JPS6020670B2 - absorption refrigerator - Google Patents
absorption refrigeratorInfo
- Publication number
- JPS6020670B2 JPS6020670B2 JP5639977A JP5639977A JPS6020670B2 JP S6020670 B2 JPS6020670 B2 JP S6020670B2 JP 5639977 A JP5639977 A JP 5639977A JP 5639977 A JP5639977 A JP 5639977A JP S6020670 B2 JPS6020670 B2 JP S6020670B2
- Authority
- JP
- Japan
- Prior art keywords
- low
- temperature regenerator
- condenser
- temperature
- block
- 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.)
- Expired
Links
- 238000010521 absorption reaction Methods 0.000 title claims description 7
- 239000006096 absorbing agent Substances 0.000 claims description 11
- 238000010438 heat treatment Methods 0.000 claims description 9
- 239000003507 refrigerant Substances 0.000 claims description 3
- 238000005192 partition Methods 0.000 description 9
- 239000007788 liquid Substances 0.000 description 6
- 239000004071 soot Substances 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 230000009977 dual effect Effects 0.000 description 3
- 230000005856 abnormality Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000007789 sealing Methods 0.000 description 2
- 101100204059 Caenorhabditis elegans trap-2 gene Proteins 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003350 kerosene Substances 0.000 description 1
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 1
- 229910052753 mercury Inorganic materials 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000000638 solvent extraction Methods 0.000 description 1
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Description
【発明の詳細な説明】
この発明は高温再生器、低温再生器、凝縮器、蒸発器、
吸収器、熱交換器、1冷煤循環ポンプおよび溶液ポンプ
をそなえた吸収式冷凍機に関するものである。[Detailed Description of the Invention] This invention provides a high temperature regenerator, a low temperature regenerator, a condenser, an evaporator,
This invention relates to an absorption refrigerator equipped with an absorber, a heat exchanger, a cold soot circulation pump, and a solution pump.
二重効用式冷凍機における暖房サイクルの構成手段には
、溢水器を使用するものと、凝縮器を使用するものとが
ある。There are two ways to configure the heating cycle in a dual-effect refrigerator: one that uses a flooder and the other that uses a condenser.
温水器を使用するものでは、高温再生器、温水器のブロ
ックと凝縮器、低温再生器、吸収器のブロックとに二分
するが、両ブロックの圧力差がlk9/地になっても同
一シェル内で二分していないので問題はない。また、凝
縮器を温水器として使用するものでも、二つのブロック
に遮断しないで「冷凍機全体をそのまま使用する手段を
とれば問題はないし、二つのブロックに遮断しても、蒸
発器および吸収器、低温再生器および凝縮器をそれぞれ
のシェル内に構成する双胴形を採用すれば問題はない。
しかし、凝縮器、低温再生器、蒸発器、吸収器を同一シ
ェル内におさめ、二つのブロックに遮断する暖房サイク
ルを採用すれば、凝縮器および低温再生器のブロックと
蒸発器および吸収器のブロックとを同一シェル内で二分
することになり、それぞれを分離しているシェル内の隔
壁板が、異常時に少なくともlk9/地の圧力差に耐え
られなければならなくなり、構造が極めて限定され、シ
ェル内部の構造および配置に制約を受けるため実施され
ていない。For those that use a water heater, the block is divided into two blocks: a high-temperature regenerator, water heater block, and a condenser, low-temperature regenerator, and absorber block, but even if the pressure difference between the two blocks is lk9/kg, they are still in the same shell. There is no problem because it is not divided into two. In addition, even if the condenser is used as a water heater, there is no problem if you use the entire refrigerator as it is without separating it into two blocks, or if you use the method of using the entire refrigerator as is, even if it is separated into two blocks, the evaporator and absorber There is no problem if a twin shell type is adopted in which a low temperature regenerator and a condenser are constructed in each shell.
However, if you adopt a heating cycle in which the condenser, low-temperature regenerator, evaporator, and absorber are housed in the same shell and separated into two blocks, the condenser and low-temperature regenerator block and the evaporator and absorber block can be used. are divided into two parts within the same shell, and the partition plate inside the shell that separates each must be able to withstand a pressure difference of at least lk9/ground in the event of an abnormality, which makes the structure extremely limited and the inside of the shell This has not been implemented due to restrictions on the structure and placement of the
この発明の目的は、単8同形シェルを採用し、暖房サイ
クル時における所定の圧力差を超えた圧力差の発生に対
して、シェル内を凝縮器および低温再生器と蒸発器およ
び吸収器とに区画している隔壁板を保護することができ
る吸収式冷凍機を提供するにある。An object of the present invention is to adopt an AAA shell, and to prevent a pressure difference exceeding a predetermined pressure difference from occurring during a heating cycle, a condenser, a low-temperature regenerator, an evaporator, and an absorber are installed in the shell. An object of the present invention is to provide an absorption refrigerator capable of protecting partitioning partition plates.
