JPS6269073A - Method of controlling absorption refrigerator - Google Patents

Method of controlling absorption refrigerator

Info

Publication number
JPS6269073A
JPS6269073A JP20966385A JP20966385A JPS6269073A JP S6269073 A JPS6269073 A JP S6269073A JP 20966385 A JP20966385 A JP 20966385A JP 20966385 A JP20966385 A JP 20966385A JP S6269073 A JPS6269073 A JP S6269073A
Authority
JP
Japan
Prior art keywords
temperature
regenerator
absorption
absorption liquid
exhaust gas
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
JP20966385A
Other languages
Japanese (ja)
Other versions
JPH0646122B2 (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 JP60209663A priority Critical patent/JPH0646122B2/en
Publication of JPS6269073A publication Critical patent/JPS6269073A/en
Publication of JPH0646122B2 publication Critical patent/JPH0646122B2/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
器に導入される吸収液量を増減するようにした吸収冷凍
機の制御方法に関する。
[Detailed Description of the Invention] [Field of Industrial Application] The present invention relates to a method of controlling an absorption refrigerator, and more particularly, to a method of controlling an absorption refrigerator that increases or decreases the amount of absorption liquid introduced into 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ず
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1は、
臭化リチウムの稀吸収液から多量の蒸気を濃度の高い吸
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。
Some absorption refrigerators have a regenerator equipped with a heating source, in which cold water or hot water can be obtained by receiving and receiving heat generated during repeated evaporation and condensation of an aqueous lithium bromide solution. In such an absorption refrigerator, 1 is
Since an absorption liquid with a large amount of vapor and a high concentration can be obtained from a dilute absorption liquid of lithium bromide, 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IM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(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
が溶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間匙がある。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 IM% sulfur will condense at about 140°C, and if the content is lower than that, condensation will occur. The dew point temperature also becomes lower. Therefore, if fuel with a high sulfur content is used, when the load is low (and the temperature of the heat absorption surface of the regenerator and exhaust gas decreases), condensation will easily occur on the heat absorption surface of the regenerator.The dew will contain sulfur dioxide gas. When melted, it becomes dilute sulfuric acid, which corrodes regenerators made of iron-based metals in a short period of time.Furthermore, unburned carbon and other substances adhere to the condensation, narrowing the exhaust gas passage and causing heating. The performance of the air blower is forced to deteriorate, leading to problems such as combustion abnormalities and a rapid increase in the amount of unburned carbon.

このような事態を回避するために、従来は再生器におけ
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
費が嵩む問題で、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 the regenerator, but this has led to high fuel costs, and improvements are being made. 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] 本発明の吸収冷凍機の制御方法の特徴とするところは、
再生器に導入される吸収液の液量を増減し、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、再生器
における収熱面での結露による障害を防止できるように
したことである。
[Structure of the Invention] The absorption chiller control method of the present invention is characterized by the following:
The amount of absorption liquid introduced into the regenerator can be increased or decreased to increase the pressure inside the regenerator and raise the temperature of the absorption liquid and heat absorption surface to prevent problems caused by condensation on the heat absorption surface of the regenerator. That's what I did.

〔作  用〕[For production]

圧力または温度センサなどで排気ガス温度が露点温度に
なったことを検出すると、再生器に供給される吸収液量
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、再生器
での吸収液の加熱が相対的に強められ、再生器内の吸収
液の濃度、温度および圧力は高くなる。その濃度、温度
、圧力に応じて収熱面の温度も上昇し、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
および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 or temperature sensor detects that the exhaust gas temperature has reached the dew point temperature, the amount of absorption liquid supplied to the regenerator is reduced. Since the burnup at the heating source is maintained as long as the withdrawal temperature of cold or hot water remains unchanged, the heating of the absorption liquid in the regenerator is relatively strengthened, and the concentration, temperature and pressure of the absorption liquid in the regenerator are high. Become. The temperature of the heat absorption surface increases according to its concentration, temperature, and pressure, and the temperature of the heat absorption surface is maintained above the dew point temperature of the exhaust gas, leading to corrosion on the heat absorption surface and an increase in the amount of unburned carbon attached. This avoids problems caused by

〔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適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 is 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.

このような高温再生器7内に温度センサ12ガ(取付け
られ、排ガスまたは収熱面の温度が使用燃料の硫黄含有
率に基づく露点温度になったことを検出できるようにな
っている。一方、高温再生器7に吸収液を導入する管路
13には、吸収液を移送するための吸収液ポンプ14と
流量調整弁15が介在されている。この流量調整弁は温
度センサ12からの温度信号に応じてその開度を変える
ものであり、高温再生器7に導入される吸収液の液量を
減少させることによって、高温再生器7内の吸収液の濃
度、温度および圧力を高めることができるようになって
いる。なお、吸収液ポンプ14が可変容量型であれば、
流量調整弁15を設けることなく、温度センサ12から
の信号でその吐出量を変えることができる。ちなみに、
このような温度の検出による方法に代えて、圧力センサ
17からの信号で吸収液量を調整してもよい。
A temperature sensor 12 (attached to such a high-temperature regenerator 7) can detect when the temperature of the exhaust gas or the heat absorption surface has reached the dew point temperature based on the sulfur content of the fuel used. An absorption liquid pump 14 for transferring the absorption liquid and a flow rate adjustment valve 15 are interposed in the pipe line 13 that introduces the absorption liquid into the high temperature regenerator 7. This flow rate adjustment valve receives a temperature signal from the temperature sensor 12. The opening degree is changed according to the temperature, and by reducing the amount of absorption liquid introduced into the high-temperature regenerator 7, the concentration, temperature, and pressure of the absorption liquid in the high-temperature regenerator 7 can be increased. If the absorption liquid pump 14 is a variable displacement type,
The discharge amount can be changed by the signal from the temperature sensor 12 without providing the flow rate adjustment valve 15. By the way,
Instead of such a method based on temperature detection, the amount of absorption liquid may be adjusted using a signal from the pressure sensor 17.

