JPH10213358A - Cooling operation method of absorption refrigerating machine - Google Patents
Cooling operation method of absorption refrigerating machineInfo
- Publication number
- JPH10213358A JPH10213358A JP9031091A JP3109197A JPH10213358A JP H10213358 A JPH10213358 A JP H10213358A JP 9031091 A JP9031091 A JP 9031091A JP 3109197 A JP3109197 A JP 3109197A JP H10213358 A JPH10213358 A JP H10213358A
- Authority
- JP
- Japan
- Prior art keywords
- cooling water
- cooling
- temperature
- pump
- refrigerant
- 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
Links
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A30/00—Adapting or protecting infrastructure or their operation
- Y02A30/27—Relating to heating, ventilation or air conditioning [HVAC] technologies
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
- Y02B30/62—Absorption based systems
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
- Y02B30/70—Efficient control or regulation technologies, e.g. for control of refrigerant flow, motor or heating
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は吸収冷凍機が冷却水
温度の低下する冬期等に冷房運転を行う場合の運転方法
に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method of operating an absorption refrigerator for cooling operation in winter or the like when the temperature of cooling water decreases.
【0002】[0002]
【従来の技術】図3は従来のこの種の吸収冷凍機の構成
を示す図である。図示するように、吸収冷凍機は蒸発器
1、吸収器2、再生器3、凝縮器4、冷却塔23を具備
している。再生器3と吸収器2は溶液配管12で連絡さ
れ、吸収器2と再生器3は溶液ポンプ10を介して溶液
配管11で連絡されている。再生器3と凝縮器4は冷媒
配管13で連絡され、凝縮器4と蒸発器1は冷媒配管1
4で連絡され、蒸発器1と吸収器2は冷媒配管17で連
絡され吸収サイクルを形成している。2. Description of the Related Art FIG. 3 is a diagram showing the structure of a conventional absorption refrigerator of this type. As shown, the absorption refrigerator includes an evaporator 1, an absorber 2, a regenerator 3, a condenser 4, and a cooling tower 23. The regenerator 3 and the absorber 2 are connected by a solution pipe 12, and the absorber 2 and the regenerator 3 are connected by a solution pipe 11 via a solution pump 10. The regenerator 3 and the condenser 4 are connected by a refrigerant pipe 13, and the condenser 4 and the evaporator 1 are connected by the refrigerant pipe 1.
4, the evaporator 1 and the absorber 2 are connected by a refrigerant pipe 17 to form an absorption cycle.
【0003】吸収器2、凝縮器4及び冷却塔23は冷却
水配管6で連絡され、冷却水ポンプ5で冷却塔23に冷
却水を循環させるようになっている。また、7は冷媒ポ
ンプで蒸発器1の冷媒を循環させるものであり、8は加
熱弁で再生器3に加熱配管9を通して入熱される熱流量
を制御するものである。21は冷水ポンプで冷水配管2
0を通して負荷側(空調機24)と蒸発器1の間に冷水
を循環させるものである。19は制御機器で冷水温度セ
ンサ18の出力を受け加熱弁8及び冷媒ポンプ7を制御
する。[0003] The absorber 2, condenser 4 and cooling tower 23 are connected by a cooling water pipe 6, and a cooling water pump 5 circulates cooling water to the cooling tower 23. Reference numeral 7 denotes a refrigerant pump for circulating the refrigerant in the evaporator 1, and reference numeral 8 denotes a heating valve for controlling a heat flow rate of heat input to the regenerator 3 through the heating pipe 9. 21 is a chilled water pump and a chilled water pipe 2
0 circulates cold water between the load side (air conditioner 24) and the evaporator 1. Reference numeral 19 denotes a control device which receives the output of the cold water temperature sensor 18 and controls the heating valve 8 and the refrigerant pump 7.
