JP2584728Y2 - Ammonia removal device in absorption refrigerator - Google Patents

Ammonia removal device in absorption refrigerator

Info

Publication number
JP2584728Y2
JP2584728Y2 JP1991011366U JP1136691U JP2584728Y2 JP 2584728 Y2 JP2584728 Y2 JP 2584728Y2 JP 1991011366 U JP1991011366 U JP 1991011366U JP 1136691 U JP1136691 U JP 1136691U JP 2584728 Y2 JP2584728 Y2 JP 2584728Y2
Authority
JP
Japan
Prior art keywords
absorption refrigerator
absorption
refrigerant
adsorbent
removal device
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.)
Expired - Lifetime
Application number
JP1991011366U
Other languages
Japanese (ja)
Other versions
JPH04110350U (en
Inventor
純 黒田
健二 高橋
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.)
Yazaki Corp
Original Assignee
Yazaki Corp
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 Yazaki Corp filed Critical Yazaki Corp
Priority to JP1991011366U priority Critical patent/JP2584728Y2/en
Publication of JPH04110350U publication Critical patent/JPH04110350U/en
Application granted granted Critical
Publication of JP2584728Y2 publication Critical patent/JP2584728Y2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Sorption Type Refrigeration Machines (AREA)

Description

【考案の詳細な説明】[Detailed description of the invention]

【0001】[0001]

【産業上の利用分野】本考案は、吸収溶液中に硝酸塩及
び/又は亜硝酸塩を含む吸収式冷凍機内のアンモニア除
去装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for removing ammonia in an absorption refrigerator containing nitrate and / or nitrite in an absorption solution.

【0002】[0002]

【従来の技術】吸収式冷凍機の吸収溶液中に硝酸塩又は
亜硝酸塩を含むものは、同機内で腐食等によって凝縮性
ガスであるアンモニア(NH3)が発生する。このNH3
は同機内の真空度を低下させると共に、冷媒中に溶け込
んで銅材を腐食させるため、該NH3を除去する必要が
ある。従来、このNH3の除去は通常のガス排気法では
除去できないため、メンテナンスにより行なわれてい
る。また、冷温水等を用いるエゼクター方式で排出する
方法もある。
2. Description of the Related Art When nitrate or nitrite is contained in an absorption solution of an absorption refrigerator, ammonia (NH 3 ) as a condensable gas is generated in the absorption refrigerator due to corrosion or the like. This NH 3
It is necessary to remove the NH 3 because it lowers the degree of vacuum in the machine and dissolves in the refrigerant to corrode the copper material. Conventionally, since the removal of NH 3 cannot be removed by a normal gas exhaust method, it is performed by maintenance. There is also a method of discharging by an ejector method using cold and hot water.

【0003】[0003]

【考案が解決しようとする課題】吸収式冷凍機内の真空
度が低下する度に、抽気メンテナンスしてNH3を除去
していたのでは、使用効率が低く、また、NH3は冷媒
に溶け込んでいるため、その除去も充分には行なえない
問題があった。一方、冷温水等を用いたエゼクター方式
ではNH3が冷温水等に溶け込み、銅コイルの応力腐食
割れを起こす危険があった。
[Problems to be Solved by the Invention] When NH 3 is removed by bleeding maintenance every time the degree of vacuum in the absorption refrigerator decreases, the usage efficiency is low, and NH 3 dissolves in the refrigerant. Therefore, there is a problem that it cannot be sufficiently removed. On the other hand, in the ejector method using cold and hot water, there was a risk that NH 3 would be dissolved in cold and hot water and the like, causing stress corrosion cracking of the copper coil.

【0004】本考案の目的は、ノーメンテナンスで吸収
式冷凍機内の高真空を保つことができ、銅材を腐食させ
る恐れの少ない吸収式冷凍機内のNH3除去装置を提供
することにある。
An object of the present invention is to provide an NH 3 removal apparatus in an absorption refrigerator that can maintain a high vacuum in the absorption refrigerator without maintenance and is less likely to corrode a copper material.

