JP2696576B2 - Absorption refrigeration equipment - Google Patents

Absorption refrigeration equipment

Info

Publication number
JP2696576B2
JP2696576B2 JP1290994A JP29099489A JP2696576B2 JP 2696576 B2 JP2696576 B2 JP 2696576B2 JP 1290994 A JP1290994 A JP 1290994A JP 29099489 A JP29099489 A JP 29099489A JP 2696576 B2 JP2696576 B2 JP 2696576B2
Authority
JP
Japan
Prior art keywords
low
heat exchanger
temperature
pressure stage
refrigerant
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 - Fee Related
Application number
JP1290994A
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Japanese (ja)
Other versions
JPH03152357A (en
Inventor
修行 井上
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.)
Ebara Corp
Original Assignee
Ebara Corp
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Filing date
Publication date
Application filed by Ebara Corp filed Critical Ebara Corp
Priority to JP1290994A priority Critical patent/JP2696576B2/en
Publication of JPH03152357A publication Critical patent/JPH03152357A/en
Application granted granted Critical
Publication of JP2696576B2 publication Critical patent/JP2696576B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Sorption Type Refrigeration Machines (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は吸収冷凍機に係り、特に、全体としては三重
効用吸収冷凍機として働き、圧力容器の点検は高圧段側
だけでよい吸収冷凍機に関する。
Description: BACKGROUND OF THE INVENTION The present invention relates to an absorption refrigerator, and more particularly, to an absorption refrigerator which functions as a triple effect absorption refrigerator as a whole, and only needs to check the pressure vessel on the high pressure stage side. About.

〔従来の技術〕[Conventional technology]

従来、二重効用、三重効用等の多重効用吸収冷凍機は
公知であり、高温発生器、中温発生器、低温発生器、凝
縮器、吸収器、蒸発器及び熱交換器類を主要構成機器と
する三重効用吸収冷凍機は、高温発生器の内圧(溶液の
飽和温度)が高くなりがちであり、また、吸収器から出
た希溶液は、熱交換器を通って全量高温発生器に導入さ
れている。
Conventionally, multi-effect absorption refrigerators such as double-effect and triple-effect are known, and a high-temperature generator, a medium-temperature generator, a low-temperature generator, a condenser, an absorber, an evaporator, and a heat exchanger are main components. In triple-effect absorption refrigerators, the internal pressure of the high-temperature generator (saturation temperature of the solution) tends to be high, and the dilute solution coming out of the absorber is entirely introduced into the high-temperature generator through the heat exchanger. ing.

高温発生器の内圧は、圧力容器としての法規制によ
り、所定の圧力以下で運転するのが一般的である。これ
は、圧力容器としての分類でも異なるが、高い圧力とな
るほど機器の製作費が高くなるためである。
Generally, the internal pressure of the high-temperature generator is operated at a predetermined pressure or lower according to laws and regulations as a pressure vessel. This is because although the pressure vessel is classified differently, the higher the pressure, the higher the production cost of the device.

しかし、高温発生器の内圧は、冷却水温度が高くなる
に連れて、高くなるし、また、負荷が増えるに従い、す
なわち全負荷近くになるに従い高くなるため、冷却水温
度が高いときとか、全負荷近くの場合の運転をどのよう
にするかという問題があった。
However, the internal pressure of the high-temperature generator increases as the cooling water temperature increases, and increases as the load increases, that is, as the load approaches the full load. There was a problem how to operate when near the load.

また、二重効用吸収冷凍機においては、吸収器からの
希液を分岐して、一部を低温発生器に導入したり、排熱
回収を有効に行う方法等の技術が開発されているが、三
重効用吸収冷凍機においては、いまだ十分に熱量の有効
利用を図った省エネルギー面の研究はなされていなかっ
た。
In addition, in the double effect absorption refrigerator, techniques such as a method of branching a dilute solution from the absorber and introducing a part to the low temperature generator or effectively recovering waste heat have been developed. As for the triple effect absorption refrigerator, research on energy saving has not yet been made to sufficiently utilize heat effectively.

