JP3460915B2 - Absorption refrigeration equipment - Google Patents
Absorption refrigeration equipmentInfo
- Publication number
- JP3460915B2 JP3460915B2 JP29986396A JP29986396A JP3460915B2 JP 3460915 B2 JP3460915 B2 JP 3460915B2 JP 29986396 A JP29986396 A JP 29986396A JP 29986396 A JP29986396 A JP 29986396A JP 3460915 B2 JP3460915 B2 JP 3460915B2
- Authority
- JP
- Japan
- Prior art keywords
- cooling water
- temperature
- cooling
- circulation path
- 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 - Fee Related
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B29/00—Combined heating and refrigeration systems, e.g. operating alternately or simultaneously
- F25B29/006—Combined heating and refrigeration systems, e.g. operating alternately or simultaneously of the sorption type system
-
- 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
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Description
【0001】[0001]
【発明の属する技術分野】本発明は、吸収冷凍装置に係
り、特に吸収器及び凝縮器に供給する冷却水を冷却塔で
冷却して循環する吸収冷凍装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an absorption refrigeration system, and more particularly to an absorption refrigeration system in which cooling water supplied to an absorber and a condenser is cooled by a cooling tower and circulated.
【0002】[0002]
【従来の技術】従来、吸収冷温水機の冷房運転停止の
際、通常、溶液のサイクル内の濃度を平均化させ、場合
によっては、蒸発器の冷媒液を溶液サイクル側に戻し
て、サイクル濃度を平均化させ、冷温水機停止中の溶液
の結晶を防止している(通常、この操作を希釈サイクル
と称する)。この希釈サイクル中、ポンプ消費電力低減
のため、なるべく速く、冷却水ポンプを停止したいとい
う要求がある。しかし、速く止め過ぎると、溶液温度が
高く、この溶液が吸収器伝熱管に散布されるため、吸収
器伝熱管内の冷却水温度が上昇する。また、冷温水同時
取出しの吸収式冷温水装置で、冷水負荷が無く、冷却水
ポンプを停止し、冷却水の流れを停止する場合、吸収冷
温水機は溶液を循環して運転状態にあるので、吸収器伝
熱管内の冷却水温度が上昇する。このような場合、吸収
器伝熱管内の冷却水温度は高温であるので、そのまま、
冷却塔の充填材(プラスチック製)に散布されると、充
填材が変形してしまうという恐れがあった。2. Description of the Related Art Conventionally, when the cooling operation of an absorption chiller-heater is stopped, the concentration of the solution in the cycle is usually averaged, and in some cases, the refrigerant liquid in the evaporator is returned to the solution cycle side to obtain the cycle concentration. Are averaged to prevent crystallization of the solution while the cold water heater is stopped (this operation is usually called a dilution cycle). During this dilution cycle, there is a demand to stop the cooling water pump as quickly as possible in order to reduce the power consumption of the pump. However, if it is stopped too quickly, the solution temperature will be high and this solution will be sprayed onto the absorber heat transfer tube, so that the temperature of the cooling water in the absorber heat transfer tube will rise. In addition, in the absorption type hot and cold water device that simultaneously takes out cold and hot water, when there is no cold water load and the cooling water pump is stopped and the flow of cooling water is stopped, the absorption cold water heater is operating by circulating the solution. , The temperature of the cooling water in the absorber heat transfer tube rises. In such a case, the cooling water temperature in the absorber heat transfer tube is high, so
When sprayed on the filler (made of plastic) of the cooling tower, the filler may be deformed.
【0003】[0003]
【発明が解決しようとする課題】本発明は、上記従来技
術に鑑み、冷凍機内に高温の冷却水が生じた場合でも、
冷却塔の充填材を変形せずに保護すると共に、冷却水を
適温に保持することができる吸収冷凍装置を提供するこ
とを課題とする。SUMMARY OF THE INVENTION The present invention has been made in view of the above-mentioned prior art, even when high temperature cooling water is generated in the refrigerator,
An object of the present invention is to provide an absorption refrigerating apparatus that can protect the cooling tower filling material without being deformed and can hold cooling water at an appropriate temperature.
