JPH10220900A - Absorbing type air conditioner - Google Patents
Absorbing type air conditionerInfo
- Publication number
- JPH10220900A JPH10220900A JP9018417A JP1841797A JPH10220900A JP H10220900 A JPH10220900 A JP H10220900A JP 9018417 A JP9018417 A JP 9018417A JP 1841797 A JP1841797 A JP 1841797A JP H10220900 A JPH10220900 A JP H10220900A
- Authority
- JP
- Japan
- Prior art keywords
- cooling
- regenerator
- temperature
- evaporator
- heating
- 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
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、吸収液を用いる吸
収式空調装置に関する。The present invention relates to an absorption type air conditioner using an absorption liquid.
【0002】[0002]
【従来の技術】冷却塔、吸収器伝熱管、及び凝縮器伝熱
管を順に環状接続してなり、冷房運転時には冷却水を循
環させる冷却水回路と、室内熱交換器、蒸発器伝熱管を
環状接続してなり、冷温水を循環させる冷温水回路と、
加熱源により低濃度吸収液中の冷媒を気化させて高濃度
吸収液と蒸気冷媒とに分離する再生器、前記凝縮器伝熱
管を配設し冷房運転時には再生器から高温の蒸気冷媒が
送り込まれる凝縮器、冷房運転時には前記凝縮器で液化
した液冷媒を低圧下で蒸発させる蒸発器、該蒸発器に併
設され前記吸収器伝熱管を配設し冷房運転時には前記蒸
発器で蒸発した蒸気冷媒を前記再生器から送られる高濃
度吸収液に吸収させる吸収器、及び該吸収器内の吸収液
を前記再生器に戻す溶液ポンプを有する吸収液回路と、
前記加熱源及び前記溶液ポンプを制御する制御器とを備
える吸収式空調装置が従来より知られている。2. Description of the Related Art A cooling tower, an absorber heat transfer tube, and a condenser heat transfer tube are sequentially connected in a ring shape, and a cooling water circuit for circulating cooling water during cooling operation, an indoor heat exchanger, and an evaporator heat transfer tube are formed in a ring shape. A cold and hot water circuit that connects and circulates cold and hot water,
A regenerator that vaporizes the refrigerant in the low-concentration absorbing liquid by a heating source and separates the refrigerant into a high-concentration absorbing liquid and a vapor refrigerant, and the condenser heat transfer tube is provided. During cooling operation, high-temperature vapor refrigerant is sent from the regenerator. A condenser, an evaporator for evaporating the liquid refrigerant liquefied in the condenser at a low pressure during the cooling operation, and the absorber heat transfer tube is provided in parallel with the evaporator, and the vapor refrigerant evaporated by the evaporator during the cooling operation is disposed. An absorber for absorbing the high-concentration absorbent sent from the regenerator, and an absorbent circuit having a solution pump for returning the absorbent in the absorber to the regenerator;
2. Description of the Related Art An absorption type air conditioner including a heating source and a controller for controlling the solution pump has been conventionally known.
【0003】[0003]
【発明が解決しようとする課題】上記従来の吸収式空調
装置では、冷房運転停止の際に、加熱停止後、局部的な
高温部での吸収液の晶析を防止するため、溶液ポンプを
作動継続して稀釈運転を行っているが、吸収器内の吸収
液を再生器に送り込むものであるため、稀釈運転終了時
点で再生器内における吸収液の液面の高さが高くなる。
この状態で運転を再開して加熱開始により再生器内の吸
収液が沸騰すると、吸収液が高温の液状態で冷媒回路側
に溢れて凝縮器に回り込むので能力ダウン状態に陥る。In the above-mentioned conventional absorption type air conditioner, when the cooling operation is stopped, after the heating is stopped, the solution pump is operated in order to prevent crystallization of the absorption liquid in a locally high temperature part. Although the dilution operation is continuously performed, since the absorption liquid in the absorber is sent to the regenerator, the liquid level of the absorption liquid in the regenerator becomes high at the end of the dilution operation.
In this state, when the operation is restarted and the absorption liquid in the regenerator boils due to the start of heating, the absorption liquid overflows to the refrigerant circuit side in a high-temperature liquid state and goes around the condenser, so that the capacity falls.
【0004】本発明の目的は、運転停止時に稀釈運転を
行っても再生器内の吸収液の液面の高さが適正に調整さ
れ、全停止できる吸収式空調装置の提供にある。[0004] It is an object of the present invention to provide an absorption type air conditioner in which the height of the liquid level of the absorbing liquid in the regenerator can be properly adjusted even when the dilution operation is performed when the operation is stopped, and can be completely stopped.
【0005】[0005]
【課題を解決するための手段】上記課題を解決する為、
本発明は、以下の構成を採用した。 (1)冷却塔、吸収器伝熱管、及び凝縮器伝熱管を順に
環状接続してなり、冷房運転時には冷却水を循環させる
冷却水回路と、室内熱交換器、蒸発器伝熱管を環状接続
してなり、冷温水を循環させる冷温水回路と、吸収液が
入れられ加熱部が加熱源により加熱され冷房運転時には
低濃度吸収液中の冷媒を気化させて高濃度吸収液と蒸気
冷媒とに分離する再生器、前記凝縮器伝熱管を配設し冷
房運転時には前記再生器から高温の蒸気冷媒が送り込ま
れる凝縮器、冷房運転時には前記凝縮器で液化した液冷
媒を低圧下で蒸発させる蒸発器、該蒸発器と連通状態に
併設され前記吸収器伝熱管を配設し冷房運転時には前記
蒸発器で蒸発した蒸気冷媒を前記再生器から送られる高
濃度吸収液に吸収させる吸収器、及び該吸収器内の吸収
液を前記再生器に戻す溶液ポンプを有する吸収液回路
と、途中に電磁開閉弁を配設し、前記再生器と前記蒸発
器とを接続するバイパス管と、再生器内の吸収液の温度
を検出する温度検出手段と、前記加熱源、前記溶液ポン
プ、及び前記電磁開閉弁を制御する制御器とを備える吸
収式空調装置において、冷房運転中に運転停止が指示さ
れると前記制御器は前記加熱源の作動を停止し、前記溶
液ポンプの作動を継続させ、その後、前記電磁開閉弁を
開弁状態に維持する稀釈運転を実施し、再生器内の吸収
液の温度が所定温度に降温すると、前記制御器は前記溶
液ポンプの作動を停止し、この停止から所定時間経過後
に前記電磁開閉弁を閉弁する。In order to solve the above-mentioned problems,
The present invention employs the following configuration. (1) A cooling tower, an absorber heat transfer tube, and a condenser heat transfer tube are sequentially connected in a ring shape, and a cooling water circuit for circulating cooling water in a cooling operation, an indoor heat exchanger, and an evaporator heat transfer tube are connected in a ring shape. A cooling / heating water circuit that circulates cooling / heating water, and an absorption liquid is filled and the heating unit is heated by a heating source. During cooling operation, the refrigerant in the low concentration absorption liquid is vaporized and separated into high concentration absorption liquid and vapor refrigerant. A regenerator, a condenser in which the condenser heat transfer tubes are disposed and a high-temperature vapor refrigerant is sent from the regenerator during a cooling operation, and an evaporator that evaporates the liquid refrigerant liquefied by the condenser at a low pressure during a cooling operation, An absorber which is provided in parallel with the evaporator and is provided with the absorber heat transfer tube, and which absorbs the vapor refrigerant evaporated by the evaporator into a high-concentration absorbent sent from the regenerator during cooling operation, and the absorber Absorbent in the regenerator An absorbent circuit having a solution pump, an electromagnetic on-off valve arranged in the middle, a bypass pipe connecting the regenerator and the evaporator, and temperature detecting means for detecting the temperature of the absorbent in the regenerator. In an absorption air conditioner including a controller that controls the heating source, the solution pump, and the electromagnetic on-off valve, when an operation stop instruction is given during a cooling operation, the controller stops the operation of the heating source. Then, the operation of the solution pump is continued, and thereafter, a dilution operation for maintaining the electromagnetic on-off valve in an open state is performed, and when the temperature of the absorbent in the regenerator falls to a predetermined temperature, the controller The operation of the solution pump is stopped, and after a lapse of a predetermined time from the stop, the solenoid on-off valve is closed.