〔発明が解決しようとする課題〕[Problems to be solved by the invention]

そこで、本発明は、上記のような問題点を解決し、圧
力容器としての点検は高圧段側だけでよく、また、高圧
段の圧力を所定の圧力以内に保持でき、しかもエネルギ
ーの有効利用を図った吸収冷凍装置を提供することを目
的とする。
Therefore, the present invention solves the above-mentioned problems, and the inspection as a pressure vessel only needs to be performed on the high-pressure stage side, and the pressure of the high-pressure stage can be maintained within a predetermined pressure. It is an object of the present invention to provide an absorption refrigeration system.

〔課題を解決するための手段〕[Means for solving the problem]

上記目的を達成するために、本発明では、高温発生
器、吸収器、蒸発器、溶液熱交換器、および外部凝縮器
を主要構成機器とし、これらを溶液配管、冷媒配管で結
んで単効用サイクルを構成する高圧段冷凍機と、中温発
生器、低温発生器、凝縮器、吸収器、蒸発器、および低
温溶液熱交換器、中温溶液熱交換器を主要構成機器と
し、これらを溶液配管、冷媒配管で結んで二重効用サイ
クルを構成する低圧段冷凍機とからなる吸収冷凍装置に
おいて、前記高圧段の外部凝縮器が、低圧段の中温発生
器の加熱側になっており、高圧段冷凍機の高温発生器の
熱源として蒸気を用い、低圧段冷凍機の中温溶液熱交換
器被加熱側出口と中温発生器との間に、中温ドレン熱交
換器を設け、さらに、低温溶液熱交換器被加熱側出口と
中温溶液熱交換器との間に、低温ドレン熱交換器を設
け、これらのドレン熱交換器の加熱側を前記熱源配管ラ
インに順次接続したことを特徴とする吸収冷凍装置とし
たものである。
In order to achieve the above object, in the present invention, a high-temperature generator, an absorber, an evaporator, a solution heat exchanger, and an external condenser are used as main components, and these are connected by a solution pipe and a refrigerant pipe to form a single-effect cycle. The main components are a high-pressure stage refrigerator, a medium temperature generator, a low temperature generator, a condenser, an absorber, an evaporator, a low temperature solution heat exchanger, and a medium temperature solution heat exchanger. In an absorption refrigeration apparatus comprising a low-pressure stage refrigerator connected by piping to form a double-effect cycle, the high-pressure stage external condenser is on the heating side of a low-pressure stage medium temperature generator, Using steam as a heat source of the high-temperature generator of the above, a medium-temperature drain heat exchanger is provided between the heated outlet of the medium-temperature solution heat exchanger of the low-pressure stage refrigerator and the medium-temperature generator. Between the heating side outlet and the medium temperature solution heat exchanger , Provided a low-temperature drain heat exchanger is a heating side of the drain heat exchanger that the absorption refrigerating apparatus characterized by sequentially connected to the heat source pipe line.

また、本発明では、高温発生器、吸収器、蒸発器、溶
液熱交換器、および外部凝縮器を主要構成機器とし、こ
れらを溶液配管、冷媒配管で結んで単効用サイクルを構
成する高圧段冷凍機と、中温発生器、低温発生器、凝縮
器、吸収器、蒸発器、および低温溶液熱交換器、中温溶
液熱交換器を主要構成機器とし、これらを溶液配管、冷
媒配管で結んで二重効用サイクルを構成する低圧段冷凍
機とからなる吸収冷凍装置において、前記高圧段の外部
凝縮器が、低圧段の中温発生器の加熱側になっており、
高圧段冷凍機の中温発生器で発生した冷媒蒸気を、低温
発生器の加熱側をバイパスして、低圧段冷凍機の凝縮器
に直接導く冷媒ラインを設け、該冷媒ラインには、弁を
設けることを特徴とする吸収冷凍装置としたものであ
る。
Further, in the present invention, a high-pressure stage refrigeration system comprising a high-temperature generator, an absorber, an evaporator, a solution heat exchanger, and an external condenser as main constituent devices, and connecting these with a solution pipe and a refrigerant pipe to form a single-effect cycle. The main components of the machine are a medium-temperature generator, low-temperature generator, condenser, absorber, evaporator, low-temperature solution heat exchanger, and medium-temperature solution heat exchanger. In an absorption refrigerating apparatus comprising a low-pressure stage refrigerator constituting a utility cycle, the high-pressure stage external condenser is on the heating side of a low-pressure stage medium temperature generator,
A refrigerant line is provided for directly guiding the refrigerant vapor generated by the medium temperature generator of the high pressure stage refrigerator to the condenser of the low pressure stage refrigerator, bypassing the heating side of the low temperature generator, and a valve is provided for the refrigerant line. An absorption refrigerating apparatus characterized in that:

該吸収冷凍装置において、冷媒ラインに設けた弁に
は、高圧段冷凍機の高温発生器の内圧が、所定の圧力を
越えないように冷媒のバイパス流量を調節する機構とな
っている。
In the absorption refrigeration system, a valve provided in the refrigerant line has a mechanism for adjusting the bypass flow rate of the refrigerant so that the internal pressure of the high-temperature generator of the high-pressure stage refrigerator does not exceed a predetermined pressure.

そして、前記吸収冷凍装置においては、低圧段冷凍機
の低温溶液熱交換器被加熱側出口に、冷媒ドレン熱交換
器を設け、高圧段冷凍機の高温発生器からの冷媒蒸気
を、まず、低圧段冷凍機の中温発生器に導き、ついで、
該冷媒ドレン熱交換器に導く配管ラインを設けたもので
あり、上記冷媒ドレン熱交換器と高圧段蒸発器との間
の、冷媒配管中には、冷媒ドレン冷却器をもうけたもの
である。
In the absorption refrigerating apparatus, a refrigerant drain heat exchanger is provided at a low-temperature solution heat exchanger heated side outlet of the low-pressure stage refrigerator, and refrigerant vapor from a high-temperature generator of the high-pressure stage refrigerator is first supplied to the low-pressure stage refrigerator. Led to the medium temperature generator of the stage refrigerator,
A pipe line leading to the refrigerant drain heat exchanger is provided, and a refrigerant drain cooler is provided in the refrigerant pipe between the refrigerant drain heat exchanger and the high-pressure stage evaporator.

また、本発明の吸収冷凍装置においては、冷凍装置へ
の冷水は、まず、低圧段冷凍機に導き、ついで、高圧段
冷凍機に導く冷水配管ラインを設け、また、冷却水は、
まず、低圧段冷凍機に導き、ついで、高圧段冷凍機に導
く冷却水配管ラインを設けている。
Further, in the absorption refrigeration apparatus of the present invention, the chilled water to the refrigeration apparatus is first guided to the low-pressure chiller, and then provided with a chilled water piping line to the high-pressure chiller.
First, a cooling water piping line leading to the low-pressure stage refrigerator and then to the high-pressure stage refrigerator is provided.

〔作 用〕(Operation)

本発明においては、高圧段の冷凍機は、通常の単効用
吸収冷凍機において、凝縮器を外部にもうけ、さらに冷
却媒体として、低圧段の溶液を用いたものである。一
方、低圧段の冷凍機は、通常の二重効用吸収冷凍機にお
いて、熱源を、高圧段からの冷媒蒸気としたものであ
る。
In the present invention, the high-pressure stage refrigerator is a conventional single-effect absorption refrigerator in which a condenser is provided outside and a low-pressure stage solution is used as a cooling medium. On the other hand, in the low-pressure stage refrigerator, a heat source is a refrigerant vapor from the high-pressure stage in a normal double effect absorption refrigerator.

また、熱回収としては、熱源蒸気のドレン熱の回収、
および、高圧段からの冷媒蒸気のドレンと成ったものの
2種類があり、それぞれ、回収可能とした。
In addition, as heat recovery, recovery of drain heat of heat source steam,
Also, there are two types of refrigerant drain from the high-pressure stage, each of which can be recovered.