【0004】[0004]
【課題を解決するための手段】上記課題を解決するため
に、本発明では、少なくとも、吸収器、蒸発器、再生
器、凝縮器、溶液熱交換器を有し、これらの機器を結ん
で冷凍サイクルを形成すると共に、吸収器及び凝縮器に
供給する冷却水を冷却する冷却塔と冷却水を循環するた
めの冷却水ポンプを有し、冷却塔、吸収器、凝縮器及び
冷却水ポンプを結んで冷却水循環経路を形成する吸収冷
凍装置において、前記冷却塔が、上部から散水装置、充
填材を充填した充填層、及び、下部に水槽を有してお
り、前記散水装置へ接続する冷却水循環経路の配管中の
分岐点に、冷却水を該散水装置をバイパスして、冷却塔
の充填層より下に導く冷却水バイパス配管を設け、前記
冷却水循環経路に温度センサーを設けると共に、前記冷
却水ポンプをインバータ駆動とし、前記温度センサーの
検出温度が所定の温度以上の場合に、冷却水循環経路に
循環する冷却水流量を少水量とする制御機構を有するこ
ととしたものである。前記吸収冷凍装置において、温度
センサーの検出温度が、所定の温度を越えて高い場合
に、前記バイパス配管を作動させ、また、該検出温度が
所定の温度以下にならないよう、バイパス配管の流量を
調節する制御機構を有することとした。In order to solve the above-mentioned problems, the present invention has at least an absorber, an evaporator, a regenerator, a condenser, and a solution heat exchanger. It has a cooling tower that forms a cycle and cools the cooling water supplied to the absorber and the condenser, and a cooling water pump that circulates the cooling water, and connects the cooling tower, the absorber, the condenser, and the cooling water pump. In the absorption refrigeration apparatus forming a cooling water circulation path with the cooling tower, the cooling tower has a sprinkler from the upper part, a packed bed filled with a filler , and a water tank in the lower part , and a cooling water circulation path connected to the sprinkler. to the <br/> branch point in the piping, the cooling water bypasses the diverging water system, a cooling water bypass pipe for guiding below the packed bed of the cooling tower is provided, a temperature sensor provided in the coolant circulation path Rutotomoni , The cold
The water discharge pump is driven by an inverter, and the temperature sensor
If the detected temperature is higher than the specified temperature, the cooling water circulation path
The control mechanism for reducing the circulating cooling water flow rate is provided. In the absorption refrigeration system, when the temperature detected by the temperature sensor is higher than a predetermined temperature, the bypass pipe is operated, and the flow rate of the bypass pipe is adjusted so that the detected temperature does not fall below the predetermined temperature. It has a control mechanism to operate.
【0005】前記温度センサーは、冷却水循環経路の凝
縮器から前記分岐点の間、及び/又は、冷却水循環経路
の冷却塔から吸収器の間に設けることができ、冷却塔側
から吸収器、凝縮器に供給する冷却水温度を検出し、こ
の温度が所定の温度以下とならないように前記バイパス
配管の流量を調節する制御機構を有することとしてもよ
い。前記バイパス配管を作動又は調節する制御機構は、
前記分岐点部に設けた3方弁又はバイパス配管に設けた
2方弁を制御するのがよい。 [0005] The temperature sensor is between coagulation <br/> condenser cooling water circulation path of the branch point, and / or can kick set between the absorber from the cooling tower of the cooling water circulation path, the cooling tower A control mechanism that detects the temperature of the cooling water supplied to the absorber and the condenser from the side and adjusts the flow rate of the bypass pipe so that this temperature does not fall below a predetermined temperature may be provided. The control mechanism that operates or adjusts the bypass pipe,
It is preferable to control a three-way valve provided at the branch point or a two-way valve provided in the bypass pipe .