まず、この発明にかかる二重効用吸収式冷凍機の一例を
第1図により説明する。First, an example of a dual-effect absorption refrigerator according to the present invention will be explained with reference to FIG.
冷凍機は主な構成要素として高温再生器1、低温再生器
2、凝縮器3、蒸発器4、吸収器5、熱交換器6、袷煤
循環ポンプ7、溶液循環ポンプ8をそなえており、各機
器は図示のようにバルブ9,10,11,12,13,
14を取付けた配管によりつらねられている。The refrigerator has a high temperature regenerator 1, a low temperature regenerator 2, a condenser 3, an evaporator 4, an absorber 5, a heat exchanger 6, a soot circulation pump 7, and a solution circulation pump 8 as main components. Each device has valves 9, 10, 11, 12, 13,
It is suspended by piping with 14 attached.
低温再生器2および凝縮器3は隔壁17で区画された同
一シェル内の一方の部分におさめられ、蒸発器4および
吸収器5は他方の部分におさめられている。暖房サイク
ル時には各バルブ9,10,11,12,13,14を
遮断する。The low-temperature regenerator 2 and the condenser 3 are housed in one part of the same shell divided by a partition wall 17, and the evaporator 4 and the absorber 5 are housed in the other part. During the heating cycle, each valve 9, 10, 11, 12, 13, 14 is shut off.
都市ガス、灯油などの熱源15で加熱された溶液は「高
温再生器1内で冷媒を分離し、分離された冷擬は低温再
生器2の管内を通り、管外の溶液を加熱して、高温再生
器1に戻る。一方、低温再生器2の管外の溶液は加熱さ
れて袷煤を分離し、分離された冷煤は凝縮器3で管内を
通る温水16の加熱源として働き、凝縮した袷煤は低温
再生器2に戻る。このようにして暖房サイクルが形成さ
れる。この暖房サイクルでは、低温側の蒸発器4および
吸収器5がtバルブ10〜13とシェル内の隔壁17と
で高温側と区画されている。The solution heated by a heat source 15 such as city gas or kerosene is separated into a refrigerant in the high-temperature regenerator 1, and the separated refrigerant passes through the pipes of the low-temperature regenerator 2, which heats the solution outside the pipe. It returns to the high temperature regenerator 1. On the other hand, the solution outside the tube of the low temperature regenerator 2 is heated to separate the soot, and the separated cold soot acts as a heating source for the hot water 16 passing through the tube in the condenser 3, and is condensed. The generated soot returns to the low-temperature regenerator 2. In this way, a heating cycle is formed. In this heating cycle, the evaporator 4 and absorber 5 on the low-temperature side are connected to the T-valves 10 to 13 and the partition wall 17 in the shell. It is separated from the high temperature side.
正常運転時には、低温側は高真空に保たれ、隔壁ITに
より区画された低温再生器2および凝縮器3の圧力は2
0財物日鱗bs以下であり、したがって、隔壁17の差
圧は20仇岬Hga戊程度であるが、運転に異常が生じ
ると、低温再生器2および凝縮器3の圧力は、高温再生
器1の圧力まで、あるいは外部との洩れが発生すると大
気圧まで昇圧する。その時の隔壁17の差圧はlk9/
泳程度となり、隔壁17が変形したり、破損したりする
。この発明の特徴は、高温側ブロックと低温側ブロック
との間に、両ブロック間の圧力差が所定値を超えたとき
に、両ブロック同士を蓮通させる安全装置を設置したも
のである。つぎに、この発明の一実施態様を第2図によ
り説明する。During normal operation, the low temperature side is maintained at a high vacuum, and the pressure in the low temperature regenerator 2 and condenser 3, which are separated by the partition wall IT, is 2.
