JPS61173058A - Method of operating heat pump - Google Patents

Method of operating heat pump

Info

Publication number
JPS61173058A
JPS61173058A JP1106585A JP1106585A JPS61173058A JP S61173058 A JPS61173058 A JP S61173058A JP 1106585 A JP1106585 A JP 1106585A JP 1106585 A JP1106585 A JP 1106585A JP S61173058 A JPS61173058 A JP S61173058A
Authority
JP
Japan
Prior art keywords
antifreeze
heat pump
tower
concentration
heat
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
Application number
JP1106585A
Other languages
Japanese (ja)
Other versions
JPH0510576B2 (en
Inventor
堺田 進
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 JP1106585A priority Critical patent/JPS61173058A/en
Publication of JPS61173058A publication Critical patent/JPS61173058A/en
Publication of JPH0510576B2 publication Critical patent/JPH0510576B2/ja
Granted legal-status Critical Current

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  • Compression-Type Refrigeration Machines With Reversible Cycles (AREA)
  • Other Air-Conditioning Systems (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】 この発明はヒートポンプの運転方法に関する。[Detailed description of the invention] The present invention relates to a method of operating a heat pump.

冬期に空気から集熱を行うヒーティングタワー兼用のク
ーリングタワーを有するヒートポンプにおいて、冬期に
使用する時に循還液の氷結を防ぐため循還液として不凍
液を使用することがあるが。
In a heat pump that has a cooling tower that also serves as a heating tower that collects heat from the air in the winter, antifreeze may be used as the circulating fluid to prevent the circulating fluid from freezing when used in the winter.

この場合ヒーティングタワーを夏期にクーリングタワー
として兼用するに当り、(a)不凍液を回収して真水に
入れ替えて冷却水として使用するか、又は(b)不凍液
をそのま\冷却水として使用するかの2つの方法が考え
られる。しかしくa)の方法では不凍液回収用として大
きな槽が必要となる。さらに(b)の方法では「伝熱の
悪い不凍液を冷却水として使用するためヒートポンプ機
及び循還ポンプの動力増になる」、「不凍液を年間使用
するため冬期のみの使用に比して劣化が早まる」、「夏
期の使用では不凍液の濃縮が生じるため稀釈のために補
給水が必要である。それで不純分を含む補給水では不凍
液が汚れるため純水の補給が必要でおるが、純水製造設
備は高価でsb、維持費も多くかかる。」等の欠点があ
った。そこでこの発明はこれらの従来の欠点を解消する
ため(a)の不凍液回収の方法を改善して、その欠点を
取シ除くものでろる。即ち冬期運転から夏期運転へ移行
した当初は一般に冷水負荷は小さく、外気温も低い。こ
の期間を利用して不凍液の濃縮運転を行い、濃縮し九不
凍液を槽に回収すれば槽は小さくてすみ従来の欠点を解
消したものとなる。
In this case, when the heating tower is also used as a cooling tower in the summer, there are two options: (a) collect the antifreeze and replace it with fresh water and use it as cooling water, or (b) use the antifreeze as is as cooling water. Two methods are possible. However, method a) requires a large tank for antifreeze recovery. Furthermore, in method (b), ``antifreeze, which has poor heat transfer, is used as cooling water, which increases the power of the heat pump and circulation pump,'' and ``because antifreeze is used all year round, there is less deterioration compared to when it is used only in winter.''"When used in the summer, the antifreeze becomes concentrated, so make-up water is required to dilute it. If the make-up water contains impurities, the antifreeze becomes contaminated, so it is necessary to replenish pure water, but There were drawbacks such as ``the equipment is expensive, SB, and maintenance costs are high.'' Therefore, the present invention aims to eliminate these drawbacks by improving the antifreeze recovery method (a). That is, at the beginning of the transition from winter operation to summer operation, the chilled water load is generally small and the outside temperature is low. If this period is used to concentrate the antifreeze solution and the concentrated antifreeze solution is collected in a tank, the tank can be made smaller and the drawbacks of the conventional method can be overcome.

図はこの発明の方法を実施するヒートポンプのシステム
例を示し、ヒーティングタカ−兼用クーリングタワ−1
、温水用凝縮器2、ブースター圧縮機6、冷却水用凝縮
器4、主圧縮機5.ブライン(不凍液)用蒸発器6、冷
水用蒸発器7を有している。
The figure shows an example of a heat pump system that implements the method of the present invention.
, hot water condenser 2, booster compressor 6, cooling water condenser 4, main compressor 5. It has a brine (antifreeze) evaporator 6 and a cold water evaporator 7.

