JPS6269072A - Absorption type water heater and chiller - Google Patents

Absorption type water heater and chiller

Info

Publication number
JPS6269072A
JPS6269072A JP20860785A JP20860785A JPS6269072A JP S6269072 A JPS6269072 A JP S6269072A JP 20860785 A JP20860785 A JP 20860785A JP 20860785 A JP20860785 A JP 20860785A JP S6269072 A JPS6269072 A JP S6269072A
Authority
JP
Japan
Prior art keywords
water
temperature regenerator
heater
absorption type
chiller
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.)
Pending
Application number
JP20860785A
Other languages
Japanese (ja)
Inventor
渡瀬 一雄
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.)
Hitachi Ltd
Original Assignee
Hitachi 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 Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP20860785A priority Critical patent/JPS6269072A/en
Publication of JPS6269072A publication Critical patent/JPS6269072A/en
Pending legal-status Critical Current

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  • 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】 〔発明の利用分野〕 本発明は吸収式冷温水機に係り、特に冷水、温水を同時
に取出す場合に好適な制御方式に関する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Application of the Invention] The present invention relates to an absorption type water chiller/heater, and particularly to a control system suitable for taking out cold water and hot water at the same time.

〔発明の背景°〕[Background of the invention °]

従来、暖房負荷により高温再生器への入熱を制御し一部
冷房を取出す場合の冷凍容量の制御方法は特開58−2
14761号公報に示されているように、冷媒ポンプ、
溶液ポンプの発停及び低温再生器への溶液の供給を制御
していた。
Conventionally, a method for controlling refrigeration capacity when controlling heat input to a high-temperature regenerator and extracting a portion of the air conditioner based on the heating load is disclosed in JP-A No. 58-2.
As shown in Publication No. 14761, a refrigerant pump,
It controlled the start/stop of the solution pump and the supply of solution to the low temperature regenerator.

そのため、暖房用温水の取り出しが主で、同時に冷水を
も取出す暖主併給運転時においては、暖房負荷が少なく
ガると、高温再生器の器内圧力が下がるため同時に取り
出し得る冷房能力も減少する問題があった。
Therefore, during combined heating and main supply operation where hot water for heating is mainly taken out and cold water is also taken out at the same time, when the heating load is low, the internal pressure of the high temperature regenerator decreases, and the cooling capacity that can be taken out at the same time also decreases. There was a problem.

〔発明の目的〕[Purpose of the invention]

本発明の目的は吸収式冷温水機が暖主併給運転時(暖房
負荷により高温再生器への入熱を制御し、高温再生器で
発生した蒸気を利用し一重効用サイクルで冷水を取り出
す運転)暖房負荷が減ったときでも必要な冷房能力を確
保できる吸収式冷温水機を提供することにある。
The purpose of the present invention is when an absorption type water chiller/heater is operated in combination with heating and main supply (operation in which the heat input to the high-temperature regenerator is controlled by the heating load, and the steam generated in the high-temperature regenerator is used to extract cold water in a single-effect cycle). To provide an absorption type water chiller/heater that can secure necessary cooling capacity even when heating load is reduced.

〔発明の[@) 本発明は、温水器への通水埜を変えろことにより蒸気の
飽和温度を変化させ、冷凍サイクルへの入熱を制御して
冷房能力を変えることを特徴とする。
[@ of the invention] The present invention is characterized in that the saturation temperature of steam is changed by changing the water flow rate to the water heater, and the cooling capacity is changed by controlling the heat input to the refrigeration cycle.

〔発明のf剃イ利〕[Advantages of invention]

まず吸収式冷温水機の冷房ザイクルを第1図により説明
する。
First, the cooling cycle of an absorption type water chiller/heater will be explained with reference to FIG.