【0004】上記従来構成の吸収冷凍機において、冷房
運転では、冷却水入口温度が例えば15℃以下の低温の
状態で起動すると、吸収溶液濃度が低く、溶液温度が過
度に低下するため、吸収器2における吸収能力が過大と
なっていた。In the above-described absorption refrigerator of the conventional construction, in the cooling operation, if the cooling water inlet temperature is started at a low temperature of, for example, 15 ° C. or less, the absorption solution concentration is low and the solution temperature is excessively lowered. 2, the absorption capacity was excessive.
【0005】[0005]
【発明が解決しようとする課題】上記のように、吸収能
力が過大となるため蒸発器1側に冷媒をスプレーする冷
媒ポンプ7を有する吸収冷凍機では、蒸発器1側の冷媒
液が吸収器2に過大に吸収されるため、冷媒液不足が生
じポンプのキャビテーション運転でポンプ故障が発生
し、また冷凍能力が過大となり、冷水負荷が少ないと急
激な冷水温度低下による凍結事故が発生するという問題
があった。As described above, in the absorption refrigerator having the refrigerant pump 7 for spraying the refrigerant to the evaporator 1 side because the absorption capacity becomes excessive, the refrigerant liquid on the evaporator 1 side absorbs the refrigerant liquid. 2 is excessively absorbed, causing a shortage of the refrigerant liquid, causing a pump failure during cavitation operation of the pump, and an excessively high refrigeration capacity. If the chilled water load is small, a freezing accident due to a sharp drop in chilled water temperature occurs. was there.
【0006】本発明は上述の点に鑑みてなされたもの
で、冷却水ポンプの循環水量を設定制御温度と実際の冷
却水出口温度の偏差に応じて設定温度になるように制御
することにより、冬期等に該冷却水温度が過度に低下し
たときでも安定した冷房運転をすることができる吸収冷
凍機の冷房運転方法を提供することを目的とする。SUMMARY OF THE INVENTION The present invention has been made in view of the above points, and controls the amount of circulating water of a cooling water pump to a set temperature in accordance with a deviation between a set control temperature and an actual cooling water outlet temperature. An object of the present invention is to provide a cooling operation method of an absorption refrigerator capable of performing a stable cooling operation even when the temperature of the cooling water is excessively lowered in winter or the like.
【0007】[0007]
【課題を解決するための手段】上記課題を解決するため
に請求項1に記載の発明は、再生器、吸収器、蒸発器、
凝縮器及びそれらを連絡する溶液通路、冷媒通路を有し
吸収サイクルを形成すると共に、吸収器と凝縮器と冷却
塔を連絡する冷却水配管を有し冷却水ポンプで冷却水を
循環させるように構成し、蒸発器の冷媒循環用の冷媒ポ
ンプ、再生器に入熱する熱量を制御するための加熱弁、
蒸発器と負荷側を連絡する冷温水配管に設けた冷水ポン
プ、冷却水ポンプを制御して冷却水循環量を制御する制
御機器を具備する吸収冷凍機の冷房運転方法において、
冷却水の凝縮器出口温度及び吸収器入口温度を検知する
冷却水出入口温度センサを設け、吸収冷凍機の起動時に
冷却水の吸収器入口温度が低いときは、冷媒ポンプの運
転を遅らせるようにし、冷却水配管を通る冷却水の循環
水量を設定制御温度と実際の冷却水出口温度の偏差に応
じて設定温度になるように制御することを特徴とする。Means for Solving the Problems In order to solve the above problems, the invention according to claim 1 comprises a regenerator, an absorber, an evaporator,
A cooling water pipe connecting the condenser, the condenser, and the cooling tower is formed while having a condenser, a solution passage connecting the liquid passage and a refrigerant passage, and a cooling water pump. A refrigerant pump for circulating refrigerant in the evaporator, a heating valve for controlling the amount of heat input to the regenerator,
In a cooling operation method of an absorption refrigerator including a control device for controlling a cooling water circulation amount by controlling a cooling water pump provided in a cooling / heating water pipe communicating an evaporator and a load side,
A cooling water inlet / outlet temperature sensor for detecting the cooling water condenser outlet temperature and the absorber inlet temperature is provided, and when the cooling water absorber inlet temperature is low at the time of starting the absorption refrigerator, the operation of the refrigerant pump is delayed, It is characterized in that the circulating water amount of the cooling water passing through the cooling water pipe is controlled so as to reach the set temperature in accordance with a deviation between the set control temperature and the actual cooling water outlet temperature.
