JPH01285751A - Absorption type refrigerating machine - Google Patents
Absorption type refrigerating machineInfo
- Publication number
- JPH01285751A JPH01285751A JP11293688A JP11293688A JPH01285751A JP H01285751 A JPH01285751 A JP H01285751A JP 11293688 A JP11293688 A JP 11293688A JP 11293688 A JP11293688 A JP 11293688A JP H01285751 A JPH01285751 A JP H01285751A
- Authority
- JP
- Japan
- Prior art keywords
- temperature
- water temperature
- cold water
- control valve
- chilled water
- 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
- 238000010521 absorption reaction Methods 0.000 title claims description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 72
- 239000003507 refrigerant Substances 0.000 claims description 20
- 239000007788 liquid Substances 0.000 claims description 12
- 238000005057 refrigeration Methods 0.000 claims description 4
- 239000006096 absorbing agent Substances 0.000 claims description 3
- 239000012530 fluid Substances 0.000 claims 5
- 238000010438 heat treatment Methods 0.000 abstract description 33
- 238000000034 method Methods 0.000 abstract description 2
- 238000010586 diagram Methods 0.000 description 10
- 230000007423 decrease Effects 0.000 description 8
- 239000000446 fuel Substances 0.000 description 5
- 238000002485 combustion reaction Methods 0.000 description 4
- 238000001816 cooling Methods 0.000 description 4
- 239000002253 acid Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 238000004378 air conditioning Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 238000013021 overheating Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Abstract
Description
【発明の詳細な説明】
C産業上の利用分野]
この発明は吸収式冷凍機、特に冷水温度を負荷の多少に
かかわらず、常に温度設定範囲内に保つように制御する
ようにした吸収式冷凍機に関するものである。[Detailed Description of the Invention] Field of Industrial Application] This invention relates to an absorption refrigerating machine, particularly an absorption refrigerating machine that controls the temperature of chilled water to always be within a set temperature range regardless of the amount of load. It's about machines.
[従来の技術]
従来この種の冷凍機の一例を第3図および第4図に示す
。この例は実公昭61−35894号に開示されたもの
である。[Prior Art] An example of a conventional refrigerator of this type is shown in FIGS. 3 and 4. This example is disclosed in Utility Model Publication No. 61-35894.
tJSs図において、(1)は高温i4生器で、ガス等
の燃焼加熱室(2)を存し、稀酸から冷媒を加熱分離す
る。(3)は再生器(1)からの冷媒を更に加熱分離す
る低温再生器で、両再生器(1)、(3)からの冷媒は
凝縮器(4)によって冷却液化される。In the tJSs diagram, (1) is a high-temperature i4 generator, which includes a combustion heating chamber (2) for gas, etc., and heats and separates the refrigerant from the dilute acid. (3) is a low temperature regenerator that further heats and separates the refrigerant from the regenerator (1), and the refrigerant from both regenerators (1) and (3) is cooled and liquefied by the condenser (4).
凝縮器(4)からの冷媒は蒸発器(5)に送られ、吸収
器(6)によって冷水とされる。(7)及び(8)は低
温及び高温の熱交換器で、これらは冷媒蒸気導管(9)
、冷媒液流下管(10)、冷媒ポンプ(11)を何する
冷媒循環器(12)、吸収液ポンプ(13)を存する稀
酸管(14)、中間液管(15)及び濃液管(16)で
配管接続されて冷凍サイクルを構成している。The refrigerant from the condenser (4) is sent to the evaporator (5) and is turned into cold water by the absorber (6). (7) and (8) are low temperature and high temperature heat exchangers, which are connected to the refrigerant vapor conduit (9).
, a refrigerant liquid down-flow pipe (10), a refrigerant circulator (12) with a refrigerant pump (11), a dilute acid pipe (14) with an absorption liquid pump (13), an intermediate liquid pipe (15) and a concentrated liquid pipe ( 16) are connected by piping to form a refrigeration cycle.
