JP2008286441A - Absorption refrigerator - Google Patents

Absorption refrigerator Download PDF

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JP2008286441A
JP2008286441A JP2007130195A JP2007130195A JP2008286441A JP 2008286441 A JP2008286441 A JP 2008286441A JP 2007130195 A JP2007130195 A JP 2007130195A JP 2007130195 A JP2007130195 A JP 2007130195A JP 2008286441 A JP2008286441 A JP 2008286441A
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corrosion
electrodes
pair
absorption
absorption refrigerator
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Kenji Machizawa
健司 町澤
Yoichi Hirata
陽一 平田
Masahiko Ito
雅彦 伊藤
Hitoshi Yashiro
仁 八代
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Iwate University
Hitachi Building Systems Co Ltd
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Iwate University
Hitachi Building Systems Co Ltd
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    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A30/00Adapting or protecting infrastructure or their operation
    • Y02A30/27Relating to heating, ventilation or air conditioning [HVAC] technologies
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02BCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/62Absorption based systems

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  • Sorption Type Refrigeration Machines (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide an absorption refrigerator capable of surely detecting local corrosion. <P>SOLUTION: In this absorption refrigerator comprising at least devices of a regenerator, a condenser, an evaporator, an absorber, a heat exchanger and a pump, using the water or dilute lithium bromide as a refrigerant, and using lithium bromide aqueous solution including an inhibitor composed of oxygen acid salt and alkaline metal hydroxide as an absorbing solution, the purpose can be achieved by disposing a corrosion detecting means 14 detecting corrosion of component materials of inner walls of the device. The corrosion detecting means 14 is disposed in a state of being dipped in the absorbing solution in one or more devices of at least the regenerator, the absorber and the heat exchanger, and composed of at least a pair of electrodes 15, 16 composed of metal same as the component material of the inner walls of the devices, a current measuring means 19 for measuring electric current flowing between the pair of electrodes 15, 16, and a warning means 20 providing warning when the electric current measured by the current measuring means 19 is over a specific value determined in advance. <P>COPYRIGHT: (C)2009,JPO&INPIT

Description

本発明は、主に、ビルの空調に用いるのに好適な吸収式冷凍機に関するものである。   The present invention mainly relates to an absorption refrigerator suitable for use in building air conditioning.

近年、水を冷媒とし、かつ、臭化リチウム水溶液を吸収液として用いた吸収式冷凍機は、オゾン層の破壊原因となるフロンガスの使用が規制されてきたため、ビルの中大型空調用熱源機の主流となっている。そして、従来、吸収式冷凍機の吸収液として用いられる臭化リチウム水溶液は、腐食性が強いので、その臭化リチウム水溶液に、インヒビターと称する酸素酸塩及びアルカリ金属水酸化物からなる腐食抑制剤を添加(混入)することで、吸収式冷凍機の機器内壁を構成している炭素鋼(鉄鋼部材)の表面(壁面)に酸化皮膜を形成することにより、その炭素鋼(鉄鋼部材)の腐食を抑制するとともに、その炭素鋼(鉄鋼部材)の腐食に伴って水素ガスなどの不凝縮ガスが発生するのを抑制するようにしていた。   In recent years, absorption refrigerators that use water as a refrigerant and an aqueous lithium bromide solution as an absorbent have been restricted from using chlorofluorocarbons that cause ozone layer destruction. It has become mainstream. And since the aqueous solution of lithium bromide used as an absorption liquid for absorption refrigerators has been highly corrosive, a corrosion inhibitor comprising an oxyacid salt and an alkali metal hydroxide called an inhibitor in the aqueous solution of lithium bromide. Corrosion of the carbon steel (steel member) by forming an oxide film on the surface (wall surface) of the carbon steel (steel member) constituting the inner wall of the absorption refrigerator As well as suppressing the generation of non-condensable gases such as hydrogen gas along with the corrosion of the carbon steel (steel member).

ところで、インヒビターは、酸化剤として作用し、吸収式冷凍機の機器内壁を構成している炭素鋼(鉄鋼部材)の表面(壁面)に、酸化皮膜を形成するものであるため、酸化作用を果たした結果、還元されて、酸化作用、すなわち、酸化膜形成能力が消失してしまうものである。したがって、吸収液中で酸化皮膜の健全性が維持されない場合には、酸化皮膜が局部的に破壊されることで、腐食が開始される。   By the way, the inhibitor acts as an oxidant and forms an oxide film on the surface (wall surface) of the carbon steel (steel member) constituting the inner wall of the absorption refrigerator. As a result, it is reduced and the oxidation action, that is, the ability to form an oxide film disappears. Therefore, when the soundness of the oxide film is not maintained in the absorbing liquid, the oxide film is locally destroyed, and corrosion starts.

ところが、臭化リチウム水溶液中にインヒビターが十分に混入(添加)されている状態では、破壊された酸化皮膜が補修されることで、吸収式冷凍機の機器内壁を構成している炭素鋼(鉄鋼部材)の腐食が抑制されるが、臭化リチウム水溶液中のインヒビターの量が不足した状態では、破壊された酸化皮膜の補修が十分になされずに局部腐食が進行してしまい、やがて、吸収式冷凍機の機器内壁を構成している炭素鋼(鉄鋼部材)に貫通孔が形成されるという危険な状態に至る。   However, when the inhibitor is sufficiently mixed (added) in the lithium bromide aqueous solution, the broken oxide film is repaired, so that the carbon steel (steel) that forms the inner wall of the absorption refrigerator Corrosion of the component) is suppressed, but in the state where the amount of the inhibitor in the aqueous solution of lithium bromide is insufficient, the damaged oxide film is not sufficiently repaired, and the local corrosion proceeds. This leads to a dangerous state in which through holes are formed in the carbon steel (steel member) constituting the equipment inner wall of the refrigerator.

