JPH05231680A - Operation of heating tower type heat pump - Google Patents

Operation of heating tower type heat pump

Info

Publication number
JPH05231680A
JPH05231680A JP7210991A JP7210991A JPH05231680A JP H05231680 A JPH05231680 A JP H05231680A JP 7210991 A JP7210991 A JP 7210991A JP 7210991 A JP7210991 A JP 7210991A JP H05231680 A JPH05231680 A JP H05231680A
Authority
JP
Japan
Prior art keywords
heat
cooler
heating tower
heat pump
antifreeze
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
JP7210991A
Other languages
Japanese (ja)
Other versions
JPH0772637B2 (en
Inventor
Toshihiko Ito
俊彦 伊東
Takao Kobayashi
隆夫 小林
Rikuo Tamura
陸男 田村
Masami Ishikawa
正美 石川
Masaki Moto
雅樹 元
Sadaichi Mochizuki
貞一 望月
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
Takenaka Komuten Co Ltd
Original Assignee
Ebara Corp
Takenaka Komuten 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 Ebara Corp, Takenaka Komuten Co Ltd filed Critical Ebara Corp
Priority to JP7210991A priority Critical patent/JPH0772637B2/en
Publication of JPH05231680A publication Critical patent/JPH05231680A/en
Publication of JPH0772637B2 publication Critical patent/JPH0772637B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

PURPOSE:To enable condensation of antifreezing fluid even if exterior humidity is high without providing a condensation equipment by a method wherein an antifreezing fluid system of a heating tower is connected to a coolant condenser, and the antifreezing fluid system on a cooler side is circulated between the coolant condenser and a heat exchanger, so that a heat pump makes cooling operation. CONSTITUTION:When antifreezing fluid is diluted, an antifreezing fluid system is divided into one system which circulates through a heating tower 1 and a coolant condenser 3 and the other system which circulates through a cooler 2 and a heat exchanger 7. The heat exchanger 7 heats the anti-freezing fluid, while the cooler 7 cools it. In a heat pump, refrigerant takes heat from the antifreezing fluid at the cooler 2, and is raised in temperature by a compressor, introduced into the coolant condenser 3, whereby the antifreezing fluid is heated, and then returned to the cooler 2. The antifreezing fluid heated by the coolant condenser 3 is introduced into the heating tower to release water for condensation. As a result, the condensation of the antifreezing fluid is realized without providing any condensation equipment.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、ヒーティングタワー方
式ヒートポンプの運転方法に係り、特に暖房運転中の不
凍液濃度を保持するための運転方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an operating method of a heating tower type heat pump, and more particularly to an operating method for maintaining the concentration of antifreeze during heating operation.

【0002】[0002]

【従来の技術】不凍液を使用して、空気から集熱を行う
ヒーティングタワー方式ヒートポンプは、不凍液の濃度
を或る範囲に保つ必要があり、不凍液が希釈されると氷
点が上がり不凍液の効果が無くなって凍結する恐れがあ
る。そのため不凍液希釈時は、従来次に示すような方法
が行われてきた。 (1)濃厚な不凍液を追加し、不凍液を濃縮する。 (2)ヒートポンプ停止時、ヒーティングタワーに不凍
液を通水し、かつヒーティングタワー用ファンを運転す
ることにより、不凍液を濃縮する。(特願昭60−87
226) (3)特別な、不凍液濃縮装置を設置し、不凍液の濃縮
を行う。これらの方法には、それぞれ次のような問題点
がある。 (1)の方法によると、結局不凍液中の氷点降下剤例え
ばエチレングリコールの量が増大し、濃縮限界に近ずき
過濃縮され易くなってしまう。 (2)の方法では、外気湿度が高い場合には濃縮効果が
望めない。 (3)の方法では、不凍液濃縮装置のために機械室スペ
ースを確保しなければならなく、かつ、不凍液濃縮装置
自身高価な物である。 一方、クーラの不凍液系統に不凍液と熱源水とを熱交換
する熱交換器を有するヒーティングタワー方式ヒートポ
ンプは、暖房運転時に、同時に冷房を行う運転方式とし
て知られている。(特願昭62−54169)
2. Description of the Related Art A heating tower type heat pump that collects heat from air using an antifreeze liquid needs to maintain the concentration of the antifreeze liquid within a certain range. When the antifreeze liquid is diluted, the freezing point rises and the effect of the antifreeze liquid is increased. There is a risk that it will disappear and freeze. Therefore, when diluting the antifreeze solution, the following method has been conventionally performed. (1) Add a thick antifreeze solution and concentrate the antifreeze solution. (2) When the heat pump is stopped, the antifreeze liquid is passed through the heating tower and the fan for the heating tower is operated to concentrate the antifreeze liquid. (Japanese Patent Application Sho 60-87
226) (3) Install a special antifreeze concentrator to concentrate the antifreeze. Each of these methods has the following problems. According to the method (1), the amount of the freezing point depressant, for example, ethylene glycol, in the antifreeze liquid eventually increases, and the concentration limit is approached and overconcentration tends to occur. In the method (2), the concentration effect cannot be expected when the outside air humidity is high. In the method (3), the machine room space must be secured for the antifreeze concentrator, and the antifreeze concentrator itself is expensive. On the other hand, a heating tower type heat pump having a heat exchanger for exchanging heat between the antifreezing liquid and the heat source water in the antifreezing liquid system of the cooler is known as an operating system for simultaneously performing cooling during heating operation. (Japanese Patent Application No. 62-54169)

