第5の実施の形態の効果> <Effect of Fifth Embodiment>

(1) 第5の実施の形態の熱交換ユニット2によれば、第4の実施の形態と同様に、一缶三水型の暖房給湯機などの二次熱交換器に利用することができる。   (1) According to the heat exchange unit 2 of the fifth embodiment, as in the fourth embodiment, the heat exchange unit 2 can be used for a secondary heat exchanger such as a single-can three-water heating water heater. .

(2) 熱交換部10−1では第4の実施の形態と同様に邪魔板44−1による排気流EG1の流路変更による効果が得られ、さらに、熱交換部10−2では燃焼排気EGのすり抜けを防止でき、熱交換効率を高めることができる。   (2) In the heat exchanging unit 10-1, the effect of changing the flow path of the exhaust flow EG1 by the baffle plate 44-1 is obtained as in the fourth embodiment, and further, in the heat exchanging unit 10-2, the combustion exhaust EG Can be prevented, and the heat exchange efficiency can be improved.

〔第6の実施の形態〕 [Sixth Embodiment]

図7のAは、第6の実施の形態に係る二次熱交換ユニットを示している。この二次熱交換ユニット2では第4の実施の形態の二次熱交換ユニット2の邪魔板44−1と同様の位置に邪魔板54−1が備えられる。邪魔板44−1では天井板16から底面板18に向かって垂下する垂直板であるのに対し、邪魔板54−1では天井板16から底面板18に向かって垂下するとともに、燃焼排気EGの流れ方向と対抗方向に湾曲する面を持つ円弧板が用いられている。   FIG. 7A shows a secondary heat exchange unit according to the sixth embodiment. In the secondary heat exchange unit 2, a baffle plate 54-1 is provided at the same position as the baffle plate 44-1 of the secondary heat exchange unit 2 of the fourth embodiment. The baffle plate 44-1 is a vertical plate that hangs down from the ceiling plate 16 toward the bottom plate 18, whereas the baffle plate 54-1 hangs down from the ceiling plate 16 toward the bottom plate 18, and the combustion exhaust EG A circular arc plate having a surface curved in a direction opposite to the flow direction is used.

このような邪魔板54−1を備えれば、図7のBに示すように、邪魔板54−1に衝突した主として排気流EG1は、その湾曲面に沿って流路が曲げられ、垂直板に比較して排気流EG1の滞留ないし渦を生じさせ、他の主として排気流EG2との交差による拡散を助長させることができる。   If such a baffle plate 54-1 is provided, as shown in FIG. 7B, the exhaust flow EG1 that has collided with the baffle plate 54-1 has its flow path bent along its curved surface, and a vertical plate. Compared to the above, the stagnation or vortex of the exhaust flow EG1 can be generated, and the diffusion mainly due to the intersection with the exhaust flow EG2 can be promoted.

<第6の実施の形態の効果> <Effect of the sixth embodiment>

(1) この第6の実施の形態の熱交換ユニット2によれば、第5の実施の形態と同様に、一缶三水型の暖房給湯機などの二次熱交換器に利用して同様の効果が得られる。   (1) According to the heat exchange unit 2 of the sixth embodiment, as in the fifth embodiment, the heat exchange unit 2 is used for a secondary heat exchanger such as a single-can three-water type heating water heater. The effect is obtained.

(2) 邪魔板54−1が湾曲面を備えているので、主として衝突する排気流EG1が湾曲面に沿って曲げられ、排気流EG1がすり抜けることなく、熱交換部10−1の各熱交換管12−1すなわち、天井板16側および底面板18側にある熱交換管12−1に区別なく絡み、被加熱流体の熱交換に寄与する。   (2) Since the baffle plate 54-1 has a curved surface, the colliding exhaust flow EG1 is bent along the curved surface, and the heat exchange of the heat exchanging unit 10-1 does not pass through the exhaust flow EG1. The tube 12-1, that is, the heat exchange tube 12-1 on the ceiling plate 16 side and the bottom plate 18 side is entangled without distinction and contributes to heat exchange of the fluid to be heated.

(4) 燃焼排気EGの高温排気と熱交換部10−1の熱交換を促進でき、熱交換後の燃焼排気EGが拡散されて下流側の熱交換部10−2の熱交換管12−2に絡ませることができる。   (4) The heat exchange between the high-temperature exhaust gas of the combustion exhaust EG and the heat exchange unit 10-1 can be promoted, and the combustion exhaust EG after the heat exchange is diffused and the heat exchange pipe 12-2 of the downstream heat exchange unit 10-2 Can be entangled with.

