JP3224766B2 - Double effect absorption chiller / heater - Google Patents

Double effect absorption chiller / heater

Info

Publication number
JP3224766B2
JP3224766B2 JP30331397A JP30331397A JP3224766B2 JP 3224766 B2 JP3224766 B2 JP 3224766B2 JP 30331397 A JP30331397 A JP 30331397A JP 30331397 A JP30331397 A JP 30331397A JP 3224766 B2 JP3224766 B2 JP 3224766B2
Authority
JP
Japan
Prior art keywords
valve
heater
temperature regenerator
refrigerant
hot water
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 - Lifetime
Application number
JP30331397A
Other languages
Japanese (ja)
Other versions
JPH11118278A (en
Inventor
修行 井上
晃好 鈴木
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
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 Ebara Corp filed Critical Ebara Corp
Priority to JP30331397A priority Critical patent/JP3224766B2/en
Publication of JPH11118278A publication Critical patent/JPH11118278A/en
Application granted granted Critical
Publication of JP3224766B2 publication Critical patent/JP3224766B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A30/00Adapting or protecting infrastructure or their operation
    • Y02A30/27Relating to heating, ventilation or air conditioning [HVAC] technologies
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02BCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/62Absorption based systems

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、二重効用吸収冷温
水機に係り、特に温水専用運転(高温再生器からの溶液
の出入りをなくした温水の単独運転)の際に、高温再生
器からの冷媒経路を凝縮器、蒸発器から遮断することが
できる二重効用吸収冷温水機に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a double-effect absorption chiller / heater, and more particularly to a hot water regenerator for hot water only operation (single operation of hot water with no solution flowing in and out of the high temperature regenerator). The present invention relates to a double-effect absorption chiller / heater capable of blocking a refrigerant path from a condenser and an evaporator.

【0002】[0002]

【従来の技術】従来、冷水と温水とを同時に取出す冷温
水機においては、高温再生器の冷媒蒸気を温水加熱器に
導き入れ、その凝縮潜熱により温水を取出す方式が一般
に採用されている。冷水負荷が全くなく、温水負荷だけ
の場合は、温水専用運転として、高温再生器と温水加熱
器を、吸収器、蒸発器、凝縮器、低温再生器(被加熱
側)から分離し、高温再生器からの冷媒経路と溶液経路
を遮断する必要があった。また、冷房運転と暖房運転を
切り替えて運転する冷温水機にあっても上述と同様の温
水加熱器を設けることがあり、この場合の暖房運転の際
には、上述と同様の分離遮断が必要であった。
2. Description of the Related Art Conventionally, in a chiller / heater which simultaneously takes out cold water and hot water, a system in which refrigerant vapor from a high-temperature regenerator is introduced into a hot water heater and hot water is taken out by the latent heat of condensation is generally adopted. If there is no chilled water load and only hot water load, the high-temperature regenerator and hot water heater are separated from the absorber, evaporator, condenser, and low-temperature regenerator (heated side) as a dedicated hot water operation, and high-temperature regeneration is performed. It was necessary to shut off the refrigerant path and the solution path from the vessel. Further, even in a chiller / heater operated by switching between the cooling operation and the heating operation, a hot water heater similar to the above may be provided, and in the heating operation in this case, the same separation and interruption as described above is necessary. Met.

【0003】従来は、図3に記載のように、高温再生器
GHからの冷媒蒸気配管13に弁を設けて遮断してお
り、この場合、配管口径が大きく、高価な弁となり、取
付スペースも大きな弁となる。また、発生蒸気が過熱蒸
気であり高温であることから、全閉性能を保持するには
高価なシールと、大きな開閉トルクが必要となる等の問
題があった。この問題を解決するために、低温再生機
(加熱側)出口の冷媒配管に弁を設けて遮断する方式も
知られていたが、この方式には、低温再生器(過熱側)
に冷媒液が溜まり、高温再生器内の溶液量が不足し、直
火式にあっては空焚きの危険があり、また、濃度が上昇
して、停止中の結晶の危険もある等の問題があった。
Conventionally, as shown in FIG. 3, a valve is provided in the refrigerant vapor pipe 13 from the high-temperature regenerator GH to shut off the pipe. In this case, the pipe diameter is large, the valve becomes expensive, and the mounting space is small. It becomes a big valve. Further, since the generated steam is superheated steam and has a high temperature, there are problems that an expensive seal and a large opening / closing torque are required to maintain the fully closed performance. In order to solve this problem, there has been known a method in which a valve is provided in a refrigerant pipe at an outlet of a low-temperature regenerator (heating side) to shut off the refrigerant pipe.
The refrigerant liquid accumulates in the regenerator and the amount of solution in the high-temperature regenerator is insufficient. In the case of the direct fire type, there is a danger of empty firing, and there is a danger that the concentration increases and there is a danger of stopping crystals. was there.