本発明は、全体として、三重効用吸収冷凍機として働
き、高圧段の高温発生器の内圧が問題となるが、この場
合、圧力容器としての点検は、高圧段側だけですむの
で、三重効用として、一体化したものに比し、点検が容
易になる。なお、高圧段の圧力を所定の圧力以内にした
い場合は、低圧段の中温発生器の溶液温度を下げればよ
く、この場合、中温発生器の冷却蒸気を低圧段に逃がす
方法が利用できる。
The present invention works as a triple effect absorption refrigerator as a whole, and the internal pressure of the high-temperature stage high-temperature generator becomes a problem. In this case, the inspection as a pressure vessel only needs to be performed on the high-pressure stage side. Inspection is easier than in the case of integrated one. When it is desired to keep the pressure of the high-pressure stage within a predetermined pressure, the solution temperature of the medium-temperature generator of the low-pressure stage may be lowered. In this case, a method of releasing the cooling steam of the medium-temperature generator to the low-pressure stage can be used.

〔実施例〕〔Example〕

以下、図面を参照にして本発明を具体的に説明する
が、本発明はこれに限定されない。
Hereinafter, the present invention will be specifically described with reference to the drawings, but the present invention is not limited thereto.

第1図は、本発明の吸収冷凍装置の一例を示す概略工
程図である。
FIG. 1 is a schematic process diagram showing an example of the absorption refrigeration apparatus of the present invention.

第1図に記載のように、本発明の吸収冷凍装置は、中
温発生器と低温発生器をもつ低圧段冷凍機と、高温発生
器をもつ高圧段冷凍機からなっている。
As shown in FIG. 1, the absorption refrigerating apparatus of the present invention comprises a low-pressure stage refrigerator having a medium-temperature generator and a low-temperature generator, and a high-pressure stage refrigerator having a high-temperature generator.

まず、低圧段冷凍機では、吸収器2からの希溶液は溶
液ポンプ8により、低温溶液熱交換器6、冷媒ドレン熱
交換器14、中温溶液熱交換器7の被加熱側を順次通って
熱交換して温度を高めて、中温発生器4に導入される。
中温発生器4では、高圧段冷凍機の高温発生機12から発
生する冷媒蒸気により加熱されて溶液の濃縮が行われ、
この際発生する冷媒蒸気は、管32から低温発生器5の加
熱側に導かれる。一方、濃縮された溶液は管28から中温
溶液熱交換器7の加熱側を通って冷されてから管29から
低温発生器5に導かれ、さらに濃縮されて、管30から低
温溶液熱交換器6の加熱側を通って管31から吸収器2に
入り冷媒ガスを吸収する。
First, in the low-pressure stage refrigerator, the dilute solution from the absorber 2 is heated by the solution pump 8 through the low-temperature solution heat exchanger 6, the refrigerant drain heat exchanger 14, and the medium-temperature solution heat exchanger 7 in order. It is exchanged to increase the temperature and is introduced into the intermediate temperature generator 4.
In the medium temperature generator 4, the solution is concentrated by being heated by the refrigerant vapor generated from the high temperature generator 12 of the high pressure stage refrigerator,
The refrigerant vapor generated at this time is guided from the pipe 32 to the heating side of the low-temperature generator 5. On the other hand, the concentrated solution is cooled from the pipe 28 through the heating side of the medium-temperature solution heat exchanger 7 and then guided from the pipe 29 to the low-temperature generator 5 where it is further concentrated. 6 enters the absorber 2 from the pipe 31 through the heating side and absorbs the refrigerant gas.

