JPH1038405A - Absorption cold/warm water machine - Google Patents
Absorption cold/warm water machineInfo
- Publication number
- JPH1038405A JPH1038405A JP8195978A JP19597896A JPH1038405A JP H1038405 A JPH1038405 A JP H1038405A JP 8195978 A JP8195978 A JP 8195978A JP 19597896 A JP19597896 A JP 19597896A JP H1038405 A JPH1038405 A JP H1038405A
- Authority
- JP
- Japan
- Prior art keywords
- temperature
- solution
- pressure
- heating
- cooling
- 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.)
- Pending
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】本発明は吸収冷温水機に関す
る。TECHNICAL FIELD The present invention relates to an absorption chiller / heater.
【0002】[0002]
【従来の技術】従来の吸収式冷温水機の暖房運転から冷
房運転への切替を図2に示す。蒸発器1,吸収器5,凝
縮器13,高温再生器10,低温再生器11,高温熱交
換器9,低温熱交換器8の七つの熱交換器からなる吸収
式冷凍機において、暖房運転から冷房運転に切り替える
ためには、機械を2〜3時間放置する必要があった。暖
房運転では、蒸気配管仕切弁21を開状態とする。機内
の溶液は溶液ポンプ7によって循環され、高温再生器1
0,低温再生器11,吸収器5の内部溶液の温度は60
℃〜80℃程度である。仮に暖房運転を停止直後、冷房
運転をすべく蒸気配管仕切弁21を閉状態とし、冷却塔
20から冷却水3(外気温度と同じ15〜25℃程度)
を吸収器5,凝縮器13に通水すると、急激に吸収器
5,凝縮器13の機内圧力が低下する。一方高温再生器
10は暖房運転直後のため、機内圧力は高い。高温再生
器10と吸収器5は互いに溶液配管で結ばれているた
め、暖房直後にこのように冷却水3を通水すると高温再
生器10から吸収器5に溶液の移動、あるいは機内の冷
媒蒸気が吸収器5に吹き抜けることがある。また吸収器
内の溶液も激しく沸騰するため、吸収器5から邪魔板6
を通りぬけ、隣接した蒸発器1へ溶液が混入する。一
方、蒸発器1では冷房運転時に常に純度の高い水(冷
媒)が必要であり、もしこの中に吸収器5から溶液の粒
が流入すると蒸発性能が低下し冷凍能力も低下する。ま
た、一旦、蒸発器1へ混入した溶液は、蒸発器1内の液
冷媒4を吸収器5へ導くブロー配管15から仕切弁14
を開いて吸収器5へブローしない限り蒸発器1からで
ず、液冷媒4と共に蓄積されることになる。これらを防
止するために、高温再生器10の機内圧力と、機内の溶
液の温度が低下するまで冷房運転に切替しないよう人間
が確認して手動起動するか、無条件にタイマ等で一定時
間以上放置するのが一般的である。また、蒸気配管仕切
弁21の操作は人手によるか、電動弁等を用いてタイマ
等で自動的に弁の操作を行っていた。2. Description of the Related Art FIG. 2 shows switching of a conventional absorption chiller / heater from a heating operation to a cooling operation. In the absorption refrigerator including the seven heat exchangers of the evaporator 1, the absorber 5, the condenser 13, the high-temperature regenerator 10, the low-temperature regenerator 11, the high-temperature heat exchanger 9, and the low-temperature heat exchanger 8, the heating operation is started. To switch to cooling operation, the machine had to be left for 2-3 hours. In the heating operation, the steam pipe gate valve 21 is opened. The solution in the machine is circulated by the solution pump 7 and the high-temperature regenerator 1
0, the temperature of the solution inside the low-temperature regenerator 11 and the absorber 5 is 60
C. to about 80.degree. Immediately after the heating operation is stopped, the steam pipe gate valve 21 is closed to perform the cooling operation, and the cooling water 3 from the cooling tower 20 (about the same as the outside air temperature, about 15 to 25 ° C.)
When water is passed through the absorber 5 and the condenser 13, the pressure inside the absorber 5 and the condenser 13 suddenly drops. On the other hand, since the high-temperature regenerator 10 is immediately after the heating operation, the internal pressure is high. Since the high-temperature regenerator 10 and the absorber 5 are connected to each other by a solution pipe, when the cooling water 3 is passed in this way immediately after heating, the solution is transferred from the high-temperature regenerator 10 to the absorber 5 or the refrigerant vapor in the machine. May blow through the absorber 5. Since the solution in the absorber also boils violently, the baffle 6
And the solution is mixed into the adjacent evaporator 1. On the other hand, the evaporator 1 always requires high-purity water (refrigerant) during the cooling operation, and if particles of the solution flow into the evaporator 1 from the absorber 5, the evaporation performance is reduced and the refrigerating capacity is also reduced. The solution once mixed into the evaporator 1 is supplied from a blow pipe 15 for guiding the liquid refrigerant 4 in the evaporator 1 to the absorber 5 through a gate valve 14.