(5) 熱交換部10−1の熱交換管12−1との熱交換を経た燃焼排気EGを下流側の熱交換部10−2に流すことができるので、熱交換部10−2の上流側にある熱交換管12−2に循環する被加熱流体の部分沸騰を防止できる。   (5) Since the combustion exhaust EG that has undergone heat exchange with the heat exchange pipe 12-1 of the heat exchange unit 10-1 can flow to the heat exchange unit 10-2 on the downstream side, upstream of the heat exchange unit 10-2 It is possible to prevent partial boiling of the heated fluid circulating in the heat exchange pipe 12-2 on the side.

〔第7の実施の形態〕 [Seventh Embodiment]

図8のAは、第7の実施の形態に係る二次熱交換ユニットを示している。この二次熱交換ユニット2では、図7のAに示した第6の実施の形態に係る二次熱交換ユニット2にある邪魔板54−1に加え、熱交換部10−1の入口側に邪魔板54−2を備えている。   FIG. 8A shows a secondary heat exchange unit according to the seventh embodiment. In this secondary heat exchange unit 2, in addition to the baffle plate 54-1 in the secondary heat exchange unit 2 according to the sixth embodiment shown in FIG. 7A, on the inlet side of the heat exchange unit 10-1. A baffle plate 54-2 is provided.

邪魔板54−2は邪魔板54−1と同様に湾曲面を持つ円弧板であり、湾曲方向を邪魔板54−1と向き合わせている。つまり、邪魔板54−2の背面側に凸の湾曲面を備えており、この湾曲面を排気導入部6に対向させている。   The baffle plate 54-2 is a circular arc plate having a curved surface like the baffle plate 54-1, and the curved direction faces the baffle plate 54-1. That is, a convex curved surface is provided on the back side of the baffle plate 54-2, and this curved surface is opposed to the exhaust introduction part 6.

このように、排気導入部6側に邪魔板54−2を備えれば、図8のBに示すように、燃焼排気EGの主として排気流EG2、EG3が邪魔板54−2の湾曲面に当たり、流路が変更される。流路変更を伴った排気流EG2、EG3は排気導入部6側の天井板16および背面部から邪魔板54−1に至る。これにより、排気流EG2、EG3は排気流EG1と拡散し、熱交換部10−1の熱交換管12−1に絡んで通流させ、熱交換後の燃焼排気EGが拡散状態で熱交換部10−2に流れる。   Thus, if the baffle plate 54-2 is provided on the exhaust introduction part 6 side, as shown in FIG. 8B, the exhaust flow EG2, EG3 of the combustion exhaust EG mainly hits the curved surface of the baffle plate 54-2, The flow path is changed. The exhaust flows EG2 and EG3 accompanied by the flow path change reach the baffle plate 54-1 from the ceiling plate 16 and the back surface on the exhaust introduction portion 6 side. As a result, the exhaust flows EG2 and EG3 are diffused with the exhaust flow EG1, and are entangled with the heat exchange pipe 12-1 of the heat exchange unit 10-1, so that the combustion exhaust EG after the heat exchange is diffused and the heat exchange unit It flows to 10-2.

<第7の実施の形態の効果> <Effect of the seventh embodiment>

(1) 第7の実施の形態に係る二次熱交換ユニット2によれば、上記実施の形態の二次熱交換ユニットと同様に一缶三水型の暖房給湯機などの二次熱交換器として用いることができる。   (1) According to the secondary heat exchange unit 2 according to the seventh embodiment, a secondary heat exchanger such as a single can three-water type heating water heater as in the secondary heat exchange unit of the above embodiment. Can be used as

(2) 邪魔板54−1、54−2の双方を備えたことにより、燃焼室から導入された燃焼排気EGを排気導入部6側にある熱交換部10−1の熱交換管12−1に滞留させるとともに攪拌を行い、熱交換部10−1側で熱交換を充分に行い、熱交換後の燃焼排気を熱交換部10−2側に導くことができる。   (2) By providing both the baffle plates 54-1 and 54-2, the combustion exhaust EG introduced from the combustion chamber is used as the heat exchange pipe 12-1 of the heat exchange unit 10-1 on the exhaust introduction unit 6 side. And the agitation, and sufficient heat exchange is performed on the heat exchange unit 10-1 side, and the combustion exhaust after the heat exchange can be guided to the heat exchange unit 10-2 side.