【0006】(2)冷却塔、吸収器伝熱管、及び凝縮器
伝熱管を順に環状接続してなり、冷房運転時には冷却水
を循環させる冷却水回路と、室内熱交換器、蒸発器伝熱
管を環状接続してなり、冷温水を循環させる冷温水回路
と、吸収液が入れられ加熱部が加熱源により加熱され冷
房運転時には低濃度吸収液中の冷媒を気化させて高濃度
吸収液と蒸気冷媒とに分離する再生器、前記凝縮器伝熱
管を配設し冷房運転時には前記再生器から高温の蒸気冷
媒が送り込まれる凝縮器、暖房運転時には前記再生器か
ら高温の吸収液が送り込まれ冷房運転時には前記凝縮器
で液化した液冷媒を低圧下で蒸発させる蒸発器、該蒸発
器と連通状態に併設され前記吸収器伝熱管を配設し冷房
運転時には前記蒸発器で蒸発した蒸気冷媒を前記再生器
から送られる高濃度吸収液に吸収させる吸収器、及び該
吸収器内の吸収液を前記再生器に戻す溶液ポンプを有す
る吸収液回路と、途中に電磁開閉弁を配設し、前記再生
器と前記蒸発器とを接続するバイパス管と、再生器内の
吸収液の温度を検出する温度検出手段と、前記加熱源、
前記溶液ポンプ、及び前記電磁開閉弁を制御する制御器
とを備える吸収式空調装置において、暖房運転中に運転
停止が指示されると、前記制御器は前記加熱源の作動を
停止し、前記電磁開閉弁を開弁状態にしたまま前記溶液
ポンプの作動を継続する稀釈運転を実施し、再生器内の
吸収液の温度が前記所定温度に降温すると、前記制御器
は前記溶液ポンプの作動を停止し、この停止から所定時
間経過後に前記電磁開閉弁を閉弁する。(2) A cooling tower, an absorber heat transfer tube, and a condenser heat transfer tube are sequentially connected in a ring shape, and a cooling water circuit for circulating cooling water during cooling operation, an indoor heat exchanger, and an evaporator heat transfer tube. A cooling / heating water circuit that is circularly connected and circulates cooling / heating water, and a heating unit is heated by a heating source in which the absorbing liquid is filled, and during cooling operation, the refrigerant in the low-concentration absorbing liquid is vaporized to form a high-concentration absorbing liquid and a vapor refrigerant. A condenser in which a high-temperature vapor refrigerant is fed from the regenerator during cooling operation, and a high-temperature absorbing liquid is sent from the regenerator during heating operation during cooling operation. An evaporator for evaporating the liquid refrigerant liquefied by the condenser under a low pressure; an evaporator heat transfer tube provided in communication with the evaporator; and an evaporator for evaporating the vapor refrigerant evaporated by the evaporator during a cooling operation. Sent from Takano An absorber for absorbing the absorbent, an absorbent circuit having a solution pump for returning the absorbent in the absorber to the regenerator, and an electromagnetic on-off valve disposed in the middle, the regenerator and the evaporator A bypass pipe to be connected, a temperature detecting means for detecting a temperature of the absorbing solution in the regenerator, the heating source,
In the absorption type air conditioner including the solution pump, and a controller that controls the electromagnetic on-off valve, when an operation stop is instructed during the heating operation, the controller stops the operation of the heating source, When a dilution operation is performed in which the operation of the solution pump is continued while the on-off valve is kept open, and the temperature of the absorbent in the regenerator drops to the predetermined temperature, the controller stops the operation of the solution pump. Then, after a lapse of a predetermined time from this stop, the electromagnetic on-off valve is closed.
【0007】[0007]
〔請求項1の作用〕 (冷房運転)冷房運転時、再生器の加熱部が加熱源によ
り加熱され、低濃度吸収液は冷媒が気化して高濃度吸収
液と蒸気冷媒とに分離する。再生器から高温の蒸気冷媒
が凝縮器に送り込まれる。[Action of Claim 1] (Cooling operation) During the cooling operation, the heating section of the regenerator is heated by the heating source, and the low-concentration absorbing liquid is vaporized by the refrigerant and separated into the high-concentration absorbing liquid and the vapor refrigerant. High-temperature vapor refrigerant is sent from the regenerator to the condenser.
【0008】凝縮器から蒸発器に送り込まれた液冷媒
は、冷温水が流れる蒸発器伝熱管に当たって蒸発し冷温
水を冷却する。冷却された冷温水が室内熱交換器に供給
されて室内熱交換器を通過することにより室内冷房が行
われる。蒸発器で蒸発した蒸気冷媒は吸収器内に進入
し、再生器から送られる高濃度の吸収液に吸収され吸収
器内に溜まる。吸収器内に溜まった吸収液は、溶液ポン
プにより再生器に戻される。[0008] The liquid refrigerant sent from the condenser to the evaporator impinges on the evaporator heat transfer tube through which cold and hot water flows, and evaporates to cool the cold and hot water. Cooled hot and cold water is supplied to the indoor heat exchanger and passes through the indoor heat exchanger, thereby performing indoor cooling. The vapor refrigerant evaporated by the evaporator enters the absorber, is absorbed by the high-concentration absorbing liquid sent from the regenerator, and accumulates in the absorber. The absorbent collected in the absorber is returned to the regenerator by the solution pump.
【0009】(冷房運転停止後における液面調整運転)
冷房中に運転停止が指示されると制御器は、加熱源の作
動を停止し、溶液ポンプの作動を継続させ、その後、電
磁開閉弁を開弁状態に維持する稀釈運転を実施する。そ
して、再生器内の吸収液の温度が所定温度に降温する
と、制御器は、溶液ポンプの作動を停止し、この停止か
ら所定時間経過後に電磁開閉弁を閉弁する。(Liquid level adjustment operation after cooling operation is stopped)
When the operation stop is instructed during the cooling, the controller stops the operation of the heating source, continues the operation of the solution pump, and then performs a dilution operation for maintaining the electromagnetic on-off valve in the open state. Then, when the temperature of the absorbent in the regenerator falls to a predetermined temperature, the controller stops the operation of the solution pump, and closes the electromagnetic on-off valve after a lapse of a predetermined time from the stop.
