JPS6269074A - Method of controlling absorption refrigerator - Google Patents

Method of controlling absorption refrigerator

Info

Publication number
JPS6269074A
JPS6269074A JP20966485A JP20966485A JPS6269074A JP S6269074 A JPS6269074 A JP S6269074A JP 20966485 A JP20966485 A JP 20966485A JP 20966485 A JP20966485 A JP 20966485A JP S6269074 A JPS6269074 A JP S6269074A
Authority
JP
Japan
Prior art keywords
regenerator
temperature
absorption
exhaust gas
heat
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
Application number
JP20966485A
Other languages
Japanese (ja)
Other versions
JPH0670539B2 (en
Inventor
高畠 修藏
金谷 利彦
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Kawaju Reinetsu Kogyo KK
Original Assignee
Kawaju Reinetsu Kogyo KK
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Kawaju Reinetsu Kogyo KK filed Critical Kawaju Reinetsu Kogyo KK
Priority to JP20966485A priority Critical patent/JPH0670539B2/en
Publication of JPS6269074A publication Critical patent/JPS6269074A/en
Publication of JPH0670539B2 publication Critical patent/JPH0670539B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Sorption Type Refrigeration Machines (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は吸収冷凍機の制御方法に関し、詳しくは、再生
器の蒸気出口に設けられた開度調整弁の開度を調整する
制御方法に関する。
[Detailed Description of the Invention] [Field of Industrial Application] The present invention relates to a control method for an absorption refrigerator, and more particularly, to a control method for adjusting the opening of an opening adjustment valve provided at a steam outlet of a regenerator. .

〔従来技術〕[Prior art]

臭化リチウム水溶液が蒸発や凝縮を繰り返す間に発生す
る熱の授受により冷水や温水を得ることができるように
なっている吸収冷凍機においては、加熱源を備えた再生
器を有するものがある。このような吸収冷凍機では、臭
化リチウムの稀吸収液から多量の蒸気と濃度の高い吸収
液が得られるので、吸収冷凍機の性能の向上を図ること
ができる。
BACKGROUND ART Among absorption refrigerators that can obtain cold water or hot water by receiving and receiving heat generated during repeated evaporation and condensation of a lithium bromide aqueous solution, some have a regenerator equipped with a heating source. In such an absorption refrigerator, a large amount of vapor and a highly concentrated absorption liquid can be obtained from a dilute absorption liquid of lithium bromide, so that the performance of the absorption refrigerator can be improved.

ところで、加熱器における燃焼度は、得られた冷水また
は温水の温度に応じて制御されるようになっていて、負
荷が高ければ再生器における加熱が強められ、再生器を
介して排気される排ガス温度は高くなる。一方、負荷が
低いと加熱器での燃焼度が弱められるので、再生器を流
過する排ガス温度も低下する。加熱源で使用される燃料
に含まれる硫黄分などが少ない場合には問題とならない
が、かなりの量の硫黄分などが含まれていると、亜硫酸
ガスおよび未燃分などを伴った排ガスが再生器を流過す
ることになる。燃焼ガスの露点温度は燃料に含有される
硫黄量などにより異なることはよく知られており、例え
ば1重量%の硫黄分を含む燃料では約140℃で結露し
、それより含有率が低くければ露点温度も低くなる。し
たがって、硫黄分などの多い燃料を使用すれば、負荷が
低くて再生器の収熱面および排気ガス温度が下ったとき
再生器の収熱面で結露し易くなる。その露に亜硫酸ガス
が熔けると希硫酸となり、鉄系金属で製作されている再
生器が短時間で腐蝕する問題がある。また、その結露に
未燃炭素分などが付着して排ガス通路が狭められ、加熱
のための送風機の性能低下が余儀なくされ、燃焼異常を
誘発して未燃炭素の発生が急増する問題なども生じる。
By the way, the burnup in the heater is controlled according to the temperature of the obtained cold water or hot water, and if the load is high, the heating in the regenerator is increased, and the exhaust gas exhausted through the regenerator is The temperature increases. On the other hand, when the load is low, the burn-up in the heater is weakened, so the temperature of the exhaust gas flowing through the regenerator also decreases. This is not a problem if the sulfur content contained in the fuel used in the heating source is small, but if it contains a considerable amount of sulfur content, exhaust gas containing sulfur dioxide gas and unburned substances may be regenerated. It will flow through the vessel. It is well known that the dew point temperature of combustion gas varies depending on the amount of sulfur contained in the fuel. For example, a fuel containing 1% by weight of sulfur will condense at approximately 140°C, and if the content is lower than that, condensation will occur. The dew point temperature also becomes lower. Therefore, if a fuel with a high sulfur content is used, dew condensation is likely to occur on the heat absorption surface of the regenerator when the load is low and the temperature of the heat absorption surface of the regenerator and the exhaust gas decrease. When the sulfur dioxide gas melts in the dew, it becomes dilute sulfuric acid, which causes the problem that regenerators made of iron-based metals corrode in a short period of time. In addition, unburned carbon and other substances adhere to the condensation, narrowing the exhaust gas passage, forcing the performance of the blower for heating to deteriorate, causing combustion abnormalities, and causing problems such as a rapid increase in the generation of unburned carbon. .

