JP2002195678A - Method and device for performance recovery of absorption refrigerator - Google Patents

Method and device for performance recovery of absorption refrigerator

Info

Publication number
JP2002195678A
JP2002195678A JP2000393813A JP2000393813A JP2002195678A JP 2002195678 A JP2002195678 A JP 2002195678A JP 2000393813 A JP2000393813 A JP 2000393813A JP 2000393813 A JP2000393813 A JP 2000393813A JP 2002195678 A JP2002195678 A JP 2002195678A
Authority
JP
Japan
Prior art keywords
refrigerant
cleaning
washing
liquid
absorption
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
JP2000393813A
Other languages
Japanese (ja)
Other versions
JP3787757B2 (en
Inventor
Kenji Machizawa
健司 町澤
Masahiko Ito
雅彦 伊藤
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.)
Hitachi Building Systems Co Ltd
Original Assignee
Hitachi Building Systems Co Ltd
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 Hitachi Building Systems Co Ltd filed Critical Hitachi Building Systems Co Ltd
Priority to JP2000393813A priority Critical patent/JP3787757B2/en
Publication of JP2002195678A publication Critical patent/JP2002195678A/en
Application granted granted Critical
Publication of JP3787757B2 publication Critical patent/JP3787757B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • 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

Landscapes

  • Sorption Type Refrigeration Machines (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a technology for making performance of a lithium-bromide absorption-refrigerator recover, when a spray nozzle is clogged and the performance is degraded. SOLUTION: From the refrigerator, a refrigerant spray pump (not shown) is demounted, which sucks and discharges liquid refrigerant (water) accumulated in the bottom of an evaporator 4 to a spray nozzle 15, and a cleaning liquid circulating tank 17 is temporarily placed. A cleaning liquid circulation pump 19 is connected to the tank 17 to suck and discharge the cleaning liquid of the tank. An inert gas (e.g., nitrogen gas) is injected in a high vacuum space of the refrigerant circulation system to inhibit inflow of air. The cleaning liquid is sent to the nozzle 15 and sprayed, and at the same time, the liquid refrigerant accumulated in the bottom of the evaporator 4 is conducted to the tank 17, and sucked by the pump 19 for circulation.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、臭化リチウム吸収
式冷凍機が長時間の稼働によってノズルに詰まりを生じ
たために性能が低下した場合、上記ノズルに堆積した異
物を除去して性能を回復させる方法および同装置に関す
るものである。
[0001] The present invention relates to a lithium bromide absorption refrigerating machine that recovers its performance by removing foreign matter deposited on the nozzle when the performance of the refrigerator has been reduced due to clogging of the nozzle due to long-term operation. And a device for performing the method.

【0002】[0002]

【従来の技術】図3は、水を冷媒とするとともに、吸収
媒体として臭化リチウムを用いた吸収式冷凍機の1例を
示す模式的な系統図である。本図3の右下方に凡例を示
してあるように、ハッチングを付して示した冷媒液12
は液状の水である。網目印を付して示した濃溶液13は
臭化リチウムの濃厚な水溶液であって、水蒸気を吸収す
る力が非常に強い。斑点を付して示した稀溶液14は臭
化リチウムの稀薄な水溶液であって、加熱されると水蒸
気を発生して濃溶液13に変化する性質を有している。
高温再生器1および低温再生器2は加熱管を備えた熱交
換器であって、臭化リチウム水溶液を加熱して水蒸気を
発生させる。水蒸気を発生させた臭化リチウム水溶液は
濃縮されて濃溶液13(網目印)となる。再生器で発生
した水蒸気は凝縮器3に導かれ、冷却水で冷されて液状
の水(平行斜線で示す冷媒液12)となり、矢印aのよ
うに蒸発器4内へ送り込まれる。蒸発器4は吸収器9に
連通されていて、後述する理由によって真空に近い低圧
に保たれているので、送り込まれた水(冷媒)は蒸発し
て気化潜熱を奪い、冷水を冷却させる。
2. Description of the Related Art FIG. 3 is a schematic system diagram showing an example of an absorption refrigerator using water as a refrigerant and lithium bromide as an absorption medium. As shown in the legend at the lower right of FIG. 3, the refrigerant liquid 12 indicated by hatching
Is liquid water. The concentrated solution 13 shown with a mesh mark is a concentrated aqueous solution of lithium bromide, and has a very strong ability to absorb water vapor. The dilute solution 14 indicated by spots is a dilute aqueous solution of lithium bromide, and has the property of generating steam when heated and changing to a concentrated solution 13.
The high-temperature regenerator 1 and the low-temperature regenerator 2 are heat exchangers provided with a heating tube, and heat a lithium bromide aqueous solution to generate steam. The aqueous solution of lithium bromide that has generated water vapor is concentrated to become a concentrated solution 13 (a mesh mark). The water vapor generated in the regenerator is guided to the condenser 3 and cooled by the cooling water to become liquid water (refrigerant liquid 12 indicated by oblique parallel lines) and is sent into the evaporator 4 as shown by the arrow a. Since the evaporator 4 is connected to the absorber 9 and is kept at a low pressure close to vacuum for the reason described later, the supplied water (refrigerant) evaporates to remove latent heat of vaporization and cools the cold water.

【0003】蒸発器4内で蒸発し切れなかった液状の水
は、蒸発器の下方の冷媒タンク5に溜まり、冷媒スプレ
ーポンプ6に吸入、吐出されてスプレーダクト8に送ら
れ、スプレーノズル15から噴射される。図4は上記ノ
ズル15付近の拡大断面図である。上記蒸発器4に連通
された吸収器9内には、再生器で濃縮された臭化リチウ
ム濃溶液13が導かれ、蒸発器4で気化した水蒸気を吸
収する。吸収器9内で水蒸気を吸収した濃溶液13は稀
溶液14(斑点を付して示す)となり、溶液ポンプ10
によって、熱交換器11を経て高温再生器1に返送さ
れ、その後、以上の作用を繰り返して吸収サイクルを形
成する。
The liquid water that has not completely evaporated in the evaporator 4 accumulates in a refrigerant tank 5 below the evaporator, is sucked into and discharged from a refrigerant spray pump 6, sent to a spray duct 8, and sent from a spray nozzle 15. It is injected. FIG. 4 is an enlarged sectional view near the nozzle 15. The lithium bromide concentrated solution 13 concentrated in the regenerator is led into the absorber 9 connected to the evaporator 4, and absorbs the vaporized vapor in the evaporator 4. The concentrated solution 13 that has absorbed water vapor in the absorber 9 becomes a dilute solution 14 (shown with spots),
Is returned to the high-temperature regenerator 1 through the heat exchanger 11, and then the above operation is repeated to form an absorption cycle.

【0004】[0004]

【発明が解決しようとする課題】吸収式冷凍機が上述の
ように吸収サイクルを構成するため、機内を高真空に保
持しなければならない。しかし、冷媒循環系統内に高温
の濃厚な臭化リチウム水溶液が封入されているため、密
閉循環系を構成している金属材料の腐食によって真空度
を低下させる虞れが有る。真空度の低下は冷凍性能を低
下させるので、防食については種々の工夫が為されてい
るが、腐食を完全に無くすことは、現段階では不可能で
ある。このため、微量ではあるが腐食生成物が発生し
て、冷媒循環系統内に蓄積されてゆく。このため、スプ
レーノズル15を含む散布系統(図3,図4を併せて参
照)に異物が付着して体積する虞れが有る。スプレーノ
ズル15が目詰まりすると冷媒の散布量が少なくなり、
冷凍能力が低下する。
Since the absorption refrigerator constitutes the absorption cycle as described above, the inside of the equipment must be kept at a high vacuum. However, since the high temperature concentrated lithium bromide aqueous solution is sealed in the refrigerant circulation system, there is a possibility that the degree of vacuum may be reduced due to corrosion of the metal material constituting the closed circulation system. Since a reduction in the degree of vacuum lowers the refrigerating performance, various measures have been taken to prevent corrosion, but it is impossible at this stage to completely eliminate corrosion. For this reason, a small amount of corrosion products are generated and accumulated in the refrigerant circulation system. For this reason, there is a possibility that foreign matter may adhere to the spraying system including the spray nozzle 15 (see also FIGS. 3 and 4) and become bulky. When the spray nozzle 15 is clogged, the amount of the sprayed refrigerant decreases,
Refrigeration capacity decreases.

