JPS5834732B2 - Single and double effect absorption refrigerator - Google Patents

Single and double effect absorption refrigerator

Info

Publication number
JPS5834732B2
JPS5834732B2 JP11751279A JP11751279A JPS5834732B2 JP S5834732 B2 JPS5834732 B2 JP S5834732B2 JP 11751279 A JP11751279 A JP 11751279A JP 11751279 A JP11751279 A JP 11751279A JP S5834732 B2 JPS5834732 B2 JP S5834732B2
Authority
JP
Japan
Prior art keywords
temperature
generator
heat source
low
absorber
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
Application number
JP11751279A
Other languages
Japanese (ja)
Other versions
JPS55121361A (en
Inventor
龍雄 宮城
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.)
Tokyo Sanyo Electric Co Ltd
Sanyo Denki Co Ltd
Original Assignee
Tokyo Sanyo Electric Co Ltd
Sanyo Denki Co Ltd
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 Tokyo Sanyo Electric Co Ltd, Sanyo Denki Co Ltd filed Critical Tokyo Sanyo Electric Co Ltd
Priority to JP11751279A priority Critical patent/JPS5834732B2/en
Publication of JPS55121361A publication Critical patent/JPS55121361A/en
Publication of JPS5834732B2 publication Critical patent/JPS5834732B2/en
Expired legal-status Critical Current

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  • Sorption Type Refrigeration Machines (AREA)

Description

【発明の詳細な説明】 本発明は一重二重効用吸収冷凍機に関するもので、太陽
熱温水などの低温熱源を主熱源とし、蒸気などの高温熱
源を補助熱源として、熱源状態や負荷に応じて吸収冷凍
機の運転態様を選択し、エネルギーの有効利用を図ると
共に効率のよい運転を行うことを目的とする。
Detailed Description of the Invention The present invention relates to a single-double effect absorption refrigerator, which uses a low-temperature heat source such as solar hot water as the main heat source and a high-temperature heat source such as steam as an auxiliary heat source. The purpose is to select the operating mode of the refrigerator, to aim for effective use of energy, and to perform efficient operation.

すなわち1台の吸収冷凍機を、太陽熱が十分に得られ、
高い温度(85°C〜90°C)の温水が供給されてい
る時は一重効用運転を行い、温水温度が低下し補助熱源
を加える時は一重二重併用運転、温水温度が低く運転が
不可能な時は補助熱源による二重効用運転を、弁の切替
え操作など必要としないで行うようにしたものである。
In other words, enough solar heat can be obtained for one absorption refrigerator,
Single-effect operation is performed when hot water at a high temperature (85°C to 90°C) is supplied, and when the hot water temperature drops and an auxiliary heat source is added, single- and dual-effect operation is performed, and operation is disabled when the hot water temperature is low. When possible, dual-effect operation is performed using an auxiliary heat source without the need for valve switching operations.

以下本発明を図に示す実施例について説明する。The present invention will be described below with reference to embodiments shown in the drawings.

1は太陽熱温水を熱源として稀液より冷媒を加熱分離す
る低温熱源用発生器、2は高温蒸気を熱源として一次中
間液から冷媒を加熱分離する高温発生器、3は前記高温
発生器2で分離された冷媒蒸気を熱源として二次中間液
を再熱し冷媒を更に加熱分離する低温発生器、4は前記
各発生器1,2゜3から流入する冷媒を冷却器5で冷却
して凝縮する凝縮器、6は前記凝縮器4からの冷媒液を
散布し気化させる際の潜熱を利用して冷水器7から冷房
用の冷水を得るようにした蒸発器、8は前記低温熱源発
生器1及び高温発器2と低温発生器3で適宜冷媒を分離
して濃縮された濃液を散布して器内の冷媒蒸気を吸収す
ることにより前記蒸発器6の内部を低圧に維持し連続し
た冷水の供給を行なえるようにした吸収器、9及び10
は低温と高温の溶液熱交換器で、これらは冷媒蒸気配管
11゜冷媒液流下管12、冷媒ポンプ13を有する冷媒
循環路14、稀液ポンプ15を有する種族管路16、中
間液ポンプ17を有する一次中間液管路18、二次中間
液管路19及び濃液管路20により配管接続して吸収冷
凍サイクルを構成している。
1 is a low-temperature heat source generator that heats and separates a refrigerant from a dilute liquid using solar hot water as a heat source; 2 is a high-temperature generator that heats and separates a refrigerant from a primary intermediate liquid using high-temperature steam as a heat source; 3 is a high-temperature generator that separates the refrigerant from a primary intermediate liquid by heating. A low-temperature generator 4 uses the generated refrigerant vapor as a heat source to reheat the secondary intermediate liquid and further heat and separate the refrigerant. 4 is a condenser that cools and condenses the refrigerant flowing from each of the generators 1, 2 and 3 in a cooler 5. 6 is an evaporator that obtains cold water for air conditioning from a water cooler 7 by using latent heat when the refrigerant liquid from the condenser 4 is dispersed and vaporized; 8 is an evaporator that uses the low temperature heat source generator 1 and the high temperature The refrigerant is appropriately separated by the generator 2 and the low-temperature generator 3, and the concentrated liquid is dispersed to absorb the refrigerant vapor inside the container, thereby maintaining the inside of the evaporator 6 at a low pressure and continuously supplying cold water. Absorbers 9 and 10
is a low-temperature and high-temperature solution heat exchanger, which includes a refrigerant vapor pipe 11°, a refrigerant liquid down-flow pipe 12, a refrigerant circuit 14 with a refrigerant pump 13, a mixed pipe 16 with a dilute liquid pump 15, and an intermediate liquid pump 17. A primary intermediate liquid pipe 18, a secondary intermediate liquid pipe 19, and a concentrated liquid pipe 20 are connected to form an absorption refrigeration cycle.