一方、中温発生器4で発生し、低温発生器5の加熱側
を通った冷媒蒸気は管23を通り、低温発生器5で発生し
た冷媒蒸気と共に凝縮器3に導かれ、冷却水23によって
冷却されて凝縮し、管34から蒸発器1に導かれる。蒸発
器1では、冷媒液は冷水20から熱を奪い冷凍効果を発揮
して蒸発する。蒸発した冷媒蒸気は吸収器2で溶液に吸
収され、蒸発しない冷媒は、冷媒ポンプ9により管37を
通り蒸発器1に循環される。
On the other hand, the refrigerant vapor generated by the intermediate temperature generator 4 and passing through the heating side of the low temperature generator 5 passes through the pipe 23 and is guided to the condenser 3 together with the refrigerant vapor generated by the low temperature generator 5, and is cooled by the cooling water 23. Then, it is condensed and led to the evaporator 1 from the pipe 34. In the evaporator 1, the refrigerant liquid evaporates by exhibiting a refrigerating effect by removing heat from the cold water 20. The evaporated refrigerant vapor is absorbed by the solution in the absorber 2, and the non-evaporated refrigerant is circulated to the evaporator 1 through the pipe 37 by the refrigerant pump 9.

高圧段冷凍機では、吸収器11からの希溶液は溶液ポン
プ18により、溶液熱交換器13の被加熱側を通り、管41か
ら高温発生器12に導かれる。高温発生器12では、外部熱
源25により加熱されて溶液の濃縮が行われ、この際発生
する冷媒蒸気は、管44から、低圧段冷凍機の中温発生器
4の加熱側を通り、次で、管45から冷媒ドレン熱交換器
14の加熱側を通り、さらに、冷媒ドレン冷却器15で冷却
水により冷却されて、蒸発器10に導入される。一方、高
温発生器12で濃縮された溶液は、管42から溶液熱交換器
13の加熱側を通り、管43から吸収器11に入る。
In the high-pressure refrigerator, the dilute solution from the absorber 11 is guided by the solution pump 18 through the heated side of the solution heat exchanger 13 to the high temperature generator 12 through the pipe 41. In the high temperature generator 12, the solution is concentrated by being heated by the external heat source 25, and the refrigerant vapor generated at this time passes from the pipe 44 to the heating side of the medium temperature generator 4 of the low pressure stage refrigerator, and then, Refrigerant drain heat exchanger from pipe 45
After passing through the heating side of 14, it is further cooled by cooling water in a refrigerant drain cooler 15 and introduced into the evaporator 10. On the other hand, the solution concentrated in the high-temperature generator 12
It passes through the heating side of 13 and enters the absorber 11 through the tube 43.

蒸発器10では、低圧段冷凍機で冷却された冷水20が導
入され、この冷水から熱を奪い冷媒液が蒸発して冷凍効
果を発揮する。蒸発した冷媒蒸気は吸収器11で溶液に吸
収され、蒸発しない冷媒は、冷媒ポンプにより管47を通
り蒸発器10に循環される。
In the evaporator 10, cold water 20 cooled by the low-pressure stage refrigerator is introduced, heat is taken from the cold water, and the refrigerant liquid evaporates to exhibit a refrigeration effect. The evaporated refrigerant vapor is absorbed by the solution in the absorber 11, and the refrigerant that does not evaporate is circulated to the evaporator 10 through the pipe 47 by the refrigerant pump.

この装置において、冷却水は、まず低圧段冷凍機の吸
収器2を通り、次いで、凝縮器3を冷却して、更に高圧
段冷却機の吸収器11に導入される経路で流れる。
In this device, the cooling water first flows through the absorber 2 of the low-pressure stage refrigerator, then cools the condenser 3 and flows further into the absorber 11 of the high-pressure stage refrigerator.

また、高温発生器12において、外部熱源25として蒸気
を用いた場合は、高温発生器12を加熱してドレンになっ
た蒸気を管48で引き出し、低圧段冷凍機の中温溶液熱交
換器7を出た希溶液の加熱用である中温ドレン熱交換器
16の加熱側に通し、該熱交換器16を出たドレンを、さら
に、希溶液の冷媒ドレン熱交換器14の後に設けた低温ド
レン熱交換器17の加熱側を通して十分に排熱利用をす
る。
In the case where steam is used as the external heat source 25 in the high-temperature generator 12, the high-temperature generator 12 is heated and drained steam is drawn out through the pipe 48, and the medium-temperature solution heat exchanger 7 of the low-pressure stage refrigerator is used. Medium temperature drain heat exchanger for heating dilute solution
The drain that has passed through the heating side of the heat exchanger 16 and exited the heat exchanger 16 is further subjected to exhaust heat utilization through the heating side of a low-temperature drain heat exchanger 17 provided after the dilute solution refrigerant drain heat exchanger 14. .