【0005】(図1参照)スプレーノズル15が半ば閉
塞したとき、従来技術では密閉容器である蒸発器4を切
り開いて該スプレーノズル15を清掃しなければならな
かった。蒸発器4を切断したり、再度溶接したりする作
業には多大の時間,労力を要し、その間、冷凍機として
の稼働を休止しなければならず、高額の修理費を必要と
する。さらに重大な問題は、密閉循環系を形成している
蒸発器4を切開したとき、高真空に保持されていた冷媒
循環系の中に空気が流入し、機内の腐食が一気に促進さ
れることである。本発明の目的とするところは、臭化リ
チウム吸収冷凍機のノズルが目詰まりして冷凍性能が低
下したとき、該吸収冷凍機を構成している密閉容器を切
開することなく、しかも、密閉循環系統の内周面を空気
に触れさせることなく、迅速,容易、かつ低廉な費用で
冷凍性能を回復せしめ得る方法、および同装置を提供す
るにある。
(See FIG. 1.) When the spray nozzle 15 is partially closed, in the prior art, the evaporator 4 as a closed container had to be cut open to clean the spray nozzle 15. The work of cutting or re-welding the evaporator 4 requires a great deal of time and labor. During that time, the operation as a refrigerator must be stopped, and high repair costs are required. A more serious problem is that when the evaporator 4 forming the closed circulation system is cut, air flows into the refrigerant circulation system maintained at a high vacuum, and corrosion inside the machine is promoted at a stretch. is there. It is an object of the present invention to provide a method for reducing the refrigerating performance due to clogging of a nozzle of a lithium bromide absorption refrigerator without cutting a closed container constituting the absorption refrigerator, and furthermore, a closed circulation. An object of the present invention is to provide a method and a device capable of restoring refrigeration performance quickly, easily, and at low cost without exposing the inner peripheral surface of the system to air.

【0006】[0006]

【課題を解決するための手段】上記の目的を達成するた
めに創作した本発明の基本的な原理について、その1実
施形態に対応する図1を参照して略述すると次のとおり
である、すなわち、臭化リチウム吸収式冷凍機における
スプレーノズルが目詰まりして、該冷凍機の性能が低下
したとき、その性能を回復させる技術を提供するため、
蒸発器4の低部に溜まった冷媒液(水)を吸入・吐出し
てスプレーノズル15に送給する冷媒スプレーポンプ
(図示省略)を取り外し、洗浄液循環タンク17を一時
的に設置するとともに、該洗浄液循環タンク内の洗浄液
を吸入・吐出する洗浄液循環ポンプ19を接続する。そ
して、吸収式冷凍機の冷媒循環系統内の高真空の空間内
に不活性ガス(例えば窒素ガス)を注入して空気の流入
を防止し、前記洗浄液をノズル15に供給して散布する
とともに、蒸発器4の底部に溜まった洗浄液を洗浄液循
環タンク17に導き、洗浄液循環ポンプ19に吸入させ
て循環させる。
The basic principle of the present invention created to achieve the above object will be briefly described below with reference to FIG. 1 corresponding to one embodiment of the present invention. That is, when the spray nozzle in the lithium bromide absorption refrigerator is clogged and the performance of the refrigerator is reduced, to provide a technology for recovering the performance,
A refrigerant spray pump (not shown) for sucking / discharging the refrigerant liquid (water) accumulated in the lower part of the evaporator 4 and supplying it to the spray nozzle 15 is removed, and a cleaning liquid circulation tank 17 is temporarily installed. A cleaning liquid circulation pump 19 for sucking and discharging the cleaning liquid in the cleaning liquid circulation tank is connected. Then, an inert gas (for example, nitrogen gas) is injected into a high-vacuum space in the refrigerant circulation system of the absorption refrigerator to prevent the inflow of air, and the cleaning liquid is supplied to the nozzle 15 and sprayed. The cleaning liquid collected at the bottom of the evaporator 4 is guided to the cleaning liquid circulation tank 17 and sucked and circulated by the cleaning liquid circulation pump 19.

【0007】以上に説明した原理に基づいて請求項1に
係る発明方法の構成は、水を冷媒とし、吸収媒体として
臭化リチウムを用いる吸収式冷凍機について、冷媒をス
プレーするノズルや散布孔などの散布装置に異物が付
着,堆積して性能が低下した場合、その性能を回復させ
る方法において、冷媒の散布系統を、薬液によって化学
的に洗浄して、堆積した異物を洗浄除去することを特徴
とする。以上に説明した請求項1の発明方法によると、
蒸発器を切開して露出させなくても、冷凍機のケース外
に設けた洗浄液循環タンクや洗浄液循環タンクを用いて
遠隔的にスプレーノズルを洗浄して異物を除去し、性能
を回復させることができる。
Based on the principle described above, the method according to the first aspect of the present invention relates to an absorption refrigerator using water as a refrigerant and lithium bromide as an absorption medium. In the method of recovering the performance when foreign matter adheres and accumulates on the spraying device of the above, the performance is recovered by chemically cleaning the spraying system of the refrigerant with a chemical solution to wash and remove the accumulated foreign matter. And According to the invention method of claim 1 described above,
Even if the evaporator is not cut and exposed, the spray nozzle can be remotely cleaned using the cleaning liquid circulation tank or cleaning liquid circulation tank provided outside the refrigerator case to remove foreign substances and restore performance. it can.

【0008】請求項2に係る発明方法の構成は、前記請
求項1の発明方法の構成要件に加えて、前記の化学的洗
浄に用いる薬液が、2種類以上の化学薬品から成る酸性
水溶液であることを特徴とする。以上に説明した請求項
2の発明方法によると、複数種類の薬剤を調合した酸性
溶液を用いることにより、鉄系腐食生成物および銅系腐
食生成物の両方を含むスプレーノズル堆積物を効果的に
溶解除去することができる。
According to a second aspect of the present invention, in addition to the constituent elements of the first aspect of the present invention, the chemical solution used for the chemical cleaning is an acidic aqueous solution comprising two or more chemicals. It is characterized by the following. According to the method of the present invention described above, the spray nozzle deposit containing both iron-based corrosion products and copper-based corrosion products can be effectively reduced by using an acidic solution prepared by mixing a plurality of types of chemicals. It can be dissolved and removed.

【0009】請求項3に係る発明方法の構成は、前記請
求項2の発明方法の構成要件に加えて、前記の酸性水溶
液が「塩酸,硫酸,硝酸、もしくはこれに類似する無機
酸、および蓚酸,マロン酸,コハク酸もしくはこれに類
似する有機酸」の内の少なくとも1種類を主成分とし、
かつ、「腐食抑制剤および電位抑制剤」の少なくとも何
れか一方を含有していることを特徴とする。以上に説明
した請求項3の発明方法によると、散布装置に堆積した
腐食生成物を能率的に溶解除去することができ、しか
も、冷媒循環系統を構成している金属材料を腐食させる
などの不具合を生じる虞れが無い。
According to a third aspect of the present invention, in addition to the constituent elements of the second aspect of the present invention, the acidic aqueous solution may be a mixture of hydrochloric acid, sulfuric acid, nitric acid or an inorganic acid similar thereto, and oxalic acid. , Malonic acid, succinic acid or similar organic acids "as a main component,
Further, it is characterized by containing at least one of a "corrosion inhibitor and a potential inhibitor". According to the above-described method of the third aspect of the invention, corrosion products deposited on the spraying device can be efficiently dissolved and removed, and moreover, the metal material constituting the refrigerant circulation system is corroded. Does not occur.

【0010】請求項4に係る発明方法の構成は、前記請
求項1の発明方法の構成要件に加えて、冷媒の散布系統
を薬液で洗浄する際、該スプレー系統の内部表面に空気
を接触させないことを特徴とする。以上に説明した請求
項4の発明方法によると、スプレー系統を構成している
金属製容器や金属製管路の内側面を空気によって酸化腐
食させる虞れが無い。
According to a fourth aspect of the present invention, in addition to the constituent features of the first aspect of the present invention, when the spraying system of the refrigerant is washed with a chemical, air is not brought into contact with the inner surface of the spray system. It is characterized by the following. According to the method of the invention described in claim 4 described above, there is no fear that the inner surface of the metal container or the metal pipe constituting the spray system is oxidized and corroded by air.