【0008】また、請求項2に記載の発明は請求項1に
記載の吸収冷凍機の冷房運転方法において、冷却水の循
環量制御を前記冷却水配管に設けた通水量制御弁で行う
ことを特徴とする。According to a second aspect of the present invention, in the cooling operation method of the absorption chiller according to the first aspect, the circulation amount control of the cooling water is performed by a flow rate control valve provided in the cooling water pipe. Features.
【0009】また、請求項3に記載の発明は請求項1に
記載の吸収冷凍機の冷房運転方法において、冷却水の循
環量制御を前記冷却水ポンプの回転数制御で行うことを
特徴とする。According to a third aspect of the present invention, in the cooling operation method of the absorption refrigerator according to the first aspect, the cooling water circulation amount is controlled by controlling the rotation speed of the cooling water pump. .
【0010】[0010]
【発明の実施の形態】以下、本発明の実施の形態例を図
面に基づいて説明する。図1は本発明に係る冷房運転方
法を実施する吸収冷凍機の構成例を示す図である。同図
において、図3と同一符号を付した部分は同一又は相当
部分を示す。本吸収冷凍機は、蒸発器1、吸収器2、再
生器3、凝縮器4を具備し、これらを溶液配管11、1
2及び冷媒配管13,14,17で連結し吸収サイクル
を形成している。Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 is a diagram illustrating a configuration example of an absorption refrigerator that performs a cooling operation method according to the present invention. In the figure, the portions denoted by the same reference numerals as those in FIG. 3 indicate the same or corresponding portions. The absorption refrigerator includes an evaporator 1, an absorber 2, a regenerator 3, and a condenser 4, and these are connected to a solution pipe 11,
2 and the refrigerant pipes 13, 14, 17 to form an absorption cycle.
【0011】また、冷却水ポンプ5で冷却水配管6を介
して、冷却水を吸収器2、凝縮器4、冷却塔23と循環
させるようになっている。また、蒸発器1の冷媒循環用
の冷媒ポンプ7、再生器3の熱量を制御するための加熱
弁8および負荷側の冷水配管20に設けた冷水ポンプ2
1を具備し、冷却水の出口温度を検出する冷却水出口温
度センサ15、冷却水の入口温度を検出する冷却水入口
温度センサ25、その出力信号を受けて冷却水通水量制
御弁16及び冷却水ポンプを制御する冷却水通水量制御
機器22を設けることにより、本発明の冷房運転方法を
実施する。The cooling water is circulated by the cooling water pump 5 through the cooling water pipe 6 to the absorber 2, the condenser 4, and the cooling tower 23. Further, a refrigerant pump 7 for circulating the refrigerant of the evaporator 1, a heating valve 8 for controlling the amount of heat of the regenerator 3, and a chilled water pump 2 provided in the chilled water pipe 20 on the load side.
1, a cooling water outlet temperature sensor 15 for detecting a cooling water outlet temperature, a cooling water inlet temperature sensor 25 for detecting a cooling water inlet temperature, a cooling water flow rate control valve 16 receiving an output signal thereof, and a cooling The cooling operation method of the present invention is implemented by providing the cooling water flow control device 22 for controlling the water pump.
