JPH10332222A - Absorption cooler - Google Patents

Absorption cooler

Info

Publication number
JPH10332222A
JPH10332222A JP13951497A JP13951497A JPH10332222A JP H10332222 A JPH10332222 A JP H10332222A JP 13951497 A JP13951497 A JP 13951497A JP 13951497 A JP13951497 A JP 13951497A JP H10332222 A JPH10332222 A JP H10332222A
Authority
JP
Japan
Prior art keywords
fin
exhaust gas
burner
exhaust
outer peripheral
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP13951497A
Other languages
Japanese (ja)
Other versions
JP3481079B2 (en
Inventor
Yasuhei Hayashi
泰平 林
Kazumi Yamamoto
和美 山本
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Osaka Gas Co Ltd
Rinnai Corp
Original Assignee
Osaka Gas Co Ltd
Rinnai Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Osaka Gas Co Ltd, Rinnai Corp filed Critical Osaka Gas Co Ltd
Priority to JP13951497A priority Critical patent/JP3481079B2/en
Publication of JPH10332222A publication Critical patent/JPH10332222A/en
Application granted granted Critical
Publication of JP3481079B2 publication Critical patent/JP3481079B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To provide an absorption cooling device which is free from high temperature oxidation due to overheat of a fin even if the fin is provided on a wall face, by employing a structure wherein exhaust gas is made to flow along the wall face of an annular cylindrical container part of a heating container. SOLUTION: An outer peripheral fin 25 is omitted at an outer side of a lower part 25a. Therefore, the most upstream end part of the outer peripheral fin 25 is constituted only of an outer peripheral wall face 23b side. The outer peripheral wall face 23b has a good heat sink property, and an extreme high temperature is not reached so that corrosion of the outer peripheral fin 25 due to high temperature oxidation is not caused. In a downstream side an outer side is exposed to exhaust gas, but, since temperature of the exhaust gas is lowered due to progress of heat exchange, high temperature oxidation hardly occurs on the outer peripheral fin 25.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、吸収式冷凍サイク
ルを用いた冷却装置に関するもので、特に高温の排気ガ
スによって吸収液を加熱する技術に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a cooling apparatus using an absorption refrigeration cycle, and more particularly to a technique for heating an absorption liquid with high-temperature exhaust gas.

【0002】[0002]

【従来の技術】従来技術の一例を図7に示す。燃焼装置
J1 の排気ガスによって吸収液を加熱する加熱容器J2
として、バーナJ3 を上方から覆うとともに、環状の環
状筒容器部J4 を備えた断面略コ字型の容器形状を呈
し、排気ガスが環状筒容器部J4の内周排気通路J5 お
よび外周排気通路J6 を流れるように設けられたものが
知られている。環状筒容器部J4 の外周壁面J7 には、
排気ガスの熱を効率的に環状筒容器部J4 へ伝えるため
に、外周フィンJ8 が接合されている。
2. Description of the Related Art FIG. 7 shows an example of the prior art. Heating vessel J2 for heating the absorbing liquid by the exhaust gas of combustion device J1
In addition to covering the burner J3 from above, it has a substantially U-shaped container shape having an annular annular cylindrical container J4, and the exhaust gas flows through the inner peripheral exhaust passage J5 and the outer peripheral exhaust passage J6 of the annular cylindrical container J4. What is provided so that it may flow is known. On the outer peripheral wall J7 of the annular cylindrical container J4,
Outer peripheral fins J8 are joined to efficiently transfer the heat of the exhaust gas to the annular cylindrical container J4.

【0003】[0003]

【発明が解決しようとする課題】排気ガスは環状筒容器
部J4 の外周壁面J7 に沿って下から上に向けて流れ
る。この時、外周フィンJ8 の下端は上部に比べて吸熱
が進んでいない高温の排気ガスに触れる。この結果、外
周フィンJ8 の外端は、内端に比べて外周壁面J7への
熱引きが悪い(伝熱が遅い)ため、高温になり、高温酸
化による腐蝕が進んでしまう不具合があった。
Exhaust gas flows upward from the bottom along the outer peripheral wall J7 of the annular cylindrical container J4. At this time, the lower end of the outer peripheral fin J8 touches a high-temperature exhaust gas whose heat absorption has not progressed as compared with the upper part. As a result, the outer end of the outer fin J8 has a drawback that heat is drawn to the outer wall surface J7 (slow heat transfer) at a lower temperature than the inner end, so that the temperature becomes high and corrosion by high-temperature oxidation proceeds.

【0004】[0004]

【発明の目的】本発明は、上記の事情に鑑みてなされた
もので、その目的は、加熱容器の環状筒容器部の壁面に
沿って排気ガスが流れる構造を採用し、壁面にフィンを
設けても、フィンの過熱による高温酸化が起こらない吸
収式冷却装置の提供にある。
SUMMARY OF THE INVENTION The present invention has been made in view of the above circumstances, and has as its object to adopt a structure in which exhaust gas flows along the wall surface of an annular cylindrical container portion of a heating container, and to provide fins on the wall surface. However, an object of the present invention is to provide an absorption cooling device that does not cause high-temperature oxidation due to overheating of the fin.

【0005】[0005]

【課題を解決するための手段】[Means for Solving the Problems]

〔請求項1の手段〕吸収式冷却装置は、燃料の燃焼を行
うバーナ、このバーナに燃焼用の空気を強制的に送る燃
焼ファンを備えた燃焼装置と、この燃焼装置によって加
熱されるとともに吸収液が供給される加熱容器を備え、
吸収液の一部を気化させる再生器、この再生器で発生し
た気化冷媒を冷却して液化する凝縮器、この凝縮器で液
化した液化冷媒を低圧下で蒸発させて熱媒体を冷却する
蒸発器、この蒸発器で蒸発した気化冷媒を吸収液に吸収
させる吸収器、この蒸発器内で気化冷媒を吸収した吸収
液を前記再生器へ圧送する溶液ポンプを備える吸収式冷
凍サイクルと、を具備する。
According to a first aspect of the present invention, there is provided an absorption-type cooling apparatus comprising: a burner for burning fuel; a combustion apparatus having a combustion fan for forcibly sending air for combustion to the burner; A heating vessel to which the liquid is supplied,
A regenerator that evaporates part of the absorbing liquid, a condenser that cools and liquefies the vaporized refrigerant generated by the regenerator, and an evaporator that cools the heat medium by evaporating the liquefied refrigerant liquefied by the condenser under low pressure. An absorber for absorbing the vaporized refrigerant evaporated by the evaporator into the absorbent, and an absorption refrigeration cycle including a solution pump for pressure-feeding the absorbent absorbing the vaporized refrigerant in the evaporator to the regenerator. .