〔第8の実施の形態〕 [Eighth Embodiment]

図9は、第8の実施の形態に係る熱源機を示している。この熱源機60は一缶三水型の熱源機の一例である。この熱源機60は一次熱交換器側の筐体62の上側に第1の実施の形態に係る二次熱交換ユニット2(図1)が設置されている。   FIG. 9 shows a heat source machine according to the eighth embodiment. The heat source unit 60 is an example of a can-and-water type heat source unit. In the heat source device 60, the secondary heat exchange unit 2 (FIG. 1) according to the first embodiment is installed on the upper side of the casing 62 on the primary heat exchanger side.

筐体62には燃焼室64が備えられ、この燃焼室64にはバーナー66とともに一次熱交換器68が備えられる。バーナー66の下側には給気ファン70が設置され、燃焼室64の下側から燃焼用空気がバーナー66に供給される。   The casing 62 is provided with a combustion chamber 64, and the combustion chamber 64 is provided with a burner 66 and a primary heat exchanger 68. An air supply fan 70 is installed below the burner 66, and combustion air is supplied to the burner 66 from below the combustion chamber 64.

一次熱交換器68の熱交換管72には二次熱交換部10の熱交換管12が連結される。熱交換管12で燃焼排気EGの潜熱などにより予備加熱された被加熱流体たとえば、暖房水Mが通流する。   The heat exchange pipe 12 of the secondary heat exchange unit 10 is connected to the heat exchange pipe 72 of the primary heat exchanger 68. A fluid to be heated, such as heating water M, preheated by the latent heat of the combustion exhaust gas EG in the heat exchange pipe 12 flows.

係る構成によれば、燃料ガスGの燃焼によりバーナー66で生じた燃焼排気EGは、給気ファン70の給気により、一次熱交換器68を通過した後、燃焼室64から排気導入部6を通ってより二次熱交換ユニット2に導入される。   According to such a configuration, the combustion exhaust EG generated in the burner 66 by the combustion of the fuel gas G passes through the primary heat exchanger 68 by the supply of the supply fan 70, and then passes through the exhaust introduction unit 6 from the combustion chamber 64. It is introduced into the secondary heat exchange unit 2 through.

一次熱交換器68の熱交換管72では、上流側の燃焼排気EGを受け、燃焼排気EGが持つ顕熱と被加熱流体たとえば、暖房水Mとの一次熱交換が行われる。この一次熱交換を経た燃焼排気EGは二次熱交換ユニット2に流れ、熱交換部10で二次熱交換が行われた後、排出部8より外気に放出される。   The heat exchange pipe 72 of the primary heat exchanger 68 receives the upstream combustion exhaust EG, and performs primary heat exchange between the sensible heat of the combustion exhaust EG and the fluid to be heated, for example, the heating water M. The combustion exhaust gas EG that has undergone the primary heat exchange flows into the secondary heat exchange unit 2, undergoes secondary heat exchange in the heat exchange unit 10, and is then discharged from the discharge unit 8 to the outside air.

二次熱交換ユニット2での燃焼排気EGの流路変更や拡散については第1の実施形態で詳述しているので、その説明を割愛する。   Since the flow path change and diffusion of the combustion exhaust EG in the secondary heat exchange unit 2 are described in detail in the first embodiment, the description thereof is omitted.

<第8の実施の形態の効果> <Effect of the eighth embodiment>

この熱源機60によれば、燃焼排気EGと被加熱流体との熱交換効率を高めることができるとともに、熱源機60の熱効率を高めることができ、コンパクト化を図ることができる。   According to the heat source unit 60, the heat exchange efficiency between the combustion exhaust EG and the fluid to be heated can be increased, the thermal efficiency of the heat source unit 60 can be increased, and the size reduction can be achieved.

<第1の実施例> <First embodiment>

図10のAは、第1の実施例に係る二次熱交換ユニットを示している。この二次熱交換ユニット80は、第6の実施形態に係る二次熱交換ユニット2(図7)を具体化したものである。   FIG. 10A shows the secondary heat exchange unit according to the first embodiment. This secondary heat exchange unit 80 embodies the secondary heat exchange unit 2 (FIG. 7) according to the sixth embodiment.

この二次熱交換ユニット80にはユニット筐体82が備えられ、このユニット筐体82の上面部に天井板84が備えられ、この天井板84と平行な底面板86が備えられている。天井板84と底面板86との間に排気空間88が形成されている。   The secondary heat exchange unit 80 is provided with a unit case 82, a ceiling plate 84 is provided on the upper surface of the unit case 82, and a bottom plate 86 parallel to the ceiling plate 84 is provided. An exhaust space 88 is formed between the ceiling plate 84 and the bottom plate 86.