そこで、高温再生器に、化学的に不活性な測定電極を配置して、この測定電極の自然電位を計測し、この自然電位の値に基づいて吸収液のインヒビターの濃度を算出することで、そのインヒビターの濃度を管理することにより、吸収式冷凍機の機器内壁を構成している炭素鋼(鉄鋼部材)の腐食を抑制するようにした吸収式冷凍機が提案されている(例えば、特許文献1参照)。
特開平11−248301号公報
Therefore, by placing a chemically inert measuring electrode in the high-temperature regenerator, measuring the natural potential of this measuring electrode, and calculating the concentration of the inhibitor of the absorbing solution based on the value of this natural potential, An absorption refrigerator has been proposed in which the corrosion of carbon steel (steel member) constituting the inner wall of the absorption refrigerator is suppressed by controlling the concentration of the inhibitor (for example, patent document) 1).
JP-A-11-248301

しかし、上記特開平11−248301号公報に記載された吸収式冷凍機では、吸収液のインヒビターの濃度を管理することにより、吸収式冷凍機の機器内壁を構成している炭素鋼(鉄鋼部材)の腐食の進行を抑制することができても、その腐食の程度が局部腐食であるか否かを確認できないという問題があった。   However, in the absorption refrigerator described in JP-A-11-248301, the carbon steel (steel member) constituting the inner wall of the absorption refrigerator is managed by controlling the concentration of the inhibitor in the absorption liquid. Even if the progress of the corrosion can be suppressed, there is a problem that it cannot be confirmed whether or not the degree of the corrosion is a local corrosion.

本発明は、上述した従来技術における実状からなされたもので、その目的は吸収式冷凍機の機器内壁に発生した局部腐食を的確に検出することのできる吸収式冷凍機を提供することにある。   The present invention has been made from the above-described prior art, and an object of the present invention is to provide an absorption refrigerator that can accurately detect local corrosion occurring on the inner wall of the absorption refrigerator.

上記目的を達成するために、本発明は、再生器、凝縮器、蒸発器、吸収器、熱交換器及びポンプの機器を少なくとも備え、水若しくは希薄臭化リチウム水溶液を冷媒とし、かつ、酸素酸塩及びアルカリ金属水酸化物を含むインヒビターを混入した臭化リチウム水溶液を吸収液として用いてなる吸収式冷凍機において、前記機器内壁の構成材料の腐食を検知する腐食検出手段を設け、この腐食検出手段を、少なくとも前記再生器、吸収器若しくは熱交換器のいずれか一つ以上の機器内の吸収液中に浸漬するように設置されて前記機器内壁の構成材料と同一金属からなる少なくとも一対の電極と、この一対の電極間を流れる電流を測定する電流測定手段と、この電流測定手段によって測定された電流が予め設定した所定値を超えた場合に警報を発する警報手段とが包含される構成としたことを特徴とするものである。   In order to achieve the above object, the present invention comprises at least a regenerator, a condenser, an evaporator, an absorber, a heat exchanger, and a pump, and water or a diluted lithium bromide aqueous solution as a refrigerant, and an oxygen acid In an absorption refrigerator using an aqueous solution of lithium bromide mixed with an inhibitor containing a salt and an alkali metal hydroxide as an absorbing solution, a corrosion detecting means is provided for detecting corrosion of the constituent material of the inner wall of the device, and this corrosion detection is provided. And at least a pair of electrodes made of the same metal as the constituent material of the inner wall of the device, wherein the means is immersed in an absorbing liquid in at least one of the regenerator, the absorber and the heat exchanger. Current measuring means for measuring the current flowing between the pair of electrodes, and an alarm is generated when the current measured by the current measuring means exceeds a predetermined value. It is characterized in that the alarm means is configured to be encompassed that.

さらに、本発明は、前記電流測定手段は、前記一対の電極間を流れる電流の絶対値を検知するゼロシャント電流計から少なくとも構成したことを特徴とするものである。   Furthermore, the present invention is characterized in that the current measuring means comprises at least a zero shunt ammeter that detects an absolute value of a current flowing between the pair of electrodes.

さらに、本発明は、前記一対の電極の材質を、前記機器内壁の構成材料に合わせて、炭素鋼、銅、キュプロニッケル、ステンレス鋼,ロウ材のいずれかとしたことを特徴とするものである。   Furthermore, the present invention is characterized in that the material of the pair of electrodes is any one of carbon steel, copper, cupronickel, stainless steel, and brazing material according to the constituent material of the inner wall of the device.

本発明によれば、機器内の吸収液中に浸漬するように設置されて機器内壁の構成材料と同一金属からなる一対の電極と、この一対の電極間を流れる電流を測定する電流測定手段と、この電流測定手段によって測定された電流が予め設定した所定値を超えた場合に警報を発する警報手段とを少なくとも備えてなる腐食検出手段を設けることにより、吸収式冷凍機の機器内壁に発生した局部腐食を的確に検出することを可能にし、その機器内壁に貫通孔が形成されるという危険な状態の発生を阻止できる吸収式冷凍機が得られる。   According to the present invention, a pair of electrodes that are installed so as to be immersed in the absorbent in the device and are made of the same metal as the constituent material of the device inner wall, and a current measuring unit that measures a current flowing between the pair of electrodes, The corrosion detection means comprising at least an alarm means for issuing an alarm when the current measured by the current measurement means exceeds a preset predetermined value is generated on the inner wall of the absorption chiller device. It is possible to obtain an absorption refrigerator capable of accurately detecting local corrosion and preventing the occurrence of a dangerous state in which a through hole is formed in the inner wall of the device.

