JPS5855656A - Absorption type refrigerating and/or heating machine - Google Patents
Absorption type refrigerating and/or heating machineInfo
- Publication number
- JPS5855656A JPS5855656A JP15194281A JP15194281A JPS5855656A JP S5855656 A JPS5855656 A JP S5855656A JP 15194281 A JP15194281 A JP 15194281A JP 15194281 A JP15194281 A JP 15194281A JP S5855656 A JPS5855656 A JP S5855656A
- Authority
- JP
- Japan
- Prior art keywords
- generator
- valve
- self
- heating machine
- solution
- 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
Links
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
本発明は、冷媒液及び徴釈涛筐tM−る吸駅式冷凍展び
/又は暖房機OII生優筐璽制御に関する〇
なお、本明細書にお−て「徴収式冷凍及び/又は暖房機
」とは機状式冷凍機単独又は徴収式暖房−単独あるht
i% 1ljlj式冷暖房機におiで、冷凍運転Oみ、
暖房運転のみ、着しくは冷凍及び暖房運転を併用する場
合aS通)Oこと管意味する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a refrigerant liquid and a suction station type refrigeration expansion/or heating machine OII production cabinet control. ``type refrigeration and/or heating machine''
i% 1ljlj type air conditioner and heater with i, refrigeration operation is turned on,
When only heating operation is used, or when both refrigeration and heating operation are used, aS (aS) means ``tube''.
従乗の徴収式冷凍及び/又は暖房機では、尭生5iii
*o異當上昇管防止するために、発生器K11li検出
用Oレベルスイツチ【設け、諌レベルスイッチでIIl
箪ポンプを発停させて一究◎を究、i!F液ポンプO発
停を1吸駅器O筐両を検出することによや行う方式も提
案されて−る〇この従来例【添付O第1図に基づiて説
明する0第1図は、従来O二重効用1lllL式冷凍及
び/又は暖房機の装置の系統図である・111図におi
て、1は吸収器、2は蒸発器、1はI11発生器、4は
l[2発生器、Sは凝縮器、6は第2熟交換器、7は第
1熱交換器、6は**ポンプ、!は冷媒ポンプ、10が
液藺レベルスイッチである0すなわち、第1図の方式で
は、IOKよ)、60発停を行って−る@
しかしながら、上記方式の場合には、腋機械の起動時、
及び冷却水温度の低下時1c#i、1111発生器5か
ら第2発生器4 K11iIt−循環させる駆動力(第
1発生器と第2発生器の圧力差十位置ヘッド)が小さく
なるため、gi11発生BSの液位が上昇し、溶液ポン
プの発停が頻繁とな夛寿命上好11.<ない。In the secondary levy type refrigeration and/or heating machine, Kyo 5iii
*In order to prevent an abnormal riser, an O level switch for detecting the generator K11li is provided, and the level switch
Start and stop the 箪 pump to find out ◎, i! A method has also been proposed in which the F liquid pump O is started and stopped by detecting the 1 suction station O housing.〇This conventional example [Explained based on attached O Fig. 1] is a system diagram of a conventional O double effect 1lllll type refrigeration and/or heating machine.
1 is the absorber, 2 is the evaporator, 1 is the I11 generator, 4 is the l[2 generator, S is the condenser, 6 is the second ripening exchanger, 7 is the first heat exchanger, 6 is * *pump,! is the refrigerant pump, and 10 is the liquid level switch (0, in other words, in the method shown in Figure 1, it starts and stops at 60). However, in the case of the above method, when starting the armpit machine,
And when the cooling water temperature decreases, 1c#i, 1111 generator 5 to second generator 4 K11iIt- Since the driving force for circulating (the pressure difference between the first generator and the second generator 10-position head) becomes smaller, gi11 11. The liquid level of generated BS rises and the solution pump starts and stops frequently. <No.
それに加えて、液面リレーによjIilII液ポンプの
発停【行うため、制御系統が複雑KThるという欠点が
あった。In addition, there was a drawback that the control system was complicated because the liquid level relay was used to start and stop the liquid pump.
