JPH02192554A - Air-cooled absorptive type refrigerator - Google Patents
Air-cooled absorptive type refrigeratorInfo
- Publication number
- JPH02192554A JPH02192554A JP1104789A JP1104789A JPH02192554A JP H02192554 A JPH02192554 A JP H02192554A JP 1104789 A JP1104789 A JP 1104789A JP 1104789 A JP1104789 A JP 1104789A JP H02192554 A JPH02192554 A JP H02192554A
- Authority
- JP
- Japan
- Prior art keywords
- absorber
- heat exchanger
- cooled
- concentrated liquid
- air
- 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
Links
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Abstract
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.
〈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一部再循環し
て、濃液と混合して吸収器に散布する構成となっている
。<Prior Art> As a technology of a conventional air-cooled absorption refrigerator, for example, Japanese Patent Laid-Open No. 58-208559 is known. In this case, the absorption chiller recirculates the concentrated liquid directly from the low-temperature heat exchanger, or partially recirculates the dilute acid sent from the absorber to the high-temperature regenerator, mixes it with the concentrated liquid, and supplies it to the absorber. It is configured to be dispersed.
〈発明が解決しようとする課題〉
しかし、従来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
ラッシュするものとなる。このため、限られた長さの縦
型流下液膜式吸収器では、蒸発器からの冷媒蒸気を十分
に吸収できないと云う問題があった。<Problem to be solved by the invention> However, in conventional air-cooled absorption refrigerators of this type, 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 sprayed on the absorber, it becomes a flash. For this reason, there is a problem in that a vertical falling film type absorber having a limited length cannot sufficiently absorb refrigerant vapor 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
、低温熱交換器出口から流出の痛液を、吸収器の流下管
位置にあって冷却空気で冷却する熱交換器を少なくとも
2個設け、濃液の上流側に当たる該熱交換器を前記流下
管の出口側の冷却空気で冷却し、最下流側に当たる該熱
交換器を前記流下管の入口側の冷却空気で冷却し、十分
冷却された濃液を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 refrigerating machine, in which the pain fluid flowing out from the outlet of a low-temperature heat exchanger is cooled by cooling air at a downstream pipe position of the absorber. At least two exchangers are provided, and the heat exchanger on the upstream side of the concentrated liquid is cooled with the cooling air on the outlet side of the downstream pipe, and the heat exchanger on the most downstream side is cooled with the cooling air on the inlet side of the downstream pipe. The concentrated liquid is cooled sufficiently and then sprayed using an absorber.
く作用〉
上記のような構成のため、高温再生器を出た濃液を、先
ず出口側(流下管の下部)を流れる冷却空気で冷却し、
最下流となる熱交換器には入口側(流下管の上部)の冷
却空気を通して冷却する。このため、濃液は吸収器内圧
力の飽和温度以下まで冷却されるので、吸収器でフラッ
シュすることもなく、容易に伝熱管に均等の散布がなさ
れる。また、吸収器内の冷媒蒸気通路は蒸発器で発生し
た冷媒蒸気のみとなるので、吸収器本来の性能を発揮す
る。Due to the above configuration, the concentrated liquid that exits the high-temperature regenerator is first cooled by cooling air flowing through the outlet side (lower part of the downstream pipe).
Cooling air from the inlet side (at the top of the downflow tube) is passed through the heat exchanger that is the most downstream side for cooling. For this reason, the concentrated liquid is cooled to below the saturation temperature of the pressure inside the absorber, so it does not flash in the absorber and is easily and evenly distributed over the heat exchanger tubes. Furthermore, since the refrigerant vapor passage within the absorber is filled with only the refrigerant vapor generated in the evaporator, the absorber exhibits its original performance.
〈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.
図面はパラレルフローの空冷吸収式冷凍機を示し、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に溜まった移液は吸収液ポンプ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
えた高温再生器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、且つ前記対向せる流下管4,6の中間上方にファ
ン8を設置し、また、前記吸収器1の流下管4の出口側
となる下部に設けた一つの熱交換器14の上端に、低温
熱交換器12を経て流れる濃液の上流側を導き、該熱交
換器14の下端より流出の最下流の濃液を、前記流下管
4の人口側となる上部に設けた二つ目の熱交換器15の
下端より導き、該熱交換器15の上端より流出させ濃液
を吸収器1の上端の散布部に導き散布する構成とじてな
る。The drawing shows a parallel flow air-cooled absorption refrigerator, in which 1 is an absorber in which a downflow pipe 4 with fins 3 is arranged vertically at the top, an evaporator 2 is provided at the upper end of the absorber 1, and an evaporator 2 is provided at the upper end of the absorber 1. The transferred liquid accumulated in the absorber 1 is guided from the low-temperature heat exchanger 12 to the high-temperature heat exchanger 11 via the absorption liquid pump 13 to the high-temperature regenerator 9 equipped with a burner 10, and the concentrated liquid generated in the high-temperature regenerator 9 is The liquid is led to a low temperature regenerator 3, and a flow pipe 6 with fins 3 disposed above the condenser 5 is provided at the lower part of the low temperature regenerator 7, and a flow pipe 6 with fins 3 disposed above the condenser 5 is provided at the lower part of the low temperature regenerator 7, and a flow pipe 6 with fins 3 disposed above the condenser 5 is provided at the lower part of the low temperature regenerator 7. A fan 8 is installed at the upper end of one heat exchanger 14 provided at the lower part of the outlet side of the downstream pipe 4 of the absorber 1, and the upstream side of the concentrated liquid flowing through the low-temperature heat exchanger 12 is installed at The most downstream concentrated liquid flowing out from the lower end of the heat exchanger 14 is guided from the lower end of the second heat exchanger 15 provided at the upper part of the downflow pipe 4 on the artificial side. The structure is such that the concentrated liquid flows out from the upper end and is guided to the dispersion section at the upper end of the absorber 1 and is sprayed.