以下、本発明に係る吸収式冷凍機の一実施形態を、図1及び図2に基づいて説明する。図1は、本発明の一実施形態に係る吸収式冷凍機の要部構成説明図である。図2は、本発明の一実施形態に係る吸収式冷凍機の腐食電流に関する実験結果を示す図である。   Hereinafter, an embodiment of an absorption refrigerator according to the present invention will be described with reference to FIGS. 1 and 2. FIG. 1 is an explanatory view of a main part configuration of an absorption refrigerator according to an embodiment of the present invention. FIG. 2 is a diagram showing experimental results regarding the corrosion current of the absorption refrigerator according to the embodiment of the present invention.

図1に示す本発明の一実施形態に係る密閉真空系の吸収式冷凍機1は、二重効用吸収式冷凍機であって、高温再生器2B及び低温再生器2Aからなる再生器2、凝縮器3、蒸発器4、吸収器5、熱交換器6並びに第1ポンプ7A及び第2ポンプ7Bからなるポンプ7を、少なくとも備えている。   A hermetic vacuum type absorption refrigerator 1 according to an embodiment of the present invention shown in FIG. 1 is a double-effect absorption refrigerator, and includes a regenerator 2 composed of a high temperature regenerator 2B and a low temperature regenerator 2A, a condensing unit. And at least a pump 7 including an evaporator 3, an evaporator 4, an absorber 5, a heat exchanger 6, and a first pump 7A and a second pump 7B.

吸収式冷凍機1内には、水からなる冷媒X1と臭化リチウム水溶液からなる吸収液Y1が、封入されている。臭化リチウム水溶液からなる吸収液Y1には、酸素酸塩及びアルカリ金属水酸化物などからなるインヒビター(腐食抑制材)が混入(添加)されている。吸収式冷凍機1の機内は、通常大気圧以下に設定されて作動するようにしてある。   In the absorption refrigerator 1, a refrigerant X1 made of water and an absorption liquid Y1 made of a lithium bromide aqueous solution are enclosed. In the absorbent Y1 made of an aqueous lithium bromide solution, an inhibitor (a corrosion inhibitor) made of an oxyacid salt, an alkali metal hydroxide, or the like is mixed (added). The interior of the absorption chiller 1 is normally set to operate at atmospheric pressure or lower.

蒸発器4は、図1に示すように、多数の蒸発用管体8を有し、これら蒸発用管体8に冷水送込み用配管9及び冷水戻り用配管9Aが連結されており、蒸発用管体8外周に散水ノズル10で冷媒X1を散布することによって、蒸発用管体8内を流れる冷水W1から気化熱により熱を奪う機能を有している。冷媒X1は、第2ポンプ7Bによって散水ノズル10に送られる。蒸発器4内は、真空に保持されている。   As shown in FIG. 1, the evaporator 4 has a large number of evaporation pipes 8, and these evaporation pipes 8 are connected with a chilled water feed pipe 9 and a chilled water return pipe 9 </ b> A. By spraying the refrigerant X1 on the outer periphery of the tubular body 8 with the watering nozzle 10, it has a function of removing heat from the cold water W1 flowing in the evaporation tubular body 8 by heat of vaporization. The refrigerant X1 is sent to the watering nozzle 10 by the second pump 7B. The inside of the evaporator 4 is kept in a vacuum.

吸収器5は、蒸発器4で発生した冷媒X1の蒸気を吸収する。このとき、発生した熱は、吸収器5の多数の吸収用管体11内を流れる冷却水W2によって冷却される。吸収用管体11には、冷却水送込み用配管12及び冷却水戻り用配管12Aが連結されている。   The absorber 5 absorbs the vapor of the refrigerant X1 generated in the evaporator 4. At this time, the generated heat is cooled by the cooling water W <b> 2 flowing through the numerous absorption tubes 11 of the absorber 5. A cooling water feed pipe 12 and a cooling water return pipe 12 </ b> A are connected to the absorption pipe body 11.

吸収器5で冷媒X1の蒸気を吸収して臭化リチウム濃度の低下した吸収液(低温の希薄溶液)Y1は、第1ポンプ7Aにより、一部が高温再生器2Bに送られて、ガスバーナー、蒸気などの加熱源によって加熱濃縮される。加熱により発生した高温の冷媒蒸気X2は、低温再生器2Aの加熱管内に導かれて、臭化リチウム濃度の低下した吸収液Y1を加熱することにより、臭化リチウム濃度の高い吸収液(高温の濃厚溶液)Y2にする。臭化リチウム濃度が高くなった吸収液Y2は、熱交換器6を介して蒸発器4に戻るようにしてある。   A part of the absorbing liquid (low-temperature dilute solution) Y1 having a reduced lithium bromide concentration by absorbing the vapor of the refrigerant X1 by the absorber 5 is sent to the high-temperature regenerator 2B by the first pump 7A, and the gas burner It is heated and concentrated by a heating source such as steam. The high-temperature refrigerant vapor X2 generated by heating is introduced into the heating pipe of the low-temperature regenerator 2A, and the absorption liquid Y1 with a low lithium bromide concentration is heated to heat the absorption liquid (high-temperature lithium bromide concentration). Concentrated solution) Y2. The absorbing liquid Y2 having a high lithium bromide concentration is returned to the evaporator 4 via the heat exchanger 6.