【0006】前記加熱容器は、上方から前記バーナを覆
うとともに環状の環状筒容器部を備えた断面略コ字型の
容器形状を呈し、前記燃焼装置は、前記バーナで発生し
た排気ガスを、前記環状筒容器部の壁面に沿って流す排
気通路を備え、前記環状筒容器部の壁面には、排気ガス
の熱を効率的に前記環状筒容器部へ伝えるフィンを備
え、このフィンの排気通路における最上流端部は、前記
壁面から遠い側が欠落していることを特徴とする。
[0006] The heating vessel has a substantially U-shaped cross-sectional shape provided with a ring-shaped cylindrical vessel portion while covering the burner from above, and the combustion device discharges exhaust gas generated by the burner into the vessel. An exhaust passage that flows along the wall surface of the annular cylindrical container portion; and a fin that efficiently transfers heat of exhaust gas to the annular cylindrical container portion on the wall surface of the annular cylindrical container portion. The most upstream end is characterized in that a side far from the wall surface is missing.

【0007】〔請求項2の手段〕請求項1の吸収式冷却
装置において、前記フィンの最上流端部は、下流側に向
かうに従って欠落幅が小さくなるように斜めにカットし
た形状に設けられたことを特徴とする。
According to a second aspect of the present invention, in the absorption type cooling apparatus according to the first aspect, the most upstream end portion of the fin is cut obliquely so that the width of the fin becomes smaller toward the downstream side. It is characterized by the following.

【0008】〔請求項3の手段〕吸収式冷却装置は、燃
料の燃焼を行うバーナ、このバーナに燃焼用の空気を強
制的に送る燃焼ファンを備えた燃焼装置と、この燃焼装
置によって加熱されるとともに吸収液が供給される加熱
容器を備え、吸収液の一部を気化させる再生器、この再
生器で発生した気化冷媒を冷却して液化する凝縮器、こ
の凝縮器で液化した液化冷媒を低圧下で蒸発させて熱媒
体を冷却する蒸発器、この蒸発器で蒸発した気化冷媒を
吸収液に吸収させる吸収器、この蒸発器内で気化冷媒を
吸収した吸収液を前記再生器へ圧送する溶液ポンプを備
える吸収式冷凍サイクルと、を具備する。
According to a third aspect of the present invention, there is provided an absorption-type cooling device, which includes a burner for burning fuel, a combustion device provided with a combustion fan for forcibly sending combustion air to the burner, and a heating device which is heated by the combustion device. A regenerator for vaporizing a part of the absorbing liquid, a condenser for cooling and liquefying the vaporized refrigerant generated in the regenerator, and a liquefied refrigerant for liquefying in the condenser. An evaporator that evaporates under a low pressure to cool the heat medium, an absorber that absorbs the vaporized refrigerant evaporated by the evaporator into an absorbent, and pumps the absorbent that has absorbed the vaporized refrigerant in the evaporator to the regenerator. An absorption refrigeration cycle including a solution pump.

【0009】前記加熱容器は、上方から前記バーナを覆
うとともに環状の環状筒容器部を備えた断面略コ字型の
容器形状を呈し、前記燃焼装置は、前記バーナで発生し
た排気ガスを、前記環状筒容器部の壁面に沿って流す排
気通路を備え、前記環状筒容器部の壁面には、排気ガス
の熱を効率的に前記環状筒容器部へ伝えるフィンを備
え、前記排気通路は、前記フィンの上流側に、排気ガス
を前記環状筒容器部の壁面側に導く制限板を備えること
を特徴とする。
The heating container has a substantially U-shaped cross-sectional shape which covers the burner from above and has an annular tubular container portion. The combustion device converts the exhaust gas generated by the burner into An exhaust passage that flows along the wall surface of the annular cylindrical container portion is provided.The wall surface of the annular cylindrical container portion includes a fin that efficiently transfers heat of exhaust gas to the annular cylindrical container portion. A restriction plate is provided upstream of the fins for guiding exhaust gas to the wall surface side of the annular cylindrical container portion.

【0010】〔請求項4の手段〕請求項3の吸収式冷却
装置において、前記排気通路は、排気ガスを収集して外
部に排出する排気口を備え、前記制限板は、前記排気口
に近い側の排気ガスの通る排気面積を小さくし、前記排
気口から遠い側の排気ガスの通る排気面積を大きくする
ことを特徴とする。
According to a fourth aspect of the present invention, in the absorption cooling apparatus of the third aspect, the exhaust passage has an exhaust port for collecting exhaust gas and discharging the exhaust gas to the outside, and the restricting plate is close to the exhaust port. The exhaust area through which the exhaust gas passes is reduced, and the exhaust area through which the exhaust gas passes far from the exhaust port is increased.

【0011】[0011]

【作用および発明の効果】[Action and effect of the invention]

〔請求項1の作用および効果〕フィンの最上流端部が下
流側に比較して壁面から遠い側が欠落して設けられたこ
とにより、フィンの最上流端部が受ける排気ガスの熱量
は、フィンの壁面側のみとなる。この壁面側のフィン
は、壁面に伝熱が行われて熱引きが良いため、極度に高
温にならず、高温酸化による腐蝕が抑えられる。
[Function and Effect of Claim 1] Since the most upstream end of the fin is provided so as to be cut off on the side farther from the wall surface than the downstream side, the amount of heat of the exhaust gas received by the most upstream end of the fin is smaller than that of the fin. Only on the wall side. The fins on the wall surface side conduct heat transfer to the wall surface and have good heat dissipation, so that the fins do not become extremely high in temperature and corrosion due to high-temperature oxidation is suppressed.