Is not discharged from the evaporator 1 unless the air is blown into the absorber 5 and is blown into the absorber 5, and is accumulated together with the liquid refrigerant 4. In order to prevent such a situation, a human operator confirms that the internal pressure of the high-temperature regenerator 10 does not switch to the cooling operation until the temperature of the solution in the apparatus is lowered, or manually starts the operation, or unconditionally uses a timer or the like for a predetermined time or more. It is common to leave it alone. Further, the steam pipe gate valve 21 is operated manually or automatically by a timer or the like using an electric valve or the like.
【0003】特開平7−260282 号公報では、暖房から冷
房の運転指令が出たときに、吸収液温度検出手段で温度
が運転開始判定の上限よりも高温の時は停止状態で待機
し、上限以下の時は冷房運転を開始するとある。In Japanese Unexamined Patent Publication No. Hei 7-260282, when an operation command for heating to cooling is issued, when the temperature of the absorbent temperature detecting means is higher than the upper limit for judging the start of operation, the apparatus stands by in a stopped state, In the following cases, cooling operation is started.
【0004】[0004]
【発明が解決しようとする課題】暖房運転から冷房運転
に切り替える時に、タイマで一定時間以上待つことはす
ぐさま冷房運転を行いたいユーザーにとっては苦痛であ
る。また暖房から冷房に切り替えるような季節では、暖
房運転そのものも全負荷運転とは考えにくく、低負荷つ
まり、溶液の温度や機内の圧力も低いことが多い。つま
り機械側は暖房から冷房に切り替えても差し支えないと
きまで、タイマで待つ制御になっていた。When switching from the heating operation to the cooling operation, waiting for a certain period of time with a timer is a pain for a user who wants to immediately perform the cooling operation. In a season in which heating is switched to cooling, the heating operation itself is unlikely to be a full load operation, and the load is low, that is, the temperature of the solution and the pressure in the machine are often low. In other words, the machine is controlled to wait by a timer until it is safe to switch from heating to cooling.
【0005】[0005]
【課題を解決するための手段】本発明では、機内の圧力
または機内溶液の温度を感知し、設定値になったところ
で暖房から冷房運転に切り替える制御を行う。According to the present invention, the pressure in the machine or the temperature of the solution in the machine is sensed, and when the set value is reached, control for switching from heating to cooling operation is performed.
【0006】[0006]
【発明の実施の形態】図1により、暖房運転から冷房運
転の切替を説明する。暖房運転では加熱装置12によっ
て高温再生器10内の溶液が加熱され、冷媒蒸気が発生
する。高温の冷媒蒸気は蒸気配管16を通って蒸発器1
に貫通されたチューブ内の温水17によって冷却され液
化し、このときチューブ内の水に熱を与え暖房に供す
る。液化した液冷媒は再び蒸発器1から吸収器5に導か
れ、溶液と混合し溶液ポンプ7によって高温再生器10
に搬送される。ここで吸収器5又は、高温再生器10又
は、低温再生器11の溶液温度を感知するセンサ18を
設置する。又は高温再生器10から発生する蒸気が通る
蒸気配管16に圧力を感知するセンサ19を設置する。
冷房運転を行うためには、冷却水ポンプ2を運転し、吸
収器5,凝縮器13に冷却水を通水する。この時、機内
の溶液温度又は、高温再生器10の機内圧力が高いと前
述のように蒸発器1内の液冷媒4に溶液が混入し、冷房
運転に支障がでるため、これがある一定の温度又は圧力
以下になるまで、待つ制御を行う。例えば暖房運転中、
吸収器5,高温再生器10,低温再生器11内部の溶液
温度は、60℃〜80℃なので、吸収器5の溶液温度が
40℃以下になったら、冷房運転に切り替える制御とす
れば、吸収器5内の溶液沸騰が防げるため、溶液の粒が
蒸発器1に溶液が混入する心配がなく、冷房運転を開始
できる。ここで、高温再生器10の機内圧力を検知する
制御としてもよい。例えば、高温再生器10の機内圧力
が−600mmHg以下まで低下したら、冷房運転開始す
る制御とすれば、高温再生器10から吸収器5への蒸気
の吹き抜けを防止でき、蒸発器1に溶液が混入する心配
がなく、安定した冷房運転を実現できる。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Referring to FIG. 1, switching from a heating operation to a cooling operation will be described. In the heating operation, the solution in the high-temperature regenerator 10 is heated by the heating device 12, and refrigerant vapor is generated. The high-temperature refrigerant vapor passes through the vapor pipe 16 and passes through the evaporator 1.
The liquid is cooled and liquefied by the warm water 17 in the tube penetrated into the tube, and at this time, heat is given to the water in the tube to provide heating. The liquefied liquid refrigerant is guided again from the evaporator 1 to the absorber 5, where it is mixed with the solution, and the solution is pumped by the solution pump 7 to the high temperature regenerator
Transported to Here, a sensor 18 for detecting the solution temperature of the absorber 5, the high-temperature regenerator 10 or the low-temperature regenerator 11 is provided. Alternatively, a sensor 19 for sensing pressure is installed in a steam pipe 16 through which steam generated from the high-temperature regenerator 10 passes.