ブライン(不凍液)はヒーティングタワー兼用クーリン
グタワー1(以下単にタワー1と記載する)から循還用
ポンプ71により、配管21.22により循還し、配管
2ろ、24によル冷却水用凝縮器4にゆき、又配管26
.27によシライン用蒸発器6にゆく。25は凝縮器4
内の熱交換部−28は蒸発器6内の熱交換部を示してい
る。
Brine (antifreeze) is circulated from the heating tower/cooling tower 1 (hereinafter simply referred to as tower 1) by a circulation pump 71, through piping 21 and 22, and through piping 2 and 24 to the cooling water condenser. Moving on to 4, piping 26
.. 27 to the siline evaporator 6. 25 is condenser 4
A heat exchange section 28 inside indicates a heat exchange section within the evaporator 6.

冬期の冷媒の流れは、シライン用蒸発器6から配管66
で主圧縮機5にゆき、以下配管37.冷却水用凝縮器4
、配管68.ブースター圧縮機6、配管39.温水用凝
縮器2、配管40、凝縮器4、配管41、冷水用蒸発器
7、配管35.蒸発器6となる。その陳弁56,57,
59,61,62は開かれ、又、弁51,52,54,
55.60は閉じられ、不凍液の循還路と槽8とは切#
)はなされる。
During the winter, the refrigerant flows from the si-line evaporator 6 to the pipe 66.
It goes to the main compressor 5, and the following piping 37. Cooling water condenser 4
, piping 68. Booster compressor 6, piping 39. Condenser 2 for hot water, piping 40, condenser 4, piping 41, evaporator 7 for cold water, piping 35. This becomes the evaporator 6. That statement 56, 57,
59, 61, 62 are opened, and valves 51, 52, 54,
55 and 60 are closed, and the antifreeze circulation path and tank 8 are disconnected.
) is done.

尚56は逆止弁、72は補給用ポンプでるる。弁58は
蒸発器7の圧力に応じて開閉されている。
Note that 56 is a check valve, and 72 is a replenishment pump. The valve 58 is opened and closed depending on the pressure of the evaporator 7.

冬期のシステムの作用を説明すれば冷媒はブライン用蒸
発器6で蒸発して熱交換部28で配管中のブライン(即
ち不凍液)から熱を奪い配管36で圧縮機5にゆき配管
37で冷却水用凝縮器4に吐出される。次に配管68で
ブースター圧縮機6にゆき、温水用凝縮器2へ配管39
で導かれ、配管29.50を流れる暖房用等の温水に熱
交換部31で熱を与え、凝縮される。配管40で再び凝
縮器4を経て配管41によって冷水用蒸発器7にゆき一
部蒸発して配管52.63を流れる冷水から熱交換部3
4で熱を奪い配管65で蒸発器6に戻る。
To explain the operation of the system in winter, the refrigerant is evaporated in the brine evaporator 6, takes heat from the brine (i.e., antifreeze) in the piping in the heat exchanger 28, goes to the compressor 5 in the piping 36, and is transferred to the cooling water in the piping 37. It is discharged to the condenser 4 for use. Next, the pipe 68 goes to the booster compressor 6, and the pipe 39 goes to the hot water condenser 2.
The heat exchange section 31 gives heat to hot water for heating and the like flowing through the piping 29.50, and the water is condensed. The cold water passes through the condenser 4 again through the pipe 40, goes to the cold water evaporator 7 through the pipe 41, is partially evaporated, and flows through the pipes 52 and 63, and then is transferred to the heat exchange section 3.
4 removes heat and returns to the evaporator 6 through a pipe 65.

ブラインとしての不凍液は循還用ポンプ71で循還する
が、冬期はタワー1で散水部11から散水され外気から
熱を集熱し、配管21から、配管27.26によってブ
ライン用蒸発器6に入シ、熱交換部28で冷媒に熱を与
え、配管22でタワー1に戻る。尚12は外気を送風す
るファンを示している。
Antifreeze as a brine is circulated by a circulation pump 71, but in winter, it is sprinkled with water from the water sprinkler section 11 in the tower 1 to collect heat from the outside air, and then enters the brine evaporator 6 via piping 21 and piping 27.26. Heat is applied to the refrigerant in the heat exchange section 28, and the refrigerant returns to the tower 1 through the piping 22. Note that 12 indicates a fan that blows outside air.

この状態から夏期運転に入るKは、図示の例では配管2
6.27をパイAスする管43の弁55及び弁60を開
いて系内の不凍液を槽8に回収し。
K starts summer operation from this state, in the example shown, piping 2
6. Open the valves 55 and 60 of the pipe 43 that passes through 27 to collect the antifreeze in the system into the tank 8.