【0012】〔請求項2の作用および効果〕高温になり
易い上流側ほど、大きくカットした形状に設けたことに
より、高温酸化の生じ易さに応じた部分が欠落したフィ
ンになり、高温酸化を防止しながら、熱交換効率の低下
を最小限に抑えることができる。
According to the second aspect of the present invention, since the upstream side where the temperature is likely to be high becomes larger, the fin has a portion cut off according to the possibility of the high temperature oxidation. While preventing this, it is possible to minimize the decrease in the heat exchange efficiency.

【0013】〔請求項3の作用および効果〕フィンの上
流側の排気通路に、排気ガスを壁面側に導く制限板を設
けたことにより、フィンの壁面から遠い側が排気ガスの
流れの死角となって、フィンの壁面から遠い側の受ける
熱量が小さくなり、フィンの壁面から遠い側が極度の高
温にならず、高温酸化による腐蝕が抑えられる。なお、
排気ガスの流れが当たる壁面側のフィンは、壁面に伝熱
が行われて熱引きが良いため、極度に高温にならず、高
温酸化による腐蝕が抑えられる。また、下流に行くほど
制限板による死角の効果が小さくなるため、壁面より遠
い側のフィンにも排気ガスの流れが当たるが、吸収液と
の熱交換が進んで排気ガスの温度が下がっているため、
フィンが高温酸化する不具合がない。
According to the third aspect of the present invention, a restriction plate for guiding the exhaust gas to the wall surface is provided in the exhaust passage on the upstream side of the fin, so that the far side from the wall surface of the fin becomes a blind spot of the flow of the exhaust gas. Therefore, the amount of heat received on the side far from the wall surface of the fin is reduced, and the side far from the wall surface of the fin does not become extremely high in temperature, so that corrosion due to high-temperature oxidation is suppressed. In addition,
The fins on the wall surface to which the exhaust gas flows receive heat from the wall surface and have good heat dissipation, so that the fins do not become extremely high in temperature and corrosion due to high-temperature oxidation is suppressed. In addition, since the effect of the blind spot by the limiting plate becomes smaller toward the downstream, the flow of the exhaust gas also hits the fins farther from the wall surface, but heat exchange with the absorbing liquid proceeds and the temperature of the exhaust gas decreases. For,
There is no problem that the fin is oxidized at high temperature.

【0014】〔請求項4の作用および効果〕制限板によ
って排気口に近い側の排気ガスの通る排気面積が小さく
設けられ、排気口から遠い側の排気ガスの通る排気面積
が大きく設けられたことによって、排気通路の全周の排
気ガス量が均一化され、フィンの局部過熱がさらに防止
できる。
According to a fourth aspect of the present invention, the restriction plate provides a small exhaust area for exhaust gas near the exhaust port and a large exhaust area for exhaust gas far from the exhaust port. Thereby, the amount of exhaust gas in the entire circumference of the exhaust passage is made uniform, and local overheating of the fins can be further prevented.

【0015】[0015]

【発明の実施の形態】次に、本発明の実施の形態を、実
施例および変形例に基づいて説明する。 〔第1実施例の構成〕この実施例は、本発明の吸収式冷
却装置を空調装置に適用したもので、図1ないし図3を
用いて説明する。なお、図2は本実施例の空調装置の概
略構成図である。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Next, embodiments of the present invention will be described based on examples and modifications. [Structure of the First Embodiment] In this embodiment, the absorption cooling device of the present invention is applied to an air conditioner, and will be described with reference to FIGS. FIG. 2 is a schematic configuration diagram of the air conditioner of the present embodiment.

【0016】(空調装置1の概略説明)本実施例に示す
空調装置1は、家庭用等に使用される比較的小型なもの
で、室外に配置される室外機Aと、室内に配置される室
内空調機Bとを備える。室外機Aは、吸収液(本実施例
では臭化リチウム水溶液)を加熱する燃焼装置2と、室
内空調に用いられる冷温水(室内を冷暖房するための熱
媒体、本実施例では水)を冷却あるいは加熱する2重効
用型の吸収式冷凍サイクル3と、吸収式冷凍サイクル3
内で主に気化冷媒(本実施例では水蒸気)を冷やすため
に用いられる冷却水を冷却する冷却塔4とを備える。な
お、空調装置1に搭載される各電気機能部品は、室外機
Aに配置された制御装置5によって制御される。
(Schematic Description of Air Conditioning Apparatus 1) An air conditioning apparatus 1 shown in this embodiment is a relatively small one used for home use or the like, and has an outdoor unit A disposed outdoors and an outdoor unit A disposed indoors. And an indoor air conditioner B. The outdoor unit A cools the combustion device 2 that heats the absorbing liquid (a lithium bromide aqueous solution in the present embodiment) and cold / hot water (a heat medium for cooling and heating the room, water in the present embodiment) used for indoor air conditioning. Alternatively, a double effect absorption refrigeration cycle 3 for heating and an absorption refrigeration cycle 3
And a cooling tower 4 for cooling cooling water mainly used for cooling a vaporized refrigerant (steam in this embodiment). Each electric functional component mounted on the air conditioner 1 is controlled by the control device 5 arranged in the outdoor unit A.