(20)は冷水配管で、室内負荷対応の冷房機(図示省
略)に接続され、室内の冷房を行う。Reference numeral (20) denotes a cold water pipe, which is connected to an air conditioner (not shown) for indoor load and cools the room.
(17)は加熱−制御弁で、燃焼加熱室(2)への燃料
供給管(18)に取り付けられる。冷水管(20)の冷
水出口側には温度検出器(19)が設けられている。(
21)は冷凍サイクルを制御する制御器である。(17) is a heating control valve, which is attached to the fuel supply pipe (18) to the combustion heating chamber (2). A temperature detector (19) is provided on the cold water outlet side of the cold water pipe (20). (
21) is a controller that controls the refrigeration cycle.
次に、上述した従来装置の動作について説明する。Next, the operation of the above-mentioned conventional device will be explained.
制御器(21)は温度検出器(19)の信号を取り入れ
、内蔵された温度設定器によって設定された751度、
例えば5℃以下になれば加熱量制御弁(17)を開き、
燃焼加熱室(2)への燃料供給を開始し、冷水温度を一
定範囲、例えば5℃〜15℃の範囲に制御する。The controller (21) takes in the signal from the temperature detector (19) and adjusts the temperature to 751 degrees, which is set by the built-in temperature setting device.
For example, if the temperature drops below 5℃, open the heating amount control valve (17),
Fuel supply to the combustion heating chamber (2) is started, and the temperature of the cold water is controlled within a certain range, for example, within a range of 5°C to 15°C.
また、冷水温度低下時、即ち設定温度5℃よりよりさら
に冷水’/24度が低下した場合、例えば4℃になった
場合には冷媒ポンプ(11)を停止し、さらに温度が以
下した場合、例えば3℃になった場合には溶液ポンプ(
13)を停止し、冷水が凍結することを防止している。In addition, when the chilled water temperature decreases, that is, when the chilled water'/24 degrees falls further than the set temperature of 5 degrees Celsius, for example, when it reaches 4 degrees Celsius, the refrigerant pump (11) is stopped, and when the temperature further falls below, For example, if the temperature reaches 3℃, the solution pump (
13) is stopped to prevent cold water from freezing.
上述した制御を第4図(A)〜(C)を用いて詳述する
と次の如きである。The above control will be explained in detail with reference to FIGS. 4(A) to 4(C) as follows.
即ち、冷水温度低下時に制御器(21)内の温度設定器
で設定された温度T2−5℃に達した時点a点で、加熱
量制御弁(17)を閉じる。That is, the heating amount control valve (17) is closed at point a when the temperature reaches T2-5°C set by the temperature setting device in the controller (21) when the cold water temperature decreases.
高温再生器(1)での加熱が停止した後も溶液の持つ予
熱で冷媒は蒸発し、かつ冷媒ポンプ(11)、吸収液ポ
ンプ(13)も運転しているため、蒸発器(5)内での
冷媒の蒸発サイクルは継続することになる。従って、冷
房負荷の小さい時、冷水出口温度はさらに低下すること
になる。Even after heating in the high-temperature regenerator (1) has stopped, the refrigerant evaporates due to the preheating of the solution, and the refrigerant pump (11) and absorption liquid pump (13) are also operating, so the inside of the evaporator (5) The refrigerant evaporation cycle will continue. Therefore, when the cooling load is small, the cold water outlet temperature will further decrease.
一方、冷水温度が上昇した時、即ち、温度設定器の設定
温度T、−15℃になった0点では加熱量制御弁(17
)を開き、高温再生器(1)の加熱を開始する。On the other hand, when the cold water temperature rises, that is, at the 0 point where the set temperature T of the temperature setting device reaches -15℃, the heating amount control valve (17
) and start heating the high temperature regenerator (1).