底面板86には排気導入部90が開口され、この排気導入部90の上側に排気ガイド92が形成されている。燃焼排気EGは排気ガイド92に当たり、排気空間88に導かれる。   An exhaust introduction portion 90 is opened in the bottom plate 86, and an exhaust guide 92 is formed above the exhaust introduction portion 90. The combustion exhaust EG hits the exhaust guide 92 and is guided to the exhaust space 88.

排気空間88には第1の熱交換部94−1、第2の熱交換部94−2が第1の熱交換部94−1を燃焼排気EGの上流側にして配置されている。天井板84には、熱交換部94−2側に下方に突出する膨出部96が備えられ、底面板86は排気部98側に傾斜する傾斜面を成し、排気部98側にドレン溜め100が底面板86により形成されている。   In the exhaust space 88, a first heat exchange section 94-1 and a second heat exchange section 94-2 are arranged with the first heat exchange section 94-1 on the upstream side of the combustion exhaust EG. The ceiling plate 84 is provided with a bulging portion 96 that protrudes downward on the heat exchanging portion 94-2 side, and the bottom plate 86 forms an inclined surface that is inclined on the exhaust portion 98 side, and a drain reservoir on the exhaust portion 98 side. 100 is formed by a bottom plate 86.

熱交換部94−1には熱交換管102−1の集合体が配置され、熱交換部94−2には熱交換管102−2の集合体が配置されている。熱交換部94−2と熱交換部94−1とを分離させる邪魔板104が排気ガイド92に向かって備えられる。   An assembly of heat exchange tubes 102-1 is disposed in the heat exchange unit 94-1, and an assembly of heat exchange tubes 102-2 is disposed in the heat exchange unit 94-2. A baffle plate 104 that separates the heat exchange unit 94-2 and the heat exchange unit 94-1 is provided toward the exhaust guide 92.

係る構成によれば、図10のBに示すように、燃焼室側から排気導入部90に導入される燃焼排気EGは排気ガイド92により流路方向が変えられて熱交換部94−1の熱交換管102−1を通過し、主として排気流EG1が邪魔板104により跳ね返り、再び熱交換部94−1の熱交換管102−1に絡む。これにより、燃焼排気EGの滞留と拡散とが行われ、熱交換管102−1を流れる被加熱流体との熱交換が行われる。   According to such a configuration, as shown in FIG. 10B, the flow direction of the combustion exhaust EG introduced from the combustion chamber side into the exhaust introduction section 90 is changed by the exhaust guide 92, and the heat of the heat exchange section 94-1 is obtained. Passing through the exchange pipe 102-1, the exhaust flow EG1 mainly bounces off by the baffle plate 104, and is entangled with the heat exchange pipe 102-1 of the heat exchange section 94-1 again. Thereby, the combustion exhaust gas EG is retained and diffused, and heat exchange with the heated fluid flowing through the heat exchange pipe 102-1 is performed.

<第1の実施例の効果> <Effect of the first embodiment>

(1) この熱交換後の燃焼排気EGは、熱交換部94−2側に流れ、邪魔板104による燃焼排気EGの流路変更により、熱交換管102−1での熱交換前に熱交換部94−2の上流側の熱交換管102−2に当たるのが回避される。   (1) The combustion exhaust EG after this heat exchange flows to the heat exchange section 94-2 side, and heat exchange is performed before heat exchange in the heat exchange pipe 102-1 by changing the flow path of the combustion exhaust EG by the baffle plate 104. Contact with the heat exchange pipe 102-2 on the upstream side of the section 94-2 is avoided.

(2) 上流側の熱交換管102−2側での被加熱流体の部分沸騰を防止できる。   (2) Partial boiling of the fluid to be heated on the heat exchange pipe 102-2 side on the upstream side can be prevented.

<第2の実施例> <Second embodiment>

図11は、第2の実施例に係る熱源機を示している。この熱源機において、第8の実施の形態の熱源機60および第1の実施例の二次熱交換ユニット80と同一部分には同一符号を付し、その説明を割愛する。   FIG. 11 shows a heat source apparatus according to the second embodiment. In this heat source unit, the same parts as those of the heat source unit 60 of the eighth embodiment and the secondary heat exchange unit 80 of the first example are denoted by the same reference numerals, and description thereof is omitted.

一次熱交換器68には複数の熱交換管72が設置され、各熱交換管72には複数の共通の吸熱フィン106が備えられる。各熱交換管72には燃焼排気EGの熱が吸熱されるとともに、吸熱フィン106に吸熱された熱が各熱交換管72に伝達される。各吸熱フィン106は、各熱交換管72の加熱状態を一様化する熱伝導機能を備える。   The primary heat exchanger 68 is provided with a plurality of heat exchange tubes 72, and each heat exchange tube 72 is provided with a plurality of common heat absorbing fins 106. Each heat exchange pipe 72 absorbs the heat of the combustion exhaust EG, and the heat absorbed by the heat absorption fins 106 is transmitted to each heat exchange pipe 72. Each heat absorption fin 106 has a heat conduction function for making the heating state of each heat exchange tube 72 uniform.