さらに、このような冷凍装置において、中温発生器4
で発生した冷媒蒸気を、低温発生器5の加熱側を通さず
に、直接凝縮器3に導くバイパス管35を設け、この管35
を弁36を設けることにより高温発生器12の圧力を低下さ
せることができる。また、この弁36に高温発生器12の圧
力と連動しコントロール機構を設ければ、高温発生器12
の圧力が自動的に制御できる。
Further, in such a refrigeration system, the medium temperature generator 4
A bypass pipe 35 is provided for directly guiding the refrigerant vapor generated in step 3 to the condenser 3 without passing through the heating side of the low-temperature generator 5.
By providing the valve 36, the pressure of the high temperature generator 12 can be reduced. If a control mechanism is provided for the valve 36 in conjunction with the pressure of the high-temperature generator 12,
Pressure can be controlled automatically.

なお、この実施例では、低圧段冷凍機をシリーズフロ
ーで示したが、パラレルフロー機、分岐フロー機でもよ
い。
In this embodiment, the low-pressure stage refrigerator is shown as a series flow, but may be a parallel flow machine or a branch flow machine.

〔発明の効果〕〔The invention's effect〕

本発明によると、全体としては三重効用吸収冷凍機と
して働き、しかも、圧力容器としての点検は高圧段側だ
けですむ。また、高圧段の圧力を所定の圧力以内にした
い場合は、低圧段の中温発生器の冷媒蒸気を、低圧段の
凝縮器に逃がすバイパス等を設けているので、容易にコ
ントロールが可能である。さらに、本発明においては、
熱源蒸気のドレン熱の回収及び冷媒蒸気のドレン熱の回
収を行っており、十分に熱回収ができる。
According to the present invention, as a whole, it works as a triple effect absorption refrigerator, and the inspection as a pressure vessel only needs to be performed on the high pressure stage side. Further, when the pressure of the high pressure stage is desired to be within a predetermined pressure, a bypass or the like for releasing the refrigerant vapor of the intermediate temperature generator of the low pressure stage to the condenser of the low pressure stage is provided, so that the control can be easily performed. Further, in the present invention,
The recovery of the drain heat of the heat source vapor and the recovery of the drain heat of the refrigerant vapor can be performed sufficiently.

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

第1図は、本発明の吸収冷凍機の一例を示す概略工程図
である。 1、10……蒸発器、2、11……吸収器、3……凝縮器、
4……中温発生器、5……低温発生器、6……低温溶液
熱交換器、7……中温溶液熱交換器、8、18……溶液ポ
ンプ、9、19……冷媒ポンプ、12……高温発生器、13…
…溶液熱交換器、14……冷媒ドレン熱交換器、15……冷
媒ドレン冷却器、16……中温ドレン熱交換器、17……低
温ドレン熱交換器、20、21……冷水、22、23、24……冷
却水、25……熱源、35……バイパス管、36……バイパス
FIG. 1 is a schematic process diagram showing an example of an absorption refrigerator of the present invention. 1, 10 ... evaporator, 2, 11 ... absorber, 3 ... condenser,
4 Medium-temperature generator, 5 Low-temperature generator, 6 Low-temperature solution heat exchanger, 7 Medium-temperature solution heat exchanger, 8, 18 Solution pump, 9, 19 Refrigerant pump, 12 … High temperature generator, 13…
... solution heat exchanger, 14 ... refrigerant drain heat exchanger, 15 ... refrigerant drain cooler, 16 ... medium temperature drain heat exchanger, 17 ... low temperature drain heat exchanger, 20, 21 ... cold water, 22, 23, 24 ... cooling water, 25 ... heat source, 35 ... bypass pipe, 36 ... bypass valve