【0004】[0004]

【発明が解決しようとする課題】本発明は、上記従来技
術の問題点を解決し、冷媒液配管に弁を設けることによ
り、蒸気配管に弁を設ける問題点をなくすると共に、温
水を取出す場合も高温再生器内の溶液量が不足せず、空
焚きとか結晶化の危険性のない二重効用吸収冷温水機を
提供することを課題とする。
SUMMARY OF THE INVENTION The present invention solves the above-mentioned problems of the prior art, and eliminates the problem of providing a valve in the steam pipe by providing a valve in the refrigerant liquid pipe, and also removes hot water. It is another object of the present invention to provide a double-effect absorption chiller / heater in which the amount of solution in the high-temperature regenerator is not insufficient and there is no danger of boil-off or crystallization.

【0005】[0005]

【課題を解決するための手段】上記課題を解決するため
に、本発明では、吸収器、蒸発器、高温再生器、低温再
生器、凝縮器、高温溶液熱交換器、低温溶液熱交換器、
温水加熱器、溶液ポンプ、及びこれらの機器を接続する
溶液経路、冷媒経路を備え、該冷媒経路は、高温再生器
から発生する冷媒蒸気を分ける冷媒分岐点から、一方は
低温再生器の加熱側を経由して、凝縮器から蒸発器に至
る冷凍サイクル系冷媒経路とし、他方は温水加熱器の加
熱側を経由して、高温再生器に至る温水サイクル系冷媒
経路とした二重効用吸収冷温水機において、前記冷凍サ
イクル系冷媒経路の低温再生器の加熱側出口を出た冷媒
配管に弁aを設け、該低温再生器の加熱側出口と弁aと
の間の冷媒配管に、高温再生器に向かう弁bを備えた冷
媒配管を接続し、前記温水サイクル系冷媒経路には、温
水加熱器と凝縮器又は蒸発器とを結ぶ弁eを有する冷媒
配管を設けると共に、溶液経路の溶液ポンプ出口から高
温再生器入口までの溶液配管中と、高温再生器出口から
吸収器までの溶液配管中とに、それぞれ弁c、dを設け
たものである。
In order to solve the above problems, the present invention provides an absorber, an evaporator, a high temperature regenerator, a low temperature regenerator, a condenser, a high temperature solution heat exchanger, a low temperature solution heat exchanger,
A hot water heater, a solution pump, and a solution path and a refrigerant path for connecting these devices are provided. The refrigerant path is from a refrigerant branch point that separates refrigerant vapor generated from the high-temperature regenerator, and one is a heating side of the low-temperature regenerator. And a double-effect absorption chilled and heated water path, which is a refrigeration cycle system refrigerant path from the condenser to the evaporator via the hot water heater, and the other is a hot water cycle system refrigerant path from the hot water heater to the high temperature regenerator. In the apparatus, a valve a is provided in a refrigerant pipe exiting a heating-side outlet of a low-temperature regenerator in the refrigeration cycle system refrigerant path, and a high-temperature regenerator is provided in a refrigerant pipe between the heating-side outlet of the low-temperature regenerator and the valve a. Connected to a refrigerant pipe provided with a valve b toward the hot water cycle system.
Refrigerant having valve e connecting water heater and condenser or evaporator
Rutotomoni provided piping, and the solution pipe from the solution pump outlet of the solution route to the high temperature regenerator inlet, to a solution piping from the high-temperature regenerator outlet to the absorber, in which each valve c, and d provided .

