JPH02192552A - Air-cooled absorptive type freezer - Google Patents

Air-cooled absorptive type freezer

Info

Publication number
JPH02192552A
JPH02192552A JP1104589A JP1104589A JPH02192552A JP H02192552 A JPH02192552 A JP H02192552A JP 1104589 A JP1104589 A JP 1104589A JP 1104589 A JP1104589 A JP 1104589A JP H02192552 A JPH02192552 A JP H02192552A
Authority
JP
Japan
Prior art keywords
absorber
heat exchanger
liquid
low temperature
cooled
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.)
Pending
Application number
JP1104589A
Other languages
Japanese (ja)
Inventor
Mokichi Kurosawa
黒沢 茂吉
Seiichiro Fujimaki
藤巻 誠一郎
Atsushi Sekikawa
関川 敦司
Tadahito Kobayashi
唯人 小林
Yonezo Ikumi
米造 井汲
Takao Tanaka
貴雄 田中
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.)
Sanyo Electric Co Ltd
Tokyo Gas Co Ltd
Original Assignee
Sanyo Electric Co Ltd
Tokyo Gas Co Ltd
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 Sanyo Electric Co Ltd, Tokyo Gas Co Ltd filed Critical Sanyo Electric Co Ltd
Priority to JP1104589A priority Critical patent/JPH02192552A/en
Publication of JPH02192552A publication Critical patent/JPH02192552A/en
Pending legal-status Critical Current

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  • Sorption Type Refrigeration Machines (AREA)

Abstract

PURPOSE:To prevent liquid of high concentration from being flashed within an absorber and make a sufficient absorption of refrigerant vapor from an evaporator with an absorbing liquid within an absorber by a method wherein the solution of high concentra tion is cooled by a heat exchanger arranged in the midway of a high concentration liquid pipe extending from an outlet of a low temperature heat exchanger to the absorber, thereafter it is sprayed by the absorber. CONSTITUTION:Dilution liquid accumulated in an absorber 1 is guided through an absorptive liquid pump 13 from a low temperature heat exchanger 12 to a high tempera ture regenerator 9 having a burner 10 via a high temperature heat exchanger 11, the high concentration liquid generated at the high temperature regenerator 9 is guided to a low temperature regenerator 3. A flowing-down pipe 6 having some fins 3 at an upper part of the condensor 5 is arranged at a lower part of the low temperature regenerator 7 and then a fan 8 is mounted at an intermediate upper part of the opposed flowing-down pipes 4 and 6. In this case, the intermediate concentrated liquid flowed out of the low temperature regenerator 7 is passed through the low temperature heat exchanger 12, guided to a high concentrated liquid cooler 14 acting as an air cooled heat exchanger arranged above the evaporator 2 and this liquid is sprayed over the absorptive unit 1.

Description

【発明の詳細な説明】 〈産業上の利用分野〉 本発明は空冷吸収式冷凍機の改良に関するものである。[Detailed description of the invention] <Industrial application field> The present invention relates to improvements in air-cooled absorption refrigerators.

く−従来の技術〉 従来の空冷吸収式冷凍機の技術としては、例えば特開昭
58−208559号公報が知られている。この場合の
吸収式冷凍機は、低温熱交換器を出た濃液を直接、或い
は吸収器から高温再生器へ送られる稀酸を再循環して濃
液を混合して吸収器に散布する構成としてなる。
- Prior Art> As a conventional technology of an air-cooled absorption refrigerator, for example, Japanese Patent Laid-Open No. 58-208559 is known. In this case, the absorption chiller has a configuration in which the concentrated liquid that exits the low-temperature heat exchanger is recycled directly, or the dilute acid sent from the absorber to the high-temperature regenerator is recirculated, mixed with the concentrated liquid, and sprayed onto the absorber. It becomes as.

〈発明が解決しようとする課題〉 しかし、従来のこの種の空冷吸収式冷凍機においては、
低温熱交換器を出た濃液の温度が、吸収器内圧力の飽和
温度よりも高いため、濃液が吸収器に散布されたとき、
フラッシュするため、限られた長さの縦型流下液模式吸
収器では、蒸発器からの冷媒蒸発を十分に吸収すること
ができないないと云う問題があった。
<Problem to be solved by the invention> However, in this type of conventional air-cooled absorption refrigerator,
Since the temperature of the concentrated liquid leaving the low-temperature heat exchanger is higher than the saturation temperature of the pressure inside the absorber, when the concentrated liquid is sprayed into the absorber,
Due to flashing, there is a problem in that a vertical falling liquid type absorber having a limited length cannot sufficiently absorb refrigerant evaporation from the evaporator.