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は吸収液ポンプ、29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 is an absorption liquid pump, and 29 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、収熱面の温度も
高く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、収熱面および排ガス
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、管路13に設けられている流量調整弁
15の開度が小さくされ、高温再生器7に導入される吸
収液の液量が減少される。したがって、高温再生器7か
ら気液分離器8に導入される吸収液の濃度、温度および
圧力が高められるので、収熱面の温度を高め排ガス温度
も上昇し、排ガスが結露しない例えば140℃以上の温
度に維持される。
In the cooling and heating cycles, if the load on the absorption water cooler/heater is large, even if oil with a high sulfur content is used as fuel, the burnup in the heating source 6 will be high, so the temperature of the heat absorption surface will be high, and the exhaust gas will be at a high temperature. There is no condensation on the heat absorption surface of the regenerator 7. 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 heat absorption surface and exhaust gas temperature are also reduced. When the temperature sensor 12 provided in the high temperature regenerator 7 etc. detects that the dew point temperature has been reached, the opening degree of the flow rate regulating valve 15 provided in the pipe line 13 is reduced in accordance with the detection signal. The amount of absorption liquid introduced into the high temperature regenerator 7 is reduced. Therefore, the concentration, temperature, and pressure of the absorption liquid introduced from the high-temperature regenerator 7 to the gas-liquid separator 8 are increased, so the temperature of the heat absorption surface is increased and the exhaust gas temperature is also increased, so that the exhaust gas does not condense, for example, 140° C. or higher. maintained at a temperature of

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
、結露による腐蝕などの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、例示以外の吸収冷温水機についても、本発
明を適用することができることは言うまでもない。
If such control is performed appropriately when the load decreases, condensation in the exhaust gas flowing through the high-temperature regenerator can be avoided even when fuel with a high sulfur content is used, and even when cheap fuel is used, condensation can be avoided. It is possible to prevent problems such as corrosion due to Note that the absorption chiller/heater is not limited to the illustrated example, and the present invention is also applicable to absorption chiller/heater other than the illustrated one as long as it is equipped with a regenerator having a heating source that burns fuel. Needless to say, it can be done.

もちろん、高温再生器に導入される吸収液量の制御につ
いては、冷凍サイクルにおいて適用されるので、少なく
とも吸収冷凍機能を有するものであればよく、上述した
ような吸収冷温水機に限らず、一般に吸収ヒートポンプ
を含む吸収冷凍機に適用することができる。
Of course, since control of the amount of absorption liquid introduced into the high-temperature regenerator is applied in the refrigeration cycle, it is sufficient that it has at least an absorption refrigeration function, and is not limited to the above-mentioned absorption chiller/heater. It can be applied to absorption refrigerators including absorption heat pumps.

〔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、再生器内における
排ガス温度に応じて、再生器に導入される吸収液の液量
を増減させることにより、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 explained in detail above, the present invention maintains the pressure or temperature above a set value by increasing or decreasing the amount of absorption liquid introduced into the regenerator according to the exhaust gas temperature within the regenerator. Therefore, 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・一温度センサ、
14・−・吸収液ポンプ、15・−・流量調整弁、l’
l−圧力センサ。
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--
・Heating source, 7...-high temperature regenerator, 12.-1 temperature sensor,
14... Absorption liquid pump, 15... Flow rate adjustment valve, l'
l - Pressure sensor.

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、 前記再生器に導入される吸収液の液量を増減し、その再
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
ることにより排ガス温度を上昇させ、収熱面での結露に
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 heating source in addition to an absorber, a condenser, and an evaporator, the amount of absorption liquid introduced into the regenerator is increased or decreased, and A control for an absorption chiller characterized by increasing the pressure in the regenerator and increasing the temperature of the absorption liquid and the heat absorption surface to increase the temperature of the exhaust gas, thereby preventing troubles due to condensation on the heat absorption surface. Method.
JP60209663A 1985-09-20 1985-09-20 Control method for double-effect absorption refrigerator Expired - Lifetime JPH0646122B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60209663A JPH0646122B2 (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
JP60209663A JPH0646122B2 (en) 1985-09-20 1985-09-20 Control method for double-effect absorption refrigerator

Publications (2)

Publication Number Publication Date
JPS6269073A true JPS6269073A (en) 1987-03-30
JPH0646122B2 JPH0646122B2 (en) 1994-06-15

Family

ID=16576540

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60209663A Expired - Lifetime JPH0646122B2 (en) 1985-09-20 1985-09-20 Control method for double-effect absorption refrigerator

Country Status (1)

Country Link
JP (1) JPH0646122B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02101354A (en) * 1988-10-05 1990-04-13 Sanyo Electric Co Ltd Method for controlling absorptive type freezer

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS602862A (en) * 1983-06-20 1985-01-09 株式会社荏原製作所 Direct fire type double effect absorption cold and hot watermachine

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS602862A (en) * 1983-06-20 1985-01-09 株式会社荏原製作所 Direct fire type double effect absorption cold and hot watermachine

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02101354A (en) * 1988-10-05 1990-04-13 Sanyo Electric Co Ltd Method for controlling absorptive type freezer

Also Published As

Publication number Publication date
JPH0646122B2 (en) 1994-06-15

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