このような事態を回避するために、従来は高温再生器に
おける加熱用燃料として、硫黄分の少ない良質の重油や
灯油、さらには都市ガスなどといったものが使用され、
燃料費が嵩む問題があり、その改善が望まれている。
To avoid this situation, conventionally, high-quality heavy oil with low sulfur content, kerosene, or even city gas have been used as heating fuel in high-temperature regenerators.
There is a problem of rising fuel costs, and improvement is desired.

〔発明の目的〕[Purpose of the invention]

本発明は上述の問題に鑑みなされたもので、その目的は
、加熱源において硫黄分などの排ガスの露点を降下させ
る成分の多い燃料を使用しても、再生器での結露による
腐蝕や未燃炭素分などの付着を回避し、安価な燃料で稼
働させることができる吸収冷凍機の制御方法を提供する
ことである。
The present invention was made in view of the above-mentioned problems, and its purpose is to prevent corrosion and unburned fuel from condensation in the regenerator even if a fuel containing a large amount of components such as sulfur that lowers the dew point of exhaust gas is used in the heating source. It is an object of the present invention to provide a control method for an absorption refrigerating machine that can avoid adhesion of carbon components and the like and can be operated with inexpensive fuel.

〔発明の構成〕[Structure of the invention]

本発明の吸収冷凍機の制御方法の特徴とするところは、
再生器の蒸気出口部の開度調整弁の開度を増減すること
により、前記再生器内の圧力を高めて吸収液および収熱
面の温度を高め、排ガスが流過する収熱面で燃焼ガスの
結露による障害を防止できるようにしたことである。
The characteristics of the absorption chiller control method of the present invention are as follows:
By increasing or decreasing the opening degree of the opening adjustment valve at the steam outlet of the regenerator, the pressure inside the regenerator is increased, the temperature of the absorption liquid and the heat absorption surface is increased, and combustion occurs on the heat absorption surface through which the exhaust gas flows. This prevents problems caused by gas condensation.

〔作  用〕[For production]

圧力センサまたは温度センサなどで排気ガスが露点温度
になったことを検出すると、再生器の蒸気出口部に設け
られた開度調整弁の開度が減少される。加熱源における
燃焼度は冷水または温水の取出し温度が変わらない限り
維持されるので、気液分離器内の蒸気圧力の上昇に応じ
て吸収液温度が高められることで、収熱面の温度も上昇
し、再生器の排ガス温度が上昇される。したがって、再
生器における収熱面の温度が排ガスの露点温度以上に保
持され、収熱面での腐蝕などや未燃炭素などの付着量の
増加による障害が回避される。
When a pressure sensor, a temperature sensor, or the like detects that the exhaust gas has reached the dew point temperature, the opening of the opening adjustment valve provided at the steam outlet of the regenerator is reduced. The burnup at the heating source is maintained as long as the temperature at which cold water or hot water is taken out remains unchanged, so as the steam pressure in the gas-liquid separator increases, the temperature of the absorption liquid increases, which also increases the temperature of the heat absorption surface. However, the exhaust gas temperature of the regenerator is increased. Therefore, the temperature of the heat absorption surface in the regenerator is maintained above the dew point temperature of the exhaust gas, and problems such as corrosion on the heat absorption surface and increased adhesion of unburned carbon are avoided.