【0010】稀釈運転中、電磁開閉弁を開弁状態にして
いるので、バイパス管を介して再生器内から蒸発器及び
吸収器内に流れ、吸収器内の吸収液が少ない状態が回避
されて吸収液の循環が円滑に行われるが、吸収器から再
生器に向かう溶液ポンプ圧による吸収液の圧力により、
再生器内の吸収液の液面が上昇した状態で稀釈運転が終
了する場合(能力ダウン状態に陥る可能性がある)があ
る。[0010] During the dilution operation, since the electromagnetic on-off valve is opened, the state in which the amount of the absorbing liquid in the absorber is small due to the flow from the regenerator to the evaporator and the absorber through the bypass pipe is avoided. Although the circulation of the absorbing solution is performed smoothly, the pressure of the absorbing solution due to the solution pump pressure from the absorber to the regenerator causes
There is a case where the dilution operation is terminated in a state where the liquid level of the absorbing liquid in the regenerator has risen (there is a possibility that the capacity may be reduced).
【0011】しかし、請求項1では、溶液ポンプの作動
停止から所定時間の間、電磁開閉弁を開弁状態に維持す
るので、再生器内の吸収液は、溶液ポンプ圧が無い状態
のため増加すること無く、水頭差により、バイパス管を
介して再生器内から、蒸発器及び吸収器内に流れ、蒸発
器及び吸収器内の液面と再生器内の吸収液の液面とが同
一高さに落ちつく。However, in the first aspect, the electromagnetic on-off valve is maintained in the open state for a predetermined time after the operation of the solution pump is stopped, so that the absorption liquid in the regenerator increases due to the absence of the solution pump pressure. Flow from the regenerator through the bypass pipe to the evaporator and the absorber due to the head difference, and the liquid level in the evaporator and the absorber and the liquid level of the absorbent in the regenerator are at the same level. Calm down.
【0012】〔請求項1の効果〕冷房運転終了時におけ
る再生器内の吸収液の液面の高さを適正にでき、次回の
冷房運転を正常(能力ダウンが起きない)に立ち上げる
ことができる。According to the first aspect of the present invention, the height of the liquid level of the absorbent in the regenerator at the end of the cooling operation can be properly adjusted, and the next cooling operation can be started up normally (capacity does not decrease). it can.
【0013】〔請求項2の作用〕 (暖房運転)再生器の加熱部が加熱源により加熱され、
再生器から高温の吸収液が蒸発器内に送り込まれる。こ
れにより、蒸発器伝熱管を流れる冷温水が加熱される。
昇温した冷温水が室内熱交換器に供給されて室内熱交換
器を通過し室内暖房が行われる。蒸発器と連通する吸収
器の内部に溜まった吸収液は、溶液ポンプにより再生器
に戻される。[Operation of Claim 2] (Heating operation) The heating section of the regenerator is heated by a heating source,
A high-temperature absorbent is sent from the regenerator into the evaporator. Thereby, the cold / hot water flowing through the evaporator heat transfer tube is heated.
The heated and cooled water is supplied to the indoor heat exchanger, passes through the indoor heat exchanger, and performs indoor heating. The absorbing liquid accumulated inside the absorber communicating with the evaporator is returned to the regenerator by the solution pump.
【0014】(暖房運転停止後における液面調整運転)
暖房中に運転停止が指示されると制御器は、加熱源の作
動を停止し、電磁開閉弁を開弁状態のまま溶液ポンプの
作動を継続する稀釈運転を実施する。再生器内の吸収液
の温度が所定温度に降温すると、制御器は溶液ポンプの
作動を停止し、この停止から所定時間経過後に電磁開閉
弁を閉弁する。(Liquid level adjustment operation after heating operation is stopped)
When the operation stop is instructed during the heating, the controller stops the operation of the heating source and performs a dilution operation in which the operation of the solution pump is continued while the electromagnetic on-off valve is kept open. When the temperature of the absorbent in the regenerator falls to a predetermined temperature, the controller stops the operation of the solution pump, and closes the electromagnetic on-off valve after a lapse of a predetermined time from the stop.
【0015】稀釈運転中、電磁開閉弁を開弁状態にして
いるので、バイパス管を介して再生器内から蒸発器及び
吸収器内に流れ、吸収器内の吸収液が少ない状態が回避
されて吸収液の循環が円滑に行われるが、吸収器から再
生器に向かう溶液ポンプ圧による吸収液の圧力により、
再生器内の吸収器の液面が上昇した状態で稀釈運転が終
了する場合がある。During the dilution operation, since the electromagnetic on-off valve is opened, the state in which the amount of the absorbing liquid in the absorber is small due to the flow from the regenerator to the evaporator and the absorber through the bypass pipe is avoided. Although the circulation of the absorbing solution is performed smoothly, the pressure of the absorbing solution due to the solution pump pressure from the absorber to the regenerator causes
The dilution operation may be terminated with the liquid level of the absorber in the regenerator rising.
【0016】しかし、請求項2では、溶液ポンプの作動
停止から所定時間の間、電磁開閉弁を開弁状態に維持す
るので、再生器内の吸収液は、溶液ポンプ圧が無い状態
のため増加すること無く、水頭差により、バイパス管を
介して再生器から、蒸発器及び吸収器内に流れ、蒸発器
及び吸収液の液面と再生器内の吸収液の液面とが同一高
さに落ちつく。However, according to the present invention, the electromagnetic on-off valve is maintained in the open state for a predetermined time after the operation of the solution pump is stopped, so that the absorption liquid in the regenerator is increased due to the absence of the solution pump pressure. Flow from the regenerator to the evaporator and absorber through the bypass pipe due to the head difference, and the liquid level of the evaporator and the absorbent and the liquid level of the absorbent in the regenerator are at the same level. Calm down.
【0017】〔請求項2の効果〕暖房運転終了時におけ
る再生器内の吸収液の液面の高さを適正にでき、次回の
暖房運転の立ち上げを正常に行うことができる。[Effect of Claim 2] The liquid level of the absorbing liquid in the regenerator at the end of the heating operation can be made appropriate, and the next heating operation can be started normally.
【0018】[0018]
【発明の実施の形態】本発明の一実施例(請求項1、2
に対応)を図1〜図6に基づいて説明する。図1に示す
様に、家庭用の吸収式空調装置Aは、冷房運転時に冷却
水10を循環させる冷却水回路1と、冷温水20を循環
させる冷温水回路2と、高温再生器3、低温再生器4、
凝縮器5、蒸発器6、吸収器7、及び溶液ポンプ80等
を有する吸収液回路8と、制御器9、温度センサ91、
92、93とを備える。DESCRIPTION OF THE PREFERRED EMBODIMENTS One embodiment of the present invention (claims 1 and 2)
Will be described with reference to FIGS. As shown in FIG. 1, a domestic absorption air conditioner A includes a cooling water circuit 1 for circulating cooling water 10 during a cooling operation, a cooling / heating water circuit 2 for circulating cooling / heating water 20, a high-temperature regenerator 3, and a low-temperature regenerator 3. Regenerator 4,
An absorption liquid circuit 8 having a condenser 5, an evaporator 6, an absorber 7, a solution pump 80, etc., a controller 9, a temperature sensor 91,
92 and 93 are provided.