【0011】請求項5に係る発明方法の構成は、散布系
統の内面に空気を接触させないため、当該吸収式冷凍機
の冷媒循環系統の内部空間に不活性ガスを充満させた状
態で前記の洗浄を行なうことを特徴とする。以上に説明
した請求項5の発明方法によると、冷媒循環系統の内部
空間が空気に接触することを、迅速容易、かつ完全に遮
断することができる。
In the method according to the fifth aspect of the present invention, since the air is not brought into contact with the inner surface of the spraying system, the cleaning is performed in a state where the internal space of the refrigerant circulation system of the absorption refrigerator is filled with an inert gas. Is performed. According to the method of the invention described in claim 5 described above, it is possible to quickly, easily and completely shut off the contact of the internal space of the refrigerant circulation system with air.

【0012】請求項6に係る発明方法の構成は、前記請
求項1の発明方法の構成要件に加えて、前記の薬液によ
ってスプレー系統を洗浄する際、当該吸収式冷凍機の冷
媒循環系統内から冷媒および吸収媒体溶液を予め冷媒循
環系統外に回収して一時的に保管しておき、機内の薬液
循環洗浄および薬液の水洗除去を終えてから洗浄液を機
外に排出した後、保管してあった冷媒および吸収媒体溶
液を冷媒循環系統内に注入することを特徴とする。以上
に説明した請求項6の発明方法によると、冷媒および吸
収溶液に、洗浄用薬剤を混入せしめる虞れ無くスプレー
ノズルや散布孔の堆積物を洗浄除去することができる。
According to a sixth aspect of the present invention, in addition to the constituent elements of the first aspect of the present invention, when the spray system is cleaned with the chemical solution, the inside of the refrigerant circulating system of the absorption chiller is used. The refrigerant and the absorbing medium solution are collected in advance outside the refrigerant circulation system and temporarily stored, and after the chemical liquid circulation cleaning inside the apparatus and the chemical liquid are removed, the cleaning liquid is discharged out of the apparatus and then stored. The refrigerant and the absorbing medium solution are injected into a refrigerant circulation system. According to the method of the present invention described above, it is possible to wash and remove deposits in a spray nozzle and a spray hole without fear of mixing a cleaning agent into a refrigerant and an absorbing solution.

【0013】請求項7に係る発明方法の構成は、前記請
求項2の発明方法の構成要件に加えて、前記の酸性水溶
液によって散布系統を洗浄した後、アルカリ性の中和剤
溶液を循環させて、残存していた酸性水溶液を中和除去
し、pHが6.0〜8.0のほぼ中性になったことを検
知してから中和操作を終了することを特徴とする。以上
に説明した請求項7の発明方法によると、中和剤の廃液
を河川に放流することができる。pH6.0の微酸性や
pH8.0の微アルカリ性では、冷媒や吸収媒体溶液を
注入して冷凍サイクルを再開することはできないが、こ
の段階では、必ずしも完全中性にしなくても、その後の
工程で水洗によって中和剤を洗い流すことができるの
で、中和操作の終了条件はpH6.0〜pH8.0が適
当である。
According to a seventh aspect of the present invention, in addition to the constituent elements of the second aspect of the present invention, the spray system is washed with the acidic aqueous solution, and then the alkaline neutralizing solution is circulated. The neutralizing operation is terminated after neutralizing and removing the remaining acidic aqueous solution and detecting that the pH has become almost neutral at 6.0 to 8.0. According to the above-described method of the present invention, the waste liquid of the neutralizing agent can be discharged to the river. In the case of slightly acidic pH 6.0 or slightly alkaline pH 8.0, it is not possible to restart the refrigeration cycle by injecting a refrigerant or an absorbing medium solution. , The neutralizing agent can be washed away by washing with water, so that the pH of the neutralization operation is suitably set at pH 6.0 to pH 8.0.

【0014】請求項8に係る発明方法の構成は、前記請
求項7の発明方法の構成要件に加えて、冷媒スプレー系
統内がpH6.0〜8.0になるまで中和操作を行った
後、中和剤溶液を排出して上水を入れ、該上水を散布系
統内で循環させた後、上記洗浄用上水の洗浄廃液を機外
に排出し、軟水を冷媒循環系統内に流動させて仕上げ水
洗し、仕上げ水洗廃液を機外に排出することを特徴とす
る。以上に説明した請求項8の発明方法によると、スプ
レーノズルや散布孔などの散布装置が設けられている蒸
発室の内部、および、該蒸発室に連通していて洗浄液の
一部(微量)が混入する虞れの有る箇所を、効率良く、
かつ完全に中性に戻して、冷凍サイクルの再開に支障の
無い状態にすることができる。
According to an eighth aspect of the present invention, in addition to the constituent elements of the seventh aspect of the present invention, after the neutralization operation is performed until the inside of the refrigerant spray system reaches pH 6.0 to 8.0. After discharging the neutralizing agent solution and adding clean water, the clean water is circulated in the spraying system, and then the cleaning waste water for cleaning is discharged outside the machine, and the soft water flows into the refrigerant circulating system. Then, finishing water washing is performed, and the finished washing waste liquid is discharged outside the machine. According to the above-described method of the present invention, a part (a trace amount) of the cleaning liquid is communicated with the inside of the evaporation chamber provided with the spraying device such as the spray nozzle and the spraying hole, and with the evaporation chamber. Efficiently,
In addition, the refrigeration cycle can be returned to a neutral state completely without any trouble in restarting the refrigeration cycle.

【0015】請求項9に係る発明方法の構成は、前記請
求項5の発明方法の構成要件に加えて、冷媒循環系統内
に不活性ガスを充満させて洗浄液を循環させる際は、機
内のガス圧をほぼ大気圧に等しからしめた状態で洗浄を
行ない、薬液洗浄、中和剤洗浄、および水洗を終えた
後、前記のガス圧を大気圧よりも上昇させて、前記不活
性ガスの圧力を機外に放出しつつ、この放出圧力によっ
て前記水洗に用いた洗浄水の機内残留部分を機外に放出
することを特徴とする。以上に説明した請求項9の発明
方法によると、機内圧と大気圧とをバランスさせた状態
でスプレー系統内に洗浄液を循環せしめることができ、
かつ、上記洗浄液を迅速,容易に機外へ排出することが
できる。
According to a ninth aspect of the present invention, in addition to the constituent elements of the fifth aspect of the present invention, when the inert gas is filled in the refrigerant circulation system to circulate the cleaning liquid, the gas in the machine is circulated. Washing is performed in a state where the pressure is substantially equal to the atmospheric pressure, and after the chemical solution washing, the neutralizing agent washing, and the water washing are completed, the gas pressure is raised above the atmospheric pressure to remove the inert gas. It is characterized in that, while the pressure is released outside the machine, the remaining portion of the washing water used in the water washing inside the machine is discharged outside the machine by the released pressure. According to the method of the ninth aspect described above, the cleaning liquid can be circulated in the spray system in a state where the internal pressure and the atmospheric pressure are balanced,
In addition, the cleaning liquid can be quickly and easily discharged out of the apparatus.