しかし、冷凍サイクル中の溶液温度は低く、かつ溶液濃
度も低下しており、加熱開始後、直ちに冷媒分離は行わ
れず、溶液温度が−L昇後、蒸発器(5)での蒸発能力
が最大となる。従って、冷水の温度は加熱制御弁(17
)が開いた後も」二昇することになる。室内冷房負荷が
大きい場合、設定温度T1と冷水78度の差は大きくな
る。However, the solution temperature during the refrigeration cycle is low and the solution concentration is also decreasing, so refrigerant separation is not performed immediately after heating starts, and after the solution temperature rises by -L, the evaporation capacity in the evaporator (5) reaches its maximum. becomes. Therefore, the temperature of the cold water is controlled by the heating control valve (17).
) will rise again even after it opens. When the indoor cooling load is large, the difference between the set temperature T1 and the cold water of 78 degrees becomes large.
[発明が解決しようとする課題]
従来の吸収式冷凍機は以上のように構成されているため
、負荷の多少により、温度設定器の設定/11疫より冷
水温度が低く、又は高くなる現象が発生する。即ち、室
内温度も適冷又は過熱され、快適な空調が行われないと
いう問題点があった。[Problem to be solved by the invention] Since the conventional absorption chiller is configured as described above, there is a phenomenon in which the chilled water temperature becomes lower or higher than the setting of the temperature setting device/11 depending on the load. Occur. That is, there is a problem in that the indoor temperature is either cooled down or overheated, and comfortable air conditioning cannot be achieved.
従って、−に記問題点を解消しなければならないという
課題がある。Therefore, there is a problem that the problems listed in - must be solved.
この発明は、係る課題を解決するためになさたもので、
負荷の多少によって室内と度が適冷又は過熱されること
がないようにした吸収式冷凍機を得ることを目的とする
。This invention was made to solve the problem,
To provide an absorption refrigerating machine which allows the room to be cooled appropriately or not to be overheated depending on the amount of load.
〔課題を解決するための手段]
この発明に係る吸収式冷凍機は、制御器によって冷水温
度と、冷水温度変化率から、あらかじめ定められたプロ
グラムに従い、加熱は制御弁の開閉後の冷水温度変化を
演算推定し、冷水温度が設定範囲内にとどまる加熱量制
御弁の開閉温度を算出して加熱量制御弁を開閉する構成
を有する。[Means for Solving the Problems] The absorption chiller according to the present invention is heated according to a predetermined program based on the chilled water temperature and the chilled water temperature change rate by the controller, and the heating is controlled by the chilled water temperature change after opening and closing of the control valve. The heating amount control valve is opened and closed by calculating the opening/closing temperature of the heating amount control valve at which the cold water temperature remains within the set range.
この発明の制御器は冷水温度及び冷水温度変化率から加
熱量制御弁の弁開後も冷水温度が設定温度を越えない、
最も設定温度に近付く制御温度を算出し、この制御温度
で加熱量制御弁の開閉を行う。The controller of this invention prevents the chilled water temperature from exceeding the set temperature even after the heating amount control valve is opened, based on the chilled water temperature and the chilled water temperature change rate.
The control temperature closest to the set temperature is calculated, and the heating amount control valve is opened and closed at this control temperature.
[実施例]
以下、図面に示す実施例に基づいて本発明の詳細な説明
する。[Example] Hereinafter, the present invention will be described in detail based on the example shown in the drawings.
第1図及び第2図は本発明の一実施例を説明するもので
、各図中第3図または第4図と同一部分には同一符号を
付し、その説明は省略する。FIG. 1 and FIG. 2 illustrate one embodiment of the present invention. In each figure, the same parts as in FIG. 3 or 4 are designated by the same reference numerals, and the explanation thereof will be omitted.
第1図と第3図とを比較して明らかなように冷凍機の各
部の構造は同一であるが、制御器(31)による制御1
1式が全く異なる。As is clear from comparing FIG. 1 and FIG. 3, the structure of each part of the refrigerator is the same, but the control by the controller (31)
The first set is completely different.