【0012】図2は本発明に係る運転方法のフローを示
す図である。吸収冷凍機の冷房運転は運転指令により
(ステップST1)、冷水ポンプ21を起動し(ステッ
プST2)、続いて冷却水ポンプ5を起動する(ステッ
プST3)。この該冷水ポンプ5の起動後、冷却水通水
量制御機器22は予め設定された設定温度と冷却水出口
(凝縮器4の冷却水出口部)に設けられた冷却水出口温
度センサ15で検出した冷却水出口温度との偏差から、
冷却水ポンプ5のインバータ(図示せず)又は冷却水通
水量制御弁16を制御し、冷却水出口温度が該設定温度
(例えば30℃)になるように冷却水ポンプ5の回転数
又は冷却水通水量制御弁16の開度を制御して冷却水通
水量を制御する(ステップST4、ST5)。FIG. 2 is a diagram showing a flow of an operation method according to the present invention. The cooling operation of the absorption chiller starts the chilled water pump 21 (Step ST2) and then starts the chilled water pump 5 (Step ST3) according to an operation command (Step ST1). After the start of the chilled water pump 5, the cooling water flow rate control device 22 detects a preset temperature and a cooling water outlet temperature sensor 15 provided at a cooling water outlet (a cooling water outlet of the condenser 4). From the deviation from the cooling water outlet temperature,
The inverter (not shown) of the cooling water pump 5 or the cooling water flow control valve 16 is controlled so that the cooling water outlet temperature becomes the set temperature (for example, 30 ° C.). The cooling water flow rate is controlled by controlling the opening of the flow rate control valve 16 (steps ST4 and ST5).
【0013】続いて加熱弁8及び加熱配管9を通して再
生器3に加熱流体を供給する加熱源、例えば燃焼器の燃
焼を開始する(ステップST6)。続いて、前記冷却水
出口温度が設定温度(例えば15℃)以上であるか否か
を判断し(ステップST7)、設定温度以上であれば冷
媒ポンプ7を運転(通常運転)し(ステップST8)、
設定温度以下であれば冷媒ポンプ7の運転を停止する
(ステップST9)。Subsequently, the combustion of a heating source, such as a combustor, for supplying a heating fluid to the regenerator 3 through the heating valve 8 and the heating pipe 9 is started (step ST6). Subsequently, it is determined whether or not the cooling water outlet temperature is equal to or higher than a set temperature (for example, 15 ° C.) (step ST7). If the temperature is equal to or higher than the set temperature, the refrigerant pump 7 is operated (normal operation) (step ST8). ,
If the temperature is equal to or lower than the set temperature, the operation of the refrigerant pump 7 is stopped (step ST9).
【0014】例えば、図2のステップST4において、
起動時の冷却水出口温度が10℃であると、冷却水通水
量は冷却水ポンプ5が許容する最低流量に制御されて運
転される。また、ステップST8、ST9のように、冷
却水出口温度が設定温度以下である場合は冷媒ポンプ7
を運転しない。このため、蒸発器1における起動時の冷
媒液不足による冷媒ポンプ7のキャビテーション運転は
回避できる。また、冷却水通水量を設定温度との偏差の
度合いにより制御するため、吸収器2の過度な吸収能力
発生を防ぎ、蒸発器1側の冷媒や冷水の凍結の危険を回
避できる。For example, in step ST4 of FIG.
If the cooling water outlet temperature at the time of startup is 10 ° C., the cooling water flow rate is controlled to the minimum flow rate allowed by the cooling water pump 5 to operate. When the cooling water outlet temperature is equal to or lower than the set temperature as in steps ST8 and ST9, the refrigerant pump 7
Do not drive. For this reason, the cavitation operation of the refrigerant pump 7 due to the shortage of the refrigerant liquid at the time of starting the evaporator 1 can be avoided. Further, since the cooling water flow rate is controlled based on the degree of deviation from the set temperature, excessive absorption capacity generation of the absorber 2 can be prevented, and the danger of freezing of the refrigerant and cold water on the evaporator 1 side can be avoided.