【0003】[0003]

【発明が解決しようとする課題】本発明は、上記の問題
点を解決し、クーラの不凍液系統に不凍液と熱源水とを
熱交換する熱交換器を有するヒーティングタワー方式ヒ
ートポンプにおいて、余分な濃縮設備を設けることな
く、外気湿度が高い場合でも、ヒーティングタワー方式
ヒートポンプを用いて不凍液の濃縮を行うことのできる
運転方法を提供することを目的とする。
DISCLOSURE OF THE INVENTION The present invention solves the above problems and, in a heating tower type heat pump having a heat exchanger for exchanging heat between antifreeze liquid and heat source water in an antifreeze liquid system of a cooler, extra concentration An object of the present invention is to provide an operating method capable of concentrating an antifreeze liquid using a heating tower type heat pump even if the outside air humidity is high without providing equipment.

【0004】[0004]

【課題を解決するための手段】上記目的を達成するため
に、本発明では、クーラの不凍液系統に、不凍液と熱源
水とを熱交換する熱交換器を有し、外気から集排熱を行
うヒーティングタワー方式ヒートポンプの運転方法にお
いて、暖房運転中に不凍液濃度が低下した場合は、暖房
運転を一時中止し、ヒートポンプを冷房サイクルに切り
替え、同時に、ヒーティングタワーの不凍液系統はクー
ラから切離して冷却水コンデンサーに接続し、一方クー
ラー側の不凍液系統は熱交換器との間で循環して、ヒー
トポンプを冷房運転することにより、不凍液を濃縮する
ことを特徴とするヒーティングタワー方式ヒートポンプ
の運転方法としたものである。
To achieve the above object, in the present invention, a heat exchanger for exchanging heat between the antifreeze liquid and the heat source water is provided in the antifreeze liquid system of the cooler to collect and exhaust heat from the outside air. In the operation method of the heating tower heat pump, if the antifreeze concentration decreases during heating operation, the heating operation is temporarily stopped, the heat pump is switched to the cooling cycle, and at the same time, the antifreeze system of the heating tower is disconnected from the cooler and cooled. A heating tower type heat pump operating method characterized in that the antifreeze system is connected to a water condenser, while the antifreeze system on the cooler side circulates between the heat exchanger and the heat pump to perform cooling operation, thereby concentrating the antifreeze solution. It was done.

【0005】上記本発明の運転方法においては、不凍液
の濃縮を外気湿度が高い場合に行っても有効に濃縮で
き、また、濃縮するための冷房運転においては、熱交換
器に通水する熱源水が冷水であるのがよい。
In the operating method of the present invention, the antifreeze can be effectively concentrated even when the outside air humidity is high, and in the cooling operation for concentration, the heat source water to be passed through the heat exchanger. Is preferably cold water.