即ち、第2図(A)〜(C)本方式で冷水出口温度制御
を行った場合における冷水出口温度、加熱制御升の状態
及び冷房能力を示す線図であるが、図においてT 、、
T は設定1Iii&、T、T は加熱量制御弁(1
7)の開閉を行う温度を示す。That is, FIGS. 2(A) to 2(C) are diagrams showing the cold water outlet temperature, the state of the heating control cell, and the cooling capacity when the cold water outlet temperature is controlled by this method.
T is the setting 1Iiii&, T, T is the heating amount control valve (1
7) indicates the temperature at which the opening and closing are performed.
制御器(31)は内蔵された不図示の温度設定器で設定
した温度(例えば温度低下時5℃、温度上昇時15℃)
と、温度検出器(19)による検出信号をもとに、冷水
温度変化率(例えば冷水温度が1分間に1 dcg低下
した場合には温度変化率は1 / 60 (dcg /
5ec)となる)を演算すると共に、現在の冷水温度
より、あらかじめ設定されたプログラムにより、加熱量
制御弁(17)を開閉(冷水温度低下で閉)する信号を
発する。The controller (31) controls the temperature set by a built-in temperature setting device (not shown) (for example, 5°C when the temperature drops and 15°C when the temperature rises).
Based on the detection signal from the temperature detector (19), the rate of change in chilled water temperature (for example, if the chilled water temperature decreases by 1 dcg per minute, the rate of temperature change is 1/60 (dcg/
5ec)), and also generates a signal to open/close the heating amount control valve (17) (close when the cold water temperature drops) according to a preset program based on the current cold water temperature.
また、プログラムは冷水温度低下時に、冷水の温度変化
率が大きければ設定温度(5℃)より高温(例えば6℃
)で、逆に温度変化率が小さければ設定温度に近い温度
(例えば5.5℃)で加熱量制御弁(17)を閉じるよ
うに構成されている。In addition, when the temperature of the chilled water decreases, the program will set the temperature higher than the set temperature (5℃) (for example, 6℃) if the rate of change in temperature of the chilled water is large.
), and conversely, if the rate of temperature change is small, the heating amount control valve (17) is configured to close at a temperature close to the set temperature (for example, 5.5° C.).
また、プログラムは加熱量制御弁(17)を閉(13)
の運転により、さらに冷水温度が低下しても、温度設定
器により設定された温度(5℃)以下にならないように
、冷凍機の性能を考慮し、加熱量制御弁(17)の開閉
温度を算出するように設定されている。The program also closes the heating amount control valve (17) (13).
Even if the chilled water temperature further decreases due to the operation of It is set to be calculated.
即ち、冷水温度低下時は冷水温度の変化率(ΔT1/Δ
11)と現在の冷水温度からあらかじめ定められたプロ
グラムにより、加熱* ill @J弁(17)を閉じ
る温度(T2゜)を算出し、冷水温度がT2□になれば
、加熱量制御弁(17)を閉じ、高温再生器(1)の加
熱を停止する。In other words, when the chilled water temperature decreases, the rate of change in the chilled water temperature (ΔT1/Δ
11) and the current cold water temperature, calculate the temperature (T2°) at which the heating* ill @ J valve (17) is closed, and when the cold water temperature reaches T2□, the heating amount control valve (17 ) and stop heating the high temperature regenerator (1).
しかし、冷媒ポンプ(11)、吸収液ポンプ(13)が
運転されているため、冷水温度はさらに低下するが、冷
水温度が設定温度T2を下回らないように加熱量制御弁
(17)の閉温度T29は決定される。However, since the refrigerant pump (11) and the absorption liquid pump (13) are in operation, the chilled water temperature further decreases, but the closing temperature of the heating amount control valve (17) is maintained so that the chilled water temperature does not fall below the set temperature T2. T29 is determined.