【0015】再生器3における加熱熱量は負荷対応の
他、吸収溶液の濃縮と冷却水への放熱に使用されるが冷
却塔23では冷却水通水量が少ないため放熱は抑制され
る。このことにより、徐々に蒸発器1内の冷媒量が濃縮
により増加し、冷却水系の温度も冷却水への放熱により
上昇する。冷却水入口温度が所定温度(本例では15
℃)に達すると、冷媒ポンプ7の吸い込み液面は許容N
PSH以上になり、該冷媒ポンプ7はキャビテーション
無しに運転ができる。冷却水通水量は冷却水設定温度
(本例では30℃)と冷却水出口温度センサ15の温度
との偏差に逆比例するように加熱弁8の開度を制御し、
冷却水出口温度が設定温度になると冷却水通水量は最大
となり、通常運転となる。The amount of heating heat in the regenerator 3 is used not only for the load but also for the concentration of the absorbing solution and the heat radiation to the cooling water. As a result, the amount of refrigerant in the evaporator 1 gradually increases due to concentration, and the temperature of the cooling water system also rises due to heat radiation to the cooling water. The cooling water inlet temperature is a predetermined temperature (15 in this example).
℃), the suction liquid level of the refrigerant pump 7 becomes the allowable N
PSH or more, and the refrigerant pump 7 can be operated without cavitation. The opening of the heating valve 8 is controlled so that the cooling water flow rate is inversely proportional to the deviation between the cooling water set temperature (30 ° C. in this example) and the temperature of the cooling water outlet temperature sensor 15,
When the cooling water outlet temperature reaches the set temperature, the cooling water flow rate becomes the maximum, and the normal operation is performed.
【0016】冷却水通水量制御は冷却水ポンプ5の許容
できる範囲で行い、冷却水循環系に設けた冷却水通水量
制御弁16によることもでき、ポンプ回転数の制御によ
ることでもよい。また、冷媒ポンプ7の起動条件は、上
述の例では冷却水所定温度によって行ったが、蒸発器1
の下部(冷媒ポンプの液吸い込み部)の液面にレベルセ
ンサを設け、このレベルで許容NPSH以上を感知しポ
ンプを起動するようにしてもよい。The control of the cooling water flow rate is performed within an allowable range of the cooling water pump 5, and may be performed by a cooling water flow control valve 16 provided in the cooling water circulation system, or by controlling the pump rotation speed. In addition, the starting condition of the refrigerant pump 7 is set at the predetermined temperature of the cooling water in the above-described example.
May be provided with a level sensor at the liquid level below (the liquid suction part of the refrigerant pump), and at this level, the pump is started upon sensing an allowable NPSH or more.
【0017】冷却水の制御設定温度は、運転サイクル濃
度特性、吸収溶液充填量、冷媒の充填量により適正値は
異なるので、本例の値を初期値として実際の運転環境に
応じて設定すればより安定した制御運転が可能である。Since the proper value of the control temperature of the cooling water differs depending on the operating cycle concentration characteristics, the amount of the absorbing solution and the amount of the refrigerant, the value of this embodiment is set as an initial value according to the actual operating environment. More stable control operation is possible.