【0006】[0006]

【作用】本システムにおいて、ヒーティングタワーの不
凍液系統を冷却水コンデンサーに接続し、クーラー側の
不凍液系統を熱交換器との間で循環すようになし、ヒー
トポンプを冷房運転することにより、ヒーティングタワ
ーに於て不凍液は、空気と熱交換すると同時に水分を空
気中に放出し濃縮される。本作用は、空気の湿度が高い
場合でも、不凍液の温度が空気の湿球温度より高いこと
により可能であり、かつ、この場合が本運転方式が最も
有効に作用する。熱源水が冷水の場合には、不凍液を濃
縮すると同時に冷水を製造することが可能になる。
[Operation] In this system, the antifreeze system of the heating tower is connected to the cooling water condenser, the antifreeze system of the cooler side is not circulated with the heat exchanger, and the heat pump is cooled to perform heating. In the tower, the antifreeze liquid exchanges heat with the air and at the same time releases moisture into the air to be concentrated. This action is possible because the temperature of the antifreeze liquid is higher than the wet-bulb temperature of air even when the humidity of the air is high, and in this case, the present operation method works most effectively. When the heat source water is cold water, it becomes possible to concentrate the antifreeze liquid and simultaneously manufacture cold water.

【0007】[0007]

【実施例】以下、本発明の実施例を図面を用いて具体的
に説明するが、本発明はこれらに限定されるものではな
い。 実施例1 図1は本発明に用いるヒーティングタワー方式ヒートポ
ンプの工程図である。図1において、1はヒーティング
タワー兼用クーリングタワー、2はクーラ、3は冷却水
コンデンサ、4は温水コンデンサ、5は主圧縮機、6は
ブースタ圧縮機、7は熱交換器、8はブライン槽、9は
温水槽を示し、10〜13はポンプ、14、15は膨張
弁、16〜25は弁を示す。次にこのヒートポンプを用
いた暖房運転について説明すると、弁16、17を開
き、弁18〜23を閉じ、ポンプ11を稼動させること
により、不凍液はヒーティングタワー1−管30−弁1
6−管31−クーラ2−管32−弁27−管33−ヒー
ティングタワー1のように循環する。そして、ヒーティ
ングタワー1で空気より集熱し、クーラ2で放熱する。
ヒートポンプでは、冷媒がクーラ2で不凍液より熱を取
り、主圧縮機5で圧縮し、作動していない冷却水コンデ
ンサ3を通り、ブースタ圧縮機6でさらに圧縮され昇温
し、温水コンデンサ4で温水42を加熱する。温水42
を加熱した冷媒は管28から膨張弁15により減圧され
て冷却水コンデンサ3を通り、管29、膨張弁14を通
りさらに減圧されてクーラ2に還流される。得られた温
水は温水槽9に貯蔵される。弁24、25はヒーティン
グタワー液面計の信号により開閉し、ヒーティングタワ
ー液面を所定のレベルにコントロールする。この運転で
は冷却水コンデンサ3には冷却水は通水されてなく、ま
た不凍液と熱源水との熱交換器7の系統も弁で切り放さ
れて運転されない。
EXAMPLES Examples of the present invention will be specifically described below with reference to the drawings, but the present invention is not limited thereto. Example 1 FIG. 1 is a process diagram of a heating tower type heat pump used in the present invention. In FIG. 1, 1 is a cooling tower that also serves as a heating tower, 2 is a cooler, 3 is a cooling water condenser, 4 is a hot water condenser, 5 is a main compressor, 6 is a booster compressor, 7 is a heat exchanger, 8 is a brine tank, Reference numeral 9 denotes a hot water tank, 10 to 13 are pumps, 14 and 15 are expansion valves, and 16 to 25 are valves. Next, the heating operation using this heat pump will be described. By opening the valves 16 and 17, closing the valves 18 to 23 and operating the pump 11, the antifreeze liquid is heated tower 1-tube 30-valve 1.
6-tube 31-cooler 2-tube 32-valve 27-tube 33-heating tower 1 Then, the heating tower 1 collects heat from the air, and the cooler 2 radiates heat.
In the heat pump, the refrigerant takes heat from the antifreeze in the cooler 2, compresses it in the main compressor 5, passes through the cooling water condenser 3 that is not operating, is further compressed in the booster compressor 6 and rises in temperature, and warm water in the hot water condenser 4. Heat 42. Hot water 42
The refrigerant that has been heated is decompressed by the expansion valve 15 from the pipe 28, passes through the cooling water condenser 3, passes through the pipe 29 and the expansion valve 14, and is further decompressed, and is returned to the cooler 2. The obtained warm water is stored in the warm water tank 9. The valves 24 and 25 are opened and closed by the signal of the heating tower level gauge to control the heating tower level to a predetermined level. In this operation, the cooling water is not passed through the cooling water condenser 3, and the system of the heat exchanger 7 for the antifreezing liquid and the heat source water is cut off by the valve and is not operated.