系内に真水を注入するか、或いは夏期も不凍液をそのま
\使用しつづけるかの2つの方法がめるが、前述の如く
その何れにも欠点がめった。
Two methods have been proposed: injecting fresh water into the system or continuing to use antifreeze in the summer, but as mentioned above, both methods have many drawbacks.

夏期運転の場合は、弁51,52.58を開き、弁54
,55,56,57.60は閉じる。すると冷媒は冷水
用蒸発器7で蒸発し配管52.38を流れる冷房用等の
冷水から熱を奪い配管42で主圧縮器5にゆき、ついで
配管37で冷水用凝縮器4に入り、配管2L24を流れ
る冷却用水(前記の如く水又は不凍液)K熱を与え、配
管41で蒸発器7に戻る。冷却用水は凝縮器4内の熱交
換部25で加熱され、配管22でタワー1に戻り、今度
は散水により大気中に放熱し、ポンプ71によυ配管2
1から配管26に入る。
For summer operation, open valves 51, 52, and 58, and close valve 54.
, 55, 56, 57.60 close. Then, the refrigerant evaporates in the cold water evaporator 7, removes heat from the cold water for air conditioning, etc. flowing through the pipes 52 and 38, goes to the main compressor 5 through the pipe 42, then enters the cold water condenser 4 through the pipe 37, and passes through the pipe 2L24. Cooling water (water or antifreeze as described above) flowing through the evaporator 7 gives K heat and returns to the evaporator 7 via a pipe 41. The cooling water is heated in the heat exchange section 25 in the condenser 4, returns to the tower 1 through the piping 22, radiates heat into the atmosphere by sprinkling water, and is transferred to the υ piping 2 by the pump 71.
1 into the pipe 26.

この発明の運転方法においては、この冬期運転から夏期
運転への移行に当シ、当初は一般に冷水負荷は小さく、
外気温も低い期間を利用し、暫ら〈不凍液をそのま\使
用して夏期運転に入る。
In the operating method of the present invention, during the transition from winter operation to summer operation, initially the chilled water load is generally small;
Take advantage of the period when the outside temperature is low and start summer operation by using antifreeze for a while.

すると不凍液は系内を循還しているとき、タワー1内で
散水により放熱するとき、水分を蒸発し、少しづつ濃縮
される。そうしである程度濃縮がすすんだときこの濃縮
された不凍液を槽8に回収すれば槽は小さくてすむ。例
えば30%のエチレングリコール水を60%に濃縮して
槽8に回収すれば檜の大きさを1Aにすることができる
。そうして系内から不凍液を回収した後真水を使用する
ことによシ、従来の欠点は凡て解消することができた。
Then, as the antifreeze fluid circulates within the system and radiates heat through water sprinkling within the tower 1, water evaporates and becomes concentrated little by little. In this way, when the concentration has progressed to a certain extent, the concentrated antifreeze solution can be collected in the tank 8, so that the tank can be made smaller. For example, if 30% ethylene glycol water is concentrated to 60% and collected in tank 8, the size of the cypress can be made 1A. By using fresh water after recovering the antifreeze from the system, all of the conventional drawbacks could be overcome.

実際の装置においては、系の適当な個所に不凍液の濃度
を検知する手段を設け、濃縮運転の中止の指令を出すよ
うにしてもよいし、又はヒーティングタワー兼用クーリ
ングタワーの液位を検知して不凍液の濃縮が所定の程度
まで進行したことを確認し、濃縮運転の中止指令を出し
てもよい。
In an actual device, a means for detecting the concentration of antifreeze liquid may be provided at an appropriate location in the system to issue a command to stop the concentration operation, or a means for detecting the liquid level in a cooling tower that also serves as a heating tower may be provided. After confirming that the antifreeze concentration has progressed to a predetermined level, a command to stop the concentration operation may be issued.

又冬期の集熱運転時は不凍液が稀釈される傾向&lるが
、この冬期の集熱運転の末期には不凍液が稀釈されるの
にまかせ不凍液量の増大した分は槽内に保管しておき、
夏期運転に移行した当初の前述の濃縮運転期にこの槽内
に保管されている稀釈された不凍液も同時に濃縮させる
方法をとってもよい。
Also, during winter heat collection operation, antifreeze tends to be diluted, but at the end of winter heat collection operation, let the antifreeze be diluted and store the increased amount in the tank. ,
A method may be adopted in which the diluted antifreeze solution stored in this tank during the above-mentioned concentration operation period at the beginning of summer operation is also concentrated at the same time.