【0017】(燃焼装置2の説明)本実施例の燃焼装置
2は、燃料であるガスを燃焼して熱を発生させ、発生し
た熱によって吸収式冷凍サイクル3の加熱容器10を加
熱し、加熱容器10内に供給された低濃度吸収液(以
下、低液)を加熱するガス燃焼装置で、ガスの燃焼を行
うガスバーナ11、このガスバーナ11へガスの供給を
行うガス供給管12、ガスバーナ11へ燃焼用の空気を
供給する燃焼ファン13等から構成される。ガス供給管
12には、ガス供給管12の開閉を行うガス開閉弁12
aと、ガスの供給量を調節することで燃焼量を調節する
ガス量調節弁12bとが設けられている。なお、燃焼装
置2および加熱容器10の構造の詳細は後述する。
(Explanation of Combustion Apparatus 2) The combustion apparatus 2 of this embodiment generates heat by burning gas as a fuel, and heats the heating vessel 10 of the absorption refrigeration cycle 3 by the generated heat. A gas combustion device that heats a low-concentration absorbing liquid (hereinafter referred to as a low liquid) supplied to a container 10, a gas burner 11 that burns gas, a gas supply pipe 12 that supplies gas to the gas burner 11, and a gas burner 11. It comprises a combustion fan 13 for supplying air for combustion. The gas supply pipe 12 has a gas on-off valve 12 for opening and closing the gas supply pipe 12.
a and a gas amount control valve 12b for adjusting the combustion amount by adjusting the gas supply amount. The details of the structures of the combustion device 2 and the heating vessel 10 will be described later.

【0018】(吸収式冷凍サイクル3の説明)吸収式冷
凍サイクル3は、燃焼装置2によって加熱される加熱容
器10を備え、この加熱容器10内に供給された低液が
加熱されることによって低液に含まれる冷媒(水)を気
化(蒸発)させて中濃度吸収液(以下、中液)にする高
温再生器15と、この高温再生器15内の気化冷媒の凝
縮熱を利用して、高温再生器15側から圧力差を利用し
て供給される中液を加熱し、中液に含まれる冷媒を気化
させて中液を高濃度吸収液(以下、高液)にする低温再
生器16と、高温再生器15および低温再生器16から
の気化冷媒(水蒸気)を冷却して液化する凝縮器17
と、この凝縮器17で液化した液化冷媒(水)を真空に
近い圧力下で蒸発させる蒸発器18と、この蒸発器18
で蒸発した気化冷媒を低温再生器16で得られた高液に
吸収させる吸収器19と、この吸収器19内で気化冷媒
を吸収した低液を加熱容器10へ圧送する溶液ポンプ2
0とから構成される。
(Explanation of Absorption Refrigeration Cycle 3) The absorption refrigeration cycle 3 includes a heating vessel 10 heated by the combustion device 2, and the low liquid supplied into the heating vessel 10 is heated to reduce the temperature. A high-temperature regenerator 15 that evaporates (evaporates) a refrigerant (water) contained in the liquid into a medium-concentration absorbing liquid (hereinafter, medium liquid), and utilizes heat of condensation of the vaporized refrigerant in the high-temperature regenerator 15, A low-temperature regenerator 16 that heats an intermediate liquid supplied from the high-temperature regenerator 15 using a pressure difference, vaporizes a refrigerant contained in the intermediate liquid, and turns the intermediate liquid into a high-concentration absorbing liquid (hereinafter, high liquid). And a condenser 17 for cooling and liquefying the vaporized refrigerant (steam) from the high-temperature regenerator 15 and the low-temperature regenerator 16
And an evaporator 18 for evaporating the liquefied refrigerant (water) liquefied in the condenser 17 under a pressure close to vacuum, and an evaporator 18
An absorber 19 for absorbing the vaporized refrigerant evaporated in the high-temperature liquid obtained by the low-temperature regenerator 16 and a solution pump 2 for pressure-feeding the low liquid absorbed by the vaporized refrigerant in the absorber 19 to the heating vessel 10
0.

【0019】また、本実施例の吸収式冷凍サイクル3に
は、上述の作動による冷房運転の他に、暖房運転を行う
ために、燃焼装置2で加熱された高温の吸収液を蒸発器
18へ導く暖房管21と、この暖房管21を開閉する冷
暖切替弁22とを備える。この冷暖切替弁22は暖房運
転時に開弁されて、高温の吸収液を蒸発器18へ導き、
室内空調機Bに供給される冷温水を加熱するものであ
る。
In the absorption refrigeration cycle 3 of the present embodiment, in addition to the cooling operation by the above-described operation, in order to perform the heating operation, the high-temperature absorption liquid heated by the combustion device 2 is sent to the evaporator 18. The air conditioner includes a heating pipe 21 for guiding and a switching valve 22 for opening and closing the heating pipe 21. The cooling / heating switching valve 22 is opened during the heating operation to guide the high-temperature absorbing liquid to the evaporator 18,
The hot and cold water supplied to the indoor air conditioner B is heated.

【0020】(冷房運転の作動説明)制御装置5に冷房
の指示が与えられると、各電気機能部品の作動により、
燃焼装置2および吸収式冷凍サイクル3が作動する。吸
収式冷凍サイクル3は、燃焼装置2が加熱容器10を加
熱することにより、高温再生器15で、低液から気化冷
媒と中液が取り出されるとともに、低温再生器16で、
中液から気化冷媒と高液が取り出される。
(Explanation of operation of cooling operation) When an instruction for cooling is given to the control device 5, the operation of each electric functional component causes
The combustion device 2 and the absorption refrigeration cycle 3 operate. In the absorption refrigeration cycle 3, when the combustion device 2 heats the heating vessel 10, the high-temperature regenerator 15 removes the vaporized refrigerant and the middle liquid from the low liquid, and the low-temperature regenerator 16
Vaporized refrigerant and high liquid are taken out of the middle liquid.

【0021】高温再生器15および低温再生器16で取
り出された気化冷媒は、凝縮器17で凝縮されて液化し
た後に蒸発器18内に散布され、室内空調機Bに供給さ
れる冷温水から気化熱を奪って蒸発する。そして、蒸発
器18で冷却された冷温水は、室内空調機Bに供給され
て室内を冷房する。
The vaporized refrigerant taken out by the high-temperature regenerator 15 and the low-temperature regenerator 16 is condensed and liquefied by the condenser 17 and then dispersed in the evaporator 18 to be vaporized from the cold and hot water supplied to the indoor air conditioner B. Take away heat and evaporate. Then, the cold and hot water cooled by the evaporator 18 is supplied to the indoor air conditioner B to cool the room.