【0008】次に、不凍液が希釈された場合の不凍液濃
縮運転について説明する。まず、弁16、17を閉じ
て、不凍液の系統をヒーティングタワー1と冷却水コン
デンサ3とを循環する系統と、クーラ2と熱交換器7と
を循環す系統の2つの系統に分ける。ここで、弁18、
19、20、21、23は開き、ポンプ11、12は稼
動させることにより不凍液は、ヒーティングタワー1−
管30−弁18−管34−冷却水コンデンサ3−管35
−弁19−管33−ヒーティングタワー1を循環する系
統と、管31−クーラ2−管32−弁23−管38−弁
21−管37−熱交換器7−管36−弁20−管31を
循環する系統を形成する。弁22は熱源水出口温度によ
って制御され、熱源水の凍結を防ぐべくブラインの一部
が熱交換器7をバイパスされる。そして、熱交換器7で
は熱源水44により不凍液に熱が与えられ、クーラ2で
は、不凍液より冷媒に熱が与えられる。ヒートポンプで
は、冷媒がクーラ2で不凍液から熱を取り、主圧縮機に
より昇温して、冷却水コンデンサ3に導入され、冷却水
コンデンサ3で不凍液を加熱する。そして冷媒は管29
から膨張弁14を通りクーラ2に循環される。一方冷却
水コンデンサ3で加熱された不凍液は、ヒーティングタ
ワーに導入されて空気中に放熱すると同時に水分を放出
して濃縮される。この時は、ブースタ圧縮機6は停止さ
れ、温水の温水コンデンサ4への通水もポンプ10を停
止することにより中止されている。また、外気湿度を検
出するセンサーを取り付け、コントローラを介して外気
湿度の高い時のみ、上記の不凍液濃縮運転を行うのがよ
い。
Next, the operation of concentrating the antifreeze liquid when the antifreeze liquid is diluted will be described. First, the valves 16 and 17 are closed, and the antifreeze system is divided into two systems: a system that circulates the heating tower 1 and the cooling water condenser 3, and a system that circulates the cooler 2 and the heat exchanger 7. Where the valve 18,
19, 20, 21 and 23 are opened, and the pumps 11 and 12 are operated so that the antifreeze liquid is heated by the heating tower 1-
Pipe 30-valve 18-pipe 34-cooling water condenser 3-pipe 35
-Valve 19-Pipe 33-System for circulating heating tower 1, pipe 31-cooler 2-pipe 32-valve 23-pipe 38-valve 21-pipe 37-heat exchanger 7-pipe 36-valve 20-pipe 31 forms a system that circulates. The valve 22 is controlled by the heat source water outlet temperature, and a part of the brine bypasses the heat exchanger 7 to prevent the heat source water from freezing. Then, in the heat exchanger 7, heat is applied to the antifreeze liquid by the heat source water 44, and in the cooler 2, heat is applied to the refrigerant from the antifreeze liquid. In the heat pump, the refrigerant takes heat from the antifreeze liquid by the cooler 2, the temperature is raised by the main compressor, is introduced into the cooling water condenser 3, and the cooling water condenser 3 heats the antifreezing liquid. And the refrigerant is pipe 29
To the cooler 2 through the expansion valve 14. On the other hand, the antifreeze liquid heated by the cooling water condenser 3 is introduced into the heating tower to radiate heat into the air and at the same time release water to be concentrated. At this time, the booster compressor 6 is stopped, and the water flow to the hot water condenser 4 is also stopped by stopping the pump 10. Further, it is preferable that a sensor for detecting the outside air humidity is attached and the above antifreeze solution concentration operation is performed only when the outside air humidity is high via the controller.