【0006】前記二重効用吸収冷温水機において、弁a
と弁bは、一体化して三方弁とすることができ、温水加
熱器から温水を取出す際には、弁a、弁c及び弁dを閉
止、弁bを開放とすることにより、高圧再生器と温水加
熱器を吸収器及び蒸発器等から分離できる。また、温水
加熱器と凝縮器又は蒸発器とを結ぶ弁eを有する冷媒配
管を設けており、温水加熱の際にできた冷媒液を、冷媒
サイクル系に導き、冷凍効果を発揮させる冷温水機であ
り、この場合、温水加熱器から温水を取出すには、弁
a、弁c、弁d及び弁eを閉止、弁bを開放することに
より、高圧再生器と温水加熱器を吸収器及び蒸発器等か
ら分離することができる。上記のように、本発明では、
高温再生器から低温再生器(過熱側)を経て、凝縮器
(又は蒸発器)への配管中に弁aを設けて、高温再生器
を分離したものであり、低温再生器(過熱側)から凝縮
器(又は蒸発器)への配管は冷媒液配管となっており、
配管口径は非常に小さくなっている。例えば、冷媒に水
を用いた吸収冷凍機では口径で1/5〜1/10程度に
なることが多い。またこの冷媒配管系は、飽和温度にな
っており、温度的にも条件が緩和されている。
In the double effect absorption chiller / heater, the valve a
And the valve b can be integrated into a three-way valve. When hot water is taken out from the hot water heater, the valves a, c and d are closed and the valve b is opened, so that the high-pressure regenerator And the hot water heater can be separated from the absorber and the evaporator. In addition, a refrigerant pipe having a valve e connecting the hot water heater and the condenser or the evaporator is provided , and a refrigerant liquid generated at the time of hot water heating is guided to a refrigerant cycle system, and a chiller / heater for exhibiting a refrigeration effect. In
In this case, in order to take out hot water from the hot water heater, the high pressure regenerator and the hot water heater are connected to the absorber and the evaporator by closing the valves a, c, d and e and opening the valve b. Etc. can be separated. As described above, in the present invention,
A valve a is provided in the pipe from the high-temperature regenerator to the condenser (or evaporator) through the low-temperature regenerator (superheated side) to separate the high-temperature regenerator from the low-temperature regenerator (superheated side). The piping to the condenser (or evaporator) is a refrigerant liquid piping,
The pipe diameter is very small. For example, an absorption refrigerator using water as a refrigerant often has a diameter of about 1/5 to 1/10. The refrigerant piping system is at a saturation temperature, and the conditions are relaxed in terms of temperature.

【0007】[0007]

【発明の実施の形態】以下、本発明を図面を用いて詳細
に説明する。図1に、本発明の二重効用吸収冷温水機の
フロー図を示す。図1において、吸収器A、蒸発器E、
高温再生器GH、低温再生器GL、凝縮器C、温水加熱
器W、高温熱交換器XH及び低温熱交換器XLが配備さ
れている。溶液経路として、溶液ポンプPS、弁c、弁
d、管路1,2,3,4,5,6,7,8,9,10,
11により、上記各機器の一部のものを接続し、溶液循
環路が形成されている。冷媒経路としては、冷凍サイク
ル系冷媒経路と温水サイクル系冷媒経路とを備えてい
る。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described below in detail with reference to the drawings. FIG. 1 shows a flow chart of the double effect absorption chiller / heater of the present invention. In FIG. 1, an absorber A, an evaporator E,
A high temperature regenerator GH, a low temperature regenerator GL, a condenser C, a hot water heater W, a high temperature heat exchanger XH, and a low temperature heat exchanger XL are provided. As a solution path, a solution pump PS, a valve c, a valve d, lines 1, 2, 3, 4, 5, 6, 7, 8, 9, 10,
11, a part of each of the above devices is connected to form a solution circulation path. The refrigerant path includes a refrigeration cycle type refrigerant path and a hot water cycle type refrigerant path.