本発明は上記実情に鑑み、吸収器内での濃液のフラッシ
ュを防止し、蒸発器からの冷媒蒸気を吸収器内の吸収液
が十分に吸収することができるようにした空冷吸収式冷
凍機を提供することを目的としたものである。
In view of the above-mentioned circumstances, the present invention is an air-cooled absorption refrigerator that prevents the flash of concentrated liquid in the absorber and allows the absorbent liquid in the absorber to sufficiently absorb refrigerant vapor from the evaporator. The purpose is to provide the following.

く課題を解決するための手段〉 本発明は、パラレルフローの空冷吸収式冷凍機において
、低温熱交換器の出口から吸収器へ至る濃液管路の途中
に濃液を冷却空気で冷却する熱交換器を設け、該熱交換
器で濃液を冷却した後、吸収器で散布するようにしたも
のである。
Means for Solving the Problems> The present invention provides a parallel flow air-cooled absorption refrigerator that cools the concentrated liquid with cooling air in the middle of the concentrated liquid pipe line from the outlet of the low-temperature heat exchanger to the absorber. An exchanger is provided, and after the concentrated liquid is cooled by the heat exchanger, it is sprayed by an absorber.

く作用〉 上記のような構成のため、高温再生器から低温再生器を
流出する濃液が低温熱交換器を経て吸収器に向かう途中
の熱交換器で冷却空気を持冷却し、この濃液を吸収器内
圧力の飽和温度以下まで冷却するため、吸収器内での濃
液のフラッシュすることもなく、且つ該吸収器内の冷媒
蒸気通路は、蒸発器で発生した冷媒蒸気のみであるので
、吸収器内の冷媒蒸気の圧力損失も小さい。
Due to the above configuration, the concentrated liquid flowing out from the high temperature regenerator to the low temperature regenerator passes through the low temperature heat exchanger and is cooled with cooling air in the heat exchanger on its way to the absorber. Since the liquid is cooled to below the saturation temperature of the pressure inside the absorber, there is no flash of concentrated liquid in the absorber, and the refrigerant vapor passage inside the absorber is only for the refrigerant vapor generated in the evaporator. , the pressure loss of refrigerant vapor in the absorber is also small.

〈実施例〉 以下、本発明を実施例の図面に基づいて説明すれば、次
の通りである。
<Example> The present invention will be described below based on the drawings of the example.

1はフィン3付の流下管4を上部に鉛直配設してなる吸
収器で、該吸収器1の上端に蒸発器2を設けると共に、
該吸収器1に溜まった稀酸を吸収液ポンプ13を介し低
温熱交換器12から高温熱交換器11を経てバーナ10
を備える高温再生器9に導き、該高温再生器9にて発生
する濃液を低温再生器3に導くようにし、該低温再生器
7の下部に凝縮器5の上部に配設のフィン3付の流下管
6を設け、且つこの対向せる流下管4.6の中間上方に
ファン8を設置しパラレルフロー型の空冷吸収式冷凍機
としてなる。
Reference numeral 1 denotes an absorber in which a downflow pipe 4 with fins 3 is arranged vertically at the top, and an evaporator 2 is provided at the upper end of the absorber 1.
The dilute acid accumulated in the absorber 1 is transferred from the low temperature heat exchanger 12 to the high temperature heat exchanger 11 via the absorbent pump 13 to the burner 10.
The concentrated liquid generated in the high-temperature regenerator 9 is guided to the low-temperature regenerator 3, and the lower part of the low-temperature regenerator 7 is provided with fins 3 disposed on the upper part of the condenser 5. A downflow pipe 6 is provided, and a fan 8 is installed above the middle of the opposing downflow pipes 4 and 6 to form a parallel flow type air-cooled absorption refrigerator.

この場合、低温再生器7から流出の中間濃液を低温熱交
換器12を通過して前記蒸発器2の上部に配設した空冷
の熱交換器となる濃液冷却器14に導き、吸収器1の上
部に散布する構成としている。
In this case, the intermediate concentrated liquid flowing out from the low-temperature regenerator 7 passes through the low-temperature heat exchanger 12 and is guided to the concentrated liquid cooler 14 which is an air-cooled heat exchanger disposed above the evaporator 2. The composition is such that it is sprayed on the top of 1.