而して低温熱源発器1と低温発生器3は双方の液が混合
しないように仕切板21で区画して同一圧力レベルにな
るように配置されると共に前記低温熱源発生器1と吸収
器8との間には後述の二重効用運転時に吸収液で液封さ
れ一重効用運転時に低温熱源発生器1で濃縮された吸収
液を直接吸収器8に供給できる側路管22を設け、該側
路管の入口端は二重効用運転時におけろ低温熱源発生器
1の液面より稍高い位置に開口している。
The low-temperature heat source generator 1 and the low-temperature generator 3 are separated by a partition plate 21 to prevent their liquids from mixing, and are arranged so that the pressure level is the same, and the low-temperature heat source generator 1 and the absorber 8 A side pipe 22 is provided between the absorber 8 and the side pipe 22, which is liquid-sealed with an absorbing liquid during double-effect operation, which will be described later, and which can directly supply the absorbent concentrated in the low-temperature heat source generator 1 to the absorber 8 during single-effect operation. The inlet end of the pipe opens at a position slightly higher than the liquid level of the low temperature heat source generator 1 during dual effect operation.

前記低温熱源発生器1を加熱する太陽熱温水供給回路2
3には温水三方弁24を設け、また高温発生器3を加熱
する蒸気供給回路25には蒸気制御弁26を設けると共
に前記高温発生器2で生じた蒸気ドレーンの熱回収器2
7を低温熱源発生器1に配設している。
A solar hot water supply circuit 2 that heats the low temperature heat source generator 1
3 is provided with a hot water three-way valve 24, and a steam supply circuit 25 for heating the high temperature generator 3 is provided with a steam control valve 26, and a heat recovery device 2 for the steam drain generated in the high temperature generator 2 is provided.
7 is arranged in the low temperature heat source generator 1.

28は温度制御切換器で該切換器は太陽熱温水供給回路
23に設けた温水温度検出器29により検出された太陽
熱温水の温度が設定値以上或はそれに近い場合(両者を
含み設定値の近傍という)には温接点H側に閉じて前記
温水供給回路23に設けた他の温水温度検出器30から
の信号により蒸気供給回路25に設けた蒸気制御弁26
を調節すると共に太陽熱温水の温度が設定値より相当低
い場合には前記温度制御切換器28は冷接点C側に閉じ
て冷水器7の出口側に設けた冷水温度検出器31からの
信号により前記蒸気制御弁26を調節する。
Reference numeral 28 denotes a temperature control switch, which is used when the temperature of the solar hot water detected by the hot water temperature detector 29 provided in the solar hot water supply circuit 23 is higher than or close to the set value (including both, it is called near the set value). ) is a steam control valve 26 which is closed on the hot junction H side and which is provided in the steam supply circuit 25 in response to a signal from another hot water temperature detector 30 which is provided in the hot water supply circuit 23.
and when the temperature of the solar hot water is considerably lower than the set value, the temperature control switch 28 closes to the cold junction C side, and the temperature control switch 28 closes to the cold junction C side, and the temperature control switch 28 closes to the cold water temperature sensor 31 provided on the outlet side of the water cooler 7. Adjust steam control valve 26.

次に運転状態について説明する。Next, the operating state will be explained.

イノ太陽熱温水による一重効用運転 この場合は負荷に対して十分な太陽熱温水が得られるの
で中間液ポンプ17の運転を停止する。
Single-effect operation using Inno solar hot water In this case, sufficient solar hot water is obtained for the load, so the operation of the intermediate liquid pump 17 is stopped.