冷水温度上昇時も同様で、冷水温度の変化率(ΔT /
Δt2)と冷水温度から加熱量制御弁(17)の開温度
”11を算出し、加熱を再開する。The same applies when the chilled water temperature rises, and the rate of change in chilled water temperature (ΔT /
The opening temperature "11" of the heating amount control valve (17) is calculated from Δt2) and the cold water temperature, and heating is restarted.
しかし、冷却能力の立上りが遅いため、冷水温度は上昇
するが、設定温度T1を越えることはない。However, since the rise in cooling capacity is slow, the temperature of the cold water rises but does not exceed the set temperature T1.
上述したようにして、室内温度の適冷、過熱が生じない
吸収式冷凍機を得ることができる。As described above, it is possible to obtain an absorption refrigerator that appropriately cools the indoor temperature and does not cause overheating.
なお、」二連した実施例では冷水温度(19)を冷水出
口側に取付けた例を示したが、冷水人口側に設けてもよ
い。In addition, although the example in which the cold water temperature (19) is attached to the cold water outlet side is shown in the two consecutive embodiments, it may be installed on the cold water intake side.
[発明の効果コ
この発明は以上説明したように、高温再生器への燃料供
給弁の開閉温度を冷水温度と冷水温度の変化率から温度
変化率の大きい場合は設定温度範囲内で設定温度から、
より離れた温度とする構成により、燃料供給弁開閉後の
冷水温度は設定温度を越えることがなく、負荷の変化に
かかわらず、常に設定温度範囲で制御され、安定した水
温の冷7kを供給することができる。[Effects of the Invention] As explained above, this invention changes the opening/closing temperature of the fuel supply valve to the high-temperature regenerator from the chilled water temperature and the rate of change of the chilled water temperature within the set temperature range when the rate of change of temperature is large. ,
Due to the configuration in which the temperature is set further apart, the cold water temperature after opening and closing the fuel supply valve does not exceed the set temperature, and regardless of changes in load, it is always controlled within the set temperature range and supplies cold 7K at a stable water temperature. be able to.
第1図は本発明に係る吸収式冷凍機の概略構成図、第2
図は本発明による冷水温度制御時の温度変化を示す線図
、第3図は従来の吸収式冷凍機の概略1M成図、第4図
は従来の冷水温度制御時の温度変化を示す線図である。
図中、(1)は高温再生器、(2)は燃焼加熱室、(3
)は低温再生器、(4)は凝縮器、(5)は蒸発器、(
6)は吸収器、(7)は低温熱交換器、(8)は高温熱
交換器、(9)は冷媒蒸気導管、(10)は冷媒液流下
管、(11)冷媒ポンプ、(12)は冷媒循環路、(1
3)は吸収液ポンプ、(14)は稀酸管、(15)は中
間液管、(16)は濃液管、(17)は加熱量制御弁、
(18)は燃料供給管、(19)は温度検出器、(20
)は冷水管、(21)、(31)は制御器である。
なお、図中、同一符号は同一、又はNj当部分を示す。
代理人 弁理士 大 岩 増 雄
(他 2名)
11]
冷水温度11]御時の温度ズ化を示す線図第2図
ノ
従来例の吸収式冷凍機の概略構成図
第3図
従来グ1jの冷水温度き′揄時の温度変化?示す線図第
4図
1、事件の表示 特願昭63−112936 号2
、開明の名称
吸収式冷凍機
3、補正をする者
5、補正の対象
明細書の発明の詳細な説明のJI3!。
6、補正の内容
以上Fig. 1 is a schematic configuration diagram of an absorption chiller according to the present invention, Fig. 2
The figure is a diagram showing temperature changes during chilled water temperature control according to the present invention, Figure 3 is a schematic 1M diagram of a conventional absorption chiller, and Figure 4 is a diagram showing temperature changes during conventional chilled water temperature control. It is. In the figure, (1) is a high-temperature regenerator, (2) is a combustion heating chamber, and (3) is a high-temperature regenerator.