【0019】冷却水回路1は、冷却塔ファン11を付設
した冷却塔12と、冷却水槽13と、冷却水ポンプ14
と、吸収器伝熱管15と、凝縮器伝熱管16とを順に環
状接続して構成され、冷房運転時(図3参照)には冷却
水ポンプ14を作動させて冷却水10を循環させる。冷
却塔ファン11は、交流コンデンサモータ111により
駆動される。The cooling water circuit 1 includes a cooling tower 12 provided with a cooling tower fan 11, a cooling water tank 13, and a cooling water pump 14.
, And an absorber heat transfer tube 15 and a condenser heat transfer tube 16 are sequentially connected in a ring shape. During a cooling operation (see FIG. 3), the cooling water pump 14 is operated to circulate the cooling water 10. The cooling tower fan 11 is driven by an AC condenser motor 111.
【0020】交流コンデンサモータ111は、温度セン
サ93が検出する冷却水10の温度が31.5℃に維持
される様に制御器9により制御される。尚、温度センサ
93は、冷却水ポンプ14- 吸収器伝熱管15間を接続
する冷却水管101中に配設され、吸収器伝熱管15に
供給される冷却水10の温度を検出する。暖房運転時
(図4参照)は、冷却水回路1内の冷却水10は全て抜
かれ、交流コンデンサモータ111及び冷却水ポンプ1
4には通電されない。The AC condenser motor 111 is controlled by the controller 9 so that the temperature of the cooling water 10 detected by the temperature sensor 93 is maintained at 31.5 ° C. The temperature sensor 93 is provided in the cooling water pipe 101 connecting the cooling water pump 14 and the absorber heat transfer pipe 15 and detects the temperature of the cooling water 10 supplied to the absorber heat transfer pipe 15. During the heating operation (see FIG. 4), all the cooling water 10 in the cooling water circuit 1 is drained, and the AC condenser motor 111 and the cooling water pump 1
4 is not energized.
【0021】冷温水回路2は、送風ファン211を付設
した室内熱交換器21(複数台数を並列接続可)、シス
ターン22、冷温水ポンプ81、蒸発器伝熱管37を環
状接続してなり、冷温水ポンプ81により冷温水20を
循環させている。The cold / hot water circuit 2 is formed by connecting the indoor heat exchanger 21 provided with the blower fan 211 (a plurality of heat exchangers can be connected in parallel), the cistern 22, the cold / hot water pump 81, and the evaporator heat transfer tube 37 in an annular manner. The cold / hot water 20 is circulated by the water pump 81.
【0022】高温再生器3は、ガスバーナ31により加
熱されるスカート状の加熱室32、該加熱室32から上
方に立設する分離筒321、及び捕集容器322により
構成され、低濃度吸収液(以下、希液33と呼ぶ;本実
施例では58%臭化リチウム水溶液)中の冷媒(水)を
蒸発させて中濃度吸収液(以下、中液34と呼ぶ;本実
施例では60%臭化リチウム水溶液)と蒸気冷媒35と
に分離する。尚、加熱室32には、高温再生器3の温度
(希液33の温度)を測定する為の温度センサ91が配
設されている。The high-temperature regenerator 3 is composed of a skirt-shaped heating chamber 32 heated by a gas burner 31, a separation cylinder 321 standing upright from the heating chamber 32, and a collecting vessel 322. The refrigerant (water) in the 58% lithium bromide aqueous solution (in this embodiment) is evaporated to evaporate the medium (hereinafter referred to as the middle liquid 34); (Aqueous lithium solution) and a vapor refrigerant 35. The heating chamber 32 is provided with a temperature sensor 91 for measuring the temperature of the high-temperature regenerator 3 (the temperature of the diluted liquid 33).
【0023】ガスバーナ31は、ブンゼン式であり、ガ
ス電磁弁311、312、ガス比例弁313を連設した
ガス管314によりガスが供給され、燃焼用ファン31
5により燃焼用空気が供給されて燃焼する。The gas burner 31 is of a Bunsen type. Gas is supplied by a gas pipe 314 having gas solenoid valves 311 and 312 and a gas proportional valve 313 connected thereto.
5 supplies combustion air and burns.
【0024】尚、冷房運転時は、冷暖切替弁36が閉弁
しているので、中液34(165℃)は、中液配管34
1→高温熱交換流路342→オリフィス343付きの中
液配管344を経て低温再生器4の上部に送り込まれ
る。During the cooling operation, since the cooling / heating switching valve 36 is closed, the intermediate liquid 34 (165 ° C.)
1 → high-temperature heat exchange flow path 342 → supplied to the upper part of low-temperature regenerator 4 via middle liquid pipe 344 with orifice 343.
【0025】低温再生器4は、捕集容器322を包囲
し、冷房運転時には、高温再生器3から送り込まれた中
液34は、捕集容器322から受熱して加熱される。こ
れにより、中液34の一部が蒸発して高濃度吸収液(以
下、濃液41と呼;本実施例では62%臭化リチウム水
溶液)と蒸気冷媒42とに分離する。The low-temperature regenerator 4 surrounds the collection vessel 322, and during cooling operation, the intermediate liquid 34 sent from the high-temperature regenerator 3 receives heat from the collection vessel 322 and is heated. As a result, a part of the middle liquid 34 evaporates and is separated into a high concentration absorbing liquid (hereinafter, referred to as a concentrated liquid 41; a 62% aqueous lithium bromide solution in this embodiment) and a vapor refrigerant 42.
【0026】冷暖切替弁36が開弁する暖房運転時に
は、中液配管341はオリフィス343により流路抵抗
が生じるので中液34は全て暖房配管361に流れ、低
温再生器4に送り込まれない。During the heating operation in which the cooling / heating switching valve 36 is opened, the middle liquid pipe 341 has a flow path resistance caused by the orifice 343, so that all the middle liquid 34 flows through the heating pipe 361 and is not sent to the low-temperature regenerator 4.
【0027】冷房運転時には高温再生器3、低温再生器
4から蒸気冷媒35、42が凝縮器5に送り込まれ、蒸
気冷媒35、42は、コイル状の凝縮器伝熱管16を流
れる冷却水10によって冷却され液化し、液冷媒(水)
52は凝縮器5の底部に溜まる。During the cooling operation, steam refrigerants 35 and 42 are sent from the high-temperature regenerator 3 and the low-temperature regenerator 4 to the condenser 5, and the vapor refrigerants 35 and 42 are cooled by the cooling water 10 flowing through the coil-shaped condenser heat transfer tubes 16. Cooled and liquefied, liquid refrigerant (water)
52 accumulates at the bottom of the condenser 5.