Claims (6)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】高温発生器、吸収器、蒸発器、溶液熱交換
器、および外部凝縮器を主要構成機器とし、これらを溶
液配管、冷媒配管で結んで単効用サイクルを構成する高
圧段冷凍機と、中温発生器、低温発生器、凝縮器、吸収
器、蒸発器、および低温溶液熱交換器、中温溶液熱交換
器を主要構成機器とし、これらを溶液配管、冷媒配管で
結んで二重効用サイクルを構成する低圧段冷凍機とから
なる吸収冷凍装置において、前記高圧段の外部凝縮器
が、低圧段の中温発生器の加熱側になっており、高圧段
冷凍機の高温発生器の熱源として蒸気を用い、低圧段冷
凍機の中温溶液熱交換器被加熱側出口と中温発生器との
間に、中温ドレン熱交換器を設け、さらに、低温溶液熱
交換器被加熱側出口と中温溶液熱交換器との間に、低温
ドレン熱交換器を設け、これらのドレン熱交換器の加熱
側を前記熱源配管ラインに順次接続したことを特徴とす
る吸収冷凍装置。
A high-pressure refrigerating machine comprising a high-temperature generator, an absorber, an evaporator, a solution heat exchanger, and an external condenser as main components, and connecting these with a solution pipe and a refrigerant pipe to form a single-effect cycle. And medium-temperature generator, low-temperature generator, condenser, absorber, evaporator, low-temperature solution heat exchanger, and medium-temperature solution heat exchanger as main components, and these are connected by solution piping and refrigerant piping for double effect. In an absorption refrigerating apparatus comprising a low-pressure stage refrigerator constituting a cycle, the external condenser of the high-pressure stage is on the heating side of a medium-temperature generator of the low-pressure stage, and serves as a heat source of a high-temperature generator of the high-pressure stage refrigerator. Using steam, a medium-temperature drain heat exchanger is provided between the medium-temperature solution heat exchanger heated-side outlet of the low-pressure stage refrigerator and the medium-temperature generator, and the low-temperature solution heat exchanger heated-side outlet and medium-temperature solution heat are provided. A low-temperature drain heat exchanger is installed between the , The absorption refrigerating apparatus, characterized in that the heating side of the drain heat exchanger sequentially connected to the heat source pipe line.
【請求項2】高温発生器、吸収器、蒸発器、溶液熱交換
器、および外部凝縮器を主要構成機器とし、これらを溶
液配管、冷媒配管で結んで単効用サイクルを構成する高
圧段冷凍機と、中温発生器、低温発生器、凝縮器、吸収
器、蒸発器、および低温溶液熱交換器、中温溶液熱交換
器を主要構成機器とし、これらを溶液配管、冷媒配管で
結んで二重効用サイクルを構成する低圧段冷凍機とから
なる吸収冷凍装置において、前記高圧段の外部凝縮器
が、低圧段の中温発生器の加熱側になっており、低圧段
冷凍機の中温発生器で発生した冷媒蒸気を、低温発生器
の加熱側をバイパスして、低圧段冷凍機の凝縮器に直接
導く冷媒ラインを設け、該冷媒ラインには、弁を設ける
ことを特徴とする吸収冷凍装置。
2. A high-pressure refrigerating machine comprising a high-temperature generator, an absorber, an evaporator, a solution heat exchanger, and an external condenser as main components and connecting them by a solution pipe and a refrigerant pipe to form a single-effect cycle. And medium-temperature generator, low-temperature generator, condenser, absorber, evaporator, low-temperature solution heat exchanger, and medium-temperature solution heat exchanger as main components, and these are connected by solution piping and refrigerant piping for double effect. In an absorption refrigerating apparatus comprising a low-pressure stage refrigerator constituting a cycle, the high-pressure stage external condenser is on the heating side of the low-pressure stage medium-temperature generator, and is generated by the low-pressure stage refrigerator at the medium-temperature generator. An absorption refrigerating apparatus, comprising: a refrigerant line that directly leads refrigerant vapor to a condenser of a low-pressure refrigerating machine, bypassing a heating side of a low-temperature generator, and a valve is provided in the refrigerant line.