【0016】請求項10に係る発明方法の構成は、前記
請求項1の発明方法の構成要件に加えて、冷媒の散布系
統を薬液で線上する際、当該吸収式冷凍機の冷媒循環系
路外に洗浄液循環タンク(17)を設けて、この中に洗
浄液を入れておき、上記洗浄液を洗浄循環ポンプ(1
9)で吸入,圧送して、当該吸収式温水機の蒸発器内に
本来的に設けられているスプレーノズルまたは散布孔
(15)から噴射させ、上記ノズルから噴射されて蒸発
器底部の冷媒タンク(5)に溜まった洗浄水を前記洗浄
液循環タンク(17)に導いて、前記洗浄液循環ポンプ
(19)によって吸入され得る状態ならしめ、上述のよ
うにして洗浄液を循環流動せしめつつスプレーノズルま
たは散布孔(15)流動せしめることを特徴とする。以
上に説明した請求項10の発明方法によると、既設の吸
収式冷凍機に対して大改造を加えることなく、かつ、大
形構成機器である蒸発器を切開することなく、簡単な機
器を用いてスプレーノズルを薬液洗浄することができ
る。
According to a tenth aspect of the present invention, in addition to the constituent elements of the first aspect of the present invention, when the refrigerant spraying system is lined with a chemical solution, the refrigerant circulating system of the absorption type refrigerator is out of line. A washing liquid circulation tank (17) is provided in the washing machine, and a washing liquid is put in the washing liquid circulation tank (17).
9) Inhalation and pressure feeding are performed, and are sprayed from a spray nozzle or a spray hole (15) originally provided in the evaporator of the absorption type water heater. The cleaning water accumulated in (5) is guided to the cleaning liquid circulation tank (17) to be in a state where it can be sucked by the cleaning liquid circulation pump (19), and the spray liquid or the spray nozzle is sprayed while the cleaning liquid is circulated and flowed as described above. The holes (15) are characterized by being made to flow. According to the method of the invention described in claim 10 described above, a simple device can be used without making a major modification to the existing absorption refrigerator and without incising the evaporator which is a large component device. The spray nozzle can be cleaned with a chemical solution.

【0017】請求項11に係る発明装置の構成は、冷媒
として水を用い、吸収媒体として臭化リチウムを用いる
吸収式冷凍機であって、その蒸発器(4)の中に冷媒機
を噴射するスプレーノズルまたは散布孔(15)が設け
られるとともに、該スプレーノズルまたは散布孔から噴
射されて蒸発器の底部に溜まった冷媒液を吸入して上記
スプレーノズルに送給する冷媒スプレーポンプ(6)を
備えているものにおいて、上記冷媒スプレーポンプの吸
入側管路と吐出側管路とのそれぞれに、冷媒循環締切弁
(23a、23b)が介挿接続され、かつ、上記吸入側
管路に設けられた冷媒循環締切弁(23a)の上流側管
路に分岐管が設けられて、その先端に洗浄回路接続用閉
止弁(24a)が接続されるとともに、前記吐出側管路
に設けられた冷媒循環締切弁(23b)の下流側管路に
分岐管が設けられて、その先端に洗浄回路接続用閉止弁
(24b)が接続されていることを特徴とする。以上に
説明した請求項11の発明装置によると、前記請求項1
に係る発明方法を容易に実施して、その効果を充分に発
揮せしめることができる。
An eleventh aspect of the present invention is an absorption refrigerator using water as a refrigerant and lithium bromide as an absorption medium, and injects the refrigerant into its evaporator (4). A refrigerant spray pump (6) is provided with a spray nozzle or a spray hole (15), and sucks a refrigerant liquid sprayed from the spray nozzle or the spray hole and collected at the bottom of the evaporator and sends the liquid to the spray nozzle. A refrigerant circulation shut-off valve (23a, 23b) is inserted and connected to each of the suction-side pipe and the discharge-side pipe of the refrigerant spray pump, and is provided in the suction-side pipe. A branch pipe is provided in an upstream pipe line of the refrigerant circulation shutoff valve (23a), a cleaning circuit connection closing valve (24a) is connected to a tip of the branch pipe, and a refrigerant pipe provided in the discharge side pipe line. And the branch pipe is provided on the downstream side pipeline ring shut-off valve (23b), characterized in that the washing circuit connecting the stop valve at the tip (24b) is connected. According to the device of the eleventh aspect described above, the first aspect
And the effect can be fully exhibited.

【0018】[0018]

【発明の実施の形態】図1は、本発明の1実施形態を示
す系統図である。この実施形態は、前掲の図3に示した
従来例の吸収式冷凍機のスプレーノズルまたは散布孔
(以下単にスプレーノズルという)15に目詰まりを生
じたため冷凍性能が実施したので、本発明を適用して該
スプレーノズル15を洗浄して冷凍能力を回復させた1
例である。(冷凍容量500冷凍トン・稼働年数20
年)。本図1において、蒸発器4を含まない右半部は、
前掲の図1(従来例)と同様である。図3(従来例)に
おいて、冷媒スプレーポンプ6の吸入側の管路、およ
び、該冷媒スプレーポンプ6の吐出側管路を切り離し、
冷媒スプレーポンプ6を取り外す。上記の切離しは、切
断でも良く、取り外し(例えば管継手の)でも良い。切
離した2箇所の管路のそれぞれについて、イ.蒸発器4
下方の冷媒タンク5に連通している側の管路の切離し端
は、図1に示すように開閉弁23を装着して閉止してお
く。ロ.スプレーノズル15を設けたスプレーダクト8
に連通している側の管路の切離し端は、封止板20を装
着して閉止するとともに、分岐管路を取り付けて、開閉
弁25およびフレキシブルホース22を介して洗浄液循
環ポンプ19の吐出口に接続する。
FIG. 1 is a system diagram showing one embodiment of the present invention. In this embodiment, since the spray nozzle or spray hole (hereinafter simply referred to as a spray nozzle) 15 of the conventional absorption type refrigerator shown in FIG. Then, the spray nozzle 15 was washed to restore the refrigerating ability.
It is an example. (Refrigeration capacity 500 refrigeration tons, operating years 20
Year). In FIG. 1, the right half without the evaporator 4 is:
This is the same as FIG. 1 (conventional example) described above. In FIG. 3 (conventional example), a suction-side pipe of the refrigerant spray pump 6 and a discharge-side pipe of the refrigerant spray pump 6 are cut off.
Remove the refrigerant spray pump 6. The above-mentioned separation may be cutting or removal (for example, of a pipe joint). For each of the two separated pipes, b. Evaporator 4
As shown in FIG. 1, an open / close valve 23 is attached to the cut end of the pipe on the side communicating with the lower refrigerant tank 5, and the cut end is closed. B. Spray duct 8 provided with spray nozzle 15
The cut-off end of the pipe line on the side communicating with is closed by attaching a sealing plate 20, a branch pipe line is attached, and the discharge port of the cleaning liquid circulation pump 19 is connected via the on-off valve 25 and the flexible hose 22. Connect to

【0019】前記開閉弁23に、フレキシブルホース2
1,開閉弁24、およびフレキシブルホース16を接続
して、蒸発器4の底部の冷媒タンク5内の液体を排出で
きるように配管する。本発明方法を適用して、蒸発器4
内のスプレーノズル15を洗浄剤で循環洗浄するに先立
って、吸収サイクルを形成している冷媒(水)や吸収媒
体溶液(濃厚臭化リチウム水溶液13、および稀薄臭化
リチウム水溶液14)を機外に回収しておかねばならな
い。しかし、冷媒循環系統内は高真空であるから、流出
路を設けただけでは機内の流体が機外に流出しない(そ
の反対に、勢よく空気を吸いこんでしまう)。空気の流
入は機器内を腐食させるので甚だ好ましくない。そこ
で、適宜の手段(図示省略)を用いて、冷媒循環系統内
に不活性ガス(本実施形態では窒素)を冷媒循環系統内
に流入させながら冷媒および吸収媒体溶液を機外に回収
する。この際、配管内に残留している液体を機外へ流出
させるため、窒素ガス圧を大気圧よりも若干高くして、
該窒素ガスで残液を噴き出させるように操作すると好都
合である。回収した冷媒および吸収媒体溶液は、それぞ
れポリ容器に入れ、液面に接触している空間を窒素ガス
で満たして一時的に保存しておく。
The on-off valve 23 has a flexible hose 2
1, the on-off valve 24 and the flexible hose 16 are connected, and piping is performed so that the liquid in the refrigerant tank 5 at the bottom of the evaporator 4 can be discharged. By applying the method of the present invention, the evaporator 4
Prior to circulating and cleaning the spray nozzle 15 in the inside with a cleaning agent, the refrigerant (water) and the absorbing medium solution (the concentrated lithium bromide aqueous solution 13 and the dilute lithium bromide aqueous solution 14) forming the absorption cycle are taken out of the machine. Must be recovered. However, since the inside of the refrigerant circulation system is at a high vacuum, the fluid in the device does not flow out of the device only by providing the outflow path (in contrast, air is sucked vigorously). The inflow of air is extremely undesirable because it corrodes the interior of the equipment. Therefore, using an appropriate means (not shown), the refrigerant and the absorbing medium solution are recovered outside the machine while the inert gas (nitrogen in the present embodiment) flows into the refrigerant circulation system. At this time, the nitrogen gas pressure was set slightly higher than the atmospheric pressure to allow the liquid remaining in the pipe to flow out of the machine,
It is convenient to operate such that the residual liquid is blown off with the nitrogen gas. The recovered refrigerant and the absorbing medium solution are each placed in a plastic container, and the space in contact with the liquid surface is filled with nitrogen gas and temporarily stored.