【0028】尚、吸収器伝熱管15及び凝縮器伝熱管1
6を通過して昇温(37.5℃)した冷却水10は、冷
却塔12で冷却(31.5℃)される。The absorber heat transfer tube 15 and the condenser heat transfer tube 1
The cooling water 10 that has passed through 6 and has been heated (37.5 ° C.) is cooled (31.5 ° C.) in the cooling tower 12.
【0029】蒸発器6は、コイル状(溝付き)の蒸発器
伝熱管37を配設している。そして、暖房運転時には冷
暖切替弁36が開弁するので、暖房配管361を介して
高温の中液34が蒸発器6に送り込まれる。The evaporator 6 is provided with a coil-shaped (with grooves) evaporator heat transfer tube 37. Since the cooling / heating switching valve 36 is opened during the heating operation, the high-temperature medium liquid 34 is sent to the evaporator 6 via the heating pipe 361.
【0030】冷房運転時に液冷媒52は、冷媒配管53
→散布器55を介して蒸発器伝熱管37上に散布され、
蒸発器6内は略真空(約6.5mmHg)であるので、
液冷媒52は蒸発器伝熱管37内を流れる冷温水20か
ら気化熱を奪って蒸発する。そして、冷却された冷温水
20は室内に配置された室内熱交換器21で室内に送風
される空気と熱交換して昇温し、昇温した冷温水20は
再び蒸発器伝熱管37を通過して冷却される。During the cooling operation, the liquid refrigerant 52 is
→ Sprayed on the evaporator heat transfer tube 37 via the sprayer 55,
Since the inside of the evaporator 6 is substantially vacuum (about 6.5 mmHg),
The liquid refrigerant 52 evaporates by taking heat of vaporization from the cold / hot water 20 flowing in the evaporator heat transfer tube 37. Then, the cooled cold / hot water 20 exchanges heat with the air blown into the room by the indoor heat exchanger 21 disposed in the room to raise the temperature, and the heated cold / hot water 20 passes through the evaporator heat transfer tube 37 again. And cooled.
【0031】吸収器伝熱管15を配設した吸収器7は、
蒸発器6に併設され、上部及び下部が蒸発器6と連絡し
ている。そして、冷房運転時には、蒸発器6で蒸発した
蒸気冷媒61は上部から吸収器7内に進入し、低温再生
器4→濃液配管411→低温熱交換流路412→濃液配
管413→散布器70を介して吸収器伝熱管15上に散
布される濃液41に吸収され、低濃度となった希液33
は吸収器7の底部に溜まる。The absorber 7 provided with the absorber heat transfer tube 15 is:
The upper part and the lower part are connected to the evaporator 6 in parallel with the evaporator 6. Then, during the cooling operation, the vapor refrigerant 61 evaporated by the evaporator 6 enters the absorber 7 from above, and the low-temperature regenerator 4 → the concentrated liquid pipe 411 → the low-temperature heat exchange channel 412 → the concentrated liquid pipe 413 → sprayer The diluted liquid 33 which has been absorbed by the concentrated liquid 41 scattered on the absorber heat transfer tube 15 through the
Accumulates at the bottom of the absorber 7.
【0032】溶液ポンプ80はAC- 100Vで動作す
るDCブラシレスモータである。この溶液ポンプ80に
は、ホール素子800が取り付けられ、高温再生器3内
の吸収液の温度に応じた回転数に制御器9により制御さ
れる。The solution pump 80 is a DC brushless motor operating at AC-100V. A Hall element 800 is attached to the solution pump 80, and the number of revolutions is controlled by the controller 9 according to the temperature of the absorbent in the high-temperature regenerator 3.
【0033】吸収器6の底部に溜まった希液33(暖房
運転時は吸収液)は、希液配管71→溶液ポンプ80→
希液配管72→低温高温熱交換流路73→希液配管74
を介して高温再生器3の加熱室32に送られる。The diluted liquid 33 (absorbed liquid during the heating operation) accumulated at the bottom of the absorber 6 is diluted with a diluted liquid pipe 71 → a solution pump 80 →
Dilute liquid pipe 72 → low temperature and high temperature heat exchange channel 73 → dilute liquid pipe 74
Through the heating chamber 32 of the high-temperature regenerator 3.
【0034】制御器9は、運転スイッチ(図示せず)か
らの信号、温度センサ91、92、93を含む各種セン
サからの信号等に基づき、以下のものを制御する。ガス
電磁弁311、312、ガス比例弁313、冷温水ポン
プ81、溶液ポンプ80、交流コンデンサモータ11
1、冷暖切替弁36、冷却水ポンプ14、送風ファン2
11。The controller 9 controls the following based on signals from operation switches (not shown), signals from various sensors including the temperature sensors 91, 92 and 93, and the like. Gas solenoid valves 311, 312, gas proportional valve 313, cold / hot water pump 81, solution pump 80, AC condenser motor 11
1. Cooling / heating switching valve 36, cooling water pump 14, fan 2
11.
【0035】つぎに、冷房運転停止時における吸収式空
調装置Aの作動を図5に基づいて述べる。ステップs1
0で冷房運転中である。例えば、比例制御中であれば、
制御器9は、温度センサ92の出力に基づき、室内熱交
換器21に供給される冷温水20の温度が7℃になる様
にガス比例弁313の開度を決定し、インプット量を1
500kcal〜4800kcalの範囲で比例制御し
ている。Next, the operation of the absorption type air conditioner A when the cooling operation is stopped will be described with reference to FIG. Step s1
0 indicates that cooling operation is in progress. For example, during proportional control,
The controller 9 determines the opening of the gas proportional valve 313 based on the output of the temperature sensor 92 so that the temperature of the cold / hot water 20 supplied to the indoor heat exchanger 21 becomes 7 ° C.
Proportional control is performed in the range of 500 kcal to 4800 kcal.
【0036】使用者が冷房運転スイッチ(図示せず)を
オフする(ステップs11でYES)と、制御器9は、
ガスバーナ31の燃焼及び冷温水ポンプ81の作動を停
止(ステップs12)し、ステップs13に進む。When the user turns off the cooling operation switch (not shown) (YES in step s11), the controller 9
The combustion of the gas burner 31 and the operation of the cold / hot water pump 81 are stopped (step s12), and the process proceeds to step s13.
【0037】ステップs13において、制御器9は、冷
却水ポンプ14の作動を継続したまま、溶液ポンプ80
の回転数をHGE温度に基づいて低減していく稀釈運転
を実施する。In step s13, the controller 9 continues the operation of the cooling water pump 14 while keeping the solution pump 80
A dilution operation is performed in which the number of revolutions is reduced based on the HGE temperature.
【0038】ステップs14において、制御器9は、H
GE≦125℃であるか否か判別し、HGE≦125℃
である場合(YES)にはステップs15に進み、HG
E>125℃である場合(NO)にはステップs13に
戻る。In step s14, the controller 9 sets H
It is determined whether or not GE ≦ 125 ° C., and HGE ≦ 125 ° C.