〔実施例〕〔Example〕

以下に本発明を吸収冷凍作用を行なう吸収冷温水機の一
実施例に基づいて詳細に説明する。
The present invention will be described in detail below based on an embodiment of an absorption chiller/heater that performs absorption refrigeration.

第1図は本発明の制御方法が通用される吸収冷温水機の
一例の全体系統図で、真空容器1a、1bに吸収器2、
低温再生器3、凝縮器4、蒸発器5がそれぞれ形成され
、これらに加えて加熱源6を備えた高温再生器7が設け
られている。さらに、その高温再生器で加熱された気液
混合状態の吸収液から蒸気と濃吸収液を分離する気液分
離器8が、低温再生器3との間に設けられている。高温
再生器7においては加熱源6で燃料が焚かれるので、そ
の排ガスが排気筒9から排出されるようになっている。
FIG. 1 is an overall system diagram of an example of an absorption chiller/heater to which the control method of the present invention can be applied.
A low-temperature regenerator 3, a condenser 4, and an evaporator 5 are each formed, and in addition to these, a high-temperature regenerator 7 equipped with a heating source 6 is provided. Furthermore, a gas-liquid separator 8 is provided between the low-temperature regenerator 3 and the low-temperature regenerator 3, which separates vapor and concentrated absorption liquid from the gas-liquid mixed absorption liquid heated by the high-temperature regenerator. In the high-temperature regenerator 7, the heating source 6 burns the fuel, and the exhaust gas is discharged from the exhaust pipe 9.

上述の構成に加えて、高温再生器7での結露を防止する
ために、気液分離器8の蒸気出口部に開度調整弁19が
取付けられ、気液分離器8内の蒸気圧力により高温再生
器7の圧力が増減される。
In addition to the above-mentioned configuration, in order to prevent dew condensation in the high-temperature regenerator 7, an opening adjustment valve 19 is installed at the steam outlet of the gas-liquid separator 8. The pressure in the regenerator 7 is increased or decreased.

なお、気液分離器8または蒸気管16に圧力センサ17
が設けられている。上述の開度調整弁19は、その圧力
センサ17からの信号に応じてその開度を変えるもので
、この蒸気圧力は溶液温度に比例することから温度を検
出する代わりに採用されるものであるが、図示したよう
に温度センサI2を設け、これからの信号を受けて開度
調整弁19の開度を調整するようにしてもよい。
Note that a pressure sensor 17 is installed in the gas-liquid separator 8 or the steam pipe 16.
is provided. The above-mentioned opening adjustment valve 19 changes its opening according to the signal from the pressure sensor 17, and since this vapor pressure is proportional to the solution temperature, it is used instead of detecting the temperature. However, as shown in the figure, a temperature sensor I2 may be provided, and the opening degree of the opening adjustment valve 19 may be adjusted in response to a signal from the temperature sensor I2.

本実施例における図中の25は吸収器2内の稀吸収液2
6を加熱する熱交換器、27は管路13を流過する吸収
液を加熱する熱交換器である。各熱交換器の加熱側には
、低温再生器3からの吸収液および気液分離器8からの
濃吸収液が供給され、熱交換器25.27で放熱した後
の吸収液が、吸収器2内で散布されるようになっている
。28および29は吸収液ポンプ、30は冷媒ポンプで
ある。
In this example, 25 in the figure is the dilute absorption liquid 2 in the absorber 2.
A heat exchanger 27 heats the absorption liquid flowing through the pipe line 13. The absorption liquid from the low-temperature regenerator 3 and the concentrated absorption liquid from the gas-liquid separator 8 are supplied to the heating side of each heat exchanger. It is designed to be distributed within 2. 28 and 29 are absorption liquid pumps, and 30 is a refrigerant pump.