【0006】[0006]
【発明の実施の形態】前記した吸収器伝熱管内の冷却水
温度が上昇している場合に、冷却水系の温度分布をみる
と、冷却水配管内及び冷却塔の下部水槽に溜まっている
冷却水は温度が低いので、これらを、混合平均化する
と、冷却塔の散布許容温度範囲に収まることが多く、本
発明はこの知見に基づいてなされたものである。また、
冷却水温度が高い場合、充填材に散布しなくても、下部
水槽の上部空間に、冷却水を流しているだけでも、放熱
が可能であり、温度が高い場合には、ここを流しても冷
却水温度が冷却塔の散布許容温度以下にすることができ
る。そこで、本発明は、冷却塔の散水装置をバイパスす
る弁を有する配管を設け、温度を監視して高温の場合
に、このバイパスを通して冷却水を流し、冷却塔の充填
材を保護するものである。BEST MODE FOR CARRYING OUT THE INVENTION When the temperature of the cooling water in the absorber heat transfer pipe is rising, the temperature distribution of the cooling water system is examined. The cooling water accumulated in the cooling water pipe and in the lower water tank of the cooling tower is shown. Since water has a low temperature, when mixed and averaged, it often falls within the allowable dispersion temperature range of the cooling tower, and the present invention was made based on this finding. Also,
When the temperature of the cooling water is high, it is possible to dissipate the heat by simply flowing the cooling water to the upper space of the lower water tank without spraying it on the filler. The cooling water temperature can be set to be equal to or lower than the spraying allowable temperature of the cooling tower. Therefore, the present invention provides a pipe having a valve that bypasses the sprinkler of the cooling tower, monitors the temperature, and when the temperature is high, allows the cooling water to flow through this bypass to protect the filler in the cooling tower. .
【0007】配管内の混合及び、バイパス、下部水槽で
の放熱により、冷却水温度を低下させ、冷却水温度が冷
却塔の散布許容温度以下になってから、冷却塔充填材へ
の散布を開始すればよい。また、本発明では、冷却水温
度が低下し過ぎる場合にも、このバイパス弁を利用し、
散布装置、充填材をバイパスさせて、低温になるのを防
ぐことができる。即ち、散水装置から充填材に冷却水を
散布すると低温になるが、バイパスから下部水槽に入れ
ればあまり放熱しないので、散水装置とバイパスとの流
量調整により、吸収冷凍機側への冷却水温度調整ができ
る。The cooling water temperature is lowered by the mixing in the piping, the bypass, and the heat radiation in the lower water tank, and after the cooling water temperature becomes lower than the spraying allowable temperature of the cooling tower, the spraying to the cooling tower filling material is started. do it. Further, in the present invention, even when the cooling water temperature is too low, the bypass valve is used,
By bypassing the spraying device and the filler, it is possible to prevent a low temperature. That is, if cooling water is sprayed from the sprinkler to the filler, the temperature will be low, but if you put it in the lower water tank from the bypass, it will not radiate much heat, so the cooling water temperature to the absorption refrigerator side will be adjusted by adjusting the flow rate between the sprinkler and bypass. You can
【0008】以下、本発明を図面を用いて詳細に説明す
る。図1は、本発明の吸収冷凍装置のフロー構成図であ
る。図1において、Aは吸収器、GLは低温再生器、G
Hは高温再生器、Cは凝縮器、Eは蒸発器、XLは低温
熱交換器、XHは高温熱交換器、SPは溶液ポンプ、R
Pは冷媒ポンプ、CWは冷却塔、WPは冷却水ポンプ、
T1 、T2 は温度センサー、V1 はバイパス弁、1〜4
は冷却水配管、5はバイパス配管、6は散水装置、7は
充填層、8は下部水槽、10〜14は冷媒配管、15は
熱源配管、16は冷房負荷に接続する冷水配管、21〜
23、28は希溶液配管、24〜27は濃溶液配管であ
る。The present invention will be described in detail below with reference to the drawings. FIG. 1 is a flow configuration diagram of the absorption refrigeration apparatus of the present invention. In FIG. 1, A is an absorber, GL is a low temperature regenerator, and G is
H is a high temperature regenerator, C is a condenser, E is an evaporator, XL is a low temperature heat exchanger, XH is a high temperature heat exchanger, SP is a solution pump, R
P is a refrigerant pump, CW is a cooling tower, WP is a cooling water pump,
T 1 and T 2 are temperature sensors, V 1 is a bypass valve, 1 to 4
Is a cooling water pipe, 5 is a bypass pipe, 6 is a sprinkler device, 7 is a packed bed, 8 is a lower water tank, 10 to 14 are refrigerant pipes, 15 is a heat source pipe, 16 is a cold water pipe connected to a cooling load, 21 to 21.