筐体62の上部には二次熱交換ユニット80が設置され、この二次熱交換ユニット80と筐体62の間には着座フレーム部108が備えられる。この着座フレーム部108は二次熱交換ユニット80の高さ調整機能を備えており、この実施例では、二次熱交換ユニット80の筐体62のドレン溜め100側を低く、その排気導入部90側が高く設定されている。これにより、熱交換により生じたドレンがドレン溜め100側に流れて蓄積される。   A secondary heat exchange unit 80 is installed on the top of the housing 62, and a seating frame portion 108 is provided between the secondary heat exchange unit 80 and the housing 62. The seating frame portion 108 has a function of adjusting the height of the secondary heat exchange unit 80. In this embodiment, the drain reservoir 100 side of the casing 62 of the secondary heat exchange unit 80 is lowered, and the exhaust introduction portion 90. The side is set high. Thereby, the drain produced by heat exchange flows and accumulates on the drain reservoir 100 side.

<第2の実施例の効果> <Effect of the second embodiment>

この筐体62によれば、既述の二次熱交換ユニット2の効果が得られるとともに、熱源機60の小型化および堅牢化を図ることができる。   According to the case 62, the effects of the secondary heat exchange unit 2 described above can be obtained, and the heat source device 60 can be made smaller and more robust.

<第3の実施例> <Third embodiment>

図12は、第3の実施例に係る給湯装置を示している。図12において、図11と同一部分には同一符号を付してある。   FIG. 12 shows a hot water supply apparatus according to the third embodiment. In FIG. 12, the same parts as those of FIG.

この給湯装置200は、熱源機60(図11)を備えて給湯機能、暖房機能および浴槽水追焚機能を備える。この給湯装置200は既述の一缶三水型の熱源機60を使用し、暖房水Mと燃焼排気EGとの熱交換、暖房水Mを熱媒として使用し、給水Wとの熱交換による温水HWの給湯、暖房水Mと浴槽水BWとの熱交換による浴槽水BWの給水および追焚機能を実現している。   This hot water supply apparatus 200 includes a heat source device 60 (FIG. 11) and has a hot water supply function, a heating function, and a bathtub water replenishment function. This hot water supply device 200 uses the above-described one-can three-water type heat source unit 60, exchanges heat between the heating water M and the combustion exhaust EG, uses the heating water M as a heat medium, and exchanges heat with the supply water W. The hot water supply of the hot water HW, the water supply of the bathtub water BW by the heat exchange with the heating water M, and the bathtub water BW, and the memorial function are implement | achieved.

暖房水Mの循環回路202に付した斜線部分は、ガス消費のための所定時間の継続燃焼を行う際に熱媒を循環させる循環路部である。バーナー66の燃焼時、循環する熱媒HMの循環経路が長くとられ、これにより、暖房水Mの容量が多く、燃焼熱の熱交換により沸騰に至るまでの燃焼継続時間を延長している。そして、循環回路202には暖房水タンク204が備えられ、この暖房水タンク204に暖房水Mが溜められる。   A hatched portion attached to the circulation circuit 202 of the heating water M is a circulation path portion for circulating the heat medium when performing continuous combustion for a predetermined time for gas consumption. When the burner 66 is combusted, the circulation path of the circulating heat medium HM is made longer, whereby the capacity of the heating water M is large, and the combustion continuation time until the boiling is reached by heat exchange of the combustion heat is extended. The circulation circuit 202 is provided with a heating water tank 204, and the heating water M is stored in the heating water tank 204.

給水口206には給水路208が接続され、上水などの給水Wが供給される。この給水Wにより、出湯口210から温水HWの出湯が可能である。給水路208および追焚循環路212は注湯管路214によって連結されており、浴槽注湯時、給水路208から温水HWが注湯管路214より追焚循環路212に流れ、浴槽216に注湯される。この注湯は、給湯と同様に上水の一例である水Wの給水であるから、給湯の一態様である。   A water supply path 208 is connected to the water supply port 206 and water supply W such as clean water is supplied. With this water supply W, hot water HW can be discharged from the hot water outlet 210. The water supply path 208 and the supplemental circulation path 212 are connected by a pouring pipe line 214, and at the time of bath pouring, hot water HW flows from the water supply path 208 to the memorial circuit 212 and flows into the bathtub 216. It is poured. Since this pouring is water supply of water W, which is an example of clean water, like hot water supply, it is an aspect of hot water supply.