【0005】[0005]

【課題を解決するための手段】上記目的を達成するた
め、本考案は、吸収溶液中に硝酸塩及び/又は亜硝酸塩
を含む吸収式冷凍機内のアンモニア除去装置において、
吸収冷凍機内のコンデンサーからエバポレーターへ至る
冷媒回路の中に冷媒液中のアンモニウムイオンを吸着す
るイオン交換型のアルミニウム化合物とけい素化合物と
を含む合成吸着剤を設けたことを特徴とする吸収式冷凍
機内のアンモニア除去装置である。
In order to achieve the above object, the present invention provides an apparatus for removing ammonia in an absorption refrigerator containing nitrate and / or nitrite in an absorption solution.
In the refrigerant circuit from the condenser in the absorption refrigerator to the evaporator, a synthetic adsorbent containing an ion exchange type aluminum compound and a silicon compound that adsorbs ammonium ions in the refrigerant liquid is provided in the refrigerant circuit. It is an ammonia removal device in an absorption refrigerator.

【0006】[0006]

【作用】吸収溶液中に硝酸塩及び/又は亜硝酸塩を含む
吸収冷凍機は、その運転により機内でNH3が発生する
が、このNH3は冷媒中に溶け込んでNH4イオンとなる
ため、吸収冷凍機内のコンデンサーからエバポレーター
へ至る冷媒回路中に設けられたイオン交換型のアルミニ
ウム化合物とけい素化合物とを含む合成吸着剤により吸
着除去される。従って、同機内の高真空状態が維持され
る。しかもノーメンテナンスである。
In an absorption refrigerator containing nitrate and / or nitrite in the absorption solution, NH 3 is generated inside the absorption chiller due to its operation. Since NH 3 dissolves in the refrigerant to form NH 4 ions, the absorption refrigeration is performed. Evaporator from in-flight condenser
Is adsorbed and removed by a synthetic adsorbent containing an ion-exchange type aluminum compound and a silicon compound provided in a refrigerant circuit leading to the refrigerant circuit. Therefore, the high vacuum state in the machine is maintained. Moreover, there is no maintenance.

【0007】[0007]

【実施例】以下、本考案の一実施例を図面に基づいて詳
細に説明する。図1において、1はコンデンサー、2は
冷媒ポンプ、3は冷媒貯蔵室、6はエバポレーター、7
はアブソーバーを示す。本実施例では、コンデンサー1
下部からエバポレーター6へ至るまでの間の冷媒回路8
にNH3が冷媒に溶け込んでNH4イオンとなったもの
を吸着する吸着剤5が設けられている。この吸着剤はア
ルカリ吸着能を持つイオン交換型のアルミニウム化合物
とけい素化合物とを含む合成吸着剤で、例えばAl23
・9SiO2・nH2Oである。この物質は、固体酸強度
の強い物質で非常に強いアルカリ吸着能を有している。
すなわちカチオン交換能を有している。また塩基性色素
も吸着する能力を有している。この物質が吸着剤チャン
バー4内に充填されている。この吸着剤チャンバー4は
カセット式にしてNH4イオンを吸着した後、容易に交
換できるようにするのが望ましい。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS One embodiment of the present invention will be described below in detail with reference to the drawings. In FIG. 1, 1 is a condenser, 2 is a refrigerant pump, 3 is a refrigerant storage room, 6 is an evaporator, 7
Indicates an absorber. In this embodiment, the condenser 1
Refrigerant circuit 8 from the bottom to evaporator 6
Adsorbent 5 NH 3 adsorbs and was the NH 4 ions dissolved in the refrigerant liquid is provided in the. This adsorbent is a synthetic adsorbent containing an ion-exchange type aluminum compound and a silicon compound having an alkali adsorption ability, for example, Al 2 O 3
· 9SiO 2 · nH 2 O. This substance is a substance having a strong solid acid strength and a very strong alkali adsorption ability.
That is, it has a cation exchange ability. It also has the ability to adsorb basic dyes. This substance is filled in the adsorbent chamber 4. This adsorbent chamber 4 is desirably made into a cassette type so that it can be easily replaced after adsorbing NH 4 ions.