23 and 28 are dilute solution pipes, and 24-27 are concentrated solution pipes.
【0009】この装置の冷房運転において、冷媒を吸収
した希溶液の一部は、吸収器Aから溶液ポンプSPによ
り低温熱交換器XLの被加熱側を通り回路22で分岐さ
れ、一部は高温熱交換器XHの被加熱側を通り回路23
から高温再生器GHに導入される。高温再生器GHでは
希溶液は加熱熱源15により加熱されて冷媒を蒸発して
濃縮され、濃縮された濃溶液は回路26を通り高温熱交
換器XHで熱交換され、回路27から24で低温再生器
GLからの濃溶液と合流する。一方、回路22で分岐さ
れた残りの希溶液は、回路28から低温再生器GLに導
入される。低温再生器では高温再生器からの冷媒蒸気に
より加熱濃縮された後、回路24で高温再生器GHから
の濃溶液と合流した後、低温熱交換器XLの加熱側を通
り、回路25から吸収器Aに導入される。In the cooling operation of this apparatus, a part of the diluted solution that has absorbed the refrigerant is branched from the absorber A by the solution pump SP through the heated side of the low temperature heat exchanger XL in the circuit 22, and a part of the diluted solution is high. Circuit 23 passing through the heated side of the heat exchanger XH
Is introduced into the high temperature regenerator GH. In the high temperature regenerator GH, the dilute solution is heated by the heating heat source 15 to evaporate the refrigerant to be concentrated, and the concentrated concentrated solution passes through the circuit 26 and is heat-exchanged in the high temperature heat exchanger XH, and the low temperature regeneration is performed in the circuits 27 to 24. Combine with concentrated solution from vessel GL. On the other hand, the remaining dilute solution branched in the circuit 22 is introduced into the low temperature regenerator GL from the circuit 28. In the low temperature regenerator, after being heated and concentrated by the refrigerant vapor from the high temperature regenerator, it merges with the concentrated solution from the high temperature regenerator GH in the circuit 24, then passes through the heating side of the low temperature heat exchanger XL, and from the circuit 25 to the absorber. Introduced in A.
【0010】高温再生器GHで蒸発した冷媒ガスは、冷
媒回路13を通り、低温再生器GLの熱源として用いら
れたのち凝縮器Cに導入される。凝縮器Cでは低温再生
器GLからの冷媒ガスと共に冷却水により冷却されて凝
縮し回路12から蒸発器Eに入る。蒸発器Eでは冷媒が
冷媒ポンプRP、回路10、11により循環されて蒸発
し、その際に蒸発熱を負荷側の冷水から奪い、冷水を冷
却し、冷房に供される。蒸発した冷媒は吸収器Aで冷却
水により冷却され、濃溶液により吸収されて、希溶液と
なり溶液ポンプで循環されるサイクルとなる。このよう
な冷房サイクルにおいて、吸収器A及び凝縮器Cで用い
る冷却水は、冷却塔CWの下部水槽8から冷却水ポンプ
WPにより、経路1から吸収器Aの伝熱部2を通り、次
いで凝縮器Cの伝熱部3を通って、経路4から冷却塔C
Wの散水装置6から充填層7上に散水される。この散水
によって冷却された水が、下部水槽8に貯まり、冷却水
ポンプWPによって循環するサイクルとなる。The refrigerant gas evaporated in the high temperature regenerator GH passes through the refrigerant circuit 13, is used as a heat source of the low temperature regenerator GL, and is then introduced into the condenser C. In the condenser C, the refrigerant gas from the low temperature regenerator GL is cooled by the cooling water and condensed, and the condensed gas enters the evaporator E from the circuit 12. In the evaporator E, the refrigerant is circulated and evaporated by the refrigerant pump RP and the circuits 10 and 11, and at that time, the heat of evaporation is taken from the cold water on the load side, the cold water is cooled, and the cold water is provided for cooling. The evaporated refrigerant is cooled by cooling water in the absorber A, absorbed by the concentrated solution, becomes a dilute solution, and is cycled by a solution pump. In such a cooling cycle, the cooling water used in the absorber A and the condenser C passes from the path 1 to the heat transfer section 2 of the absorber A by the cooling water pump WP from the lower water tank 8 of the cooling tower CW, and then is condensed. Cooling tower C from path 4 through heat transfer section 3 of vessel C
Water is sprinkled on the packed bed 7 from the water sprinkler 6 of W. The water cooled by this sprinkling is stored in the lower water tank 8 and circulated by the cooling water pump WP.