循環回路202の分岐管218−1、218−2、218−3には暖房放熱端末220の一例として、熱媒HMが持つ熱を放熱する低温端末220−1や高温端末220−2が接続されている。   The branch pipes 218-1, 218-2, and 218-3 of the circulation circuit 202 are connected to a low-temperature terminal 220-1 and a high-temperature terminal 220-2 that radiate the heat of the heating medium HM as an example of the heating and radiating terminal 220. ing.

熱源機60には、一次熱交換器68、二次熱交換ユニット80側に暖房二次熱交換器222−1、給湯二次熱交換222−2が備えられている。これらの詳細は、既述の通りであるので説明は割愛する。   The heat source unit 60 includes a primary heat exchanger 68, and a heating secondary heat exchanger 222-1 and a hot water supply secondary heat exchange 222-2 on the secondary heat exchange unit 80 side. Since these details are as described above, the description is omitted.

循環回路202には一次熱交換器68、暖房二次熱交換器222−1、給湯熱交換器224−1および浴槽水熱交換器224−2が備えられる。暖房二次熱交換器222−1で熱交換された暖房水Mが一次熱交換器68により燃焼排気EGと熱交換される。給湯熱交換器224−1はたとえば、プレート熱交換器であり、二次熱交換ユニット80の給湯二次熱交換器222−2で予備加熱を経た給水Wと、熱媒としての暖房水Mとの熱交換を行う。給湯熱交換器224−2はたとえば、プレート熱交換器であり、浴槽水BWと、熱媒としての暖房水Mとの熱交換を行う。   The circulation circuit 202 includes a primary heat exchanger 68, a heating secondary heat exchanger 222-1, a hot water supply heat exchanger 224-1, and a bathtub water heat exchanger 224-2. Heating water M heat-exchanged in the heating secondary heat exchanger 222-1 is heat-exchanged with the combustion exhaust gas EG by the primary heat exchanger 68. The hot water supply heat exchanger 224-1 is, for example, a plate heat exchanger, and water supply W that has been preheated in the hot water supply secondary heat exchanger 222-2 of the secondary heat exchange unit 80, and heating water M as a heat medium, Heat exchange. Hot water supply heat exchanger 224-2 is, for example, a plate heat exchanger, and performs heat exchange between bathtub water BW and heating water M as a heat medium.

この実施例では、リモコン装置226がたとえば、浴室リモコン226−1や台所リモコン226−2で構成される。   In this embodiment, the remote control device 226 includes, for example, a bathroom remote control 226-1 and a kitchen remote control 226-2.

<第3の実施例の効果> <Effect of the third embodiment>

(1) この給湯装置200によれば、既述の二次熱交換ユニット80および熱源機60と同様の効果が得られるとともに、給湯装置200のコンパクト化を図ることができる。   (1) According to the hot water supply device 200, the same effects as those of the secondary heat exchange unit 80 and the heat source device 60 described above can be obtained, and the hot water supply device 200 can be made compact.

(2) 給湯、浴槽水の追焚き、暖房水の加熱時、これらの部分沸騰を防止することができ、信頼性の高い給湯、暖房および追焚き動作が得られる。   (2) During boiling water supply, bath water reheating, and heating water heating, these partial boiling can be prevented, and highly reliable hot water supply, heating and reheating operations can be obtained.

〔他の実施の形態〕 [Other Embodiments]

a) 第2の実施例および第3の実施例では、単一の一次熱交換器68を備えて暖房水の加熱に用いているが、一次熱交換器68を複数化し、暖房水および浴槽水の双方を一次加熱によって実現する構成としてもよい。   a) In the second embodiment and the third embodiment, a single primary heat exchanger 68 is provided and used for heating water. However, a plurality of primary heat exchangers 68 are provided, and heating water and bathtub water are used. It is good also as a structure which implement | achieves both by primary heating.

b)循環回路202に他の液−液熱交換器を備え、給湯の他、暖房水Mの熱を他の被加熱媒体との熱交換を行う熱源として用いてもよい。   b) The circulation circuit 202 may be provided with another liquid-liquid heat exchanger, and in addition to hot water supply, the heat of the heating water M may be used as a heat source for exchanging heat with another heated medium.

以上説明したように、本発明の最も好ましい実施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、または明細書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 present invention has been described. The present invention is not limited to the above description. Various modifications and changes can be made by those skilled in the art based on the gist of the invention described in the claims or disclosed in the specification. It goes without saying that such modifications and changes are included in the scope of the present invention.