低温再生器2Bの加熱管内に導かれた冷媒蒸気X2は、凝縮器3に導かれると、その凝縮器3の冷却水管13内を流れる冷却水W2によって冷却され、冷媒X1となって、蒸発器4に戻るようにしてある。   When the refrigerant vapor X2 led into the heating pipe of the low-temperature regenerator 2B is led to the condenser 3, it is cooled by the cooling water W2 flowing through the cooling water pipe 13 of the condenser 3 to become the refrigerant X1, and the evaporator Return to 4.

第1ポンプ7Aは、臭化リチウム濃度の低下した吸収液Y1を循環させる駆動源となる。第1ポンプ7Aは、入口側が吸収器5の底部に、かつ、出口側が熱交換器6内の熱交換用配管6Aに、それぞれ接続されている。熱交換器6は、第1配管21により高温再生器2Bに、かつ、第2配管22により低温再生器2Aに、それぞれ接続されている。   The first pump 7A serves as a driving source for circulating the absorbing liquid Y1 having a reduced lithium bromide concentration. The first pump 7 </ b> A has an inlet side connected to the bottom of the absorber 5 and an outlet side connected to a heat exchange pipe 6 </ b> A in the heat exchanger 6. The heat exchanger 6 is connected to the high temperature regenerator 2 </ b> B by the first pipe 21 and to the low temperature regenerator 2 </ b> A by the second pipe 22.

第2ポンプ7Bは、水からなる冷媒X1を循環させる駆動源となる。第2ポンプ7Bは、入口側が凝縮器3及び蒸発器4からの冷媒戻り配管23に、かつ、出口側が散水用配管24に、それぞれ接続されている。低温再生器2Aと熱交換器6とは、第3配管25により接続されている。吸収器5と熱交換器6とは、第4配管26により接続されている。高温再生器2Bには、その高温再生器2Bで発生した高温の冷媒蒸気X2を、低温再生器2Aの加熱管内に導く第5配管27が設けられている。低温再生器2ABと凝縮器3には、低温再生器2Aの加熱管内に導かれた冷媒蒸気X2を凝縮器3に導く第6配管28が設けられている。   The second pump 7B serves as a drive source for circulating the refrigerant X1 made of water. The second pump 7B is connected to the refrigerant return pipe 23 from the condenser 3 and the evaporator 4 on the inlet side, and to the sprinkling pipe 24 on the outlet side. The low temperature regenerator 2 </ b> A and the heat exchanger 6 are connected by a third pipe 25. The absorber 5 and the heat exchanger 6 are connected by a fourth pipe 26. The high temperature regenerator 2B is provided with a fifth pipe 27 that guides the high-temperature refrigerant vapor X2 generated in the high temperature regenerator 2B into the heating pipe of the low temperature regenerator 2A. The low temperature regenerator 2AB and the condenser 3 are provided with a sixth pipe 28 that guides the refrigerant vapor X2 introduced into the heating pipe of the low temperature regenerator 2A to the condenser 3.

上記実施形態の吸収式冷凍機1によれば、図1に示すように、第2ポンプ7Bの駆動によって、冷媒X1が、散水用配管24―蒸発器4―冷媒戻り配管23―第2ポンプ7B―散水用配管24を循環するようにしてある。また、第1ポンプ7Aの駆動によって、臭化リチウム水溶液からなる吸収液Y1の一部が、熱交換用配管6A―高温再生器2A―第1配管21―熱交換器6―第4配管26―吸収器5―第1ポンプ7A―熱交換用配管6Aを循環するとともに、臭化リチウム水溶液からなる吸収液Y1の残りの一部が、熱交換用配管6A―第3配管25―低温再生器2B―第2配管22―熱交換器6―第4配管26―吸収器5―第1ポンプ7A―熱交換用配管6Aを循環するようにしてある。また、高温再生器2Bで発生した高温の冷媒蒸気X2は、第5配管27―低温再生器2Aの加熱管―第6配管28で移動して凝縮器3に至って、その凝縮器3で冷媒X1となり、その冷媒X1は、冷媒戻り配管23―第2ポンプ7B―散水用配管24を介して、蒸発器4に戻るようにしてある。   According to the absorption refrigeration machine 1 of the above embodiment, as shown in FIG. 1, the refrigerant X1 is converted into the sprinkling pipe 24 -the evaporator 4 -the refrigerant return pipe 23 -the second pump 7B by driving the second pump 7B. -It is designed to circulate through the watering pipe 24. Further, by driving the first pump 7A, a part of the absorbing liquid Y1 made of the lithium bromide aqueous solution is converted into a heat exchange pipe 6A-high temperature regenerator 2A-first pipe 21-heat exchanger 6-fourth pipe 26-. The absorber 5-the first pump 7A-the heat exchange pipe 6A circulates, and the remaining part of the absorbent Y1 made of the lithium bromide aqueous solution is the heat exchange pipe 6A-the third pipe 25-the low temperature regenerator 2B. The second pipe 22, the heat exchanger 6, the fourth pipe 26, the absorber 5, the first pump 7 </ b> A, and the heat exchange pipe 6 </ b> A are circulated. Further, the high-temperature refrigerant vapor X2 generated in the high-temperature regenerator 2B moves through the fifth pipe 27—the heating pipe of the low-temperature regenerator 2A—the sixth pipe 28 and reaches the condenser 3, where the refrigerant X1 The refrigerant X1 returns to the evaporator 4 via the refrigerant return pipe 23, the second pump 7B, and the watering pipe 24.