If (YES), the process proceeds to step s15,
If E> 125 ° C. (NO), the flow returns to step s13.
【0039】ステップs15において、制御器9は、冷
却水ポンプ14の作動を停止し、ステップs16に進
む。ステップs16で、制御器9は、冷暖切替弁36を
開弁してステップs17に進む。In step s15, the controller 9 stops the operation of the cooling water pump 14, and proceeds to step s16. In step s16, the controller 9 opens the cooling / heating switching valve 36, and proceeds to step s17.
【0040】ステップs17において、HGE≦110
℃になる(ステップs17でYES)とステップs18
に進む。又、HGE>110℃の場合はステップs16
に戻る。尚、110℃が所定温度に相当する。In step s17, HGE ≦ 110
° C (YES in step s17) and step s18
Proceed to. If HGE> 110 ° C., step s16
Return to Note that 110 ° C. corresponds to the predetermined temperature.
【0041】ステップs18で、制御器9は、溶液ポン
プ80の作動を停止(稀釈運転終了)し、ステップs1
9に進む。溶液ポンプ80の停止から10秒が経過する
と、制御器9は冷暖切替弁36を閉弁する。At step s18, the controller 9 stops the operation of the solution pump 80 (ends the dilution operation), and proceeds to step s1.
Go to 9. When 10 seconds have elapsed since the solution pump 80 was stopped, the controller 9 closes the cooling / heating switching valve 36.
【0042】稀釈運転中、冷暖切替弁36を開弁状態に
しているので、バイパス管361を介して高温再生器3
から蒸発器8及び吸収器7に流れ、吸収器7内の吸収液
が少ない状態が回避されて吸収液の循環が円滑に行われ
るが、吸収器7から高温再生器3に向かう溶液ポンプ圧
による吸収液の圧力により、高温再生器3内の吸収液の
液面が上昇した状態で稀釈運転が終了する場合(能力ダ
ウン状態に陥る可能性がある)がある。During the dilution operation, the cooling / heating switching valve 36 is in the open state.
Flows into the evaporator 8 and the absorber 7, and the state in which the amount of the absorbing liquid in the absorber 7 is small is avoided, and the circulating of the absorbing liquid is smoothly performed. In some cases, the dilution operation is terminated in a state where the liquid level of the absorbing liquid in the high-temperature regenerator 3 has risen due to the pressure of the absorbing liquid (there is a possibility that the capacity is reduced).
【0043】しかし、溶液ポンプ80の作動停止から1
0秒間、冷暖切替弁36を開弁状態に維持するので、高
温再生器3内の吸収液は、溶液ポンプ圧が無い状態のた
め増加すること無く、水頭差により、バイパス管361
を介して高温再生器3から、蒸発器8及び吸収器7内に
流れ、蒸発器8及び吸収器7の液面と高温再生器3内の
吸収液の液面とが同一高さに落ちつく。However, after the operation of the solution pump 80 is stopped,
Since the cooling / heating switching valve 36 is maintained in the open state for 0 second, the absorption liquid in the high temperature regenerator 3 does not increase due to the absence of the solution pump pressure.
Flows from the high-temperature regenerator 3 into the evaporator 8 and the absorber 7 via, and the liquid level of the evaporator 8 and the absorber 7 and the liquid level of the absorbing liquid in the high-temperature regenerator 3 fall to the same height.
【0044】つぎに、暖房運転停止時における吸収式空
調装置Aの作動を図6に基づいて述べる。ステップs2
0で暖房運転中である。例えば、比例制御中であれば、
制御器9は、温度センサ92の出力に基づき、室内熱交
換器21に供給される冷温水20の温度が60℃になる
様にガス比例弁313の開度を決定し、インプット量を
1500kcal〜8000kcalの範囲で比例制御
している。尚、冷暖切替弁36は開弁状態である。Next, the operation of the absorption type air conditioner A when the heating operation is stopped will be described with reference to FIG. Step s2
0 indicates heating operation. For example, during proportional control,
The controller 9 determines the opening of the gas proportional valve 313 based on the output of the temperature sensor 92 so that the temperature of the cold / hot water 20 supplied to the indoor heat exchanger 21 becomes 60 ° C., and sets the input amount to 1500 kcal or more. Proportional control is performed in the range of 8000 kcal. The cooling / heating switching valve 36 is in an open state.
【0045】使用者が暖房運転スイッチ(図示せず)を
オフする(ステップS21でYES)と、制御器9は、
ガスバーナ31の燃焼及び冷温水ポンプ81の作動を停
止(ステップs22)し、ステップs23に進む。When the user turns off the heating operation switch (not shown) (YES in step S21), controller 9
The combustion of the gas burner 31 and the operation of the cold / hot water pump 81 are stopped (step s22), and the process proceeds to step s23.
【0046】ステップs23において、制御器9は、冷
暖切替弁36を開弁状態のまま溶液ポンプ80の回転数
をHGE温度に基づいて低減していく稀釈運転を実施す
る。ステップs24において、制御器9は、HGE≦1
10℃であるか否か判別し、HGE≦110℃である場
合(YES)にはステップs25に進み、HGE>90
℃である場合(NO)には稀釈運転を継続する。尚、9
0℃が設定温度に相当する。In step s23, the controller 9 performs a dilution operation in which the rotation speed of the solution pump 80 is reduced based on the HGE temperature while the cooling / heating switching valve 36 is kept open. In step s24, the controller 9 determines that HGE ≦ 1
It is determined whether or not the temperature is 10 ° C., and if HGE ≦ 110 ° C. (YES), the flow proceeds to step s25, and HGE> 90
When the temperature is ° C (NO), the dilution operation is continued. In addition, 9
0 ° C. corresponds to the set temperature.
【0047】ステップs25において、制御器9は、溶
液ポンプ80の作動を停止し、ステップs26に進む。
溶液ポンプ80の停止から10秒が経過すると、制御器
9は冷暖切替弁36を閉弁する(ステップs26)。In step s25, the controller 9 stops the operation of the solution pump 80, and proceeds to step s26.
When 10 seconds have elapsed since the solution pump 80 was stopped, the controller 9 closes the cooling / heating switching valve 36 (Step s26).
【0048】上記稀釈運転中、冷暖切替弁36を開弁状
態にしているので、バイパス管361を介して高温再生
器3内から蒸発器6及び吸収器7に流れ、吸収器7内の
吸収液が少ない状態が回避されて吸収液の循環が円滑に
行われるが、吸収器7から高温再生器3に向かう溶液ポ
ンプ圧による吸収液の圧力により、高温再生器3内の吸
収液の液面が上昇した状態で稀釈運転が終了する場合が
ある。During the dilution operation, since the cooling / heating switching valve 36 is in the open state, it flows from the high-temperature regenerator 3 to the evaporator 6 and the absorber 7 through the bypass pipe 361, and the absorption liquid in the absorber 7 Is reduced and the absorption liquid is smoothly circulated, but the pressure of the absorption liquid by the solution pump pressure from the absorber 7 to the high-temperature regenerator 3 causes the level of the absorption liquid in the high-temperature regenerator 3 to rise. In some cases, the dilution operation may end with the ascent.