Therefore, the differential pressure across the partition wall 17 is about 20 Hga, but if an abnormality occurs in the operation, the pressure in the low-temperature regenerator 2 and the condenser 3 will be lower than that in the high-temperature regenerator 1. or, if a leak occurs with the outside, the pressure increases to atmospheric pressure. The differential pressure across the partition wall 17 at that time is lk9/
As a result, the partition wall 17 may be deformed or damaged. A feature of this invention is that a safety device is installed between the high temperature side block and the low temperature side block to allow the blocks to pass through each other when the pressure difference between the blocks exceeds a predetermined value. Next, one embodiment of the present invention will be explained with reference to FIG.
トラツプ23Aとトラツプ238とは水銀などのシール
液22を入れたUシール管21を介して連結されている
。The trap 23A and the trap 238 are connected via a U-seal tube 21 containing a sealing liquid 22 such as mercury.
トラップ23Aはバルブ27Aを取付けた連絡管26A
を介して低温側連絡管28に接続されており、トラップ
238はバルブ27Bを取付けた連絡管26Bを介して
高温側連絡管29に接続されている。トラツプ23A,
23Bの底部にはそれぞれプラグ24A,24Bを取付
けたドレン排出口が設けられ、トラツプ26Bの上部に
はプラグ25を敬付けたUシール液の注入口が設けられ
ている。前記のような高温側と低温側との両ブロック間
に所定の圧力差が生ずると、シール液22がトラップ2
3A内に飛散して、高温側と蓬温側とが連通する。Trap 23A is connecting pipe 26A with valve 27A attached.
The trap 238 is connected to the high temperature side communication pipe 29 via a communication pipe 26B to which a valve 27B is attached. Trap 23A,
A drain outlet with plugs 24A and 24B attached thereto is provided at the bottom of the trap 23B, and a U-seal liquid inlet with a plug 25 attached is provided at the top of the trap 26B. When a predetermined pressure difference occurs between the blocks on the high temperature side and the low temperature side as described above, the sealing liquid 22 flows into the trap 2.
3A, and the high temperature side and the low temperature side communicate with each other.
なお、高温側と低温側との間にラプチヤーデイスクを設
置したり、高温側と低温側との圧力を検出する圧力スイ
ッチを介して電動弁を作動させたり、溶液でUシールを
構成したりすることによっても、同じような効果を得る
ことができる。In addition, it is possible to install a rupture disk between the high temperature side and the low temperature side, operate an electric valve via a pressure switch that detects the pressure between the high temperature side and the low temperature side, or configure a U-seal with a solution. A similar effect can be obtained by doing so.
以上説明したように、この発明によれば〜暖房サイクル
時における所定の圧力差を超えた圧力差の発生に対して
冷凍機を保護することができ、シェル内の隔壁を耐圧力
構造にする必要がないので、シェル内の配置、構成に制
約がなくなる。As explained above, according to the present invention, it is possible to protect the refrigerator from the occurrence of a pressure difference exceeding a predetermined pressure difference during the heating cycle, and it is necessary to make the partition wall in the shell a pressure-resistant structure. There are no restrictions on placement and configuration within the shell.
第1図はこの発明にかかわる二重効用吸収式冷凍機の一
例を示す系統図、第2図はこの発明の一実施態様を示す
断面図である。
1……高温再生器、2……低温再生器、3・・・・・・
凝縮器、4・・・・・・蒸発器、5……吸収器、6・・
…・熱交換器、7・・・…袷媒循環ポンプ、8……溶液
循環ポンプ、9〜14・・・・・・バルブ、17……隔
墜、21……Uシール管、22………Uシール液〜 2
3A,23B……Uシール液のトラップ「 24A,2
4B……ドレンの排出口のプラグ、25……Uシール液
の注入口のプラグ、26A,26B・・・…連絡管、2
7A,278・・・…バルブ、28…・・・低温側連絡
管、29・・・…高温側連絡管。
好‘囚
鰭Z図FIG. 1 is a system diagram showing an example of a dual-effect absorption refrigerator according to the present invention, and FIG. 2 is a sectional view showing an embodiment of the present invention. 1...High temperature regenerator, 2...Low temperature regenerator, 3...
Condenser, 4...Evaporator, 5...Absorber, 6...