【0022】蒸発器18内で蒸発した気化冷媒は、吸収
器19内に流入する。吸収器19内には、低温再生器1
6で取り出された高液が散布されており、この散布され
た高液に蒸発器18から流入した気化冷媒が吸収され
る。なお、気化冷媒が高液に吸収される際に発生する吸
収熱は、冷却塔4から供給された冷却水に吸収されるた
め、吸収能力の低下は防止される。そして、吸収器19
で気化冷媒を吸収した高液は、低液となって溶液ポンプ
20で吸い込まれ、再び加熱容器10内に戻され、上記
のサイクルを繰り返す。
The vaporized refrigerant evaporated in the evaporator 18 flows into the absorber 19. In the absorber 19, the low temperature regenerator 1
The high liquid taken out at 6 is sprayed, and the vaporized refrigerant flowing from the evaporator 18 is absorbed by the sprayed high liquid. Note that the absorption heat generated when the vaporized refrigerant is absorbed by the high liquid is absorbed by the cooling water supplied from the cooling tower 4, so that a decrease in absorption capacity is prevented. And the absorber 19
The high liquid that has absorbed the vaporized refrigerant in step (1) becomes a low liquid, is sucked by the solution pump 20, returned to the heating vessel 10 again, and repeats the above cycle.

【0023】(加熱容器10の説明)加熱容器10は、
図1に示すように、バーナ11の上方を覆う断面略コ字
型を呈したステンレス製容器で、上方に吹出筒10aが
接続される。加熱容器10のうち環状を呈した環状筒容
器部23は、内周壁面23aの内側および外周壁面23
bの外側に沿って燃焼ガスが流れるもので、環状筒容器
部23の外周壁面23bには、図1に示すように、排気
ガスと加熱容器10との熱交換率を向上させる目的で、
熱伝動性に優れた材質(例えば銅)よりなる外周フィン
25がろう付け等の接合手段によって接合されている。
(Description of Heating Vessel 10)
As shown in FIG. 1, a stainless steel container having a substantially U-shaped cross section that covers an upper part of the burner 11 is connected to an upper part of an outlet cylinder 10 a. The annular cylindrical container portion 23 of the heating container 10 having an annular shape is formed inside the inner peripheral wall surface 23a and the outer peripheral wall surface 23a.
b, the combustion gas flows along the outside, and on the outer peripheral wall surface 23b of the annular cylindrical container portion 23, as shown in FIG. 1, for the purpose of improving the heat exchange rate between the exhaust gas and the heating container 10,
Outer peripheral fins 25 made of a material having excellent thermal conductivity (for example, copper) are joined by joining means such as brazing.

【0024】(燃焼装置2の説明)燃焼装置2は、燃焼
ファン13の発生した空気流をバーナ11へ送る給気通
路26と、バーナ11における燃焼により発生した排気
ガスを加熱容器10に触れさせて排気口27へ導く排気
通路28とを備える。この排気通路28は、バーナ11
で発生した排気ガスを、環状筒容器部23の内周壁面2
3aに沿って上から下に流す内周排気通路28aと、環
状筒容器部23の外周壁面23bに沿って下から上に流
す外周排気通路28bとを備える。
(Description of Combustion Apparatus 2) The combustion apparatus 2 causes the air supply passage 26 for sending the air flow generated by the combustion fan 13 to the burner 11 and the exhaust gas generated by the combustion in the burner 11 to contact the heating vessel 10. And an exhaust passage 28 leading to the exhaust port 27. The exhaust passage 28 is connected to the burner 11
Exhaust gas generated in the inner peripheral wall surface 2 of the annular cylindrical container portion 23
An inner exhaust passage 28a that flows downward from above along 3a, and an outer exhaust passage 28b that flows upward from below along the outer peripheral wall surface 23b of the annular cylindrical container portion 23 are provided.

【0025】(外周フィン25の説明)外周フィン25
は、薄い銅板を多数波状に屈曲させたコルゲートフィン
を、外周壁面23bに沿って接合したもので、この外周
フィン25の下部25a(最上流端部に相当する)は、
その上部25bに比較して外周側が欠落して設けられて
いる。具体的に本実施例では、外周フィン25の下端外
周側が斜め方向にカットした形状に設けられている(図
3参照)。なお、カットの形状は、下流側に向かうに従
って欠落幅が小さくなるように斜めにカットされてお
り、例えば、図4に示すように、幅が4mm、流れ方向
に沿う長さが40mmにカットされている。
(Description of Outer Fins 25) Outer Fins 25
Is formed by joining corrugated fins obtained by bending a thin copper plate into a large number of waves along the outer peripheral wall surface 23b. A lower portion 25a (corresponding to the most upstream end portion) of the outer peripheral fins 25 is
The outer peripheral side is cut off and provided compared to the upper part 25b. Specifically, in the present embodiment, the outer periphery of the lower end of the outer peripheral fin 25 is provided in a shape cut obliquely (see FIG. 3). The shape of the cut is cut diagonally so that the cut-off width becomes smaller toward the downstream side. For example, as shown in FIG. 4, the cut is cut into a width of 4 mm and a length along the flow direction of 40 mm. ing.

【0026】〔実施例の効果〕外周フィン25の下端外
周側が欠落して設けられたことにより、外周フィン25
の下端外周側が受ける排気ガスの熱量が、外周フィン2
5の外周壁面23b側のみとなる。この外周壁面23b
側の外周フィン25は、外周壁面23bから内部の吸収
液に伝熱が行われて熱引きが良いため、極度に高温にな
らず、高温酸化による腐蝕が抑えられる。また、高温に
なり易い下側ほど、大きくカットした形状に設けたこと
により、高温酸化の生じ易さに応じた部分をカットした
形状の外周フィン25になり、高温酸化を防止しなが
ら、排気ガスと吸収液との熱交換効率の低下を最小限に
抑えることができる。
[Effects of the embodiment] The outer peripheral fin 25 is provided with the lower end outer peripheral side thereof being cut off.
The amount of heat of exhaust gas received by the outer peripheral side of the lower end of the
5 only on the outer peripheral wall surface 23b side. This outer peripheral wall 23b
The outer peripheral fin 25 on the side is transferred from the outer peripheral wall surface 23b to the internal absorbing liquid and has good heat dissipation, so that the temperature does not become extremely high and corrosion due to high-temperature oxidation is suppressed. In addition, the lower side, which is likely to be heated to a high temperature, is formed in a shape that is cut larger, so that the outer peripheral fin 25 has a shape in which a portion corresponding to the possibility of high-temperature oxidation is cut. A decrease in the efficiency of heat exchange between the liquid and the absorbing liquid can be minimized.