次に、この作用を説明すると、このような空冷吸収式冷
凍機の運転にあっては、バーナ10で熱せられる高温再
生器15にて発生の濃液を高温熱交換器11を介して低
温再生器7で散布し、該低温再生器7で溜まった中間濃
液を、低温熱交換器12を通過してファン8の回転にて
流れる冷却空気を受ける濃液冷却器14で更に冷却し、
吸収器1の内圧力の飽和温度以下まで冷却するので吸収
器1内で濃液がフラッシュしない。従って、吸収器1内
の冷媒蒸気通路にあっては、凝縮器5から流れる冷媒が
蒸発器2で蒸発し、該蒸発器2で発生した冷媒蒸気のみ
であるため、吸収器1内の冷媒蒸気の圧力損失が少ない
ものとなる。
Next, to explain this effect, when operating such an air-cooled absorption refrigerator, the concentrated liquid generated in the high-temperature regenerator 15 heated by the burner 10 is regenerated at a low temperature via the high-temperature heat exchanger 11. The intermediate concentrated liquid dispersed in the container 7 and accumulated in the low-temperature regenerator 7 is further cooled in the concentrated liquid cooler 14 which passes through the low-temperature heat exchanger 12 and receives cooling air flowing by the rotation of the fan 8.
Since the absorber 1 is cooled to a temperature below the saturation temperature of the internal pressure, the concentrated liquid does not flash within the absorber 1. Therefore, in the refrigerant vapor passage in the absorber 1, the refrigerant flowing from the condenser 5 is evaporated in the evaporator 2, and only the refrigerant vapor generated in the evaporator 2 is present. This results in less pressure loss.

〈発明の効果〉 上述のように本発明の空冷吸収式冷凍機は、低温熱交換
器から吸収器に至る濃液管路の途中に空冷の熱交換器を
設け、濃液の温度を吸収器内圧力の飽和温度以下まで冷
却するようにしたため、該吸収器に散布してもフラッシ
ュを招かず、従って吸収器内の冷媒蒸気通路にあって蒸
発器で発生した冷媒蒸気のみであるので、該吸収器内の
冷媒蒸気の圧力損失も小さく、延いては吸収器の性能が
向上することができる効果を奏する。
<Effects of the Invention> As described above, the air-cooled absorption refrigerator of the present invention is provided with an air-cooled heat exchanger in the middle of the concentrated liquid pipe line from the low-temperature heat exchanger to the absorber, and the temperature of the concentrated liquid is adjusted to the absorber. Since it is cooled to below the saturation temperature of the internal pressure, it does not cause flash even if it is sprayed into the absorber.Therefore, only the refrigerant vapor generated in the evaporator is present in the refrigerant vapor passage in the absorber. The pressure loss of the refrigerant vapor within the absorber is also small, which has the effect of improving the performance of the absorber.

【図面の簡単な説明】[Brief explanation of the drawing]

図面は本発明の使用実施例を示す概略図である。 1・・・吸収器、2・・・蒸発器、3・・・フィン、4
・・・流下管、5・・・凝縮器、6・・・流下管、7・
・・低温再生器、8・・・ファン、9・・・高温再生器
、10・・・バーす、11・・・高温熱交換器、12・
・・低温熱交換器、13・・・吸収液ポンプ、14・・
・濃液冷却器。
The drawings are schematic illustrations of embodiments of use of the invention. 1...Absorber, 2...Evaporator, 3...Fin, 4
... Downstream pipe, 5... Condenser, 6... Downstream pipe, 7.
... low temperature regenerator, 8 ... fan, 9 ... high temperature regenerator, 10 ... bar, 11 ... high temperature heat exchanger, 12.
...Low temperature heat exchanger, 13...Absorption liquid pump, 14...
・Concentrated liquid cooler.

Claims (1)

【特許請求の範囲】[Claims] 1、パラレルフローの空冷吸収式冷凍機において、低温
熱交換器の出口から吸収器へ至る濃液管路の途中に濃液
を冷却空気で冷却する熱交換器を設け、該熱交換器で濃
液を冷却した後、吸収器で散布することを特徴とした空
冷吸収式冷凍機。
1. In a parallel flow air-cooled absorption refrigerator, a heat exchanger for cooling the concentrated liquid with cooling air is installed in the middle of the concentrated liquid pipe line from the outlet of the low-temperature heat exchanger to the absorber, and the heat exchanger cools the concentrated liquid with cooling air. An air-cooled absorption chiller characterized by cooling the liquid and then dispersing it in an absorber.
JP1104589A 1989-01-20 1989-01-20 Air-cooled absorptive type freezer Pending JPH02192552A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1104589A JPH02192552A (en) 1989-01-20 1989-01-20 Air-cooled absorptive type freezer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1104589A JPH02192552A (en) 1989-01-20 1989-01-20 Air-cooled absorptive type freezer

Publications (1)

Publication Number Publication Date
JPH02192552A true JPH02192552A (en) 1990-07-30

Family

ID=11767069

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1104589A Pending JPH02192552A (en) 1989-01-20 1989-01-20 Air-cooled absorptive type freezer

Country Status (1)

Country Link
JP (1) JPH02192552A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105202805A (en) * 2014-06-26 2015-12-30 江苏太阳光伏科技有限公司 Solar air conditioner

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105202805A (en) * 2014-06-26 2015-12-30 江苏太阳光伏科技有限公司 Solar air conditioner
CN105202805B (en) * 2014-06-26 2018-03-09 江苏太阳光伏科技有限公司 A kind of solar airconditioning

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