このような構成の吸収冷温水機においては、以下のよう
な稼働状態において、所定の制御がなされ、高温再生器
7における収熱面での結露が防止される。
In the absorption chiller/heater having such a configuration, predetermined control is performed in the following operating conditions to prevent dew condensation on the heat absorption surface of the high temperature regenerator 7.

冷房および暖房サイクルにおいて、吸収冷温水機の負荷
が大きいと、燃料に硫黄分の多い油が用いられていても
、加熱源6における燃焼度が高いので、排ガスが高温再
生器7の収熱面などで結露することはない。一方、負荷
が小さくなると、高温再生器7における加熱源6の燃焼
度が低下され、排ガス温度も下がる。高温再生器7内な
どに設けられた温度センサ12が露点温度になったこと
を検出すると、その検出信号に応じて、低温再生器3の
蒸気入口部に設けられた開度調整弁19の開度が小さく
される。その結果、気液分離器8における蒸気圧力が保
持され、その圧力に対応する溶液温度としてたとえば1
40℃が収熱面で維持され、高温再生器7における収熱
面での結露が防止される。
In the cooling and heating cycles, when the load on the absorption chiller/heater is large, even if oil with a high sulfur content is used as fuel, the burnup in the heating source 6 is high, so that the exhaust gas flows into the heat absorption surface of the high temperature regenerator 7. There will be no condensation. On the other hand, when the load becomes smaller, the burnup of the heating source 6 in the high-temperature regenerator 7 is reduced, and the exhaust gas temperature is also reduced. When the temperature sensor 12 installed in the high-temperature regenerator 7 detects that the dew point temperature has been reached, the opening adjustment valve 19 installed at the steam inlet of the low-temperature regenerator 3 is opened in response to the detection signal. degree is reduced. As a result, the vapor pressure in the gas-liquid separator 8 is maintained, and the solution temperature corresponding to the pressure is, for example, 1
40° C. is maintained on the heat absorption surface, and dew condensation on the heat absorption surface of the high temperature regenerator 7 is prevented.

このような制御が負荷の減少した場合に適宜行なわれる
と、硫黄分などの多い燃料であっても高温再生器を流過
する排ガスの結露が回避され、安価な燃料を使用しても
、腐蝕などによるトラブルを防止することができる。な
お、吸収冷温水機としては図示の例に限らず、燃料を燃
焼させるような加熱源を有する再生器を備えたものであ
れば、例示以外の吸収ヒー トポンプを含む吸収冷温水
機についても、本発明を通用することができることは言
うまでもない。
If such control is carried out appropriately when the load is reduced, condensation of the exhaust gas flowing through the high-temperature regenerator will be avoided even when using fuel with a high sulfur content, and even when using cheap fuel, corrosion will not occur. It is possible to prevent troubles caused by such problems. Note that the absorption chiller/heater is not limited to the illustrated example, but may also include absorption chiller/heater including an absorption heat pump other than the illustrated one, as long as it is equipped with a regenerator that has a heating source that burns fuel. It goes without saying that the present invention can be applied.

〔発明の効果〕〔Effect of the invention〕

本発明は以上詳細に説明したように、再生器の蒸気圧力
または溶液温度などを、再生器の排ガス温度などに応じ
て、再生器の蒸気出口部から導出される蒸気に差圧をつ
けて、圧力または温度を設定値以上に保持するようにし
たので、加熱源の排ガスおよび再生器の収熱面を露点温
度以下に低下するのを防止することができる。したがっ
て、再生器を流過する排ガスの結露が回避され、その収
熱面での腐蝕などや結露による未燃炭素分などの付着に
よる障害が防止される効果が発揮される。
As described in detail above, the present invention adjusts the steam pressure or solution temperature of the regenerator in accordance with the exhaust gas temperature of the regenerator, etc. by applying a pressure difference to the steam led out from the steam outlet of the regenerator, Since the pressure or temperature is maintained above the set value, it is possible to prevent the exhaust gas of the heating source and the heat absorption surface of the regenerator from dropping below the dew point temperature. Therefore, dew condensation of the exhaust gas flowing through the regenerator is avoided, and the effect of preventing damage caused by corrosion on the heat absorption surface and adhesion of unburned carbon components due to dew condensation is exhibited.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は本発明が通用される吸収冷温水機の一実施例系
統図である。 2−・吸収器、4−凝縮器、5−・蒸発器、6−・・加
熱源、7−高温再生器、12−・温度センサ、17−圧
力センサ、19・・−開度調整弁。
FIG. 1 is a system diagram of an embodiment of an absorption chiller/heater to which the present invention is applied. 2--absorber, 4--condenser, 5--evaporator, 6--heat source, 7--high temperature regenerator, 12--temperature sensor, 17-pressure sensor, 19--opening adjustment valve.