【請求項3】前記冷媒ラインに設けた弁には、高圧段冷
凍機の高温発生器の内圧が、所定の圧力を越えないよう
に、冷媒のバイパス流量を調節する機構を設けたことを
特徴とする請求項2記載の冷凍装置。
3. A valve provided in the refrigerant line is provided with a mechanism for adjusting a refrigerant bypass flow rate so that an internal pressure of a high-temperature generator of the high-pressure refrigerator does not exceed a predetermined pressure. The refrigeration apparatus according to claim 2, wherein
【請求項4】前記低圧段冷凍機の低温溶液熱交換器被加
熱側出口に、冷媒ドレン熱交換器を設け、高圧段冷凍機
の高温発生器からの冷媒蒸気を、まず、低圧段冷凍機の
中温発生器に導き、ついで、該冷媒ドレン熱交換器に導
く配管ラインを設けたことを特徴とする請求項1又は2
記載の吸収冷凍装置。
4. A refrigerant drain heat exchanger is provided at an outlet of the low-pressure stage refrigerator to be heated on the low-temperature solution heat exchanger, and refrigerant vapor from a high-temperature generator of the high-pressure stage refrigerator is first supplied to the low-pressure stage refrigerator. 3. A pipe line leading to the medium temperature generator and then leading to the refrigerant drain heat exchanger.
The absorption refrigeration apparatus as described in the above.
【請求項5】前記冷媒ドレン熱交換器と高圧段蒸発器と
の間の冷媒配管中に、冷媒ドレン冷却器を設けたことを
特徴とする請求項4記載の吸収冷凍装置。
5. The absorption refrigeration system according to claim 4, wherein a refrigerant drain cooler is provided in a refrigerant pipe between the refrigerant drain heat exchanger and the high-pressure stage evaporator.
【請求項6】前記吸収冷媒装置には、蒸発器で冷却され
る冷水を、まず、低圧段冷凍機に導き、ついで、高圧段
冷凍機に導く冷水配管ラインを設け、また、器機類を冷
却する冷却水を、まず、低圧段冷凍機に導き、ついで、
高圧段冷凍機に導く冷却水配管ラインを設けたことを特
徴とする請求項1〜5のいずれか1項記載の吸収冷凍装
置。
6. The absorption refrigerant device is provided with a chilled water pipe line for leading cold water cooled by an evaporator to a low-pressure stage refrigerator first, and then to a high-pressure stage refrigerator. The cooling water to be introduced first to the low-pressure stage refrigerator, and then
The absorption refrigeration apparatus according to any one of claims 1 to 5, wherein a cooling water piping line leading to the high-pressure refrigerator is provided.
JP1290994A 1989-11-10 1989-11-10 Absorption refrigeration equipment Expired - Fee Related JP2696576B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1290994A JP2696576B2 (en) 1989-11-10 1989-11-10 Absorption refrigeration equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1290994A JP2696576B2 (en) 1989-11-10 1989-11-10 Absorption refrigeration equipment

Publications (2)

Publication Number Publication Date
JPH03152357A JPH03152357A (en) 1991-06-28
JP2696576B2 true JP2696576B2 (en) 1998-01-14

Family

ID=17763085

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1290994A Expired - Fee Related JP2696576B2 (en) 1989-11-10 1989-11-10 Absorption refrigeration equipment

Country Status (1)

Country Link
JP (1) JP2696576B2 (en)

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5627875A (en) * 1979-08-15 1981-03-18 Hitachi Ltd Absorption refrigerating equipment
JPS58108368A (en) * 1981-12-23 1983-06-28 株式会社日立製作所 Double effect absorption type refrigerator

Also Published As

Publication number Publication date
JPH03152357A (en) 1991-06-28

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