吸収器8から稀液ポンプ15により低温溶液熱交換器9
を経由して低温熱源発生器1に送られた稀液は該発生器
で太陽熱温水により加熱され沸騰し冷媒蒸気を発生して
濃縮される。
From the absorber 8 to the low temperature solution heat exchanger 9 by the diluted liquid pump 15
The diluted liquid sent to the low-temperature heat source generator 1 is heated by solar hot water in the generator, boils, generates refrigerant vapor, and is concentrated.

濃縮された吸収液は側路管21を通り前記低温溶液熱交
換器9にむいて稀液と熱交換した後吸収器8に散布され
る。
The concentrated absorption liquid passes through the side pipe 21 to the low-temperature solution heat exchanger 9, exchanges heat with the diluted liquid, and is then sprayed into the absorber 8.

方低温熱源発生器1で加熱分離された冷媒蒸気は凝縮器
4で液化し蒸発器6に散布されて気化した後前記吸収器
8で吸収される。
The refrigerant vapor heated and separated by the low-temperature heat source generator 1 is liquefied in the condenser 4, sprayed in the evaporator 6, vaporized, and then absorbed in the absorber 8.

そしてこの時の気化熱により冷水が得られる。Cold water is obtained from the heat of vaporization at this time.

口)太陽熱温水と高温補助熱源による一重二重併用運転
及び高温補助熱源による二重効用運転。
口) Single-duplex combined operation using solar hot water and high-temperature auxiliary heat source, and double-effect operation using high-temperature auxiliary heat source.

これらの場合は負荷に対して太陽熱温水の温度が低く入
熱が不足するので中間液ポンプ17も運転する。
In these cases, the temperature of the solar hot water is low relative to the load and the heat input is insufficient, so the intermediate liquid pump 17 is also operated.

吸収器8から稀液ポンプ15により低温溶液熱交換器9
を経由して低温熱源発生器1に送られた稀液は該発生器
で太陽熱温水が供給されている場合は加熱され濃縮され
る。
From the absorber 8 to the low temperature solution heat exchanger 9 by the diluted liquid pump 15
The diluted liquid sent to the low-temperature heat source generator 1 via the generator is heated and concentrated if solar hot water is supplied to the generator.

次にこの濃縮された吸収液は中間液ポンプ17により高
温溶液熱交換器10を経由して高温発生器2に送られる
Next, this concentrated absorption liquid is sent to the high temperature generator 2 via the high temperature solution heat exchanger 10 by the intermediate liquid pump 17.

この吸収液は前記高温発生器2では補助熱源である蒸気
により沸騰濃縮された後高温溶液熱交換器10を経て低
温発生器3へ送られて更に加熱され沸騰し低温溶液熱交
換器9を経て吸収器8に散布される。
This absorption liquid is boiled and concentrated in the high temperature generator 2 using steam, which is an auxiliary heat source, and then sent to the low temperature generator 3 via the high temperature solution heat exchanger 10, where it is further heated and boiled, and then passed through the low temperature solution heat exchanger 9. It is dispersed into the absorber 8.

そして高温発生器2で分離された冷媒蒸気は低温発生器
3で凝縮し、低温発生器3及び低温熱源発生器1で分離
された冷媒蒸気はいずれも凝縮器4で凝縮し、その後蒸
発器6で気化して吸収器8で吸収される。
The refrigerant vapor separated in the high temperature generator 2 is condensed in the low temperature generator 3, and the refrigerant vapor separated in the low temperature generator 3 and the low temperature heat source generator 1 is condensed in the condenser 4, and then in the evaporator 6. It is vaporized and absorbed by the absorber 8.

この時の気化熱によりイ)の場合と同様冷水が得られる
The heat of vaporization at this time yields cold water as in case a).

本発明による一重二重効用吸収冷凍機は上述の如く、太
陽熱温水などの低温熱源により加熱される低温熱源発生
器、蒸気などの高温熱源により加熱される高温発生器、
該高温発生器で加熱分離された冷媒蒸気により加熱され
る低温発生器、凝縮器、蒸発器、吸収器及び溶液熱交換
器を接続して冷凍サイクルを構成すると共に前記吸収器
から稀液ポンプと中間液ポンプにより吸収溶液を前記各
発生器に循環するようにし、低温熱源による一重効用運
転時には前記中間液ポンプを停止[〜補液ポンプを運転
して低温熱源発生器から吸収器へは側路管を経由して濃
縮された吸収液を戻すと共に高温熱源による二重効用運
転時には稀液ポンプと中間液ポンプを運転して吸収器に
は各発生器で順次濃縮された吸収液を戻すようにしたも
のであるから、太陽熱温水などを最大限に利用した熱効
率のよい運転を行うことが出来る。
As described above, the single-double effect absorption refrigerator according to the present invention includes a low-temperature heat source generator heated by a low-temperature heat source such as solar hot water, a high-temperature generator heated by a high-temperature heat source such as steam,
A low-temperature generator heated by the refrigerant vapor heated and separated by the high-temperature generator, a condenser, an evaporator, an absorber, and a solution heat exchanger are connected to form a refrigeration cycle, and a dilute liquid pump is connected from the absorber to a dilute liquid pump. The intermediate liquid pump is used to circulate the absorption solution to each of the generators, and the intermediate liquid pump is stopped during single-effect operation using a low-temperature heat source. In addition, during dual effect operation using a high-temperature heat source, the diluted liquid pump and intermediate liquid pump were operated to return the absorbed liquid concentrated in each generator to the absorber in sequence. Because of this, it is possible to operate with high thermal efficiency by making maximum use of solar hot water.