さらに、上記実施形態の吸収式冷凍機1には、その吸収式冷凍機1の機器内壁の構成材料の腐食を検知する腐食検出手段14が設けられている。その腐食検出手段14は、図1に示すように、高温再生器2B内の吸収液Y1中に浸漬するように設置されて高温再生器2B内壁の構成材料と同一金属からなる一対の電極15、16と、この一対の電極15、16間を流れる電流を測定する電流測定手段19と、この電流測定手段19によって測定された電流が予め設定した所定値(腐食速度の許容値から算出される電流値若しくはインヒビター濃度の許容値)を超えた場合に警報を発する警報手段20とを少なくとも備えてなる構成にしたものである。なお、図1に示す腐食検出手段14では、一対の電極15、16を臭化リチウム水溶液の温度及び濃度が最も高くなる高温再生器2B内に設置しているが、高温再生器2B内の下部(低部)と上部の、それぞれに、一対の電極15、16を設置するようにしてもよい。   Further, the absorption refrigerator 1 of the above embodiment is provided with corrosion detection means 14 for detecting corrosion of the constituent material of the equipment inner wall of the absorption refrigerator 1. As shown in FIG. 1, the corrosion detecting means 14 is installed so as to be immersed in the absorbing liquid Y1 in the high temperature regenerator 2B, and a pair of electrodes 15 made of the same metal as the constituent material of the inner wall of the high temperature regenerator 2B. 16, current measuring means 19 for measuring a current flowing between the pair of electrodes 15 and 16, and a current measured by the current measuring means 19 is a predetermined value (current calculated from an allowable value of corrosion rate). And a warning means 20 that issues a warning when the value or the inhibitor concentration allowable value) is exceeded. In the corrosion detection means 14 shown in FIG. 1, the pair of electrodes 15 and 16 are installed in the high temperature regenerator 2B where the temperature and concentration of the lithium bromide aqueous solution are the highest. You may make it install a pair of electrodes 15 and 16 in (low part) and each upper part.

上記実施形態の吸収式冷凍機1では、高温再生器2B内壁の構成材料を炭素鋼として、一対の電極15、16をそれぞれ炭素鋼電極としてある。腐食検出手段14の一対の電極15、16には、リード線17、18によってその一対の電極15、16間に流れる電流を測定する電流測定手段19が接続されている。電流測定手段19は、ゼロシャント電流計から構成して、一対の電極15、16間を流れる電流の絶対値を検知できるようにしてある。警報手段20は、ランプ、ブザー、パトライトなどからなっている。   In the absorption refrigerator 1 of the above embodiment, the constituent material of the inner wall of the high-temperature regenerator 2B is carbon steel, and the pair of electrodes 15 and 16 are carbon steel electrodes. A current measuring means 19 for measuring a current flowing between the pair of electrodes 15 and 16 is connected to the pair of electrodes 15 and 16 of the corrosion detecting means 14 by lead wires 17 and 18. The current measuring means 19 is composed of a zero shunt ammeter so that the absolute value of the current flowing between the pair of electrodes 15 and 16 can be detected. The alarm means 20 includes a lamp, a buzzer, a patrol light, and the like.

さらに、上記実施形態の吸収式冷凍機1において、吸収器5内の吸収液Y1中に浸漬するように設置され、かつ、モリブデン表面に酸化モリブデン層を形成したモリブデン/酸化モリブデン電極(Mo/MoO2電極)からなる酸化物電極と、この酸化物電極に対向し、かつ、吸収器5内の吸収液Y1中に浸漬するように設置され、かつ、飽和カロメル電極(塩化カリウムをガラス管に充填した電極)や銀―塩化銀電極からなる参照電極と、酸化物電極と参照電極との間に発生した電位差を計測する電位測定器とからなるところの図示しない溶存酸素検出手段を設けて、臭化リチウム水溶液からなる吸収液Y1中の溶存酸素(吸収式冷凍機内の圧力を大気圧以下に設定した場合には、その吸収式冷凍機内の吸収液に空気が侵入してその空気中の酸素が吸収液に溶け込んでしまうため、その溶け込んだ酸素を、溶存酸素という)を検出すようにしてもよい。   Furthermore, in the absorption refrigerator 1 of the above-described embodiment, a molybdenum / molybdenum oxide electrode (Mo / MoO 2) installed so as to be immersed in the absorbing liquid Y 1 in the absorber 5 and having a molybdenum oxide layer formed on the molybdenum surface. An oxide electrode composed of an electrode), and a so-called saturated calomel electrode (potassium chloride filled into a glass tube), which is placed so as to be opposed to the oxide electrode and immersed in the absorbing liquid Y1 in the absorber 5. Electrode), a reference electrode composed of a silver-silver chloride electrode, and a non-illustrated dissolved oxygen detecting means comprising a potential measuring device for measuring a potential difference generated between the oxide electrode and the reference electrode. Dissolved oxygen in the absorption liquid Y1 composed of an aqueous lithium solution (when the pressure in the absorption chiller is set to atmospheric pressure or lower, air enters the absorption liquid in the absorption chiller and enters the air. Since oxygen will blend into the absorption liquid, the dissolved but oxygen, that dissolved oxygen) it may be to detect.