In order to perform the cooling operation, the cooling water pump 2 is operated, and the cooling water is passed through the absorber 5 and the condenser 13. At this time, if the solution temperature inside the machine or the inside pressure of the high-temperature regenerator 10 is high, the solution is mixed into the liquid refrigerant 4 inside the evaporator 1 as described above, which hinders the cooling operation. Alternatively, control is performed to wait until the pressure becomes equal to or less than the pressure. For example, during heating operation,
Since the solution temperature inside the absorber 5, the high-temperature regenerator 10 and the low-temperature regenerator 11 is 60 ° C. to 80 ° C., if the solution temperature of the absorber 5 becomes 40 ° C. or less, the control is switched to the cooling operation. Since the boiling of the solution in the vessel 5 can be prevented, the cooling operation can be started without a concern that the solution particles are mixed into the evaporator 1. Here, control for detecting the internal pressure of the high-temperature regenerator 10 may be performed. For example, if the internal pressure of the high-temperature regenerator 10 is reduced to −600 mmHg or less, if the control for starting the cooling operation is performed, it is possible to prevent the steam from flowing from the high-temperature regenerator 10 to the absorber 5 and mix the solution into the evaporator 1. There is no need to worry about this, and stable cooling operation can be realized.
【0007】[0007]
【発明の効果】本発明により、暖房から冷房への切替の
条件として機械側の温度又は、圧力を検知しある一定条
件以下になるまで待つ制御のため、タイマ等に比べ必要
以上に待つことがない。また、冷凍機本体の温度又は、
圧力の検出を行うので機種や環境による違いをキャンセ
ルできるため、安全に暖房から冷房に切替が可能であ
る。つまり暖房から冷房に切り替える際、専門のメンテ
員による操作なしに、ユーザーが任意に切替ができるよ
うになる。According to the present invention, as a control for switching from heating to cooling, the temperature or pressure on the machine side is detected and controlled to wait until a certain condition or less is obtained. Absent. Also, the temperature of the refrigerator body or
Since the pressure is detected, the difference depending on the model and the environment can be canceled, so that it is possible to safely switch from heating to cooling. That is, when switching from heating to cooling, the user can arbitrarily switch without heating by a specialized maintenance person.
【図1】本発明の実施例の暖房から冷房への切替の説明
図。FIG. 1 is an explanatory diagram of switching from heating to cooling according to an embodiment of the present invention.
【図2】従来の暖房から冷房への切替の説明図。FIG. 2 is an explanatory diagram of conventional switching from heating to cooling.
【符号の説明】 1…蒸発器、2…冷却水ポンプ、3…冷却水、4…液冷
媒、5…吸収器、6…邪魔板、7…溶液ポンプ、8…低
温熱交換器、9…高温熱交換器、10…高温再生器、1
1…低温再生器、12…燃焼器、13…凝縮器、14…
仕切弁、15…ブロー配管、16…蒸気配管、17…温
水、18…温度センサ、19…圧力センサ、20…冷却
塔、21…蒸気配管仕切弁。[Description of Signs] 1 ... evaporator, 2 ... cooling water pump, 3 ... cooling water, 4 ... liquid refrigerant, 5 ... absorber, 6 ... baffle plate, 7 ... solution pump, 8 ... low temperature heat exchanger, 9 ... High temperature heat exchanger, 10 ... High temperature regenerator, 1
DESCRIPTION OF SYMBOLS 1 ... Low temperature regenerator, 12 ... Combustor, 13 ... Condenser, 14 ...
Gate valve, 15: blow pipe, 16: steam pipe, 17: hot water, 18: temperature sensor, 19: pressure sensor, 20: cooling tower, 21: steam pipe gate valve.
Claims (1)
器,熱交換器を含む吸収冷温水機において、圧力又は温
度を感知するセンサを設け、暖房運転から冷房運転への
切替時に前記センサによって圧力又は温度が設定値に達
すると自動的に起動することを特徴とする吸収冷温水
機。1. An absorption chiller / heater including an evaporator, an absorber, a low-temperature regenerator, a high-temperature regenerator, and a heat exchanger, wherein a sensor for sensing pressure or temperature is provided, and when the heating operation is switched to the cooling operation, An absorption chiller / heater, which is automatically started when a pressure or temperature reaches a set value by a sensor.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP8195978A JPH1038405A (en) | 1996-07-25 | 1996-07-25 | Absorption cold/warm water machine |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP8195978A JPH1038405A (en) | 1996-07-25 | 1996-07-25 | Absorption cold/warm water machine |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH1038405A true JPH1038405A (en) | 1998-02-13 |
Family
ID=16350178
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP8195978A Pending JPH1038405A (en) | 1996-07-25 | 1996-07-25 | Absorption cold/warm water machine |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH1038405A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102113832A (en) * | 2010-07-08 | 2011-07-06 | 宁波沁园集团有限公司 | Water dispenser device and method for controlling outlet water of water dispenser device at constant temperature |
-
1996
- 1996-07-25 JP JP8195978A patent/JPH1038405A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102113832A (en) * | 2010-07-08 | 2011-07-06 | 宁波沁园集团有限公司 | Water dispenser device and method for controlling outlet water of water dispenser device at constant temperature |
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