これらの欠点をなくすために、添付の第2図に示した方
式も提案されている◎[[lは、従来の二重効用吸収式
冷凍反び/又は暖房faの装置の系統図である。符号の
うち、1〜9は第1図と同じでTo9.11は液面検出
箱、12はフロート弁である。すなわち第2図0方式で
は、フロート弁を介して発生IIO液面調篇管を低圧側
配管に接続してiる〇
しかしながら、上記方式の場合、)四−ト弁全閉時、弁
前後における漏れ紘許されず、万一、シールが完全でな
い場合には、発生器の高圧蒸気が低圧側に流入し、著し
め能力の低下を引起してし重うoまた、全閉時OIIれ
t皆無とするためには、弁自体の製作精度が要求され高
価なtのとなる〇
更に、7四−F弁上流側の比較的濃度の高い溶液は、循
環することなく滞留して−るため、外気温低下時等に結
晶化を引起す。In order to eliminate these drawbacks, the system shown in the attached FIG. 2 has also been proposed. Among the symbols, 1 to 9 are the same as in FIG. 1, To9.11 is a liquid level detection box, and 12 is a float valve. In other words, in the Fig. 2 0 method, the generated IIO liquid level control pipe is connected to the low pressure side pipe via a float valve.However, in the case of the above method, when the four-tooth valve is fully closed, the If leakage is not allowed and the seal is not perfect, high-pressure steam from the generator will flow into the low-pressure side, causing a significant reduction in the tightening capacity.In addition, there will be no OII when fully closed. In order to do so, the manufacturing precision of the valve itself is required and it becomes expensive.Furthermore, since the relatively high concentration solution on the upstream side of the 74-F valve stagnates without being circulated, It causes crystallization when the outside temperature drops.
本発明の目的拡、上記各欠点t−なくし、制御系統が簡
略化され、安価で、且つ安全e@収式冷凍及び/又は暖
房機動提供するにある。The object of the present invention is to provide a retractable refrigeration and/or heating system that eliminates the above-mentioned drawbacks, has a simplified control system, is inexpensive, and is safe.
すなわち本発明を概説すれ杖、本発明は、吸収器、蒸発
器、発生器、凝縮器及び熱交換器と、それら【接続する
冷1/I&径路及びS液蚤路とから構成される吸収式冷
凍及び/又は暖房機において、自刃式開閉弁を介して、
発生器からのオーバー7μ−管を、低圧側機器又は低圧
側溶液径路に接続すると共に、S液ポンプから発生器に
至る希溶液径路から分岐した管路【、前記自刃武闘閉弁
O上流儒に接続したこと1*黴とするII釈式冷凍及び
/又紘暖房機に関する〇本発IJit−1添付O第5図
に基づいて具体的に説明する0
第3図線、本発明の一実施O態様である二重効用吸収式
冷凍及び/又は暖房機の装置の系統図である0第s図に
お−で、符号1〜!はj[1図と同じで参る。1sは自
刃式開閉弁、14及び16はオーバーブ。四−管、1S
及び17は配管である。That is, to summarize the present invention, the present invention is an absorption type system consisting of an absorber, an evaporator, a generator, a condenser, a heat exchanger, and a connecting cold 1/I & S liquid path. In refrigeration and/or heating equipment, through self-cutting on-off valves,
Connect the over 7 μ-tube from the generator to the low-pressure side equipment or the low-pressure side solution path, and connect the pipe branched from the dilute solution path from the S liquid pump to the generator [upstream of the above-mentioned self-blade martial arts closing valve O]. Connections 1 * IJit-1 from this book regarding II-type refrigeration and/or heaters that make mold In Figure 0, which is a system diagram of the system of the dual-effect absorption refrigeration and/or heating machine according to this embodiment, the symbols 1 to ! is the same as in Figure 1. 1s is a self-blade opening/closing valve, 14 and 16 are overburbs. Four-tube, 1S
and 17 are piping.
吸収器1から、溶液ポンプ8により第2熱交換器6、第
1熱交換器7を経由して第1発生器5へ送られた希溶液
は、ガス又は油ohmにより加熱され、湊縮し、第1熱
交換1171過多、第2発生器4に送られる0第2発生
器4では第1発生器3からの高圧蒸気で更に加熱貴縮し
、第2熱交換器6【経由し、吸収器1にスプレーされ、
溶液ナイクルを形成する。The dilute solution sent from the absorber 1 to the first generator 5 via the second heat exchanger 6 and first heat exchanger 7 by the solution pump 8 is heated by gas or oil OHM, and is condensed. , if the first heat exchanger 1171 is too much, it is sent to the second generator 4. In the second generator 4, the high-pressure steam from the first generator 3 is further heated and precondensed, and then passed through the second heat exchanger 6 and absorbed. Sprayed on container 1,
Form a solution nicle.