本発明は、燃焼排気と被加熱流体を熱交換する複数の熱交換管を備える筐体に変流部材を備えることにより、燃焼排気に滞留や拡散を生じさせるので、燃焼排気を分散させて熱交換が可能となり、燃焼排気の熱回収が良好になり、熱交換効率が高められ、有用である。
In the present invention, since a current-transforming member is provided in a housing having a plurality of heat exchange tubes for exchanging heat between the combustion exhaust and the fluid to be heated, stagnation and diffusion are caused in the combustion exhaust. Exchange is possible, heat recovery of combustion exhaust is improved, heat exchange efficiency is improved, and useful.

2 二次熱交換ユニット
4 筐体
6 排気導入部
8 排出部
10、10−1、10−2 熱交換部
12、12−1、12−2 熱交換管
14−1、14−2、14−3 邪魔板
14−11、14−12 変流片
16 天井板
18 底面板
20−1、20−2 ヘッダ
24−1、24−2、24−3 邪魔板
34−1、34−2、34−3 邪魔板
54−1、54−2 邪魔板
44−1、44−2、44−3 邪魔板
60 熱源機
62 筐体
64 燃焼室
66 バーナー
68 一次熱交換器
70 給気ファン
72 熱交換管
80 二次熱交換ユニット
82 ユニット筐体
84 天井板
86 底面板
88 排気空間
90 排気導入部
92 排気ガイド
94−1 第1の熱交換部
94−2 第2の熱交換部
98 排気部
100 ドレン溜め
102−1、102−2 熱交換管
104 邪魔板
106 吸熱フィン
200 給湯装置
202 循環回路
204 暖房水タンク
206 給水口
208 給水路
210 出湯口
212 追焚循環路
214 注湯管路
216 浴槽
218−1、218−2、218−3 分岐管
220 暖房放熱端末
220−1 低温端末
222−1 暖房二次熱交換器
222−2 給湯二次熱交換
224−1 給湯熱交換器
224−2 浴槽水熱交換器
226 リモコン装置
226−1 浴室リモコン
226−2 台所リモコン
EG 燃焼排気
2 Secondary heat exchange unit 4 Case 6 Exhaust introduction part 8 Discharge part 10, 10-1, 10-2 Heat exchange part 12, 12-1, 12-2 Heat exchange pipe 14-1, 14-2, 14- 3 Baffle plate 14-11, 14-12 Current transformer 16 Ceiling plate 18 Bottom plate 20-1, 20-2 Header 24-1, 24-2, 24-3 Baffle plate 34-1, 34-2, 34- 3 baffle plates 54-1, 54-2 baffle plates 44-1, 44-2, 44-3 baffle plates 60 heat source machine 62 housing 64 combustion chamber 66 burner 68 primary heat exchanger 70 air supply fan 72 heat exchange pipe 80 Secondary heat exchange unit 82 Unit housing 84 Ceiling plate 86 Bottom plate 88 Exhaust space 90 Exhaust introduction part 92 Exhaust guide 94-1 First heat exchange part 94-2 Second heat exchange part 98 Exhaust part 100 Drain reservoir 102 -1,102-2 Heat exchange tube DESCRIPTION OF SYMBOLS 104 Baffle plate 106 Endothermic fin 200 Hot-water supply apparatus 202 Circulation circuit 204 Heating water tank 206 Water supply port 208 Water supply path 210 Hot water outlet 212 Recruitment circulation path 214 Pouring pipe line 216 Bathtub 218-1, 218-2, 218-3 Branch pipe 220 Heating / radiating terminal 220-1 Low temperature terminal 222-1 Heating secondary heat exchanger 222-2 Hot water supply secondary heat exchange 224-1 Hot water supply heat exchanger 224-2 Bathtub water heat exchanger 226 Remote control device 226-1 Bathroom remote control 226 -2 Kitchen remote control EG Combustion exhaust

Claims (6)