この溶存酸素検出手段は、吸収液Y1中の溶存酸素濃度に応じて参照電極に対する酸化物電極の自然電位が変化することに起因して酸化物電極と参照電極との間に発生する電位差を測定し、その測定された電位差が予め設定された所定値(溶存酸素濃度に対応して定められ電位)を超えると警報装置を作動させる機能を有している。吸収液Y1中の溶存酸素濃度が予め設定した所定値を超えると警報が発せられることで、吸収式冷凍機1の保守員、管理者若しくは所有者が、難なく知ることができ、吸収液Y1中の溶存酸素濃度を下げるような種々の手段が円滑に施されて吸収式冷凍機1内の最適腐食抑制条件を維持させることができる。したがって、吸収器5内の吸収液Y1中の溶存酸素濃度が溶存酸素検出手段によって、自動的にモニタリングされるので、吸収器5内の吸収液Y1中の溶存酸素濃度が予め設定した所定値を超えてしまった状態のままで、長時間放置されることがなく、吸収式冷凍機1を構成している炭素鋼(鉄鋼部材)の腐食の進行を阻止できる。   This dissolved oxygen detecting means measures a potential difference generated between the oxide electrode and the reference electrode due to a change in the natural potential of the oxide electrode with respect to the reference electrode in accordance with the dissolved oxygen concentration in the absorbing liquid Y1. When the measured potential difference exceeds a predetermined value (potential determined corresponding to the dissolved oxygen concentration), the alarm device is activated. When the dissolved oxygen concentration in the absorption liquid Y1 exceeds a predetermined value set in advance, an alarm is issued, so that the maintenance staff, manager or owner of the absorption refrigeration machine 1 can know without difficulty, and the absorption liquid Y1 Thus, various means for reducing the dissolved oxygen concentration can be smoothly applied to maintain the optimum corrosion suppression conditions in the absorption refrigerator 1. Therefore, the dissolved oxygen concentration in the absorbent Y1 in the absorber 5 is automatically monitored by the dissolved oxygen detecting means, so the dissolved oxygen concentration in the absorbent Y1 in the absorber 5 is set to a predetermined value. It is possible to prevent the progress of the corrosion of the carbon steel (steel member) constituting the absorption refrigerator 1 without being left for a long time in the state where it has been exceeded.

上記実施形態の腐食検出手段14によれば、一対の電極15、16の双方が同じ状態にあるときは、その一対の電極15、16間に電流(腐食電流)が流れず、一対の電極15、16のどちらかに腐食が発生すると、その腐食の進行程度に応じた電流(腐食電流)が一対の電極15、16間を流れるので、その電流(腐食電流)の発生をもって、吸収式冷凍機1の機器内壁である高温再生器2B内壁に発生した局部腐食とみなすことができる。   According to the corrosion detection means 14 of the above embodiment, when both the pair of electrodes 15 and 16 are in the same state, no current (corrosion current) flows between the pair of electrodes 15 and 16, and the pair of electrodes 15. , 16, when corrosion occurs, a current (corrosion current) corresponding to the degree of progress of the corrosion flows between the pair of electrodes 15 and 16, so that the generation of the current (corrosion current) causes the absorption refrigerator 1 can be regarded as local corrosion occurring on the inner wall of the high-temperature regenerator 2 </ b> B that is the inner wall of the apparatus 1.

上記吸収式冷凍機1において、臭化リチウム水溶液中に、LiMoO(四酸化モリブデンリチウム)とLiNO(三酸化窒素リチウム)からなるインヒビターを添加したものを吸収液(以下、この吸収液を試験用吸収液Z1と称する)として用いて、試験したところ、図2のA範囲に示すように、吸収液中にインヒビターがある間は、炭素鋼に不動態皮膜が生成されることで、腐食電流が流れない。この状態から、上記LiMoO(四酸化モリブデンリチウム)とLiNO(三酸化窒素リチウム)からなるインヒビターを、試験用吸収液Z1から取り除くと、前記不動態皮膜が局部的に破壊されることで、図2のB範囲に示すように、腐食電流が発生して時間の経過とともに増大する。その後、上記LiMoO(四酸化モリブデンリチウム)とLiNO(三酸化窒素リチウム)からなるインヒビターを、試験用吸収液Z1に所定量、添加すると、図2のC範囲に示すように、腐食電流が流れなくなり、局部的に破壊された前記不動態皮膜が補修されることが確認できた。 In the absorption refrigerator 1, an absorption liquid (hereinafter, this absorption liquid) is prepared by adding an inhibitor composed of Li 2 MoO 4 (lithium molybdenum tetraoxide) and LiNO 3 (lithium nitric oxide) to an aqueous lithium bromide solution. As a test absorbing solution Z1), as shown in the range A of FIG. 2, while there is an inhibitor in the absorbing solution, a passive film is formed on the carbon steel, Corrosion current does not flow. In this state, when the inhibitor composed of Li 2 MoO 4 (lithium molybdenum tetroxide) and LiNO 3 (lithium nitric oxide) is removed from the test absorbent Z1, the passive film is locally destroyed. Thus, as shown in the range B of FIG. 2, the corrosion current is generated and increases with time. Then, when a predetermined amount of an inhibitor composed of Li 2 MoO 4 (lithium molybdenum tetraoxide) and LiNO 3 (lithium nitric oxide) is added to the test absorbent Z1, corrosion occurs as shown in the range C in FIG. It could be confirmed that the passive film was locally repaired and no current flowed.

さらに、本発明を適用した30冷凍トンの吸収式冷凍機につき、組成を55Wt%LiBr(臭化リチウム)と0.17Wt%LiOH(水酸化リチウム)と0.03Wt%LiNO(三酸化窒素リチウム)にしてなる吸収液を封入して、全負荷で1万時間運転の実機試験運転を行ったところ、6700時間後に腐食電流が腐食検出手段14によって検知され、8320時間後に所定値を超えて警報手段20が動作して警報が発せられることが確認できた。 Further, the absorption refrigeration machine of 30 tons to which the present invention is applied has a composition of 55 Wt% LiBr (lithium bromide), 0.17 Wt% LiOH (lithium hydroxide) and 0.03 Wt% LiNO 3 (lithium nitric oxide). When the actual test operation of 10,000 hours operation at full load was performed with the absorption liquid formed in the above), the corrosion current was detected by the corrosion detection means 14 after 6700 hours, and the alarm exceeded the predetermined value after 8320 hours. It was confirmed that the means 20 was activated and an alarm was issued.