【0011】そして、本発明では、このように循環され
ている冷却水は、温度センサーT1又はさらに温度セン
サーT2 により、冷却水の冷却塔CWに導入される温
度、又はさらに冷却塔から出る温度を検出しており、次
のように制御することができる。即ち、温度センサーT
1 の検出温度が所定の温度(例えば、55℃)を越えて
高くなった場合には、制御器9の信号によりバイパス管
5の弁V1 を開として、冷却水を充填層に散水せずにバ
イパスして直接水槽に散水する。また、冷却水の温度が
低くなりすぎると、吸収サイクル濃度が希くなりすぎて
冷水負荷に対応しなくなるので、このような場合は温度
センサーT1 の検出温度が所定の温度(例えば、15
℃)以下にならないように、バイパス配管5に通す冷却
水量を、弁V1 を制御器9で制御して調整することがで
きる。このような制御は、温度センサーT2 を設けて、
この温度センサーT2 の検出温度によって、弁V1 を制
御器9によって制御することによって行うこともでき
る。In the present invention, the cooling water circulated in this way is introduced by the temperature sensor T 1 or the temperature sensor T 2 into the cooling tower CW, or further exits from the cooling tower. The temperature is detected and can be controlled as follows. That is, the temperature sensor T
When the detected temperature of 1 becomes higher than a predetermined temperature (for example, 55 ° C.), the valve V 1 of the bypass pipe 5 is opened by the signal of the controller 9 and the cooling water is not sprayed on the packed bed. Bypass and spray directly to the aquarium. Further, if the temperature of the cooling water becomes too low, the absorption cycle concentration becomes too low to support the load of cold water, and in such a case, the temperature detected by the temperature sensor T 1 is a predetermined temperature (for example, 15).
The flow rate of cooling water to be passed through the bypass pipe 5 can be adjusted by controlling the valve V 1 by the controller 9 so that the temperature does not fall below ℃). For such control, a temperature sensor T 2 is provided,
It is also possible to control the valve V 1 by the controller 9 according to the temperature detected by the temperature sensor T 2 .
【0012】図2に、本発明の吸収冷凍装置の他のフロ
ー構成図を示す。図2は、図1において、高温再生器G
Hからの冷媒回路3に、分岐点30から温水加熱器Wに
至る分岐回路31を設け、冷水と温水を同時に供給でき
るようにしたサイクルを示しており、このような吸収冷
凍機においても、本発明の冷却水循環経路を有する装置
が適用できる。図2において、31〜33、35、37
は冷媒回路、34は制御弁、39は主冷媒調整弁で、3
6は分岐点である。なお、上記の図面において、バイパ
ス管5には、二方弁V1 を設けた例で説明したが、バイ
パス管は、管路4に三方弁を設けて接続してもよい。ま
た、インパータ駆動の冷却水ポンプが利用されている場
合、冷却水が高温のとき、充填材に悪影響を及ぼさない
ように、バイパス弁V1 を作動させるのであるが、高温
時に、冷却水流量を減少させるようにすれば、バイパス
弁のサイズを小さくすることができる(低コスト化)。FIG. 2 shows another flow diagram of the absorption refrigeration system of the present invention. 2 is a high temperature regenerator G in FIG.