【0009】実施例2 図2は、熱交換器の熱源水として冷水を用い、製造した
冷水を冷水槽に貯蔵する例である。図2においては、熱
交換器の冷水系統を除いてすべて図1と同じであり、ま
た実施例1と同じ暖房運転及び不凍液濃縮運転を行うこ
とができる。ただ、不凍液濃縮運転において、クーラ2
循環系統は熱源水として冷水を用い製造した冷水を冷水
槽59に貯蔵しているものである。その系統はポンプ5
0により冷水を管55、弁51を通って熱交換器7に導
入し、不凍液中に熱を放出してさらに冷却した冷水が弁
52、管56を通って冷水槽に循環されて貯蔵される。
製造された冷水は冷房用として使用できる。また、この
不凍液濃縮運転及び冷房運転において、クーラ2循環系
統は、不凍液に代えて冷水をそのままクーラ2に循環し
て用いることができ、この場合の循環系統は、冷水槽5
9からポンプ50により冷水が管57−弁53−管31
−クーラ2−管32−弁54−管58−冷水槽59と循
環して冷水が製造される。この場合弁16、17、2
0、22、23、51、52は閉じられており、ポンプ
12は停止されている。
Example 2 FIG. 2 shows an example in which cold water is used as the heat source water of the heat exchanger and the manufactured cold water is stored in the cold water tank. 2 is the same as FIG. 1 except for the cold water system of the heat exchanger, and the same heating operation and antifreeze liquid concentration operation as in Example 1 can be performed. However, in the antifreeze concentration operation, the cooler 2
The circulation system stores cold water produced by using cold water as heat source water in the cold water tank 59. The system is pump 5
When 0, cold water is introduced into the heat exchanger 7 through the pipe 55 and the valve 51, and heat is released into the antifreeze to further cool the cold water, which is circulated and stored in the cold water tank through the valve 52 and the pipe 56. ..
The produced cold water can be used for cooling. In the antifreeze concentration operation and the cooling operation, the cooler 2 circulation system can circulate the cold water as it is into the cooler 2 instead of the antifreeze liquid, and the circulation system in this case is the cold water tank 5
The cold water is pumped from 9 by the pump 50 to the pipe 57-valve 53-pipe 31.
-Cooler 2-pipe 32-valve 54-pipe 58-cold water tank 59 is circulated to produce cold water. In this case valves 16, 17, 2
0, 22, 23, 51, 52 are closed and the pump 12 is stopped.

【0010】[0010]

【発明の効果】本発明の運転方法によれば、濃厚な不凍
液を追加することによる氷点降下剤の増大による過濃縮
傾向の発生が防止され、空気湿度が高い場合でも効果的
に不凍液の濃縮が行われ、特別な不凍液濃縮装置を設置
することなく、ヒーティングタワー方式ヒートポンプそ
のものを用いることにより濃縮を行うことが出来る。
又、濃縮と同時に冷水を製造することも可能であり、多
機能な運転方法として構成されている。
According to the operation method of the present invention, the tendency of overconcentration due to the increase of the freezing point depressant due to the addition of the thick antifreeze liquid is prevented, and the antifreeze liquid can be effectively concentrated even when the air humidity is high. The heating tower type heat pump itself can be used for concentration without installing a special antifreeze concentration device.
It is also possible to produce cold water at the same time as concentrating, which is configured as a multifunctional operation method.

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

【図1】本発明の運転方法に用いるヒーティングタワー
方式ヒートポンプの一例を示す工程図である。
FIG. 1 is a process diagram showing an example of a heating tower type heat pump used in an operating method of the present invention.

【図2】本発明の運転方法に用いるヒーティングタワー
方式ヒートポンプの他の例を示す工程図である。
FIG. 2 is a process diagram showing another example of the heating tower type heat pump used in the operating method of the present invention.

【符号の説明】[Explanation of symbols]

1:ヒーティングタワー、2:クーラ、3:冷却水コン
デンサ、4:温水コンデンサ、5:主圧縮機、6:ブー
スタ圧縮機、7:熱交換器、8:ブライン槽、9:温水
槽、10〜13、50:ポンプ、14、15:膨張弁、
16〜25、52〜54:弁、26〜29:冷媒配管、
30〜41:不凍液配管、42、43:温水配管、4
4:熱源水配管、45:外気湿度センサー、46:コン
トローラ、55〜58:冷水配管、59:冷水槽。
1: Heating tower, 2: Cooler, 3: Cooling water condenser, 4: Hot water condenser, 5: Main compressor, 6: Booster compressor, 7: Heat exchanger, 8: Brine tank, 9: Hot water tank, 10 ~ 13, 50: pump, 14, 15: expansion valve,
16-25, 52-54: valve, 26-29: refrigerant pipe,
30-41: antifreeze pipe, 42, 43: hot water pipe, 4
4: Heat source water piping, 45: Outside air humidity sensor, 46: Controller, 55-58: Cold water piping, 59: Cold water tank.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 田村 陸男 東京都大田区羽田旭町11番1号 株式会社 荏原製作所内 (72)発明者 石川 正美 東京都大田区羽田旭町11番1号 株式会社 荏原製作所内 (72)発明者 元 雅樹 東京都大田区羽田旭町11番1号 株式会社 荏原製作所内 (72)発明者 望月 貞一 東京都大田区羽田旭町11番1号 株式会社 荏原製作所内 ─────────────────────────────────────────────────── ─── Continued front page (72) Inventor Rikuo Tamura 11-1 Haneda Asahi-cho, Ota-ku, Tokyo Ebara Corporation (72) Inventor Masami Ishikawa 11-11 Haneda-asaka-cho, Ota-ku, Tokyo Inside the EBARA MFG. (72) Inventor Masaki 11-11 Haneda Asahi-cho, Ota-ku, Tokyo Inside the EBARA CORPORATION (72) Inventor Teiichi Mochizuki 11-1 Haneda-Asahi-cho, Ota-ku, Tokyo Inside the EBARA CORPORATION