【0027】〔第2実施例〕図5は第2実施例を示すも
ので、燃焼装置2および加熱容器10の断面図である。
第2実施例では、外周フィン25の最下端から所定高
(例えば40mm)の下部25aの幅を例えば6mmと
し、その上部25bの幅(例えば9mm)に比較して3
mm小さく設けたものである。
[Second Embodiment] FIG. 5 shows a second embodiment and is a sectional view of the combustion apparatus 2 and the heating vessel 10.
In the second embodiment, the width of the lower portion 25a having a predetermined height (for example, 40 mm) from the lowermost end of the outer peripheral fin 25 is set to, for example, 6 mm, and is 3 times smaller than the width of the upper portion 25b (for example, 9 mm).
mm.

【0028】〔第3実施例〕図6は第3実施例を示すも
ので、燃焼装置2および加熱容器10の断面図である。
上記の第1、第2実施例では、外周フィン25の下部2
5aを上部25bより欠落させることで、外周フィン2
5の下端外側の過熱による高温酸化を防止する例を示し
た。これに対し、この第3実施例では、外周フィン25
の直下の外周排気通路28bに、排気ガスを外周フィン
25の内側に導く制限板30(例えばステンレス製)を
設けて外周排気通路28bの内側のみに排気ガスの通る
隙間を形成して、排気ガスの流れが直接当たらない死角
を形成することにより、外周フィン25の下端外側が過
熱しないようにしたものである。
[Third Embodiment] FIG. 6 shows a third embodiment, and is a sectional view of the combustion apparatus 2 and the heating vessel 10.
In the first and second embodiments, the lower portion 2 of the outer peripheral fin 25
5a is removed from the upper part 25b, so that the outer fin 2
5 shows an example in which high-temperature oxidation due to overheating of the lower end outside is prevented. On the other hand, in the third embodiment, the outer peripheral fin 25
A restricting plate 30 (for example, made of stainless steel) for guiding the exhaust gas to the inside of the outer peripheral fins 25 is provided in the outer peripheral exhaust passage 28b immediately below the outer exhaust passage 28b to form a gap through which the exhaust gas passes only inside the outer peripheral exhaust passage 28b. Is formed so that the outside of the lower end of the outer peripheral fin 25 is not overheated by forming a blind spot where the flow does not directly hit.

【0029】外周排気通路28bにおける排気口27と
の位置関係で、排気口27側は制限板30による排気隙
間(排気面積に相当する)が小さく設けられ、排気口2
7から遠い側は制限板30による排気隙間が大きく設け
られる。このため、外周排気通路28bの全周の排気ガ
ス量が均一化され、外周フィン25の局部過熱がさらに
防止できる。なお、この実施例では、制限板30と外周
壁面23bとの間に排気隙間を設けることで、排気ガス
を外周壁面23b側に導く例を示したが、制限板30に
穴を設けて、この穴の位置で排気ガスを外周壁面23b
側に導くように設けても良い。また、穴の大きさや数に
よって、排気ガスの通過抵抗を調節し、外周排気通路2
8bの全周の排気ガス量を均一化させても良い。
Due to the positional relationship with the exhaust port 27 in the outer peripheral exhaust passage 28b, a small exhaust gap (corresponding to the exhaust area) by the restriction plate 30 is provided on the exhaust port 27 side.
On the side distant from 7, a large exhaust gap is provided by the restriction plate 30. For this reason, the amount of exhaust gas in the entire circumference of the outer peripheral exhaust passage 28b is made uniform, and local overheating of the outer peripheral fin 25 can be further prevented. In this embodiment, an example is shown in which an exhaust gap is provided between the limiting plate 30 and the outer peripheral wall surface 23b to guide the exhaust gas to the outer peripheral wall surface 23b side. Exhaust gas is supplied to the outer peripheral wall 23b at the position of the hole.
It may be provided so as to guide to the side. In addition, the passage resistance of the exhaust gas is adjusted according to the size and number of the holes, and the outer peripheral exhaust passage 2 is adjusted.
The exhaust gas amount in the entire circumference of 8b may be made uniform.

【0030】〔変形例〕上記の実施例では、吸収式冷凍
サイクルの一例として2重効用型の吸収式冷凍サイクル
3を例に示したが、1重効用型の吸収式冷凍サイクルで
も良いし、3重以上の多重効用型の吸収式冷凍サイクル
でも良い。また、低温再生器16内に中液を注入する
際、低温再生器16の上方から注入する例を示したが、
下方から注入しても良い。
[Modification] In the above embodiment, the double-effect absorption refrigeration cycle 3 has been described as an example of the absorption refrigeration cycle. However, a single-effect absorption refrigeration cycle may be used. A triple effect or more multi-effect absorption refrigeration cycle may be used. In addition, when the middle liquid is injected into the low-temperature regenerator 16, an example is shown in which the medium is injected from above the low-temperature regenerator 16.
It may be injected from below.

【0031】バーナ11の一例としてブンゼン式を示し
たが、ガスと燃焼用空気とを混合させたエアリッチ混合
気を燃焼させる全1次式ガスバーナを用いても良いし、
ガスと燃焼用空気とを混合させたガスリッチ混合気を燃
焼させるとともに、燃焼部へ2次空気を供給する予混合
式ブンゼンガスバーナを用いても良い。バーナ11の一
例として偏平器体を複数列設して設けた例を示したが、
セラミックバーナなど他のバーナを用いても良い。燃焼
装置2としてガスの燃焼を行う燃焼装置を例に示した
が、液体燃料で燃焼を行う燃焼装置を用いても良い。
Although the Bunsen type is shown as an example of the burner 11, an all-primary gas burner that burns an air-rich mixture of gas and combustion air may be used,
A premixed Bunsen gas burner that burns a gas-rich mixture of a gas and combustion air and supplies secondary air to a combustion unit may be used. As an example of the burner 11, an example in which a plurality of flattened bodies are provided and provided is shown.
Other burners such as a ceramic burner may be used. Although a combustion device that burns gas is shown as an example of the combustion device 2, a combustion device that burns with liquid fuel may be used.