上記実施形態の吸収式冷凍機1によれば、その吸収式冷凍機1の機器内壁に局部腐食が発生すると、警報手段20が自動的に動作して、局部腐食が発生したことを保守員、管理者若しくは所有者に知らしめることができるので、その局部腐食を阻止するための対策を的確に処理することができ、吸収式冷凍機1の機器内壁に貫通孔を形成させてしまうという危険な状態に至るのを阻止することができる。   According to the absorption refrigeration machine 1 of the above embodiment, when local corrosion occurs on the inner wall of the absorption refrigeration machine 1, the alarm means 20 automatically operates to indicate that the local corrosion has occurred, Since it can be notified to the manager or the owner, the countermeasure for preventing the local corrosion can be appropriately processed, and there is a danger that a through hole is formed in the inner wall of the absorption refrigerator 1. It is possible to prevent the state from being reached.

上記一実施形態では、腐食検出手段14を高温再生器2B内にのみ設置するようにしているが、低温再生器2A、吸収器5若しくは熱交換器6内の吸収液Y1中に、腐食検出手段14を浸漬するように設置するようにしてもよい。また、上記一実施形態では、冷媒X1を水としているが、希薄臭化リチウム水溶液を冷媒X1としてもよい。一対の電極15、16の材質は、炭素鋼に限定されず、吸収式冷凍機1の機器内壁の構成材料に合わせて、銅、キュプロニッケル、ステンレス鋼、ロウ材のいずれかとするようにしてもよい。   In the above embodiment, the corrosion detection means 14 is installed only in the high temperature regenerator 2B. You may make it install so that 14 may be immersed. In the above embodiment, the refrigerant X1 is water, but a diluted lithium bromide aqueous solution may be the refrigerant X1. The material of the pair of electrodes 15 and 16 is not limited to carbon steel, and may be any of copper, cupronickel, stainless steel, and brazing material according to the constituent material of the inner wall of the absorption refrigerator 1. Good.

本発明の一実施形態に係る吸収式冷凍機の要部構成説明図である。It is principal part structure explanatory drawing of the absorption refrigerator which concerns on one Embodiment of this invention. 本発明の一実施形態に係る吸収式冷凍機の腐食電流に関する実験結果を示す図である。It is a figure which shows the experimental result regarding the corrosion current of the absorption refrigerator which concerns on one Embodiment of this invention.

符号の説明Explanation of symbols

1 吸収式冷凍機
2 再生器
2A 低温再生器
2B 高温再生器
3 凝縮器
4 蒸発器
5 吸収器
6 熱交換器
6A 熱交換用配管
7 ポンプ
7A 第1ポンプ
7B 第2ポンプ
8 多数の蒸発用管体
9 冷水送込み用配管
9A 冷水戻り用配管
10 散水ノズル
11 吸収用管体
12 冷却水送込み用配管
12A 冷却水戻り用配管
13 冷却水管
14 腐食検出手段
15、16 一対の電極
17、18 リード線
19 電流測定手段
20 警報手段
21 第1配管
22 第2配管
23 冷媒戻り配管
24 散水用配管
25 第3配管
26 第4配管
27 第5配管
28 第6配管
X1 冷媒(水若しくは希薄臭化リチウム水溶液)
X2 冷媒蒸気
Y1 臭化リチウム濃度の低下した吸収液(低温の希薄溶液)
Y2 臭化リチウム濃度の高い吸収液(高温の濃厚溶液)
W1 冷水
W2 冷却水
DESCRIPTION OF SYMBOLS 1 Absorption type refrigerator 2 Regenerator 2A Low temperature regenerator 2B High temperature regenerator 3 Condenser 4 Evaporator 5 Absorber 6 Heat exchanger 6A Heat exchange pipe 7 Pump 7A 1st pump 7B 2nd pump 8 Many evaporation pipes Body 9 Cold water feed pipe 9A Cold water return pipe 10 Sprinkling nozzle 11 Absorption pipe 12 Cooling water feed pipe 12A Cooling water return pipe 13 Cooling water pipe 14 Corrosion detection means 15, 16 Pair of electrodes 17, 18 Lead Line 19 Current measuring means 20 Alarm means 21 First pipe 22 Second pipe 23 Refrigerant return pipe 24 Sprinkling pipe 25 Third pipe 26 Fourth pipe 27 Fifth pipe 28 Sixth pipe X1 Refrigerant (water or dilute lithium bromide aqueous solution) )
X2 Refrigerant vapor Y1 Absorbing liquid with low lithium bromide concentration (low temperature dilute solution)
Y2 Absorption liquid with high lithium bromide concentration (high temperature concentrated solution)
W1 Cold water W2 Cooling water

Claims (3)