しかも熱源に応じた運転の切替えも弁の切替え動作は不
要で2個の溶液ポンプのうち1台を発停するだけで簡単
に行うことができる。
Moreover, the operation can be easily changed according to the heat source by simply turning one of the two solution pumps on and off, without requiring a valve switching operation.

また各発生器に対する溶液の流れはシリーズに流れるた
め流量、濃度のバランスをとる必要がなく運転はスムー
ズとなる等の効果がある。
In addition, since the solution flows to each generator in series, there is no need to balance the flow rate and concentration, resulting in smooth operation.

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

図面は本発明による一重二重効用吸収冷凍機の構成図で
ある。 1・・・低温熱源発生器、2・・・高温発生器、3・・
・低温発生器、8・・・吸収器、15・・・稀液ポンプ
、17・・・中間液ポンプ、22゛・・・側路管。
The drawing is a block diagram of a single-double effect absorption refrigerator according to the present invention. 1...Low temperature heat source generator, 2...High temperature generator, 3...
- Low temperature generator, 8... Absorber, 15... Dilute liquid pump, 17... Intermediate liquid pump, 22゛... Side pipe.

Claims (1)

【特許請求の範囲】[Claims] 1 太陽熱温水などの低温熱源により加熱される低温熱
源発生器、蒸気などの高温熱源により加熱される高温発
生器、該高温発生器で加熱分解された冷媒蒸気により加
熱される低温発生器、凝縮器、蒸発器、吸収器及び溶液
熱交換器を接続して冷凍サイクルを構成すると共に前記
吸収器から稀液ポンプと中間液ポンプにより吸収溶液を
低温熱源発生器経由で高温発生器へ導いて吸収溶液が吸
収器、低温熱源発生器、高温発生器、低温発生器を順次
循環するようにし、低温熱源による一重効用運転時には
前記中間液ポンプを停止し稀液ポンプを運転して低温熱
源発生器から吸収器へは側路管を経由して濃縮された吸
収液を戻すと共に高温熱源による二重効用運転時には稀
液ポンプと中間液ポンプを運転して吸収器には各発生器
で順次濃縮された吸収液を戻すようにしたことを特徴と
する一重二重効用吸収冷凍機。
1. A low-temperature heat source generator heated by a low-temperature heat source such as solar hot water, a high-temperature generator heated by a high-temperature heat source such as steam, a low-temperature generator heated by refrigerant vapor thermally decomposed in the high-temperature generator, and a condenser. , an evaporator, an absorber, and a solution heat exchanger are connected to form a refrigeration cycle, and the absorbent solution is guided from the absorber to a high-temperature generator via a low-temperature heat source generator by a dilute liquid pump and an intermediate liquid pump to produce an absorbent solution. The liquid is circulated sequentially through the absorber, low-temperature heat source generator, high-temperature generator, and low-temperature generator, and during single-effect operation using a low-temperature heat source, the intermediate liquid pump is stopped and the dilute liquid pump is operated to absorb water from the low-temperature heat source generator. The concentrated absorption liquid is returned to the absorber via a side pipe, and during dual-effect operation using a high-temperature heat source, a dilute liquid pump and an intermediate liquid pump are operated, and the absorbed liquid that has been concentrated in each generator is returned to the absorber. A single-double effect absorption refrigerator characterized by returning liquid.
JP11751279A 1979-09-12 1979-09-12 Single and double effect absorption refrigerator Expired JPS5834732B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11751279A JPS5834732B2 (en) 1979-09-12 1979-09-12 Single and double effect absorption refrigerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11751279A JPS5834732B2 (en) 1979-09-12 1979-09-12 Single and double effect absorption refrigerator

Publications (2)

Publication Number Publication Date
JPS55121361A JPS55121361A (en) 1980-09-18
JPS5834732B2 true JPS5834732B2 (en) 1983-07-28

Family

ID=14713589

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11751279A Expired JPS5834732B2 (en) 1979-09-12 1979-09-12 Single and double effect absorption refrigerator

Country Status (1)

Country Link
JP (1) JPS5834732B2 (en)

Also Published As

Publication number Publication date
JPS55121361A (en) 1980-09-18

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