【0032】吸収液の一例として臭化リチウム水溶液を
例に示したが、冷媒にアンモニア、吸収剤に水を利用し
たアンモニア水溶液など他の吸収液を用いても良い。熱
媒体の一例として、水道水を用い、冷却水回路の冷却水
と共用した例を示したが、冷却水回路の冷却水とは異な
る不凍液やオイルなど他の熱媒体を用いても良い。凝縮
用熱交換器、蒸発用熱交換器、吸収用熱交換器をコイル
状に設けた例を示したが、チューブアンドフィンや、積
層型熱交換器など他の形式の熱交換器を用いても良い。
Although an aqueous solution of lithium bromide has been described as an example of the absorbing liquid, other absorbing liquids such as an aqueous ammonia solution using ammonia as a refrigerant and water as an absorbent may be used. As an example of the heat medium, tap water is used and shared with the cooling water in the cooling water circuit. However, other heat medium such as antifreeze or oil different from the cooling water in the cooling water circuit may be used. Although the example in which the heat exchanger for condensation, the heat exchanger for evaporation, and the heat exchanger for absorption are provided in a coil shape is shown, the heat exchanger of another type such as a tube and fin or a stacked heat exchanger is used. Is also good.

【0033】上記の実施例では、外周壁面23bに設け
られた外周フィン25に本発明を適用した例を示した
が、内周壁面23aに内周フィンを設け、その内周フィ
ンの最上流端である上端に欠落を設けたり、内周フィン
の上流側に制限板30を設けても良い。なお、この場合
は、外周フィン25に欠落を設けたり、外周フィン25
の上流側に制限板30を設ける必要はない。
In the above-described embodiment, an example in which the present invention is applied to the outer peripheral fin 25 provided on the outer peripheral wall surface 23b has been described. However, the inner peripheral fin is provided on the inner peripheral wall surface 23a, and the most upstream end of the inner peripheral fin is provided. May be provided at the upper end, or the restriction plate 30 may be provided upstream of the inner peripheral fin. In this case, the outer peripheral fin 25 may be provided with a missing portion,
It is not necessary to provide the restriction plate 30 on the upstream side.

【図面の簡単な説明】[Brief description of the drawings]

【図1】燃焼装置および加熱容器の断面図である(第1
実施例)。
FIG. 1 is a cross-sectional view of a combustion device and a heating vessel (first example).
Example).

【図2】吸収式冷凍サイクルを用いた空調装置の概略図
である(第1実施例)。
FIG. 2 is a schematic diagram of an air conditioner using an absorption refrigeration cycle (first embodiment).

【図3】外周フィンの要部断面図である(第1実施
例)。
FIG. 3 is a sectional view of a main part of an outer peripheral fin (first embodiment).

【図4】外周フィンの要部拡大図である(第1実施
例)。
FIG. 4 is an enlarged view of a main part of an outer peripheral fin (first embodiment).

【図5】燃焼装置および加熱容器の断面図である(第2
実施例)。
FIG. 5 is a sectional view of a combustion device and a heating vessel (second example).
Example).

【図6】燃焼装置および加熱容器の断面図である(第3
実施例)。
FIG. 6 is a sectional view of a combustion device and a heating vessel (third view).
Example).

【図7】燃焼装置および加熱容器の断面図である(従来
例)。
FIG. 7 is a cross-sectional view of a combustion device and a heating vessel (conventional example).

【符号の説明】[Explanation of symbols]

2 燃焼装置 3 吸収式冷凍サイクル 10 加熱容器 11 バーナ 13 燃焼ファン 15 高温再生器 16 低温再生器 17 凝縮器 18 蒸発器 19 吸収器 20 溶液ポンプ 23 環状筒容器部 23b 外周壁面 25 外周フィン 25a 外周フィンの下部 27 排気口 28b 外周排気通路 30 制限板 Reference Signs List 2 Combustion device 3 Absorption refrigeration cycle 10 Heating vessel 11 Burner 13 Combustion fan 15 High temperature regenerator 16 Low temperature regenerator 17 Condenser 18 Evaporator 19 Absorber 20 Solution pump 23 Annular cylindrical container part 23b Outer peripheral wall surface 25 Outer peripheral fin 25a Outer peripheral fin Lower part 27 exhaust port 28b outer peripheral exhaust passage 30 restriction plate