The refrigerant circuit 3 from H is provided with a branch circuit 31 from the branch point 30 to the hot water heater W to show a cycle in which cold water and hot water can be supplied at the same time. An apparatus having a cooling water circulation path of the invention can be applied. In FIG. 2, 31-33, 35, 37
Is a refrigerant circuit, 34 is a control valve, 39 is a main refrigerant adjusting valve, 3
6 is a branch point. In the above drawings, an example in which the bypass pipe 5 is provided with the two-way valve V 1 has been described, but the bypass pipe may be connected to the pipe line 4 by providing a three-way valve. Further, when the cooling water pump driven by an imperator is used, when the cooling water is at a high temperature, the bypass valve V 1 is operated so as not to adversely affect the filling material. If the number is reduced, the size of the bypass valve can be reduced (cost reduction).
【0013】[0013]
【発明の効果】本発明によれば、冷凍機内に高温の冷却
水が生じた場合でも、冷却塔の充填材を変形させること
なく、また、冷却水を冷水負荷に対応して適正温度に保
持することができ、吸収冷凍装置の効率的な運転が可能
となった。According to the present invention, even when high temperature cooling water is generated in the refrigerator, the cooling water is kept at an appropriate temperature without deforming the packing material of the cooling tower and corresponding to the cooling water load. It is possible to operate the absorption refrigeration system efficiently.
【図1】本発明の吸収冷凍装置のフロー構成図。FIG. 1 is a flow configuration diagram of an absorption refrigeration apparatus of the present invention.
【図2】本発明の吸収冷凍装置の他のフロー構成図。FIG. 2 is another flow configuration diagram of the absorption refrigeration apparatus of the present invention.
A:吸収器、GL:低温再生器、GH:高温再生器、
C:凝縮器、E:蒸発器、XL:低温熱交換器、XH:
高温熱交換器、SP:溶液ポンプ、RP:冷媒ポンプ、
CW:冷却塔、WP:冷却水ポンプ、T1 、T2 :温度
センサー、V1 :バイパス弁、W:温水加熱器、1〜
4:冷却水配管、5:バイパス配管、6:散水装置、
7:充填層、8:下部水槽、9:制御器、10〜14:
冷媒配管、21〜28:溶液配管、15:熱源配管、1
6:冷水配管、30、36:分岐点、31〜33、3
5、37:冷媒配管、34:制御弁、39:主冷媒調整
弁A: absorber, GL: low temperature regenerator, GH: high temperature regenerator,
C: condenser, E: evaporator, XL: low temperature heat exchanger, XH:
High temperature heat exchanger, SP: Solution pump, RP: Refrigerant pump,
CW: cooling towers, WP: cooling water pump, T 1, T 2: temperature sensor, V 1: bypass valve, W: hot water heater, 1
4: Cooling water pipe, 5: Bypass pipe, 6: Sprinkler,
7: Packed bed, 8: Lower water tank, 9: Controller, 10-14:
Refrigerant piping, 21-28: Solution piping, 15: Heat source piping, 1
6: cold water piping, 30, 36: branch points, 31-33, 3
5, 37: Refrigerant piping, 34: Control valve, 39: Main refrigerant adjusting valve
Claims (5)
凝縮器、溶液熱交換器を有し、これらの機器を結んで冷
凍サイクルを形成すると共に、吸収器及び凝縮器に供給
する冷却水を冷却する冷却塔と冷却水を循環するための
冷却水ポンプを有し、冷却塔、吸収器、凝縮器及び冷却
水ポンプを結んで冷却水循環経路を形成する吸収冷凍装
置において、前記冷却塔が、上部から散水装置、充填材
を充填した充填層、及び、下部に水槽を有しており、前
記散水装置に接続する冷却水循環経路の配管中の分岐点
に、冷却水を該散水装置をバイパスして、冷却塔の充填
層より下に導く冷却水バイパス配管を設け、前記冷却水
循環経路に温度センサーを設けると共に、前記冷却水ポ
ンプをインバータ駆動とし、前記温度センサーの検出温
度が所定の温度以上の場合に、冷却水循環経路に循環す
る冷却水流量を少水量とする制御機構を有することを特
徴とする吸収冷凍装置。1. At least an absorber, an evaporator, a regenerator,
A cooling water tower that has a condenser and a solution heat exchanger, forms a refrigeration cycle by connecting these equipment, cools the cooling water supplied to the absorber and the condenser, and a cooling water pump for circulating the cooling water. In the absorption refrigerating device having a cooling tower, an absorber, a condenser and a cooling water pump to form a cooling water circulation path, the cooling tower is a sprinkler from above, a packed bed filled with a filler , and A branch point in the piping of the cooling water circulation path that has a water tank at the bottom and is connected to the sprinkler.