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を通過させ、この濃液を、先ず
吸収器1の流下管4の下部位置に配役の熱交換器14の
上部に導き、該流下管4の出口側の冷却空気で冷却し、
この熱交換器14を流出した最下流となる濃液を流下管
4の上部位置の熱交換器15の下端から上端に導き、流
下管4の入口側で冷却するため、全体として多段的な能
率空冷となる。即ち、濃液は、吸収器内圧力の飽和温度
以下まで確実に冷却されるので、吸収器1の上部にあっ
ての散布でもフラッシュすることなく、容易に伝熱管に
均等に散布される。また、吸収器1内の冷媒蒸気通路は
、蒸発器2で発生した冷媒蒸気のみとなるので、吸収器
本来の性能を発揮させることができる。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 transferred to a low temperature via the high temperature heat exchanger 11. The intermediate concentrated liquid dispersed in the regenerator 7 and accumulated in the low-temperature regenerator 7 is passed through the low-temperature heat exchanger 12, and this concentrated liquid is first transferred to the heat exchanger located at the lower part of the downflow pipe 4 of the absorber 1. 14 and cooled by cooling air on the outlet side of the downstream pipe 4,
The most downstream concentrated liquid flowing out of the heat exchanger 14 is guided from the lower end to the upper end of the heat exchanger 15 at the upper position of the downflow pipe 4, and is cooled at the inlet side of the downflow pipe 4, resulting in multi-stage efficiency as a whole. Air-cooled. That is, since the concentrated liquid is reliably cooled to below the saturation temperature of the pressure inside the absorber, it is easily and evenly spread over the heat exchanger tubes without flashing even when it is spread at the upper part of the absorber 1. Moreover, since the refrigerant vapor passage in the absorber 1 is filled with only the refrigerant vapor generated in the evaporator 2, the absorber can exhibit its original performance.
〈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
器からの濃液を冷却空気で冷却する熱交換器を吸収器の
流下管部の上下位置に少なくとも2個設け、多段的な冷
却空気で能率冷却するため、確実に濃液を吸収器内圧力
の飽和温度以下まで冷却しえ、吸収器での散布に当たっ
てフラッシュを招かず、限られた長さの縦型流下液膜式
吸収器でも蒸発器からの冷媒蒸気を十分に吸収できる。<Effects of the Invention> As described above, the air-cooled absorption refrigerator of the present invention includes at least two heat exchangers for cooling the concentrated liquid from the low-temperature heat exchanger with cooling air at the upper and lower positions of the downstream pipe portion of the absorber. Because the system is equipped with a multi-stage cooling air system for efficient cooling, it is possible to reliably cool the concentrated liquid to below the saturation temperature of the pressure inside the absorber. A falling film absorber can also sufficiently absorb refrigerant vapor from the evaporator.
即ち、吸収器内の冷媒蒸気通路は、蒸発器で発生した冷
媒蒸気のみとなるので、吸収器本来の性能を発揮できる
等の効果を奏する。That is, since the refrigerant vapor passage within the absorber is filled with only the refrigerant vapor generated in the evaporator, it is possible to exhibit the original performance of the absorber.
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・・・バーナ、11・・・高温熱交換器、12・
・・低温熱交換器、
3・・・吸収液ポンプ、
14゜
5・・・熱交換
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...Burner, 11...High temperature heat exchanger, 12.
...Low temperature heat exchanger, 3...Absorption liquid pump, 14°5...Heat exchanger.
Claims (1)
熱交換器出口から流出の濃液を、吸収器の流下管位置に
あって冷却空気で冷却する熱交換器を少なくとも2個設
け、濃液の上流側に当たる該熱交換器を前記流下管の出
口側の冷却空気で冷却し、最下流側に当たる該熱交換器
を前記流下管の入口側の冷却空気で冷却し、十分冷却さ
れた濃液を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, at least two heat exchangers are installed at the downstream pipe position of the absorber to cool the concentrated liquid flowing out from the outlet of the low-temperature heat exchanger with cooling air. The heat exchanger on the upstream side is cooled with the cooling air on the outlet side of the downstream pipe, and the heat exchanger on the most downstream side is cooled with the cooling air on the inlet side of the downstream pipe, and the sufficiently cooled concentrated liquid is cooled. An air-cooled absorption chiller characterized by dispersion using an absorber.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1104789A JPH02192554A (en) | 1989-01-20 | 1989-01-20 | Air-cooled absorptive type refrigerator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1104789A JPH02192554A (en) | 1989-01-20 | 1989-01-20 | Air-cooled absorptive type refrigerator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH02192554A true JPH02192554A (en) | 1990-07-30 |
Family
ID=11767120
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1104789A Pending JPH02192554A (en) | 1989-01-20 | 1989-01-20 | Air-cooled absorptive type refrigerator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH02192554A (en) |
-
1989
- 1989-01-20 JP JP1104789A patent/JPH02192554A/en active Pending
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