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】燃料の燃焼を行うバーナ、このバーナに燃
焼用の空気を強制的に送る燃焼ファンを備えた燃焼装置
と、 この燃焼装置によって加熱されるとともに吸収液が供給
される加熱容器を備え、吸収液の一部を気化させる再生
器、この再生器で発生した気化冷媒を冷却して液化する
凝縮器、この凝縮器で液化した液化冷媒を低圧下で蒸発
させて熱媒体を冷却する蒸発器、この蒸発器で蒸発した
気化冷媒を吸収液に吸収させる吸収器、この蒸発器内で
気化冷媒を吸収した吸収液を前記再生器へ圧送する溶液
ポンプを備える吸収式冷凍サイクルと、を具備する吸収
式冷却装置において、 前記加熱容器は、上方から前記バーナを覆うとともに環
状の環状筒容器部を備えた断面略コ字型の容器形状を呈
し、 前記燃焼装置は、前記バーナで発生した排気ガスを、前
記環状筒容器部の壁面に沿って流す排気通路を備え、 前記環状筒容器部の壁面には、排気ガスの熱を効率的に
前記環状筒容器部へ伝えるフィンを備え、 このフィンの排気通路における最上流端部は、前記壁面
から遠い側が欠落していることを特徴とする吸収式冷却
装置。
1. A burner for burning fuel, a combustion device provided with a combustion fan for forcibly sending air for combustion to the burner, and a heating vessel heated by the combustion device and supplied with an absorbing liquid. A regenerator that evaporates a part of the absorbing liquid, a condenser that cools and liquefies the vaporized refrigerant generated by the regenerator, and cools the heat medium by evaporating the liquefied refrigerant liquefied by the condenser under low pressure. An evaporator, an absorber that absorbs the vaporized refrigerant evaporated by the evaporator into an absorbent, an absorption refrigeration cycle including a solution pump that pumps the absorbed liquid that has absorbed the vaporized refrigerant in the evaporator to the regenerator, In the absorption type cooling device provided, the heating container covers the burner from above and presents a substantially U-shaped container shape having an annular tubular container portion, and the combustion device is generated by the burner. An exhaust passage for flowing gas gas along a wall surface of the annular cylindrical container portion; a fin for efficiently transmitting heat of exhaust gas to the annular cylindrical container portion on a wall surface of the annular cylindrical container portion; An uppermost end of the fin in the exhaust passage is missing a portion farther from the wall surface.
【請求項2】請求項1の吸収式冷却装置において、 前記フィンの最上流端部は、下流側に向かうに従って欠
落幅が小さくなるように斜めにカットした形状に設けら
れたことを特徴とする吸収式冷却装置。
2. The absorption cooling device according to claim 1, wherein the most upstream end portion of the fin is cut obliquely so that a chipped width decreases toward a downstream side. Absorption cooling device.
【請求項3】燃料の燃焼を行うバーナ、このバーナに燃
焼用の空気を強制的に送る燃焼ファンを備えた燃焼装置
と、 この燃焼装置によって加熱されるとともに吸収液が供給
される加熱容器を備え、吸収液の一部を気化させる再生
器、この再生器で発生した気化冷媒を冷却して液化する
凝縮器、この凝縮器で液化した液化冷媒を低圧下で蒸発
させて熱媒体を冷却する蒸発器、この蒸発器で蒸発した
気化冷媒を吸収液に吸収させる吸収器、この蒸発器内で
気化冷媒を吸収した吸収液を前記再生器へ圧送する溶液
ポンプを備える吸収式冷凍サイクルと、を具備する吸収
式冷却装置において、 前記加熱容器は、上方から前記バーナを覆うとともに環
状の環状筒容器部を備えた断面略コ字型の容器形状を呈
し、 前記燃焼装置は、前記バーナで発生した排気ガスを、前
記環状筒容器部の壁面に沿って流す排気通路を備え、 前記環状筒容器部の壁面には、排気ガスの熱を効率的に
前記環状筒容器部へ伝えるフィンを備え、 前記排気通路は、前記フィンの上流側に、排気ガスを前
記環状筒容器部の壁面側に導く制限板を備えることを特
徴とする吸収式冷却装置。
3. A burner for burning fuel, a combustion device provided with a combustion fan for forcibly sending air for combustion to the burner, and a heating vessel heated by the combustion device and supplied with an absorbing liquid. A regenerator that evaporates a part of the absorbing liquid, a condenser that cools and liquefies the vaporized refrigerant generated by the regenerator, and cools the heat medium by evaporating the liquefied refrigerant liquefied by the condenser under low pressure. An evaporator, an absorber that absorbs the vaporized refrigerant evaporated by the evaporator into an absorbent, an absorption refrigeration cycle including a solution pump that pumps the absorbed liquid that has absorbed the vaporized refrigerant in the evaporator to the regenerator, In the absorption cooling device provided, the heating container covers the burner from above and presents a substantially U-shaped container shape having an annular tubular container portion, and the combustion device is generated by the burner. An exhaust passage for flowing gas gas along a wall surface of the annular cylindrical container portion; a fin for efficiently transmitting heat of exhaust gas to the annular cylindrical container portion on a wall surface of the annular cylindrical container portion; An absorption-type cooling device, wherein the exhaust passage includes a restriction plate on an upstream side of the fin to guide exhaust gas to a wall surface side of the annular cylindrical container portion.
【請求項4】請求項3の吸収式冷却装置において、 前記排気通路は、排気ガスを収集して外部に排出する排
気口を備え、 前記制限板は、前記排気口に近い側の排気ガスの通る排
気面積を小さくし、前記排気口から遠い側の排気ガスの
通る排気面積を大きくすることを特徴とする吸収式冷却
装置。
4. The absorption cooling device according to claim 3, wherein the exhaust passage has an exhaust port for collecting exhaust gas and discharging the exhaust gas to the outside, and the restricting plate is provided for exhaust gas on a side close to the exhaust port. An absorption type cooling apparatus characterized in that an exhaust area through which the exhaust gas passes is reduced and an exhaust area through which exhaust gas farther from the exhaust port passes is increased.
JP13951497A 1997-05-29 1997-05-29 Absorption cooling device Expired - Fee Related JP3481079B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13951497A JP3481079B2 (en) 1997-05-29 1997-05-29 Absorption cooling device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13951497A JP3481079B2 (en) 1997-05-29 1997-05-29 Absorption cooling device

Publications (2)

Publication Number Publication Date
JPH10332222A true JPH10332222A (en) 1998-12-15
JP3481079B2 JP3481079B2 (en) 2003-12-22

Family

ID=15247080

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13951497A Expired - Fee Related JP3481079B2 (en) 1997-05-29 1997-05-29 Absorption cooling device

Country Status (1)

Country Link
JP (1) JP3481079B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109654770A (en) * 2019-01-29 2019-04-19 浙江佑伏能源科技有限公司 A kind of high-efficiency generator for absorption type cold-hot unit

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109654770A (en) * 2019-01-29 2019-04-19 浙江佑伏能源科技有限公司 A kind of high-efficiency generator for absorption type cold-hot unit
CN109654770B (en) * 2019-01-29 2023-05-30 上海佑伏科技有限公司 Efficient generator for absorption type cold and hot unit

Also Published As

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