【0018】[0018]
【発明の効果】以上説明したように本発明によれば、吸
収冷凍機の起動時に冷却水の吸収器入口温度が低いとき
は、冷媒ポンプの運転を遅らせるようにし、冷却水配管
を通る冷却水の循環水量を設定制御温度と実際の冷却水
出口温度の偏差に応じて設定温度になるように制御する
ので、蒸発器側に冷媒スプレー用の冷媒ポンプを有する
吸収冷凍機において冬期冷房運転を行った場合に蒸発器
側の冷媒液が吸収器に過大に吸収される為、液不足が生
じポンプのキャビテーション運転によるポンプの故障
や、冷凍能力が過大となり急激な冷水温度低下により発
生する凍結事故を防ぐことができ、冬期等に冷却水温度
が過度に低下した場合でも、安定した冷房運転が可能と
なるという優れた効果が得られる。As described above, according to the present invention, when the temperature of the inlet of the cooling water is low when the absorption chiller is started, the operation of the refrigerant pump is delayed so that the cooling water passing through the cooling water pipe is cooled. Is controlled so as to reach the set temperature in accordance with the deviation between the set control temperature and the actual cooling water outlet temperature, so that the winter cooling operation is performed in the absorption refrigerator having a refrigerant pump for refrigerant spray on the evaporator side. In this case, the refrigerant liquid on the evaporator side is excessively absorbed by the absorber, causing a shortage of liquid and causing a failure of the pump due to cavitation operation of the pump or a freezing accident caused by a sudden decrease in chilled water temperature due to excessive refrigeration capacity. Thus, even when the temperature of the cooling water is excessively lowered in winter or the like, an excellent effect that stable cooling operation can be performed is obtained.
【図1】本発明に係る吸収冷凍機の構成例を示す図であ
る。FIG. 1 is a diagram showing a configuration example of an absorption refrigerator according to the present invention.
【図2】本発明に係る運転方法のフローを示す図であ
る。FIG. 2 is a diagram showing a flow of an operation method according to the present invention.
【図3】従来の吸収冷凍機の構成例を示す図である。FIG. 3 is a diagram showing a configuration example of a conventional absorption refrigerator.
1 蒸発器 2 吸収器 3 再生器 4 凝縮器 5 冷却水ポンプ 6 冷却水配管 7 冷媒ポンプ 8 加熱弁 9 加熱配管 10 溶液ポンプ 11 溶液配管 12 溶液配管 13 冷媒配管 14 冷媒配管 15 冷却水出口温度センサ 16 冷却水通水量制御弁 17 冷媒配管 18 冷水温度センサ 19 制御機器 20 冷水配管 21 冷水ポンプ 22 冷却水通水量制御機器 23 冷却塔 24 空調機 25 冷却水入口温度センサ Reference Signs List 1 evaporator 2 absorber 3 regenerator 4 condenser 5 cooling water pump 6 cooling water pipe 7 refrigerant pump 8 heating valve 9 heating pipe 10 solution pump 11 solution pipe 12 solution pipe 13 refrigerant pipe 14 refrigerant pipe 15 cooling water outlet temperature sensor 16 Cooling water flow control valve 17 Refrigerant piping 18 Cold water temperature sensor 19 Control device 20 Cold water piping 21 Cold water pump 22 Cooling water flow control device 23 Cooling tower 24 Air conditioner 25 Cooling water inlet temperature sensor
───────────────────────────────────────────────────── フロントページの続き (72)発明者 遠藤 哲也 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 on the front page (72) Inventor Tetsuya Endo 11-1 Haneda Asahimachi, Ota-ku, Tokyo Inside Ebara Corporation
Claims (3)
れらを連絡する溶液通路、冷媒通路を有し吸収サイクル
を形成すると共に、前記吸収器と前記凝縮器と冷却塔を
連絡する冷却水配管を有し冷却水ポンプで冷却水を循環
させるように構成し、前記蒸発器の冷媒循環用の冷媒ポ
ンプ、前記再生器に入熱する熱量を制御するための加熱
弁、前記蒸発器と負荷側を連絡する冷温水配管に設けた
冷水ポンプ、前記冷却水ポンプを制御して冷却水循環量
を制御する制御機器を具備する吸収冷凍機の冷房運転方
法において、 前記冷却水の前記凝縮器出口温度及び吸収器入口温度を
検知する冷却水出入口温度センサを設け、 前記吸収冷凍機の起動時に冷却水の吸収器入口温度が低
いときは、前記冷媒ポンプの運転を遅らせるようにし、
前記冷却水配管を通る冷却水の循環水量を設定制御温度
と実際の冷却水出口温度の偏差に応じて設定温度になる
ように制御することを特徴とする吸収冷凍機の運転方