蒸発器1内は約百分の1気圧に保たれており、この中で
冷媒である水は冷媒ポンプ2により冷水3が通る伝熱管
上に撒布され冷水の熱を奪い蒸発する。このことにより
冷凍効果が生ずる。蒸発した冷媒蒸気は、冷却水4によ
り低圧に保たれた吸収器5へ流れ込みここで溶液ポンプ
6により撒布された臭化リチウム水溶液により吸収され
臭化リチウム水溶液は稀くなる。この稀溶液は溶液ポン
プ6により熱交換器7を経て一部は高温再生器8へ残り
は低温再生器9へ送り込まれ、高温再生器8では直接熱
凍により加熱され蒸気と濃溶液に分離され、また低温再
生器では高温再生器で発生した蒸気により加熱され蒸気
と濃溶液分離される。
The inside of the evaporator 1 is maintained at approximately 1/100 atmospheric pressure, and water, which is a refrigerant, is sprayed by a refrigerant pump 2 onto a heat transfer tube through which cold water 3 passes, absorbs heat from the cold water, and evaporates. This creates a freezing effect. The evaporated refrigerant vapor flows into the absorber 5 maintained at a low pressure by the cooling water 4, where it is absorbed by the lithium bromide aqueous solution sprayed by the solution pump 6, and the lithium bromide aqueous solution becomes diluted. This dilute solution is sent to a high temperature regenerator 8 through a heat exchanger 7 by a solution pump 6, and the rest to a low temperature regenerator 9. In the high temperature regenerator 8, it is directly heated by thermal freezing and separated into steam and a concentrated solution. In addition, in the low-temperature regenerator, it is heated by the steam generated in the high-temperature regenerator, and the steam and concentrated solution are separated.

この様にして濃縮された溶液は再び熱交換器7を経て吸
収器内に導かれる。一方高温再生器で発生した蒸気の一
部は温水器10で温水を加熱することにより消費され残
りは前述の様に低温再生器界9内の溶液を加熱し凝縮し
たドレンは凝縮器11へ導かれる。また低温再生器で発
生した蒸気は凝縮器で凝縮する。この様にしてできた凝
縮冷媒は蒸発器1へ導かれサイクルを一巡する。
The solution thus concentrated is again led into the absorber via the heat exchanger 7. On the other hand, a part of the steam generated in the high-temperature regenerator is consumed by heating hot water in the water heater 10, and the remainder heats the solution in the low-temperature regenerator field 9 as described above, and the condensed condensate is led to the condenser 11. It will be destroyed. In addition, the steam generated in the low-temperature regenerator is condensed in the condenser. The condensed refrigerant thus produced is led to the evaporator 1 and goes through the cycle.

第2図は暖主併給運転時のサイクルを示す。冷房サイク
ルとの相違を以下説明する。
Figure 2 shows the cycle during combined heating and main supply operation. The differences from the cooling cycle will be explained below.

吸収器内の稀溶液は溶液ポンプ6により熱交換器7を経
て低温再生器9へ送り込まれここで管内の蒸気により加
熱され濃縮され再び熱交換器7を経て吸収器へ導かれる
。また低温再生器9で蒸発した蒸気は凝縮器11で冷却
水4により冷却され凝縮した冷媒は蒸発器1へ送られ蒸
発し冷媒効果をもたらす。また高温再生器8では溶液が
加熱され発生した蒸気は温水器10で温水を発生させド
レンは再び高温再生器へ戻る。また一部の蒸気は低温再
生器pへ流れ込み管外の溶液を加熱濃縮する。このドレ
ンも再び高温再生器へ導かれる。以上により温水と冷水
を温水側負荷に応じて高温再生器への入熱を制御するこ
とにより提供することができる。
The dilute solution in the absorber is sent by the solution pump 6 to the low-temperature regenerator 9 via the heat exchanger 7, where it is heated and concentrated by the steam in the tube, and then guided to the absorber via the heat exchanger 7 again. Further, the vapor evaporated in the low-temperature regenerator 9 is cooled by the cooling water 4 in the condenser 11, and the condensed refrigerant is sent to the evaporator 1 and evaporated to produce a refrigerant effect. Further, in the high temperature regenerator 8, the solution is heated and the generated steam generates hot water in the water heater 10, and the drain returns to the high temperature regenerator again. Further, a part of the vapor flows into the low temperature regenerator p and heats and concentrates the solution outside the tube. This drain is also led to the high temperature regenerator again. As described above, hot water and cold water can be provided by controlling the heat input to the high temperature regenerator according to the load on the hot water side.

第3図は本発明の要部を示すものである。FIG. 3 shows the main part of the present invention.