【0020】洗浄液を入れた洗浄液循環タンク17を、
当該吸収式冷凍機の傍らへ一時的に設置し、上記洗浄液
を洗浄液循環ポンプ19で吸入、吐出してスプレーノズ
ル15から散布し、蒸発器4の下方の冷媒タンク5に溜
まった洗浄液は前記洗浄液循環タンク17に流下させ、
以上のようにして循環流動させる。上記洗浄液の組成に
ついて次に述べる。吸収式冷凍機の冷媒循環系統の構成
材料は、主として鉄系合金および銅系合金である。従っ
て、ノズルに付着する異物はこれら金属材料の腐食生成
物を主成分としている。このため、洗浄液に求められる
条件は、(イ)これらの金属材料に対して激しく反応し
ないこと、および(ロ)これら金属材料の腐食生成物を
溶解すること、である。上記イ,ロの条件を両立させる
ものとして、「塩酸,硫酸,硝酸,もしくはこれに類似
する無機酸」および「蓚酸,マロン酸,コハク酸,もし
くはこれに類似する有機酸」が有り、以上各種の酸の複
数種類を調合することもできる。
The cleaning liquid circulation tank 17 containing the cleaning liquid is
The cleaning liquid is temporarily installed beside the absorption refrigerator, and the cleaning liquid is sucked and discharged by the cleaning liquid circulation pump 19 and sprayed from the spray nozzle 15, and the cleaning liquid accumulated in the refrigerant tank 5 below the evaporator 4 is the cleaning liquid. It flows down to the circulation tank 17,
The fluid is circulated as described above. Next, the composition of the cleaning solution will be described. The constituent materials of the refrigerant circulation system of the absorption refrigerator are mainly iron-based alloys and copper-based alloys. Therefore, the foreign substances adhering to the nozzle are mainly composed of corrosion products of these metallic materials. Therefore, the conditions required for the cleaning liquid are (a) not to react violently with these metal materials, and (b) to dissolve corrosion products of these metal materials. There are "hydrochloric acid, sulfuric acid, nitric acid, or similar inorganic acids" and "oxalic acid, malonic acid, succinic acid, or similar organic acids" that satisfy the above conditions (a) and (b). It is also possible to prepare a plurality of types of acids.

【0021】上述の酸性薬剤は、冷媒循環系統を構成し
ている金属材料に対する腐食性がゼロではないので、腐
食抑制剤を添加することが望ましい。鉄鋼材料および
銅、並びに銅合金の腐食を抑制する薬剤としては、カル
ボン酸類、直鎖炭化水素化合物,アミン類,アゾール類
などが有効である。これらの腐食抑制剤の複数種類を調
合して用いることも可能である。さらに、金属塩類を酸
性水溶液で溶解する作業は電気化学的反応であるから、
金属塩(付着異物)の溶解を促進し、および/または地
金金属材料の腐食を抑制するためには、電位制御剤の併
用が望ましい。これについては、公知の還元性電位制御
剤を適用することができる。公知の還元性電位制御剤に
は無機系の薬剤と有機系の薬剤とが有るが、副作用(腐
食促進)の虞れの少ない有機系電位制御剤の方が望まし
い。
Since the above-mentioned acidic chemicals have a non-zero corrosiveness to the metal material constituting the refrigerant circulation system, it is desirable to add a corrosion inhibitor. Carboxylic acids, straight-chain hydrocarbon compounds, amines, azoles, and the like are effective as agents for suppressing corrosion of iron and steel materials, copper, and copper alloys. It is also possible to mix and use a plurality of these corrosion inhibitors. Furthermore, since the work of dissolving metal salts with an acidic aqueous solution is an electrochemical reaction,
In order to promote the dissolution of the metal salt (adhering foreign matter) and / or to suppress the corrosion of the metal ingot, it is desirable to use a potential control agent in combination. In this regard, a known reducing potential control agent can be applied. Known reducing potential control agents include an inorganic drug and an organic drug, and an organic potential control agent having a low risk of side effects (promotion of corrosion) is more preferable.

【0022】本実施形態(図1)においては、硫酸と蓚
酸とを主成分とし、市販のアミン系腐食抑制剤(インヒ
ビター)および市販の還元性電位制御剤を調合した酸性
(pH1)の水溶液を洗浄剤として、その200リット
ルを使用した。洗浄剤を本図1の矢印b〜fのように循
環させる間、機内の窒素圧力はほぼ1気圧にしておく、
これが高すぎると洗浄液を機内に送入する作業が容易で
はなく、」また低すぎると機内へ空気を混入させる危険
性が増えるからである。本実施例においては、20年間
の稼働によって目詰まりしたため、−100mmHgに低
下していたスプレー圧力を、2時間の循環洗浄によって
−400mmHg(新品と同レベル)に回復させることが
できた。上述のように酸性の洗浄液を循環させた後は、
この洗浄液を排出した後、残液を中和し、水洗しておか
ねばならない。洗浄液の排出は、機内の窒素ガスを大気
圧よりも高くして行ない、洗浄液を循環させたのと同様
ないし類似の操作によって、重量比3%の水酸化ナトリ
ウム水溶液の200リットルを20分間循環させた後、
リトマス試験紙によって循環液のpHが7.5になった
ことを確認して終了した。その後、洗浄液循環タンク1
7に上水200リットルを入れ、洗浄時と同様の操作
で、10分間循環させた後に排出し、予め準備しておい
た軟水200リットルを同様の操作で循環させて仕上げ
水洗した。仕上げ水洗の残液は、窒素ガス圧を揚げて完
全に除去する。
In this embodiment (FIG. 1), an acidic (pH 1) aqueous solution containing sulfuric acid and oxalic acid as main components and a commercially available amine-based corrosion inhibitor (inhibitor) and a commercially available reducing potential control agent is prepared. 200 liters thereof were used as a cleaning agent. While the cleaning agent is circulated as indicated by arrows b to f in FIG. 1, the nitrogen pressure in the apparatus is kept at approximately 1 atm.
If this is too high, the operation of feeding the cleaning liquid into the machine is not easy, and if it is too low, the risk of air being mixed into the machine increases. In this example, the spray pressure was reduced to -100 mmHg because of clogging due to operation for 20 years, and the spray pressure could be restored to -400 mmHg (the same level as a new product) by circulating cleaning for 2 hours. After circulating the acidic cleaning solution as described above,
After draining this washing solution, the remaining solution must be neutralized and washed with water. The discharge of the cleaning liquid is performed by setting the nitrogen gas inside the apparatus to a pressure higher than the atmospheric pressure, and circulating 200 liters of a 3% by weight sodium hydroxide aqueous solution for 20 minutes by the same or similar operation as circulating the cleaning liquid. After
The process was completed after confirming that the pH of the circulating fluid had reached 7.5 using litmus paper. Then, the cleaning liquid circulation tank 1
200 liters of clean water was placed in 7 and circulated for 10 minutes by the same operation as in the washing, and then discharged. 200 liters of soft water prepared in advance were circulated by the same operation and washed with finish water. The residual liquid of the finish washing is completely removed by raising the nitrogen gas pressure.