【0008】冷凍サイクル系冷媒経路は、管路12から
冷媒分岐点20を経て、管路13、加熱器14を経て、
弁aを備えた管路15及び弁bを備えた管路16に分岐
され、管路15は凝縮器Cを経て管路17から蒸発器E
に至り、管路16は弁bを経て高温再生器に至る高温再
生器系冷媒経路と、低温再生器GLの中の溶液から蒸発
して、凝縮器Cで凝縮し、管路17を経て蒸発器Eに至
る低温再生器系冷媒経路と、蒸発器Eに冷媒を繰り返し
循環せしめるための、冷媒ポンプPM、管路18,19
より成る蒸発器系冷媒経路とが備えられている。温水サ
イクル系冷媒経路は、管路12から冷媒分岐点20を経
て管路21、温水加熱器Wの加熱側22、管路23を経
て、高温再生器GHに接続されている。
The refrigeration cycle system refrigerant path passes from the pipe 12 through the refrigerant branch point 20, through the pipe 13 and the heater 14,
The line is branched into a line 15 having a valve a and a line 16 having a valve b. The line 15 passes through a condenser C from a line 17 through an evaporator E.
The pipe 16 evaporates from the solution in the low-temperature regenerator GL via the high-temperature regenerator through the valve b to the high-temperature regenerator, condenses in the condenser C, and evaporates through the pipe 17. And a refrigerant pump PM and pipes 18 and 19 for repeatedly circulating the refrigerant to the evaporator E.
And an evaporator-based refrigerant path. The hot water cycle system refrigerant path is connected to the high temperature regenerator GH from the pipe 12 via the refrigerant branch point 20, the pipe 21, the heating side 22 of the hot water heater W, and the pipe 23.

【0009】26,27は冷却水管、28は冷水管、2
9は加熱管、30は熱源熱量制御弁であり、31及び3
2は冷水負荷又は温水負荷を検出するための温度検出器
である。また、前記の弁aと弁bは、加熱器14を経た
管路が管路15と管路16に分岐する分岐点に一体化し
た三方弁として設けても良い。図1において、暖房運転
時温水加熱器Wから温水を取出す際には、弁aを閉止し
て冷媒が凝縮器Cに流入するのを遮断すると共に、弁c
と弁dを閉止し、溶液が吸収器Aに循環するのを遮断
し、弁bを開とすることによって、管路13から加熱器
14に溜った冷媒液が管路16を通って高温再生器に流
入し、高温再生器内の溶液量を増加させ、空焚きとか停
止中の結晶の生成を防止する。そして、冷媒蒸気は、高
温再生器GHから出て管路12、分岐点20、管路21
を経て、温水加熱器Wの加熱側に入り、温水を過熱し
て、冷媒液となり管23を経て高温再生器GHに循環す
る。
26 and 27 are cooling water pipes, 28 is a cold water pipe, 2
9 is a heating tube, 30 is a heat source calorie control valve, and 31 and 3
Reference numeral 2 denotes a temperature detector for detecting a cold water load or a hot water load. Further, the valves a and b may be provided as a three-way valve integrated at a branch point where a pipe passing through the heater 14 branches into a pipe 15 and a pipe 16. In FIG. 1, when taking out hot water from the hot water heater W during the heating operation, the valve a is closed to block the refrigerant from flowing into the condenser C, and the valve c is closed.
And the valve d are closed, the solution is blocked from circulating to the absorber A, and the valve b is opened, so that the refrigerant liquid accumulated in the heater 14 from the pipe 13 passes through the pipe 16 and is regenerated at a high temperature. It flows into the vessel and increases the amount of solution in the high-temperature regenerator, preventing the generation of crystals during idle heating or during shutdown. Then, the refrigerant vapor exits from the high-temperature regenerator GH and passes through the pipe 12, the branch point 20, and the pipe 21.
And enters the heating side of the hot water heater W, overheats the hot water and turns into a refrigerant liquid and circulates through the pipe 23 to the high temperature regenerator GH.

【0010】図2は、本発明の二重効用吸収冷温水機の
他のフロー図を示し、冷水と温水を同時に取り出す冷温
水機であって図1との相違点は、図2においては、温水
加熱器Wからの管路23から分岐点24で分岐した弁e
を有する管路25を、凝縮器Cからの冷媒管路17に接
続した点及び弁f、弁gを追加した点にある。冷水負荷
と温水負荷の両方がある場合の温水能力の調整は、温度
検出器32の信号により弁gを操作し、冷水能力の調整
は、温度検出器31の信号により弁fを操作して行う。
熱源熱量制御弁には、冷水信号、温水信号のうち大信号
(弁開度を大きくする信号)の方を用いて調整する。こ
のような冷温水機で冷水負荷がなく、温水専用運転をす
る際には弁a,c,d,eを閉止、弁b,gを開放とす
る。また、本発明は、吸収器、凝縮器の冷却に冷却水を
用いる水冷式(図示)ばかりではなく、冷却空気を用い
る空冷式(図示せず)にも適用できる。
FIG. 2 shows another flow chart of the dual-effect absorption chiller / heater of the present invention, which is a chiller / heater for simultaneously taking out cold water and hot water. The difference from FIG. 1 is that FIG. Valve e branched at branch point 24 from line 23 from hot water heater W
Is connected to the refrigerant line 17 from the condenser C, and the valve f and the valve g are added. Adjustment of the hot water capacity when there is both a cold water load and a hot water load is performed by operating the valve g according to the signal of the temperature detector 32, and the adjustment of the cold water capacity is performed by operating the valve f according to the signal of the temperature detector 31. .
The heat source calorie control valve is adjusted using a larger signal (a signal for increasing the valve opening) of the cold water signal and the hot water signal. In such a chiller / heater, when there is no chilled water load and hot water only operation is performed, the valves a, c, d, and e are closed and the valves b and g are opened. Further, the present invention can be applied not only to a water-cooled type using cooling water for cooling the absorber and the condenser (illustration), but also to an air-cooled type using cooling air (not shown).