【0049】しかし、溶液ポンプの作動停止から所定時
間の間、冷暖切替弁36を開弁状態に維持するので、高
温再生器3内の吸収液は、溶液ポンプ圧が無い状態のた
め増加すること無く、水頭差により、バイパス管361
を介して高温再生器3から、蒸発器6及び吸収器7内に
流れ、蒸発器6及び吸収器7の液面と高温再生器内の吸
収液の液面とが同一高さに落ちつく。However, since the cooling / heating switching valve 36 is kept open for a predetermined time after the operation of the solution pump is stopped, the absorption liquid in the high-temperature regenerator 3 increases due to the absence of the solution pump pressure. No, due to head difference, bypass pipe 361
Flows from the high-temperature regenerator 3 into the evaporator 6 and the absorber 7, and the liquid levels of the evaporator 6 and the absorber 7 and the liquid level of the absorbing liquid in the high-temperature regenerator settle down to the same height.
【0050】本実施例の吸収式空調装置Aは以下の利点
を有する。吸収式空調装置Aは、運転停止の際に液面調
整を実施するので、冷房運転又は暖房運転終了時におけ
る、蒸発器6及び吸収器7内の吸収液の液面及び高温再
生器3の分離筒321内の吸収液の液面の高さを同一に
して、分離筒321内の液面の高さを適正にすることが
できる。この為、次回の冷房運転又は暖房運転を正常に
立ち上げることができ、能力ダウン等の不具合を防止す
ることができる。The absorption type air conditioner A of this embodiment has the following advantages. Since the absorption type air conditioner A adjusts the liquid level when the operation is stopped, the liquid level of the absorption liquid in the evaporator 6 and the absorber 7 and the separation of the high temperature regenerator 3 at the end of the cooling operation or the heating operation. The height of the liquid surface in the separation tube 321 can be made appropriate by making the height of the liquid surface of the absorption liquid in the tube 321 the same. For this reason, the next cooling operation or heating operation can be started up normally, and problems such as reduced capacity can be prevented.
【0051】本発明は、上記実施例以外に、つぎの実施
態様を含む。a.溶液ポンプ80と冷温水ポンプ81を
タンデムポンプ(単一のモータ方式)で構成しても良
い。この場合、ステップs12、s22において、タン
デムポンプを停止させず、ステップs18、s25で停
止させる。The present invention includes the following embodiments in addition to the above embodiments. a. The solution pump 80 and the cold / hot water pump 81 may be constituted by a tandem pump (single motor type). In this case, the tandem pump is not stopped in steps s12 and s22, but is stopped in steps s18 and s25.
【0052】b.上記実施例は、二重効用式であるが一
重効用式でも良い。c.加熱源は、石油バーナ以外に電
気ヒータ等でも良い。B. The above embodiment is a double-effect type, but may be a single-effect type. c. The heating source may be an electric heater or the like other than the oil burner.
【図1】本発明の一実施例に係る吸収式空調装置Aの原
理説明図である。FIG. 1 is a diagram illustrating the principle of an absorption type air conditioner A according to one embodiment of the present invention.
【図2】吸収式空調装置Aのシステム図である。FIG. 2 is a system diagram of an absorption type air conditioner A.
【図3】吸収式冷空調装置Aを冷房運転させた場合の作
動説明図である。FIG. 3 is an operation explanatory diagram when the absorption-type air conditioner A is operated for cooling.
【図4】吸収式冷空調装置Aを暖房運転させた場合の作
動説明図である。FIG. 4 is an operation explanatory diagram when the absorption-type air conditioner A is operated for heating.
【図5】吸収式冷空調装置Aにおいて、冷房運転を停止
する場合における制御器の作動を示すフローチャートで
ある。FIG. 5 is a flowchart showing the operation of the controller when stopping the cooling operation in the absorption cooling air conditioner A.
【図6】吸収式冷空調装置Aにおいて、暖房運転を停止
する場合における制御器の作動を示すフローチャートで
ある。FIG. 6 is a flowchart showing the operation of the controller when the heating operation is stopped in the absorption-type cooling / air-conditioning apparatus A.
A、B 吸収式空調装置 1 冷却水回路 2 冷温水回路(冷水回路) 3 高温再生器 4 低温再生器 5 凝縮器 6 蒸発器 7 吸収器 8 吸収液回路(吸収回路) 9 制御器 10 冷却水 12 冷却塔 14 冷却水ポンプ 15 吸収器伝熱管 16 凝縮器伝熱管 20 冷温水 21 室内熱交換器 31 ガスバーナ(加熱源) 33 希液(低濃度吸収液) 34 中液(中濃度吸収液) 35 蒸気冷媒 36 冷暖切替弁(電磁開閉弁) 37 蒸発器伝熱管 41 濃液(高濃度吸収液) 42 蒸気冷媒(高温冷媒) 52 液冷媒 61 蒸気冷媒 91 温度センサ(温度検出手段) 212 流量制御弁(電磁バルブ) 361 暖房配管(バイパス管) 801 冷温水ポンプ 80 溶液ポンプ A, B Absorption type air conditioner 1 Cooling water circuit 2 Cold and hot water circuit (cold water circuit) 3 High temperature regenerator 4 Low temperature regenerator 5 Condenser 6 Evaporator 7 Absorber 8 Absorbing liquid circuit (absorbing circuit) 9 Controller 10 Cooling water 12 Cooling Tower 14 Cooling Water Pump 15 Absorber Heat Transfer Tube 16 Condenser Heat Transfer Tube 20 Cold and Hot Water 21 Indoor Heat Exchanger 31 Gas Burner (Heating Source) 33 Rare Liquid (Low Concentration Absorbent) 34 Medium Liquid (Medium Concentration Absorbent) 35 Vapor refrigerant 36 Cooling / heating switching valve (electromagnetic on-off valve) 37 Evaporator heat transfer tube 41 Concentrated liquid (high concentration absorbing liquid) 42 Vapor refrigerant (high temperature refrigerant) 52 Liquid refrigerant 61 Vapor refrigerant 91 Temperature sensor (temperature detecting means) 212 Flow control valve (Electromagnetic valve) 361 Heating pipe (bypass pipe) 801 Cold / hot water pump 80 Solution pump
Claims (2)
管を順に環状接続してなり、冷房運転時には冷却水を循
環させる冷却水回路と、 室内熱交換器、蒸発器伝熱管を環状接続してなり、冷温
水を循環させる冷温水回路と、 吸収液が入れられ加熱部が加熱源により加熱され冷房運
転時には低濃度吸収液中の冷媒を気化させて高濃度吸収
液と蒸気冷媒とに分離する再生器、前記凝縮器伝熱管を
配設し冷房運転時には前記再生器から高温の蒸気冷媒が
送り込まれる凝縮器、冷房運転時には前記凝縮器で液化
した液冷媒を低圧下で蒸発させる蒸発器、該蒸発器と連
通状態に併設され前記吸収器伝熱管を配設し冷房運転時
には前記蒸発器で蒸発した蒸気冷媒を前記再生器から送
られる高濃度吸収液に吸収させる吸収器、及び該吸収器
内の吸収液を前記再生器に戻す溶液ポンプを有する吸収
液回路と、 途中に電磁開閉弁を配設し、前記再生器と前記蒸発器と
を接続するバイパス管と、 再生器内の吸収液の温度を検出する温度検出手段と、 前記加熱源、前記溶液ポンプ、及び前記電磁開閉弁を制
御する制御器とを備える吸収式空調装置において、 冷房運転中に運転停止が指示されると前記制御器は前記
加熱源の作動を停止し、前記溶液ポンプの作動を継続さ
せ、その後、前記電磁開閉弁を開弁状態に維持する稀釈
運転を実施し、 再生器内の吸収液の温度が所定温度に降温すると、前記
制御器は前記溶液ポンプの作動を停止し、この停止から
所定時間経過後に前記電磁開閉弁を閉弁することを特徴