【0023】上述のようにして酸洗い循環,中和循環,
上水循環,および軟水循環の4工程を終えた後、窒素ガ
スの注入を停止し、吸収式冷凍機の付属機器である真空
ポンプ(図示省略)を作動させて、冷媒循環系統内を−
740mmHgの高真空ならしめて、先に回収して一時的
に保管してあった冷媒および吸収媒体溶液を再び機内に
封入し、さらに前記真空ポンプを運転して機内圧が−7
40mmHgに到達したことを確認して試運転した。この
試運転において、先に述べたように冷媒のスプレー圧が
−400mmHgに回復したことが確認された。
As described above, pickling circulation, neutralization circulation,
After completing the four steps of water circulation and soft water circulation, the injection of nitrogen gas is stopped, and a vacuum pump (not shown), which is an accessory device of the absorption refrigerator, is operated to cut the inside of the refrigerant circulation system.
A high vacuum of 740 mmHg was applied, the refrigerant and the absorbing medium solution which had been collected and stored temporarily were sealed in the machine again, and the vacuum pump was operated to reduce the machine pressure to -7.
After confirming that the pressure reached 40 mmHg, a trial operation was performed. In this test operation, it was confirmed that the spray pressure of the refrigerant was restored to -400 mmHg as described above.

【0024】図1を参照して以上に説明した実施形態に
おいては、臨時的な修理のため図1のように配管し、ス
プレーノズル洗浄後は修理前の配管に復元した。しか
し、次回のスプレーノズル洗浄を迅速容易ならしめるた
め、配管の1部を残しておくとともに有意義である。ま
た、新機を製作した当初から、ノズル洗浄のための配管
について、その接続部分だけを設けておくことも望まし
い。ノズル洗浄を迅速,容易に行なうことができれば、
前述した例のように冷媒のスプレー圧が−100mmHg
まで低下してしまうまで放置せず、定期整備の一環とし
てノズル洗浄を用ない、常に新品同様の冷凍性能で稼働
させることができる。図2は、上述のような考慮に基づ
いて創作したノズル洗浄装置(機能回復装置)の模式的
な系統図である。符号Wを付して示した部分は洗浄回路
であって、定期整備のとき接続し、普段は取り外してお
く。符号Mを付して示した部分は冷媒回路であって、通
常の稼働時に使用される。この図2について、冷媒循環
締切弁23a,23bを開くとともに、洗浄回路接続用
閉止弁24a,24bを閉じた状態を考えると、図3に
示した従来例の吸収式冷凍機と同様に機能することが理
解される。また、洗浄回路接続用閉止弁24a,24b
を開いて、冷媒循環締切弁23a,23bを閉じた状態
を考えると、図1に示したノズル洗浄装置(性能回復装
置)と同様に機能することが理解される。
In the embodiment described above with reference to FIG. 1, piping is provided as shown in FIG. 1 for temporary repair, and after cleaning the spray nozzle, the piping is restored to that before repair. However, in order to quickly and easily clean the next spray nozzle, it is meaningful to leave a part of the piping. It is also desirable to provide only the connection portion of the pipe for nozzle cleaning from the beginning of the production of the new machine. If nozzle cleaning can be performed quickly and easily,
The spray pressure of the refrigerant is -100 mmHg as in the above example.
It is possible to always operate with the same refrigeration performance as a new one without leaving it until it has dropped and without using nozzle cleaning as part of regular maintenance. FIG. 2 is a schematic system diagram of a nozzle cleaning device (function recovery device) created based on the above considerations. The portion indicated by the reference symbol W is a cleaning circuit, which is connected during regular maintenance and is usually removed. The portion indicated by reference numeral M is a refrigerant circuit, which is used during normal operation. Referring to FIG. 2, when the refrigerant circulation shut-off valves 23a and 23b are opened and the cleaning circuit connection shut-off valves 24a and 24b are closed, it functions in the same manner as the conventional absorption type refrigerator shown in FIG. It is understood that. Further, the closing valves 24a and 24b for connecting the cleaning circuits are provided.
In consideration of a state in which the refrigerant circulation shut-off valves 23a and 23b are closed when the nozzle cleaning device is opened, it is understood that it functions similarly to the nozzle cleaning device (performance recovery device) shown in FIG.

【0025】本図2に示した装置を新品製造時に備えて
おく場合は、冷媒スプレーポンプ6の上流側(吸入側)
と下流側(吐出側)とのそれぞれに冷媒循環締切弁23
a,23bを介挿接続するとともに、上記冷媒循環締切
弁23aの上流側と下流側とのそれぞれに分岐管路を設
けて、該分岐管路の先端に洗浄回路接続用24a,24
bを装着して閉止しておくだけで良い。このように構成
された場合の実用的効果は次のごとくである。本発明の
出願人は、設置された吸収式冷凍機の整備管理を委託さ
れる技術サービス会社であり、本発明者はその従業員で
ある。こうした立場から見れば、図3において鎖線で囲
んで符号Wをタンクとポンプとホースとをサービスカー
に積んで、客先であるユーザーを巡回すれば、迅速かつ
容易にノズルを洗浄して、常に定格の冷凍性能を発揮さ
せることができる。この場合、1組のポンプとタンクと
ホースとによって、多数の吸収式冷凍機に対応できるた
め、省資源という社会的要請に関しても貢献することが
できる。また、吸収式冷凍機のユーザーの立場から見る
と、吸収式冷凍機を設置した機械室に別段の機器を常備
する必要が無く、しかも安い費用で冷凍機能を新品同様
に維持して貰うことができる。
When the apparatus shown in FIG. 2 is prepared at the time of manufacture of a new product, it is necessary to provide an upstream side (a suction side) of the refrigerant spray pump 6.
And the downstream side (discharge side) of the refrigerant circulation shutoff valve 23 respectively.
a and 23b, and a branch pipe line is provided on each of the upstream and downstream sides of the refrigerant circulation shutoff valve 23a.
It is only necessary to attach b and keep it closed. Practical effects of such a configuration are as follows. The applicant of the present invention is a technical service company entrusted with the maintenance and management of the installed absorption refrigerator, and the present inventor is an employee thereof. From this standpoint, in FIG. 3, a symbol W is enclosed by a chain line, and a tank, a pump, and a hose are loaded on a service car. Rated refrigeration performance can be exhibited. In this case, since one set of pump, tank and hose can cope with a large number of absorption refrigerators, it can also contribute to social demands for resource saving. Also, from the point of view of users of absorption chillers, there is no need to keep separate equipment in the machine room where the absorption chiller is installed, and it is possible to have the refrigeration function maintained as new at a low cost. it can.

【0026】[0026]