【0011】[0011]

【発明の効果】上記のように、本発明では、冷媒蒸気の
遮断を低温再生器の加熱側を経て液化した後に弁aを設
けて行っているので、配管口径の小さいところに弁を設
置できると共に、冷媒液を高温再生器に戻す管路を設け
ているので、高温再生器は、溶液量が不足せず、直火式
での空焚きの危険とか、濃度が上昇して停止中に結晶が
生成する危険等を回避できる。
As described above, in the present invention, since the refrigerant vapor is shut off after liquefaction via the heating side of the low-temperature regenerator and the valve a is provided, the valve can be installed at a place where the pipe diameter is small. At the same time, a pipe is provided to return the refrigerant liquid to the high-temperature regenerator. Can be avoided.

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

【図1】本発明の二重効用吸収冷温水機のフロー図。FIG. 1 is a flowchart of a double-effect absorption chiller / heater of the present invention.

【図2】本発明の二重効用吸収冷温水機の他のフロー
図。
FIG. 2 is another flow chart of the double effect absorption chiller / heater of the present invention.

【図3】従来の二重効用吸収冷温水機のフロー図。FIG. 3 is a flowchart of a conventional double effect absorption chiller / heater.

【符号の説明】[Explanation of symbols]

1〜11:溶液管路、12、13、15〜19、21、
23、25:冷媒管路、14:加熱管、20:冷媒分岐
点、22:加熱側、24:バイパス分岐点、26:冷却
水管、27:冷却水管、28:冷水管、29:加熱管、
30:熱源熱量制御弁、31、32:温度検出器、A:
吸収器、E:蒸発器、GH:高温再生器、GL:低温再
生器、C:凝縮器、W:温水加熱器、XH:高温熱交換
器、XL:低温熱交換器、PS:溶液ポンプ、PM:冷
媒ポンプ、a、b、c、d:切換弁、e、f、g:調整
1 to 11: solution pipeline, 12, 13, 15 to 19, 21,
23, 25: refrigerant pipe, 14: heating pipe, 20: refrigerant branch point, 22: heating side, 24: bypass branch point, 26: cooling water pipe, 27: cooling water pipe, 28: cold water pipe, 29: heating pipe,
30: heat source calorie control valve, 31, 32: temperature detector, A:
Absorber, E: Evaporator, GH: High temperature regenerator, GL: Low temperature regenerator, C: Condenser, W: Hot water heater, XH: High temperature heat exchanger, XL: Low temperature heat exchanger, PS: Solution pump, PM: refrigerant pump, a, b, c, d: switching valve, e, f, g: regulating valve

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 平6−347122(JP,A) 特開 昭53−15655(JP,A) 特開 昭62−218771(JP,A) 特開 昭54−34162(JP,A) (58)調査した分野(Int.Cl.7,DB名) F25B 15/00 303 ──────────────────────────────────────────────────続 き Continuation of the front page (56) References JP-A-6-347122 (JP, A) JP-A-53-15655 (JP, A) JP-A-62-218771 (JP, A) JP-A 54-1984 34162 (JP, A) (58) Field surveyed (Int. Cl. 7 , DB name) F25B 15/00 303