Claims (1)

【特許請求の範囲】[Claims] (1)吸収器、凝縮器、蒸発器に加えて、加熱源を備え
た再生器を有する吸収ヒートポンプを含む吸収冷凍機に
おいて、 前記再生器の蒸気出口部の開度調整弁の開度を増減する
ことにより、前記再生器内の圧力を高めて吸収液および
収熱面の温度を高め、排ガスが流過する収熱面で燃焼ガ
スの結露による障害を防止できるようにしたことを特徴
とする吸収冷凍機の制御方法。
(1) In an absorption refrigerator including an absorption heat pump that has a regenerator equipped with a heat source in addition to an absorber, a condenser, and an evaporator, increasing or decreasing the opening of the opening adjustment valve at the steam outlet of the regenerator. By doing so, the pressure within the regenerator is increased to increase the temperature of the absorbing liquid and the heat absorption surface, thereby making it possible to prevent problems due to condensation of combustion gas on the heat absorption surface through which exhaust gas flows. How to control an absorption refrigerator.
JP20966485A 1985-09-20 1985-09-20 Control method for double-effect absorption refrigerator Expired - Lifetime JPH0670539B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20966485A JPH0670539B2 (en) 1985-09-20 1985-09-20 Control method for double-effect absorption refrigerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20966485A JPH0670539B2 (en) 1985-09-20 1985-09-20 Control method for double-effect absorption refrigerator

Publications (2)

Publication Number Publication Date
JPS6269074A true JPS6269074A (en) 1987-03-30
JPH0670539B2 JPH0670539B2 (en) 1994-09-07

Family

ID=16576558

Family Applications (1)

Application Number Title Priority Date Filing Date
JP20966485A Expired - Lifetime JPH0670539B2 (en) 1985-09-20 1985-09-20 Control method for double-effect absorption refrigerator

Country Status (1)

Country Link
JP (1) JPH0670539B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2921468A1 (en) * 2007-09-25 2009-03-27 Peugeot Citroen Automobiles Sa METHOD FOR CALCULATING AND REGULATING ABSORBENT FLUID CONCENTRATION IN ABSORPTION AIR CONDITIONING DEVICE, AND ABSORPTION AIR CONDITIONING DEVICE FOR IMPLEMENTING SUCH METHOD

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2921468A1 (en) * 2007-09-25 2009-03-27 Peugeot Citroen Automobiles Sa METHOD FOR CALCULATING AND REGULATING ABSORBENT FLUID CONCENTRATION IN ABSORPTION AIR CONDITIONING DEVICE, AND ABSORPTION AIR CONDITIONING DEVICE FOR IMPLEMENTING SUCH METHOD
WO2009044034A1 (en) * 2007-09-25 2009-04-09 Peugeot Citroën Automobiles SA Method for calculating and adjusting the concentration of absorbing fluid in an absorption air conditioning device, and absorption air conditioning device for implementing said method
US8505319B2 (en) 2007-09-25 2013-08-13 Peugeot Citroën Automobiles SA Method for calculating and adjusting the concentration of absorbing fluid in an absorption air conditioning device, and absorption air conditioning device for implementing said method

Also Published As

Publication number Publication date
JPH0670539B2 (en) 1994-09-07

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