第3図に示す様に温水配管に三方弁15を追加し冷水出
口温度センサ14により、冷水温度が高いと温水器通過
流量を減らしこのことにより温水出口温度センサ12が
温度の低下を検知し制御弁13を開は入熱を増やす。こ
の結果として高温再生器内の蒸気温度が上昇し低温再生
器における入熱も増へ冷凍能力が増す。逆に冷水出口温
度が下がると、三方弁15により温水器通過流量を増や
し制御弁13を閉に入熱を減らし高温再生器内の蒸気温
度を下げ冷凍能力を減らす。この様にして暖主併給運転
時に冷凍容量を制御することができる。
As shown in Fig. 3, a three-way valve 15 is added to the hot water piping, and a cold water outlet temperature sensor 14 reduces the flow rate passing through the water heater when the cold water temperature is high.As a result, the hot water outlet temperature sensor 12 detects a decrease in temperature and controls the temperature. Opening valve 13 increases heat input. As a result, the steam temperature in the high temperature regenerator increases, the heat input to the low temperature regenerator also increases, and the refrigerating capacity increases. Conversely, when the chilled water outlet temperature decreases, the three-way valve 15 increases the flow rate passing through the water heater, and the control valve 13 is closed to reduce the heat input and lower the steam temperature in the high-temperature regenerator, thereby reducing the refrigeration capacity. In this way, the refrigeration capacity can be controlled during combined heating and main supply operation.

〔発明の効果〕〔Effect of the invention〕

吹上のように本発明によれば、冷水温水同時取出形冷温
水機では標準的に装置されている温水三方弁により暖主
併給運転時の、冷房能力を制御できる。
As shown in Fukiage, according to the present invention, the cooling capacity can be controlled during combined heating and main supply operation using the three-way hot water valve that is standard equipment in cold/hot water simultaneous extraction type cold/hot water machines.

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

第1図は、冷凍サイクル説明図、第2図は、暖主併給サ
イクル説明図、第3図は、本発明の詳細な説明図である
。 1・・・蒸発器、2・・・冷媒ポンプ、3・・・冷水、
4・・・冷却水、5・・・吸収器、6・・・溶液ポンプ
、7・・・熱交換器、8・・・高温再生器、9・・・低
温再生器、10・・・温水器、11・・・凝紬器、12
・・・温水出口温度センサー、13・・・燃料制御弁、
14・・・冷水出口温度センサー、15・・・温水量制
御弁。
FIG. 1 is an explanatory diagram of a refrigeration cycle, FIG. 2 is an explanatory diagram of a combined heating and main supply cycle, and FIG. 3 is a detailed explanatory diagram of the present invention. 1... Evaporator, 2... Refrigerant pump, 3... Chilled water,
4... Cooling water, 5... Absorber, 6... Solution pump, 7... Heat exchanger, 8... High temperature regenerator, 9... Low temperature regenerator, 10... Hot water Vessel, 11... Tsumugi vessel, 12
...Hot water outlet temperature sensor, 13...Fuel control valve,
14...Cold water outlet temperature sensor, 15...Hot water amount control valve.

Claims (1)

【特許請求の範囲】[Claims] 1、蒸発器、吸収器、再生器、熱交換器、溶液ポンプ、
冷媒ポンプ、温水器とこれらを作動的に結合する配管類
から成り、温水、冷水を同時に取出すことのできる吸収
式冷温水機において、温水の負荷に応じて再生器への入
熱を制御し、温水器を通過する温水量を増減することに
より冷水の容量制御をすることを特徴とする吸収式冷温
水機。
1. Evaporator, absorber, regenerator, heat exchanger, solution pump,
In an absorption type water chiller/heater, which consists of a refrigerant pump, a water heater, and piping that operatively connects these, and can extract hot and cold water at the same time, the heat input to the regenerator is controlled according to the load of hot water. An absorption type water cooler/heater characterized by controlling the capacity of cold water by increasing or decreasing the amount of hot water passing through the water heater.
JP20860785A 1985-09-24 1985-09-24 Absorption type water heater and chiller Pending JPS6269072A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20860785A JPS6269072A (en) 1985-09-24 1985-09-24 Absorption type water heater and chiller

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20860785A JPS6269072A (en) 1985-09-24 1985-09-24 Absorption type water heater and chiller

Publications (1)

Publication Number Publication Date
JPS6269072A true JPS6269072A (en) 1987-03-30

Family

ID=16559009

Family Applications (1)

Application Number Title Priority Date Filing Date
JP20860785A Pending JPS6269072A (en) 1985-09-24 1985-09-24 Absorption type water heater and chiller

Country Status (1)

Country Link
JP (1) JPS6269072A (en)

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