本発明では、wE1発生器3からのオーバーフロー管1
4【、自刃式開閉弁15、例えばフロート弁等會介して
配管ISKよ1112発生1)4に接続する一方、吸収
器1から発生IIsへの希溶液供給径路から分岐した配
管17【、自刃式開閉弁130上流側に接続したもので
ある〇作動について説明すると、上記のような吸収式冷
凍及び/又は暖房機の起動時、又は冷却水温変が低い場
合、第1発生器5と第2発生器4との間の圧力差が小さ
く、吸収器1から第1発生器5への希**供給量に対し
て、wc1発生器!1から第1熱交換器7を経由して第
2発生器4に送られる溶液量が少なくな夕、第1発生器
3内の液面は上昇する。 II 1発生器1内09面が
ある高さt越えると、f#液はオーバー7a−管14よ
少流出し、自刃式開閉弁13會通り、配管15によ月1
発生器4に送られる。更に、吸収器1から第1発生器3
sへの希i!箪径路から分岐した配管17が、自刃式開
閉弁130上流側に接続されてお夕、常時希I!液の一
部【送込んで−ゐため、自刃式開閉弁15が全閉時に、
弁前後におiて多少の漏れがあっても、第1発生器3か
らのガスバイパスt−騎ぐむとができる一方、常時希S
*が自刃式開閉弁1sの上流側に流入してiるため、結
晶化の問題も解消すゐことができる。第1発生器3から
自刃式開閉弁15t−過少第2発生器4に送られた溶液
により、第2発生器4内の液面が上昇した場合には、オ
ーバーフロー管16によシ、溶液は吸収器1にバイパス
される。In the present invention, overflow pipe 1 from wE1 generator 3
4 [, self-cutting type on-off valve 15, for example, a float valve, etc., is connected to piping ISK1112 generation 1) 4, while piping 17 [, self-cutting type It is connected to the upstream side of the on-off valve 130. To explain the operation, when the above-mentioned absorption type refrigeration and/or heating machine is started, or when the cooling water temperature change is low, the first generator 5 and the second generator The pressure difference between the wc1 generator and the generator 4 is small, and for the rare supply amount from the absorber 1 to the first generator 5, wc1 generator! When the amount of solution sent from the generator 1 to the second generator 4 via the first heat exchanger 7 is small, the liquid level in the first generator 3 rises. II 1 When the 09 surface inside the generator 1 exceeds a certain height t, the f# liquid flows out a little from the over 7a to the pipe 14, passes through the self-cutting on-off valve 13, and enters the pipe 15.
It is sent to generator 4. Furthermore, from the absorber 1 to the first generator 3
Nozomi to s! A pipe 17 branched from the short path is connected to the upstream side of the self-cutting on-off valve 130, so that it is always on! Because some of the liquid is being pumped in, when the self-blade opening/closing valve 15 is fully closed,
Even if there is some leakage before and after the valve, the gas can be bypassed from the first generator 3.
Since * flows into the upstream side of the self-blade type on-off valve 1s, the problem of crystallization can also be solved. If the liquid level in the second generator 4 rises due to the solution sent from the first generator 3 to the self-cutting on-off valve 15t--too much solution, the overflow pipe 16 will drain the solution. Bypassed to absorber 1.
なお、第1発生器5から自刃式開閉弁13t−介してオ
ーバーフローする溶液の流出光は、第1発生器3より低
圧であれば、吸収l!1又はいずれの溶液径路であって
も差支え1に一0iた、溶液ポンプ8から第1発生器3
の入口までの希溶液径路であれば、自刃式開閉弁13へ
の分岐点は、iずれの箇所でも差支えない。Incidentally, if the outflow light of the solution overflowing from the first generator 5 through the self-cutting on-off valve 13t is at a lower pressure than the first generator 3, it will be absorbed l! 1 or any solution path is acceptable from the solution pump 8 to the first generator 3.