燃焼排気を流す筐体と、
前記筐体内で前記燃焼排気と被加熱流体を熱交換する複数の熱交換管が配置され、前記燃焼排気の上流側に第1の被加熱流体を通流させる第1の熱交換部と、前記燃焼排気の下流側に前記第1の被加熱流体と循環路が異なる第2の被加熱流体を通流させる第2の熱交換部とを含む熱交換部と、
前記第2の熱交換部に流れた前記燃焼排気を前記第2の熱交換部から前記第1の熱交換部側に方向転換させる変流片であり、前記筐体に通流させた前記燃焼排気を変流することにより前記熱交換管に集合または分散させ、前記熱交換管と前記燃焼排気の熱交換を行わせる1または2以上の変流部材と、
を備えることを特徴とする熱交換器。
A casing for flowing combustion exhaust;
A plurality of heat exchange pipes for exchanging heat between the combustion exhaust and the fluid to be heated in the housing, and a first heat exchange section for allowing the first fluid to be heated to flow upstream of the combustion exhaust; A heat exchanging section including a second heat exchanging section for passing a second heated fluid different in circulation path from the first heated fluid downstream of the combustion exhaust ;
The combustion flow that is a current-transforming piece that changes the direction of the combustion exhaust gas that has flowed to the second heat exchanging portion from the second heat exchanging portion to the first heat exchanging portion, and is passed through the casing. One or two or more current-transforming members that collect or disperse the exhaust gas in the heat exchange pipe to exchange heat between the heat exchange pipe and the combustion exhaust gas;
A heat exchanger comprising:
前記変流部材は、前記燃焼排気を衝突させて前記燃焼排気の流れ方向を変更する衝突部材、前記燃焼排気を一方向に流れ方向を変更させる流れ方向変更部材、前記熱交換管の一部を包囲する包囲部材の何れかまたはこれらの組合せを含むことを特徴とする請求項1に記載の熱交換器。   The current transformation member includes a collision member that changes the flow direction of the combustion exhaust by causing the combustion exhaust to collide, a flow direction changing member that changes the flow direction of the combustion exhaust in one direction, and a part of the heat exchange pipe. The heat exchanger according to claim 1, comprising any of the surrounding members or a combination thereof. 前記変流部材は、前記第2の熱交換部に流れた前記燃焼排気を前記第2の熱交換部から前記第1の熱交換部側に方向転換させる第1の変流片と、
前記第1の熱交換部に流れた前記燃焼排気を前記第1の熱交換部から前記第2の熱交換部側に方向転換させる第2の変流片と、
を含むことを特徴とする請求項に記載の熱交換器。
The current-transforming member has a first current-transforming piece that changes the direction of the combustion exhaust gas that has flowed to the second heat exchange part from the second heat exchange part to the first heat exchange part;
A second current changing piece for changing the direction of the combustion exhaust gas that has flowed to the first heat exchange section from the first heat exchange section to the second heat exchange section;
The heat exchanger according to claim 1 , comprising:
一次熱交換後の燃焼排気を流す筐体部と、
前記筐体部で前記燃焼排気と被加熱流体を熱交換する複数の熱交換管が配置され、前記燃焼排気の上流側に第1の被加熱流体を通流させる第1の熱交換部と、前記燃焼排気の下流側に前記第1の被加熱流体と循環路が異なる第2の被加熱流体を通流させる第2の熱交換部とを含む熱交換部と、
前記第2の熱交換部に流れた前記燃焼排気を前記第2の熱交換部から前記第1の熱交換部側に方向転換させる変流片であり、前記筐体に通流させた前記燃焼排気を変流することにより前記熱交換管に集合または分散させ、前記熱交換管と前記燃焼排気の熱交換を行わせる1または2以上の変流部材と、
を備えることを特徴とする二次熱交換器。
A casing for flowing combustion exhaust after primary heat exchange;
A plurality of heat exchange pipes for exchanging heat between the combustion exhaust and the fluid to be heated in the casing, and a first heat exchange portion for passing the first fluid to be heated upstream of the combustion exhaust; A heat exchanging section including a second heat exchanging section for flowing a second heated fluid different in circulation path from the first heated fluid downstream of the combustion exhaust ;
The current-flowing piece that changes the direction of the combustion exhaust gas that has flowed to the second heat exchanging portion from the second heat exchanging portion to the first heat exchanging portion, and is passed through the housing portion. One or two or more current transformation members that collect or disperse the combustion exhaust gas in the heat exchange pipe to exchange heat between the heat exchange pipe and the combustion exhaust;
A secondary heat exchanger comprising:
前記筐体部に請求項2または請求項に記載された熱交換器を備えることを特徴とする請求項に記載の二次熱交換器。 Secondary heat exchanger according to claim 4, characterized in that it comprises a heat exchanger according to claim 2 or claim 3 in the housing part. 請求項1ないし請求項3の何れかに記載の熱交換器を備え、または請求項4と請求項5の何れかに記載の二次熱交換器を備えて被加熱流体を加熱し、該被加熱流体を用いて給湯または暖房を行うことを特徴とする熱源機。 A heat exchanger according to any one of claims 1 to 3 is provided, or a secondary heat exchanger according to any one of claims 4 and 5 is provided to heat a fluid to be heated, and A heat source machine that performs hot water supply or heating using a heating fluid.
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