... Heat exchanger, 7 ... Medium circulation pump, 8 ... Solution circulation pump, 9 to 14 ... Valve, 17 ... Separation, 21 ... U seal pipe, 22 ... ...U seal liquid ~ 2
3A, 23B...U seal liquid trap 24A, 2
4B...Drain outlet plug, 25...U seal liquid inlet plug, 26A, 26B...Connection pipe, 2
7A, 278... Valve, 28... Low temperature side communication pipe, 29... High temperature side communication pipe. Favorite prisoner fin Z diagram
Claims (1)
器、冷媒ポンプおよび溶液ポンプをそなえ、高温再生器
、低温再生器、凝縮器からなる高温ブロツクと、吸収器
、蒸発器からなる低温ブロツクとを遮断して高温側ブロ
ツクで暖房サイクルを構成する吸収式冷凍機において、
前記高温側ブロツクと低温側ブロツクとの間に両ブロ
ツク間の圧力差が所定値を超えたときに両ブロツク同士
を連通させる安全装置を設置したことを特徴とする吸収
式冷凍機。1 Equipped with a high-temperature regenerator, a low-temperature regenerator, a condenser, an evaporator, a heat exchanger, a refrigerant pump, and a solution pump, and consists of a high-temperature block consisting of a high-temperature regenerator, a low-temperature regenerator, and a condenser, an absorber, and an evaporator. In an absorption chiller, the heating cycle is constructed with the high temperature block separated from the low temperature block.
An absorption chiller characterized in that a safety device is installed between the high-temperature side block and the low-temperature side block to connect the two blocks to each other when the pressure difference between the two blocks exceeds a predetermined value.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5639977A JPS6020670B2 (en) | 1977-05-18 | 1977-05-18 | absorption refrigerator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5639977A JPS6020670B2 (en) | 1977-05-18 | 1977-05-18 | absorption refrigerator |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS53141952A JPS53141952A (en) | 1978-12-11 |
JPS6020670B2 true JPS6020670B2 (en) | 1985-05-23 |
Family
ID=13026115
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP5639977A Expired JPS6020670B2 (en) | 1977-05-18 | 1977-05-18 | absorption refrigerator |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6020670B2 (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS625367U (en) * | 1985-03-16 | 1987-01-13 | ||
JPS63107597A (en) * | 1986-10-24 | 1988-05-12 | 第一電子工業株式会社 | Ic card |
JPH0522953B2 (en) * | 1985-04-26 | 1993-03-31 | Kyodo Printing Co Ltd |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP5055071B2 (en) * | 2007-09-18 | 2012-10-24 | 日立アプライアンス株式会社 | Absorption refrigerator |
-
1977
- 1977-05-18 JP JP5639977A patent/JPS6020670B2/en not_active Expired
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS625367U (en) * | 1985-03-16 | 1987-01-13 | ||
JPH0522953B2 (en) * | 1985-04-26 | 1993-03-31 | Kyodo Printing Co Ltd | |
JPS63107597A (en) * | 1986-10-24 | 1988-05-12 | 第一電子工業株式会社 | Ic card |
Also Published As
Publication number | Publication date |
---|---|
JPS53141952A (en) | 1978-12-11 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US4265094A (en) | Unitized refrigeration and water heating system | |
JPS58500772A (en) | improved refrigeration pump | |
US4432208A (en) | Cold trap | |
JPS6020670B2 (en) | absorption refrigerator | |
JP2008537773A (en) | Refrigerant cycle with a three-way service valve for use with environmentally friendly refrigerants | |
US2505393A (en) | Combined filter, drier, heat exchanger, and surge resistor for electrical refrigerators | |
JP2709536B2 (en) | Thermo-responsive steam trap | |
US3066497A (en) | Reversible refrigeration system | |
CN208071658U (en) | Exchange heat cryogenic separation combined into one apparatus | |
JP2835674B2 (en) | Thermo-responsive steam trap | |
DK164179B (en) | heat exchanging | |
JP3341192B2 (en) | Thermo-responsive steam trap | |
JP2761675B2 (en) | Thermo-responsive steam trap | |
JPS6214756B2 (en) | ||
CN208764905U (en) | Steam sub-cylinder | |
JP2709534B2 (en) | Thermo-responsive steam trap | |
US1976800A (en) | Absorption refrigerating system | |
US3474634A (en) | Method of and apparatus for selective operation of a working medium catcher in evacuating apparatus | |
JPS6038854Y2 (en) | Accumulator with receiver | |
JP4107864B2 (en) | Plate heat exchanger and absorption refrigerator using the same | |
CN210512245U (en) | Water source heat pump unit | |
JP3414544B2 (en) | Thermo-responsive steam trap | |
SU1232905A1 (en) | Air separating system of refrigerating machine | |
JPH0875295A (en) | Pressure differential sealing method and pressure differential sealing device for absorption type freezer and cold water or hot water making machine | |
JPS59109837A (en) | Detector for leak of cooling medium in heat exchanger |