【発明の効果】以上に本発明の実施形態を挙げてその構
成機能を説明したように、請求項1の発明方法による
と、蒸発器を切開して露出させなくても、冷凍機のケー
ス外に設けた洗浄液循環タンクや洗浄液循環タンクを用
いて遠隔的にスプレーノズルを洗浄して異物を除去し、
性能を回復させることができる。請求項2の発明方法に
よると、複数種類の薬剤を調合した酸性溶液を用いるこ
とにより、鉄系腐食生成物および銅系腐食生成物の両方
を含むスプレーノズル堆積物を効果的に溶解除去するこ
とができる。請求項3の発明方法によると、スプレーノ
ズルに堆積した腐食生成物を能率的に溶解除去すること
ができ、しかも、冷媒循環系統を構成している金属材料
を腐食させるなどの不具合を生じる虞れが無い。請求項
4の発明方法によると、スプレー系統を構成している金
属製容器や金属製管路の内側面を空気によって酸化腐食
させる虞れが無い。請求項5の発明方法によると、冷媒
循環系統の内部空間が空気に接触することを、迅速容
易、かつ完全に遮断することができる。請求項6の発明
方法によると、冷媒および吸収媒体溶液に、洗浄用薬剤
を混入せしめる虞れ無くスプレーノズルの堆積物を洗浄
除去することができる。請求項7の発明方法によると、
中和剤の廃液を河川に放流することができる。すなわ
ち、本発明を適用しても循環系統内にpH6の微酸性や
pH8の微アルカリ性の中和剤廃液が残っていては、そ
のまま冷媒や吸収媒体溶液を注入して冷凍サイクルを再
開することはできなので更に水洗するなどしなければな
らないが抜き取った中和剤廃液(pH6〜8)は河川に
放流することができる。請求項8の発明方法によると、
蒸発器その他の構成機器の内部を効率良く、かつ完全に
中性に戻して冷凍サイクル再開に支障の無い状態ならし
めることができる。請求項9の発明方法によると、機内
圧と大気圧とをバランスさせた状態でスプレー系統内に
洗浄液を循環せしめることができ、かつ、上記洗浄液を
迅速,容易に機外へ排出することができる。請求項10
の発明方法によると、既設の吸収式冷凍機に対して大き
い改造を加えることなく、かつ蒸発器を切開することな
く、スプレーノズルを薬液洗浄することができる。請求
項11の発明装置によると、前記請求項1に係る発明方
法を容易に実施して、その効果を充分に発揮せしめるこ
とができる。
As described above, according to the first embodiment of the present invention, according to the method of the present invention, even if the evaporator is not cut and exposed, the evaporator can be opened outside the case of the refrigerator. Cleaning the spray nozzle remotely using the cleaning liquid circulation tank or cleaning liquid circulation tank provided in
Performance can be restored. According to the method of the present invention, the spray nozzle deposit containing both the iron-based corrosion product and the copper-based corrosion product can be effectively dissolved and removed by using an acidic solution prepared by mixing a plurality of types of chemicals. Can be. According to the method of the present invention, corrosion products deposited on the spray nozzle can be efficiently dissolved and removed, and in addition, there is a possibility that a problem such as corrosion of a metal material constituting a refrigerant circulation system may occur. There is no. According to the method of the present invention, there is no fear that the inner surface of the metal container or the metal pipe constituting the spray system is oxidized and corroded by air. According to the method of the fifth aspect, it is possible to quickly, easily, and completely shut off the contact of the internal space of the refrigerant circulation system with the air. According to the sixth aspect of the present invention, the deposits on the spray nozzle can be washed away without fear of mixing the cleaning agent into the refrigerant and the absorbing medium solution. According to the invention method of claim 7,
The neutralizer waste liquid can be discharged to the river. That is, even if the present invention is applied, if a slightly acidic neutral solution having a pH of 6 or a slightly alkaline neutral solution having a pH of 8 remains in the circulation system, it is not possible to restart the refrigeration cycle by directly injecting the refrigerant or the absorbing medium solution. Since it is completed, it must be further washed with water, etc., but the extracted neutralizer waste liquid (pH 6 to 8) can be discharged to the river. According to the invention method of claim 8,
The inside of the evaporator and other constituent devices can be efficiently and completely returned to neutral, so that there is no problem in restarting the refrigeration cycle. According to the ninth aspect of the present invention, the cleaning liquid can be circulated in the spray system in a state where the internal pressure and the atmospheric pressure are balanced, and the cleaning liquid can be quickly and easily discharged out of the apparatus. . Claim 10
According to the method of the invention, the spray nozzle can be cleaned with the chemical solution without making a major modification to the existing absorption refrigerator and without cutting the evaporator. According to the apparatus of the eleventh aspect, the method of the first aspect can be easily implemented, and its effect can be sufficiently exhibited.

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

【図1】本発明の1実施形態を示す模式的な系統図であ
る。
FIG. 1 is a schematic system diagram showing one embodiment of the present invention.

【図2】上掲の図1と異なる実施形態における模式的な
系統図である。
FIG. 2 is a schematic system diagram in an embodiment different from FIG. 1 described above.

【図3】吸収式冷凍機の従来例を示す系統図である。FIG. 3 is a system diagram showing a conventional example of an absorption refrigerator.

【図4】前掲の図3に示した従来例におけるスプレーノ
ズル付近の拡大断面図である。
FIG. 4 is an enlarged sectional view of the vicinity of a spray nozzle in the conventional example shown in FIG.

【符号の説明】[Explanation of symbols]

1…高温再生器、2…低温再生器、3…凝縮器、4…蒸
発器、5…冷媒タンク、6…冷媒スプレーポンプ、8…
スプレーダクト、9…吸収器、15…スプレーノズル、
17…洗浄液循環タンク、19…洗浄液循環ポンプ、2
0…封止板、23a,23b…冷媒循環締切弁、24
a,24b…洗浄回路接続用閉止弁、26…吸入管、2
7…フィルタ。
DESCRIPTION OF SYMBOLS 1 ... High temperature regenerator, 2 ... Low temperature regenerator, 3 ... Condenser, 4 ... Evaporator, 5 ... Refrigerant tank, 6 ... Refrigerant spray pump, 8 ...
Spray duct, 9 ... absorber, 15 ... spray nozzle,
17 cleaning liquid circulation tank, 19 cleaning liquid circulation pump, 2
0: sealing plate, 23a, 23b: refrigerant circulation shut-off valve, 24
a, 24b: shut-off valve for connecting the washing circuit, 26: suction pipe, 2
7 ... Filter.

Claims (11)