) is a low temperature regenerator, (4) is a condenser, (5) is an evaporator, (
6) is an absorber, (7) is a low temperature heat exchanger, (8) is a high temperature heat exchanger, (9) is a refrigerant vapor conduit, (10) is a refrigerant liquid flow pipe, (11) a refrigerant pump, (12) is the refrigerant circulation path, (1
3) is an absorption liquid pump, (14) is a dilute acid pipe, (15) is an intermediate liquid pipe, (16) is a concentrated liquid pipe, (17) is a heating amount control valve,
(18) is a fuel supply pipe, (19) is a temperature detector, (20
) is a cold water pipe, and (21) and (31) are controllers. In addition, in the drawings, the same reference numerals indicate the same parts or the parts corresponding to Nj. Agent: Patent attorney Masuo Oiwa (and 2 others) 11] Chilled water temperature 11] Diagram showing temperature fluctuations at the time Figure 2: Schematic diagram of a conventional absorption chiller Figure 3: Conventional diagram 1j What is the temperature change of the cold water when it is heated? Line diagram shown in Figure 4, Figure 1, Indication of the incident, Patent Application No. 112936/1983, No. 2
, Kaimei's name absorption refrigerator 3, person making the amendment 5, detailed description of the invention in the specification to be amended, JI 3! . 6. Details of amendments and above
Claims (1)
液ポンプなどを配管接続し、冷媒と吸収液の循環路を形
成し、再生器の熱源流体の供給路に制御弁を配備した吸
収式冷凍機において、前記蒸発器の冷水配管部に設けら
れた温度検出器と熱源流体制御弁とに電気的に接続され
た制御器を備え、この制御器は冷水温度設定器により設
定された冷水温度の上限値又は下限値と、冷水温度の変
化率及び冷水温度の各データを用い、冷水温度上昇時は
前記冷水温度の上限値に冷水温度が達する前に前記熱源
流体制御弁を「開」にする信号を発し、冷水温度降下時
は前記冷水温度の下限値に冷水温度が達する前に前記熱
源流体制御弁を「閉」にする信号を発するように構成し
たことを特徴とする吸収式冷凍機。An absorption system in which a regenerator, condenser, evaporator, absorber, refrigerant pump, absorption liquid pump, etc. are connected via piping to form a circulation path for the refrigerant and absorption liquid, and a control valve is installed in the supply path for the heat source fluid of the regenerator. The type refrigerator includes a controller that is electrically connected to a temperature detector and a heat source fluid control valve provided in the cold water piping section of the evaporator, and the controller is configured to control the temperature of the cold water set by the cold water temperature setting device. Using the upper limit or lower limit of temperature, the rate of change of chilled water temperature, and each data of chilled water temperature, when the chilled water temperature rises, the heat source fluid control valve is "opened" before the chilled water temperature reaches the upper limit of chilled water temperature. Absorption refrigeration characterized in that it is configured to emit a signal to "close" the heat source fluid control valve when the chilled water temperature drops, and to "close" the heat source fluid control valve before the chilled water temperature reaches the lower limit value of the chilled water temperature. Machine.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11293688A JPH0788988B2 (en) | 1988-05-09 | 1988-05-09 | Absorption refrigerator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11293688A JPH0788988B2 (en) | 1988-05-09 | 1988-05-09 | Absorption refrigerator |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH01285751A true JPH01285751A (en) | 1989-11-16 |
JPH0788988B2 JPH0788988B2 (en) | 1995-09-27 |
Family
ID=14599202
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP11293688A Expired - Fee Related JPH0788988B2 (en) | 1988-05-09 | 1988-05-09 | Absorption refrigerator |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0788988B2 (en) |
-
1988
- 1988-05-09 JP JP11293688A patent/JPH0788988B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JPH0788988B2 (en) | 1995-09-27 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
LAPS | Cancellation because of no payment of annual fees |