法。1. A cooling system comprising a regenerator, an absorber, an evaporator, a condenser and a solution passage and a refrigerant passage communicating therewith to form an absorption cycle and connecting the absorber, the condenser and a cooling tower. It is configured to circulate cooling water with a cooling water pump having a water pipe, a refrigerant pump for circulating refrigerant of the evaporator, a heating valve for controlling the amount of heat input to the regenerator, the evaporator and A cooling operation method for an absorption refrigerator including a chilled water pump provided in a chilled / hot water pipe connecting a load side, and a control device for controlling the chilled water pump to control a circulating amount of the chilled water. A cooling water inlet / outlet temperature sensor for detecting the temperature and the absorber inlet temperature is provided, and when the cooling water absorber inlet temperature is low at the time of starting the absorption refrigerator, the operation of the refrigerant pump is delayed,
An operation method of an absorption refrigerator, wherein the amount of circulating water of cooling water passing through the cooling water pipe is controlled so as to reach a set temperature in accordance with a deviation between a set control temperature and an actual cooling water outlet temperature.
管に設けた通水量制御弁で行うことを特徴とする請求項
1に記載の運転方法。2. The operation method according to claim 1, wherein the circulation amount of the cooling water is controlled by a water flow control valve provided in the cooling water pipe.
ンプの回転数制御で行うことを特徴とする請求項1に記
載の運転方法。3. The operation method according to claim 1, wherein the circulation amount control of the cooling water is performed by controlling a rotation speed of the cooling water pump.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP03109197A JP3227531B2 (en) | 1997-01-30 | 1997-01-30 | Cooling operation method of absorption refrigerator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP03109197A JP3227531B2 (en) | 1997-01-30 | 1997-01-30 | Cooling operation method of absorption refrigerator |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH10213358A true JPH10213358A (en) | 1998-08-11 |
JP3227531B2 JP3227531B2 (en) | 2001-11-12 |
Family
ID=12321741
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP03109197A Expired - Lifetime JP3227531B2 (en) | 1997-01-30 | 1997-01-30 | Cooling operation method of absorption refrigerator |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3227531B2 (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006138614A (en) * | 2004-10-13 | 2006-06-01 | Ebara Corp | Absorbing type heat pump |
JP2014190679A (en) * | 2013-03-28 | 2014-10-06 | Ebara Refrigeration Equipment & Systems Co Ltd | Absorption refrigerator |
JP2015183967A (en) * | 2014-03-25 | 2015-10-22 | 荏原冷熱システム株式会社 | absorption heat pump |
JP2019522162A (en) * | 2016-05-11 | 2019-08-08 | ストーン・マウンテン・テクノロジーズ,インコーポレーテッド | Sorption heat pump and control method |
-
1997
- 1997-01-30 JP JP03109197A patent/JP3227531B2/en not_active Expired - Lifetime
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006138614A (en) * | 2004-10-13 | 2006-06-01 | Ebara Corp | Absorbing type heat pump |
JP4588425B2 (en) * | 2004-10-13 | 2010-12-01 | 株式会社荏原製作所 | Absorption heat pump |
JP2014190679A (en) * | 2013-03-28 | 2014-10-06 | Ebara Refrigeration Equipment & Systems Co Ltd | Absorption refrigerator |
JP2015183967A (en) * | 2014-03-25 | 2015-10-22 | 荏原冷熱システム株式会社 | absorption heat pump |
JP2019522162A (en) * | 2016-05-11 | 2019-08-08 | ストーン・マウンテン・テクノロジーズ,インコーポレーテッド | Sorption heat pump and control method |
Also Published As
Publication number | Publication date |
---|---|
JP3227531B2 (en) | 2001-11-12 |
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