再生器、凝縮器、蒸発器、吸収器、熱交換器及びポンプの機器を少なくとも備え、水若しくは希薄臭化リチウム水溶液を冷媒とし、かつ、酸素酸塩及びアルカリ金属水酸化物を含むインヒビターを混入した臭化リチウム水溶液を吸収液として用いてなる吸収式冷凍機において、
前記機器内壁の構成材料の腐食を検知する腐食検出手段を設け、この腐食検出手段を、少なくとも前記再生器、吸収器若しくは熱交換器のいずれか一つ以上の機器内の吸収液中に浸漬するように設置されて前記機器内壁の構成材料と同一金属からなる少なくとも一対の電極と、この一対の電極間を流れる電流を測定する電流測定手段と、この電流測定手段によって測定された電流が予め設定した所定値を超えた場合に警報を発する警報手段とが包含される構成としたことを特徴とする吸収式冷凍機。
Equipped with at least regenerator, condenser, evaporator, absorber, heat exchanger and pump equipment, water or dilute lithium bromide aqueous solution as refrigerant, and mixed with inhibitors containing oxyacid salt and alkali metal hydroxide In an absorption refrigerator using an aqueous lithium bromide solution as an absorbent,
Corrosion detection means for detecting corrosion of the constituent material of the inner wall of the equipment is provided, and this corrosion detection means is immersed in an absorbing solution in at least one of the regenerator, absorber and heat exchanger. At least a pair of electrodes made of the same metal as the constituent material of the inner wall of the device, a current measuring means for measuring a current flowing between the pair of electrodes, and a current measured by the current measuring means is preset. An absorption refrigeration machine comprising a warning means for issuing a warning when a predetermined value is exceeded.
前記電流測定手段は、前記一対の電極間を流れる電流の絶対値を検知するゼロシャント電流計から少なくとも構成したことを特徴とする請求項1記載の吸収式冷凍機。   2. The absorption refrigerator according to claim 1, wherein the current measuring means comprises at least a zero shunt ammeter that detects an absolute value of a current flowing between the pair of electrodes. 前記一対の電極の材質を、前記機器内壁の構成材料に合わせて、炭素鋼、銅、キュプロニッケル、ステンレス鋼,ロウ材のいずれかとしたことを特徴とする請求項1若しくは2記載の吸収式冷凍機。   The absorption refrigeration according to claim 1 or 2, wherein a material of the pair of electrodes is selected from the group consisting of carbon steel, copper, cupronickel, stainless steel, and brazing material according to the constituent material of the inner wall of the device. Machine.
JP2007130195A 2007-05-16 2007-05-16 Absorption refrigerator Pending JP2008286441A (en)

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012229904A (en) * 2011-04-27 2012-11-22 Mitsubishi Electric Corp Cooling device
JP2013068359A (en) * 2011-09-22 2013-04-18 Hitachi Building Systems Co Ltd Method and apparatus for grasping inhibitor concentration in absorbing liquid, and absorption chiller heater provided with the apparatus
WO2022044439A1 (en) 2020-08-24 2022-03-03 パナソニックIpマネジメント株式会社 Refrigeration cycle device and refrigeration cycle system
WO2022044440A1 (en) 2020-08-24 2022-03-03 パナソニックIpマネジメント株式会社 Refrigeration cycle system and analysis method
CN114641659A (en) * 2019-10-09 2022-06-17 埃科利姆股份有限公司 Absorption cooling machine

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JPH07270371A (en) * 1994-03-31 1995-10-20 Hitachi Ltd Internal reference electrode and absorption type refrigerator
JPH07286287A (en) * 1994-04-18 1995-10-31 Tokyo Gas Co Ltd Corrosion inhibitor for liquid absorbent of absorption heat pump and aqueous solution composition
JPH11248301A (en) * 1998-03-04 1999-09-14 Hitachi Building Shisetsu Engineering Kk Method and apparatus for managing concentration of inhibitor for absorption refrigerator
JP2000329725A (en) * 1999-05-18 2000-11-30 Hakuto Co Ltd Device for estimating local corrosion of metal material in river system
JP2005003635A (en) * 2003-06-16 2005-01-06 Mitsubishi Chemicals Corp Management system of water system process
JP2006057895A (en) * 2004-08-19 2006-03-02 Hitachi Building Systems Co Ltd Absorption refrigerator

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JPH07270371A (en) * 1994-03-31 1995-10-20 Hitachi Ltd Internal reference electrode and absorption type refrigerator
JPH07286287A (en) * 1994-04-18 1995-10-31 Tokyo Gas Co Ltd Corrosion inhibitor for liquid absorbent of absorption heat pump and aqueous solution composition
JPH11248301A (en) * 1998-03-04 1999-09-14 Hitachi Building Shisetsu Engineering Kk Method and apparatus for managing concentration of inhibitor for absorption refrigerator
JP2000329725A (en) * 1999-05-18 2000-11-30 Hakuto Co Ltd Device for estimating local corrosion of metal material in river system
JP2005003635A (en) * 2003-06-16 2005-01-06 Mitsubishi Chemicals Corp Management system of water system process
JP2006057895A (en) * 2004-08-19 2006-03-02 Hitachi Building Systems Co Ltd Absorption refrigerator

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012229904A (en) * 2011-04-27 2012-11-22 Mitsubishi Electric Corp Cooling device
JP2013068359A (en) * 2011-09-22 2013-04-18 Hitachi Building Systems Co Ltd Method and apparatus for grasping inhibitor concentration in absorbing liquid, and absorption chiller heater provided with the apparatus
CN114641659A (en) * 2019-10-09 2022-06-17 埃科利姆股份有限公司 Absorption cooling machine
WO2022044439A1 (en) 2020-08-24 2022-03-03 パナソニックIpマネジメント株式会社 Refrigeration cycle device and refrigeration cycle system
WO2022044440A1 (en) 2020-08-24 2022-03-03 パナソニックIpマネジメント株式会社 Refrigeration cycle system and analysis method

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