, The cooling water bypasses the diverging water system, a cooling water bypass pipe for guiding below the packed bed of the cooling tower is provided, a temperature sensor provided in the coolant circulation path Rutotomoni, the cooling water ports
The temperature is detected by the temperature sensor.
If the temperature is above the specified temperature, it will circulate in the cooling water circulation path.
An absorption refrigeration apparatus having a control mechanism for reducing the flow rate of cooling water to be reduced.
温度を越えて高い場合に、前記バイパス配管を作動させ
る制御機構を有することを特徴とする請求項1記載の吸
収冷凍装置。2. The absorption refrigerating apparatus according to claim 1, further comprising a control mechanism that activates the bypass pipe when the temperature detected by the temperature sensor exceeds a predetermined temperature and is high.
温度以下にならないよう、前記バイパス配管の流量を調
節する制御機構を有することを特徴とする請求項1記載
の吸収冷凍装置。3. The absorption refrigerating apparatus according to claim 1, further comprising a control mechanism that adjusts a flow rate of the bypass pipe so that a temperature detected by the temperature sensor does not fall below a predetermined temperature.
御機構は、前記分岐点部に設けた3方弁又はバイパス配
管に設けた2方弁の制御であることを特徴とする請求項
2又は3記載の吸収冷凍装置。4. A control mechanism for actuating or regulating the bypass piping claim 2, wherein two-way valve control der Rukoto provided in 3-way valve or the bypass pipe provided in the branch point unit or 3. The absorption refrigeration system described in 3.
蒸発器から前記分岐点の間、及び/又は、冷却水循環経
路の冷却塔から吸収器の間に設けたことを特徴とする請
求項1〜4のいずれか1項記載の吸収冷凍装置。 5. The temperature sensor is a cooling water circulation path.
Between the evaporator and the branch point and / or the cooling water circulation path
Absorption refrigerating apparatus according to any one of claims 1-4, characterized in that the cooling tower of the road is provided between the absorber.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP29986396A JP3460915B2 (en) | 1996-10-25 | 1996-10-25 | Absorption refrigeration equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP29986396A JP3460915B2 (en) | 1996-10-25 | 1996-10-25 | Absorption refrigeration equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH10132412A JPH10132412A (en) | 1998-05-22 |
| JP3460915B2 true JP3460915B2 (en) | 2003-10-27 |
Family
ID=17877870
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP29986396A Expired - Fee Related JP3460915B2 (en) | 1996-10-25 | 1996-10-25 | Absorption refrigeration equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3460915B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP6459240B2 (en) * | 2014-06-25 | 2019-01-30 | 株式会社Ihi | Compressed gas cooling device and compressed gas cooling method |
-
1996
- 1996-10-25 JP JP29986396A patent/JP3460915B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH10132412A (en) | 1998-05-22 |
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