As long as the dilute solution route reaches the inlet of
次に、本発明の実施の態様として、単効用に適用した例
を示す。添付の第4図は、本発明の一実施の態様である
単効用吸収式冷凍及び/又は暖房機の装置の系統図であ
る。第4図において、符号1.2.5、魯、!及び1s
は第5図と同じである021Fi発生器、22#i熟交
換器、23はオーバーフロー管、24及び25は配管で
ある。Next, as an embodiment of the present invention, an example in which the present invention is applied to a single effect will be shown. FIG. 4 attached herewith is a system diagram of a single-effect absorption refrigeration and/or heating device that is an embodiment of the present invention. In FIG. 4, the symbols 1.2.5, Lu,! and 1s
021Fi generator, 22#i mature exchanger, 23 is an overflow pipe, and 24 and 25 are piping, which are the same as in FIG.
第4図の場合においても、希溶液径路から分岐した配管
25が、結晶化の防止に役立つ0以上の説明から明らか
なように、本発明によれば、発生器における液面制御を
行匹、従来液面レベルスイッチ管用いて制御を行ってい
た際ops液ポンプの頻繁な発停の防止、制御系統の簡
略化全可能とした。また、本発明の場合、自刃式開閉弁
は、全閉時に若干の漏れがあっても差支えないため、高
度の製作精度は要求されず、安価となる一方、溶液の結
晶化に対しても安全である。In the case of FIG. 4 as well, according to the present invention, as is clear from the above description, the pipe 25 branching from the dilute solution path is useful for preventing crystallization. This prevents frequent starting and stopping of the OPs liquid pump, which was conventionally controlled using a liquid level switch pipe, and simplifies the control system. In addition, in the case of the present invention, the self-cutting on-off valve does not require a high degree of manufacturing precision even if there is a slight leak when it is fully closed, so it is inexpensive and safe from crystallization of the solution. It is.
第1図及び第2図は、従来公知の二重効用吸収式冷凍及
び/又は暖房機の装置の系統図である。第5図は、本発
明の一実施の態様である二重効用吸収式冷凍反び/又は
暖房機の装置の系統図であり、$4図は、本発明の一実
施の態様である単効用徴収式冷凍及び/又は暖房機の装
置の系統図である・1 and 2 are system diagrams of a conventionally known dual-effect absorption refrigeration and/or heating device. FIG. 5 is a system diagram of a double-effect absorption type refrigerating/heating machine which is an embodiment of the present invention, and FIG. This is a system diagram of a collection type refrigeration and/or heating device.
Claims (1)
それら管接続すゐ冷媒後略展び溶液径路とから構成され
るIIl釈式冷凍及び/又は暖房機Kか−で、自刃式開
閉弁を介して、発生器からのオーバーアロー管を、低圧
側機器又は量圧儒11ta路に接続すると共に、iI!
筐ポンプから発生器にMゐ希***路から分岐した管路
を、前記自刃式II開閉弁上流側に接続したことt−響
黴とする機状式冷凍激び/又は暖房機・tashakuyu, evaporator, generator, #! a compressor and a heat exchanger;
In the II-type refrigeration and/or heating machine K, which is composed of the pipes connected to the refrigerant and the solution path, the overarrow pipe from the generator is connected to the low-pressure side equipment through a self-cutting shut-off valve. Or connect to the quantity pressure Confucian 11ta path and iI!
A conduit branching from the M2 *** line from the housing pump to the generator is connected to the upstream side of the self-cutting type II on-off valve.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP15194281A JPS5855656A (en) | 1981-09-28 | 1981-09-28 | Absorption type refrigerating and/or heating machine |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP15194281A JPS5855656A (en) | 1981-09-28 | 1981-09-28 | Absorption type refrigerating and/or heating machine |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5855656A true JPS5855656A (en) | 1983-04-02 |
JPS6113130B2 JPS6113130B2 (en) | 1986-04-11 |
Family
ID=15529573
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP15194281A Granted JPS5855656A (en) | 1981-09-28 | 1981-09-28 | Absorption type refrigerating and/or heating machine |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5855656A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS60111855A (en) * | 1983-11-23 | 1985-06-18 | 川重冷熱工業株式会社 | Double effect absorption refrigerator |
-
1981
- 1981-09-28 JP JP15194281A patent/JPS5855656A/en active Granted
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS60111855A (en) * | 1983-11-23 | 1985-06-18 | 川重冷熱工業株式会社 | Double effect absorption refrigerator |
JPH049981B2 (en) * | 1983-11-23 | 1992-02-21 |
Also Published As
Publication number | Publication date |
---|---|
JPS6113130B2 (en) | 1986-04-11 |
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