Claims (4)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 吸収器、蒸発器、高温再生器、低温再生
器、凝縮器、高温溶液熱交換器、低温溶液熱交換器、温
水加熱器、溶液ポンプ、及びこれらの機器を接続する溶
液経路、冷媒経路を備え、該冷媒経路は、高温再生器か
ら発生する冷媒蒸気を分ける冷媒分岐点から、一方は低
温再生器の加熱側を経由して、凝縮器から蒸発器に至る
冷凍サイクル系冷媒経路とし、他方は温水加熱器の加熱
側を経由して、高温再生器に至る温水サイクル系冷媒経
路とした二重効用吸収冷温水機において、前記冷凍サイ
クル系冷媒経路の低温再生器の加熱側出口を出た冷媒配
管に弁aを設け、該低温再生器の加熱側出口と弁aとの
間の冷媒配管に、高温再生器に向かう弁bを備えた冷媒
配管を接続し、前記温水サイクル系冷媒経路には、温水
加熱器と凝縮器又は蒸発器とを結ぶ弁eを有する冷媒配
管を設けると共に、溶液経路の溶液ポンプ出口から高温
再生器入口までの溶液配管中と、高温再生器出口から吸
収器までの溶液配管中とに、それぞれ弁c、dを設けた
ことを特徴とする二重効用吸収冷温水機。
1. An absorber, an evaporator, a high temperature regenerator, a low temperature regenerator, a condenser, a high temperature solution heat exchanger, a low temperature solution heat exchanger, a hot water heater, a solution pump, and a solution path connecting these devices A refrigerant path, and the refrigerant path is a refrigeration cycle system refrigerant from a condenser to an evaporator via a heating side of a low-temperature regenerator, from a refrigerant branch point for dividing refrigerant vapor generated from a high-temperature regenerator. In the double-effect absorption chiller / heater, which is a hot water cycle system refrigerant path to the high temperature regenerator via the heating side of the hot water heater and the other side, the heating side of the low temperature regenerator in the refrigeration cycle system refrigerant path A valve a is provided in the refrigerant pipe that has exited the outlet, and a refrigerant pipe provided with a valve b that is directed to the high-temperature regenerator is connected to the refrigerant pipe between the heating-side outlet of the low-temperature regenerator and the valve a. Hot water
A refrigerant distribution having a valve e connecting a heater and a condenser or an evaporator.
Characterized Rutotomoni, a solution pipe from the solution pump outlet of the solution route to the high temperature regenerator inlet, to a solution piping from the high-temperature regenerator outlet to the absorber, respectively valves c, and providing the d provided tube And a double-effect absorption chiller / heater.
【請求項2】 前記弁aと弁bは、一体化して三方弁と
することを特徴とする請求項1記載の二重効用吸収冷温
水機。
2. The double effect absorption chiller / heater according to claim 1, wherein the valve a and the valve b are integrated into a three-way valve.
【請求項3】 前記吸収冷温水機において、温水専用運
転時には、弁a、弁c及び弁dを閉止、弁bを開放する
ように構成したことを特徴とする請求項1又は2記載の
二重効用吸収冷温水機。
3. The absorption chiller / heater according to claim 1, wherein the valve a, the valve c, and the valve d are closed and the valve b is opened during a dedicated hot water operation. Heavy duty absorption chiller / heater
【請求項4】 前記吸収冷温水機において、温水専用運
転時には、弁a、弁c、弁d及び弁eを閉止、弁bを開
放するように構成したことを特徴とする請求項1又は2
記載の二重効用吸収冷温水機。
4. A said absorption chiller, during hot exclusive operation, valves a, claim, characterized in that the valve c, and valves d and valve e closure and configured to open the valve b 1 or 2
The dual-effect absorption chiller / heater as described.
JP30331397A 1997-10-20 1997-10-20 Double effect absorption chiller / heater Expired - Lifetime JP3224766B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP30331397A JP3224766B2 (en) 1997-10-20 1997-10-20 Double effect absorption chiller / heater

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP30331397A JP3224766B2 (en) 1997-10-20 1997-10-20 Double effect absorption chiller / heater

Publications (2)

Publication Number Publication Date
JPH11118278A JPH11118278A (en) 1999-04-30
JP3224766B2 true JP3224766B2 (en) 2001-11-05

Family

ID=17919468

Family Applications (1)

Application Number Title Priority Date Filing Date
JP30331397A Expired - Lifetime JP3224766B2 (en) 1997-10-20 1997-10-20 Double effect absorption chiller / heater

Country Status (1)

Country Link
JP (1) JP3224766B2 (en)

Also Published As

Publication number Publication date
JPH11118278A (en) 1999-04-30

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