とする吸収式空調装置。1. A cooling water circuit for circulating cooling water during a cooling operation, an indoor heat exchanger, and an evaporator heat transfer tube are annularly connected in order of a cooling tower, an absorber heat transfer tube, and a condenser heat transfer tube. A cooling / heating water circuit that connects and circulates cooling / heating water, and an absorbing liquid is put in, a heating unit is heated by a heating source, and during cooling operation, the refrigerant in the low-concentration absorbing liquid is vaporized to form a high-concentration absorbing liquid and a vapor refrigerant. A condenser in which a high-temperature vapor refrigerant is fed from the regenerator during cooling operation, and an evaporator that evaporates the liquid refrigerant liquefied by the condenser under low pressure during cooling operation. An absorber that is provided in parallel with the evaporator and is provided with the absorber heat transfer tube, and absorbs the vapor refrigerant evaporated by the evaporator in the high-concentration absorbent sent from the regenerator during cooling operation. Absorb the liquid in the absorber An absorbent circuit having a solution pump for returning to the creature, an electromagnetic on-off valve disposed in the middle, a bypass pipe connecting the regenerator and the evaporator, and a temperature for detecting the temperature of the absorbent in the regenerator In an absorption-type air conditioner including a detection unit and a controller that controls the heating source, the solution pump, and the electromagnetic on-off valve, when an operation stop is instructed during a cooling operation, the controller operates the heating source. The operation is stopped, the operation of the solution pump is continued, and then a dilution operation for maintaining the solenoid on-off valve in an open state is performed. When the temperature of the absorbent in the regenerator falls to a predetermined temperature, the control is performed. The absorption type air conditioner, wherein the vessel stops the operation of the solution pump, and closes the electromagnetic on-off valve after a lapse of a predetermined time from the stop.
管を順に環状接続してなり、冷房運転時には冷却水を循
環させる冷却水回路と、 室内熱交換器、蒸発器伝熱管を環状接続してなり、冷温
水を循環させる冷温水回路と、 吸収液が入れられ加熱部が加熱源により加熱され冷房運
転時には低濃度吸収液中の冷媒を気化させて高濃度吸収
液と蒸気冷媒とに分離する再生器、前記凝縮器伝熱管を
配設し冷房運転時には前記再生器から高温の蒸気冷媒が
送り込まれる凝縮器、暖房運転時には前記再生器から高
温の吸収液が送り込まれ冷房運転時には前記凝縮器で液
化した液冷媒を低圧下で蒸発させる蒸発器、該蒸発器と
連通状態に併設され前記吸収器伝熱管を配設し冷房運転
時には前記蒸発器で蒸発した蒸気冷媒を前記再生器から
送られる高濃度吸収液に吸収させる吸収器、及び該吸収
器内の吸収液を前記再生器に戻す溶液ポンプを有する吸
収液回路と、 途中に電磁開閉弁を配設し、前記再生器と前記蒸発器と
を接続するバイパス管と、 再生器内の吸収液の温度を検出する温度検出手段と、 前記加熱源、前記溶液ポンプ、及び前記電磁開閉弁を制
御する制御器とを備える吸収式空調装置において、 暖房運転中に運転停止が指示されると、前記制御器は前
記加熱源の作動を停止し、前記電磁開閉弁を開弁状態に
したまま前記溶液ポンプの作動を継続する稀釈運転を実
施し、 再生器内の吸収液の温度が前記所定温度に降温すると、
前記制御器は前記溶液ポンプの作動を停止し、この停止
から所定時間経過後に前記電磁開閉弁を閉弁することを
特徴とする吸収式空調装置。2. A cooling tower, an absorber heat transfer tube, and a condenser heat transfer tube are connected in a ring shape in order, and a cooling water circuit for circulating cooling water in a cooling operation, an indoor heat exchanger, and an evaporator heat transfer tube are formed in a ring shape. A cooling / heating water circuit that connects and circulates cooling / heating water, and an absorbing liquid is put in, a heating unit is heated by a heating source, and during cooling operation, the refrigerant in the low-concentration absorbing liquid is vaporized to form a high-concentration absorbing liquid and a vapor refrigerant. A condenser in which a high-temperature vapor refrigerant is sent from the regenerator during the cooling operation and the high-temperature absorbing liquid is sent from the regenerator during the heating operation, and the cooling operation is performed during the cooling operation. An evaporator that evaporates the liquid refrigerant liquefied in the condenser under low pressure, the absorber heat transfer tube is disposed in communication with the evaporator, and the vapor refrigerant evaporated in the evaporator is supplied from the regenerator during the cooling operation. High concentration suction sent An absorber for absorbing the liquid, an absorbing liquid circuit having a solution pump for returning the absorbing liquid in the absorber to the regenerator, and a solenoid on-off valve disposed in the middle of the absorbing liquid circuit to connect the regenerator and the evaporator A heating pipe, a temperature detector for detecting the temperature of the absorbent in the regenerator, and a controller for controlling the heating source, the solution pump, and the electromagnetic on-off valve. When the operation stop is instructed during the operation, the controller stops the operation of the heating source, performs a dilution operation in which the operation of the solution pump is continued while the electromagnetic on-off valve is opened, and the regenerator. When the temperature of the absorbing liquid in the temperature falls to the predetermined temperature,
An absorption type air conditioner, wherein the controller stops the operation of the solution pump, and closes the electromagnetic on-off valve after a lapse of a predetermined time from the stop.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP01841797A JP3241624B2 (en) | 1997-01-31 | 1997-01-31 | Absorption air conditioner |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP01841797A JP3241624B2 (en) | 1997-01-31 | 1997-01-31 | Absorption air conditioner |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH10220900A true JPH10220900A (en) | 1998-08-21 |
JP3241624B2 JP3241624B2 (en) | 2001-12-25 |
Family
ID=11971093
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP01841797A Expired - Fee Related JP3241624B2 (en) | 1997-01-31 | 1997-01-31 | Absorption air conditioner |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3241624B2 (en) |
-
1997
- 1997-01-31 JP JP01841797A patent/JP3241624B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JP3241624B2 (en) | 2001-12-25 |
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