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 クーラの不凍液系統に、不凍液と熱源水
とを熱交換する熱交換器を有し、外気から集排熱を行う
ヒーティングタワー方式ヒートポンプの運転方法におい
て、暖房運転中に不凍液濃度が低下した場合は、暖房運
転を一時中止し、ヒートポンプを冷房サイクルに切り替
え、同時に、ヒーティングタワーの不凍液系統はクーラ
から切離して冷却水コンデンサーに接続し、一方クーラ
ー側の不凍液系統は熱交換器との間で循環して、ヒート
ポンプを冷房運転することにより、不凍液を濃縮するこ
とを特徴とするヒーティングタワー方式ヒートポンプの
運転方法。
1. A method of operating a heating tower type heat pump that has a heat exchanger for exchanging heat between antifreeze liquid and heat source water in an antifreeze liquid system of a cooler, and collects and exhausts heat from outside air. If the temperature drops, the heating operation is temporarily stopped and the heat pump is switched to the cooling cycle.At the same time, the antifreeze system of the heating tower is disconnected from the cooler and connected to the cooling water condenser, while the antifreeze system on the cooler side is the heat exchanger. A method for operating a heating tower heat pump, characterized in that the antifreeze liquid is concentrated by circulating the heat pump to perform cooling operation of the heat pump.
【請求項2】 前記不凍液の濃縮は、外気湿度が高い場
合に行うことを特徴とする請求項1記載のヒーティング
タワー方式ヒートポンプの運転方法。
2. The method of operating a heating tower heat pump according to claim 1, wherein the concentration of the antifreeze liquid is performed when the outside air humidity is high.
【請求項3】 前記冷房運転においては、熱交換器に通
水する熱源水が冷水であることを特徴とする請求項1記
載のヒーティングタワー方式ヒートポンプの運転方法。
3. The method of operating a heating tower heat pump according to claim 1, wherein in the cooling operation, the heat source water passing through the heat exchanger is cold water.
JP7210991A 1991-03-13 1991-03-13 Operating method of heating tower type heat pump Expired - Fee Related JPH0772637B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7210991A JPH0772637B2 (en) 1991-03-13 1991-03-13 Operating method of heating tower type heat pump

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7210991A JPH0772637B2 (en) 1991-03-13 1991-03-13 Operating method of heating tower type heat pump

Publications (2)

Publication Number Publication Date
JPH05231680A true JPH05231680A (en) 1993-09-07
JPH0772637B2 JPH0772637B2 (en) 1995-08-02

Family

ID=13479890

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7210991A Expired - Fee Related JPH0772637B2 (en) 1991-03-13 1991-03-13 Operating method of heating tower type heat pump

Country Status (1)

Country Link
JP (1) JPH0772637B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009529652A (en) * 2006-03-10 2009-08-20 ヌトソス、ミカエル Method and arrangement for optimizing heat transfer characteristics in a heat exchange ventilation system

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009529652A (en) * 2006-03-10 2009-08-20 ヌトソス、ミカエル Method and arrangement for optimizing heat transfer characteristics in a heat exchange ventilation system
US8464783B2 (en) 2006-03-10 2013-06-18 Mikael Nutsos Method and arrangement for optimizing heat transfer properties in heat exchange ventilation systems

Also Published As

Publication number Publication date
JPH0772637B2 (en) 1995-08-02

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