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

図はこの発明の運転方法を実施するヒーティングタワー
兼用クーリングタワー付ヒートポンゾのシステム図であ
る。 符号の説明 1・・・ヒーティングタワー兼用クーリングタワー、2
・・・温水用凝縮器、6・・・ツースター圧縮機、4・
・・冷却水用凝縮器、5・・・主圧縮機、6・・・シラ
イン蒸発器、7・・・冷却水用蒸発器、8・・・槽、7
1.72・・・ポンプ。
The figure is a system diagram of a heat ponzo with a cooling tower that also serves as a heating tower, which implements the operating method of the present invention. Explanation of symbols 1... Cooling tower that also serves as a heating tower, 2
... Hot water condenser, 6... Two Star compressor, 4.
... Cooling water condenser, 5... Main compressor, 6... Siline evaporator, 7... Cooling water evaporator, 8... Tank, 7
1.72...Pump.

Claims (3)

【特許請求の範囲】[Claims] (1)冬期に不凍液を使用して空気から集熱するヒーテ
ィングタワー兼用クーリングタワー付のヒートポンプの
運転方法において、夏期運転への移行の当初の一時期に
この不凍液をそのまゝ冷却水として使用し不凍液の濃縮
を行わせしめ、濃縮した不凍液は槽に回収し、それまで
不凍液が充填されていた系内に真水を注入することによ
り、その後の夏期運転では冷却水として真水を使用する
ことを特徴とするヒーティングタワー兼用クーリングタ
ワー付のヒートポンプの運転方法。
(1) In the operating method of a heat pump equipped with a cooling tower that also serves as a heating tower, which collects heat from the air using antifreeze in the winter, the antifreeze is used directly as cooling water during the initial transition to summer operation. The concentrated antifreeze is collected in a tank, and fresh water is injected into the system that was previously filled with antifreeze, so that the fresh water is used as cooling water during subsequent summer operations. How to operate a heat pump with a cooling tower that also serves as a heating tower.
(2)前記の運転方法において、ヒーティングタワーで
の不凍液濃縮が所定の程度まで進行した事を確認し、濃
縮運転を中止するため、ヒーティングタワー兼クーリン
グタワー部での液位を検知し、警報を発することを特徴
とする特許請求の範囲第1項記載のヒートポンプの運転
方法。
(2) In the above operating method, in order to confirm that the antifreeze concentration in the heating tower has progressed to a predetermined level and stop the concentration operation, the liquid level in the heating tower/cooling tower section is detected and an alarm is issued. The method of operating a heat pump according to claim 1, characterized in that the heat pump generates a heat pump.
(3)前記の運転方法において、ヒーティングタワーで
の不凍液濃縮が所定の程度まで進行した事を確認し、濃
縮運転を中止するため不凍液の濃度を検知し、警報を発
することを特徴とする特許請求の範囲第1項記載のヒー
トポンプの運転方法。
(3) A patent characterized in that in the above operating method, the concentration of antifreeze is detected and an alarm is issued in order to confirm that the concentration of antifreeze in the heating tower has progressed to a predetermined level and to stop the concentration operation. A method for operating a heat pump according to claim 1.
JP1106585A 1985-01-25 1985-01-25 Method of operating heat pump Granted JPS61173058A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1106585A JPS61173058A (en) 1985-01-25 1985-01-25 Method of operating heat pump

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1106585A JPS61173058A (en) 1985-01-25 1985-01-25 Method of operating heat pump

Publications (2)

Publication Number Publication Date
JPS61173058A true JPS61173058A (en) 1986-08-04
JPH0510576B2 JPH0510576B2 (en) 1993-02-10

Family

ID=11767587

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1106585A Granted JPS61173058A (en) 1985-01-25 1985-01-25 Method of operating heat pump

Country Status (1)

Country Link
JP (1) JPS61173058A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6341779A (en) * 1986-08-07 1988-02-23 株式会社荏原製作所 Method of operating heat pump with heating tower
JPS63243660A (en) * 1987-03-30 1988-10-11 株式会社荏原製作所 Heat pump with heating tower
JPS63251757A (en) * 1987-04-07 1988-10-19 株式会社荏原製作所 Operation system of heating tower

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6341779A (en) * 1986-08-07 1988-02-23 株式会社荏原製作所 Method of operating heat pump with heating tower
JPH0451746B2 (en) * 1986-08-07 1992-08-19 Ebara Mfg
JPS63243660A (en) * 1987-03-30 1988-10-11 株式会社荏原製作所 Heat pump with heating tower
JPS63251757A (en) * 1987-04-07 1988-10-19 株式会社荏原製作所 Operation system of heating tower

Also Published As

Publication number Publication date
JPH0510576B2 (en) 1993-02-10

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