【特許請求の範囲】[Claims] 【請求項1】 水を冷媒とし、吸収媒体として臭化リチ
ウムを用いる吸収式冷凍機について、 冷媒をスプレーする散布装置に異物が付着、堆積して性
能が低下した場合、その性能を回復させる方法におい
て、 冷媒の散布系統を、薬液によって化学的に洗浄して前記
の異物を除去することを特徴とする吸収式冷凍機の性能
回復方法。
1. An absorption refrigerator using water as a refrigerant and lithium bromide as an absorption medium. A method for restoring the performance of a spraying device for spraying a refrigerant when foreign matter adheres and accumulates and deteriorates. The method for recovering the performance of an absorption refrigerator according to any one of claims 1 to 4, wherein the foreign matter is removed by chemically cleaning the refrigerant distribution system with a chemical solution.
【請求項2】 前記の化学的洗浄に用いる薬液は、2種
類以上の化学薬品からなる酸性水溶液であることを特徴
とする請求項1に記載した吸収式冷凍機の性能回復方
法。
2. The method according to claim 1, wherein the chemical used for the chemical cleaning is an acidic aqueous solution comprising two or more chemicals.
【請求項3】 前記の酸性水溶液は、塩酸、硫酸、硝
酸、もしくはこれに類似する無機酸、および蓚酸、マロ
ン酸、コハク酸もしくはこれに類似する有機酸の内の少
なくとも1種類を主成分とし、 かつ、腐食抑制剤および電位制御剤の少なくとも何れか
一方を含有していることを特徴とする、請求項2に記載
した吸収式冷凍機の性能回復方法。
3. The acidic aqueous solution contains, as a main component, at least one of hydrochloric acid, sulfuric acid, nitric acid or an inorganic acid similar thereto, and oxalic acid, malonic acid, succinic acid or an organic acid similar thereto. The method according to claim 2, further comprising at least one of a corrosion inhibitor and a potential control agent.
【請求項4】 冷媒の散布系統を薬液で洗浄する際、該
散布系統の内部表面に空気を接触させないことを特徴と
する請求項1に記載した吸収式冷凍機の性能回復方法。
4. The method for recovering the performance of an absorption refrigerator according to claim 1, wherein, when the spraying system of the refrigerant is washed with a chemical, air is not brought into contact with the inner surface of the spraying system.
【請求項5】 散布系統の内面に空気を接触させないた
め、当該吸収式冷凍機の冷媒循環系統の内部空間に不活
性ガスを充満させた状態で前記の洗浄を行なうことを特
徴とする請求項4に記載した吸収式冷凍機の性能回復方
法。
5. The method according to claim 1, wherein the cleaning is performed in a state where the internal space of the refrigerant circulating system of the absorption chiller is filled with an inert gas so that air does not contact the inner surface of the spraying system. 4. The method for recovering performance of an absorption refrigerator described in 4.
【請求項6】 前記の薬液によって散布系統を洗浄する
際、当該吸収式冷凍機の冷媒循環系統内から冷媒および
吸収媒体溶液を予め冷媒循環系統外に回収して一時的に
保管しておき、機内の薬液循環洗浄および薬液の水洗除
去を終えてから洗浄液を機外に排出した後、 保管してあった冷媒および吸収媒体溶液を冷媒循環系統
内に注入することを特徴とする請求項1に記載した吸収
式冷凍機の性能回復方法。
6. When the spraying system is washed with the chemical solution, the refrigerant and the absorbing medium solution are recovered from the refrigerant circulating system of the absorption chiller beforehand outside the refrigerant circulating system and temporarily stored therein. The method according to claim 1, wherein after the cleaning and rinsing of the chemical solution in the machine and the washing and removal of the chemical solution are completed, the cleaning solution is discharged outside the machine, and then the stored refrigerant and the absorbing medium solution are injected into the refrigerant circulating system. The described method of restoring the performance of the absorption refrigerator.
【請求項7】 前記の酸性水溶液によって散布系統を洗
浄した後、アルカリ性の中和剤溶液を循環させて、残存
していた酸性水溶液を中和除去し、pHが6.0〜8.
0のほぼ中性になったことを検知してから中和操作を終
了することを特徴とする請求項2に記載した吸収式冷凍
機の性能回復方法。
7. The spray system is washed with the acidic aqueous solution, and thereafter, an alkaline neutralizing agent solution is circulated to neutralize and remove the remaining acidic aqueous solution.
3. The method according to claim 2, wherein the neutralization operation is terminated after detecting that the value becomes substantially neutral to zero.
【請求項8】 冷媒散布系統内がpH6.0〜8.0に
なるまで中和操作を行った後、中和剤溶液を排出して上
水を入れ、該上水を散布系統内で循環させた後、上記洗
浄用上水の洗浄廃液を機外に排出し、 軟水を冷媒循環系統内に流動させて仕上げ水洗し、仕上
げ水洗廃液を機外に排出することを特徴とする、請求項
7に記載した吸収式冷凍機の性能回復方法。
8. After performing a neutralization operation until the inside of the refrigerant spraying system reaches pH 6.0 to 8.0, the neutralizing agent solution is discharged and clean water is introduced, and the clean water is circulated in the spray system. After the cleaning, the cleaning wastewater of the cleaning water is discharged out of the machine, the soft water is flown into the refrigerant circulation system to perform the finish washing, and the finished washing wastewater is discharged outside the machine. 7. The method for recovering performance of an absorption refrigerator described in 7.
【請求項9】 冷媒循環系統内に不活性ガスを充満させ
て洗浄液を循環させる際は、機内のガス圧をほぼ大気圧
に等しからしめた状態で洗浄を行ない、 薬液洗浄、中和剤洗浄、および水洗を終えた後、前記の
ガス圧を大気圧よりも上昇させて、前記不活性ガスの圧
力を機外に放出しつつ、この放出圧力によって前記水洗
に用いた洗浄水の機内残留部分を機外に放出することを
特徴とする請求項5に記載した吸収式冷凍機の性能回復
方法。
9. When circulating the cleaning liquid by filling the refrigerant circulation system with an inert gas, the cleaning is performed while keeping the gas pressure in the machine substantially equal to the atmospheric pressure, and the chemical liquid cleaning and neutralizing agent are used. After the washing and the water washing are completed, the gas pressure is raised above the atmospheric pressure to release the pressure of the inert gas to the outside of the machine. 6. The method according to claim 5, wherein the part is discharged outside the machine.
【請求項10】 冷媒の散布系統を薬液で洗浄する際、 当該吸収式冷凍機の冷媒循環系路外に洗浄液循環タンク
(17)を設けて、この中に洗浄液を入れておき、 上記洗浄液を洗浄液循環ポンプ(19)で吸入,圧送し
て、当該吸収式冷温水機の蒸発器内に本来的に設けられ
ている散布装置(15)から噴射させ、 上記散布装置から噴射されて蒸発器底部の冷媒タンク
(5)に溜まった洗浄水を前記洗浄液循環タンク(1
7)に導いて、前記洗浄液循環ポンプ(19)によって
吸入され得る状態ならしめ、 上述のようにして洗浄液を循環流動せしめつつ散布装置
(15)流通せしめることを特徴とする、請求項1に記
載した吸収式冷凍機の性能回復方法。
10. A washing liquid circulation tank (17) is provided outside the refrigerant circulation system path of the absorption refrigerator when washing the spraying system of the refrigerant with the chemical liquid, and the washing liquid is put in the tank, and the washing liquid is put in the tank. It is sucked and pumped by a washing liquid circulation pump (19), and is sprayed from a spraying device (15) originally provided in the evaporator of the absorption type chiller / heater. The washing water accumulated in the refrigerant tank (5) of the washing liquid circulation tank (1)
The method according to claim 1, wherein the cleaning liquid circulation pump (19) guides the cleaning liquid to a state in which the cleaning liquid can be sucked by the cleaning liquid circulation pump (19). To recover the performance of absorption chillers.
【請求項11】 冷媒として水を用い、吸収媒体として
臭化リチウムを用いる吸収式冷凍機であって、その蒸発
器(4)の中に冷媒液を噴射する散布装置(15)が設
けられるとともに、該散布装置から噴射されて蒸発器の
底部に溜まった冷媒液を吸入して上記散布装置に送給す
る冷媒スプレーポンプ(6)を備えているものにおい
て、 上記冷媒スプレーポンプの吸入側管路と吐出側管路との
それぞれに、冷媒循環締切弁(23a,23b)が介挿
接続され、 かつ、上記吸入側管路に設けられた冷媒循環締切弁(2
3a)の上流側管路に分岐管が設けられて、その先端に
洗浄回路接続用閉止弁(24a)が接続されるととも
に、前記吐出側管路に設けられた冷媒循環締切弁(23
b)の下流側管路に分岐管が設けられて、その先端に洗
浄回路接続用閉止弁(24b)が接続されていることを
特徴とする吸収式冷凍機の性能回復装置。
11. An absorption refrigerator using water as a refrigerant and lithium bromide as an absorption medium, wherein an evaporator (4) is provided with a spray device (15) for injecting a refrigerant liquid. And a refrigerant spray pump (6) for sucking refrigerant liquid ejected from the spraying device and collected at the bottom of the evaporator and feeding the liquid to the spraying device. A refrigerant circulation shut-off valve (23a, 23b) is inserted and connected to each of the discharge side pipeline and the refrigerant circulation shut-off valve (2) provided on the suction side pipeline.
A branch pipe is provided in the upstream pipe of 3a), a cleaning circuit connection closing valve (24a) is connected to the tip of the branch pipe, and a refrigerant circulation shut-off valve (23) provided in the discharge pipe.
A performance recovery device for an absorption refrigerator, wherein a branch pipe is provided in a downstream pipe line of b), and a closing valve (24b) for connecting a washing circuit is connected to a tip of the branch pipe.
JP2000393813A 2000-12-25 2000-12-25 Absorption refrigerator performance recovery method and apparatus Expired - Lifetime JP3787757B2 (en)

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Application Number Priority Date Filing Date Title
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Publication Number Publication Date
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JP3787757B2 JP3787757B2 (en) 2006-06-21

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JP2007303689A (en) * 2006-05-08 2007-11-22 Hitachi Kyowa Engineering Co Ltd Refrigerant purifying device and absorption type cooling and heating machine comprising the same
CN102954622A (en) * 2012-11-28 2013-03-06 江荣方 Absorption energy recovering and upgrading device
CN102954617A (en) * 2012-11-27 2013-03-06 西安交通大学 Compound heat pump with steam type injection/lithium bromide absorption
CN102954616A (en) * 2012-11-27 2013-03-06 西安交通大学 Exhaust steam direct-absorption type lithium bromide heat pump system
CN106546031A (en) * 2016-10-21 2017-03-29 西安世康佰宜能源新技术有限责任公司 Green heat pump refrigerating heating system, refrigerating and heating method and air-conditioning

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007303689A (en) * 2006-05-08 2007-11-22 Hitachi Kyowa Engineering Co Ltd Refrigerant purifying device and absorption type cooling and heating machine comprising the same
CN102954617A (en) * 2012-11-27 2013-03-06 西安交通大学 Compound heat pump with steam type injection/lithium bromide absorption
CN102954616A (en) * 2012-11-27 2013-03-06 西安交通大学 Exhaust steam direct-absorption type lithium bromide heat pump system
CN102954622A (en) * 2012-11-28 2013-03-06 江荣方 Absorption energy recovering and upgrading device
CN106546031A (en) * 2016-10-21 2017-03-29 西安世康佰宜能源新技术有限责任公司 Green heat pump refrigerating heating system, refrigerating and heating method and air-conditioning
CN106546031B (en) * 2016-10-21 2019-03-05 张晓康 Green heat pump refrigerating heating system, refrigerating and heating method and air-conditioning

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