【0008】次に上記実施例の作用を説明する。吸収式
冷凍機内で発生したNH3ガスは主に冷媒中に溶け込
む。そしてNH4イオンの状態となる。このNH4イオン
を含む冷媒がコンデンサ1とエバポレーター6間を流
れるとき、吸着剤5と接触し、NH4イオンはイオン交
換型の吸着剤に化学的に吸着される。この化学吸着によ
り一度吸着されたNH3は脱着しないので、冷媒中のN
3は漸次吸着除去され、これにより吸収式冷凍機内の
真空度が高真空に維持される。且つそのために抽気メン
テナンスも不要であり、また銅材の腐食の恐れも少な
い。吸着剤の吸着量が飽和したら、新たな吸着剤に交換
することにより、常にNH3を除去することができる。
Next, the operation of the above embodiment will be described. The NH 3 gas generated in the absorption refrigerator mainly dissolves in the refrigerant liquid . And it will be in the state of NH 4 ions. When the refrigerant liquid containing NH 4 ions flows between the condenser 1 and the evaporator 6, the refrigerant liquid comes into contact with the adsorbent 5 and the NH 4 ions are chemically adsorbed by the ion exchange type adsorbent. Since NH 3 once adsorbed by this chemisorption does not desorb, N 3 in the refrigerant
H 3 is gradually absorbed and removed, whereby the degree of vacuum in the absorption refrigerator is maintained at a high vacuum. In addition, no bleeding maintenance is required, and there is little risk of corrosion of the copper material. When the adsorption amount of the adsorbent is saturated, NH 3 can be constantly removed by replacing the adsorbent with a new adsorbent.

【0009】[0009]

【考案の効果】本考案によれば、吸収溶液中に硝酸塩及
び/又は亜硝酸塩を含む吸収式冷凍機において、その運
転中に発生したNH3を常に吸着剤により除去するた
め、吸収式冷凍機内を常に高真空に維持しておくことが
できると共に、銅材の腐食の恐れも少なくすることがで
きる。
According to the present invention, in an absorption refrigerator containing nitrate and / or nitrite in an absorption solution, NH 3 generated during the operation is always removed by an adsorbent. Can always be maintained in a high vacuum, and the risk of corrosion of the copper material can be reduced.

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

【図1】本考案に係る装置の構成図である。FIG. 1 is a configuration diagram of an apparatus according to the present invention.

【符号の説明】[Explanation of symbols]

1 コンデンサー 3 冷媒貯蔵室 4 吸着剤チャンバー 5 吸着剤 DESCRIPTION OF SYMBOLS 1 Condenser 3 Refrigerant storage room 4 Adsorbent chamber 5 Adsorbent

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.6,DB名) F25B 43/04──────────────────────────────────────────────────の Continued on the front page (58) Field surveyed (Int.Cl. 6 , DB name) F25B 43/04

Claims (1)

(57)【実用新案登録請求の範囲】(57) [Scope of request for utility model registration] 【請求項1】 吸収溶液中に硝酸塩及び/又は亜硝酸塩
を含む吸収式冷凍機内のアンモニア除去装置において、
吸収冷凍機内のコンデンサーからエバポレーターへ至る
冷媒回路の中に冷媒液中のアンモニウムイオンを吸着す
るイオン交換型のアルミニウム化合物とけい素化合物と
を含む合成吸着剤を設けたことを特徴とする吸収式冷凍
機内のアンモニア除去装置。
1. An ammonia removing apparatus in an absorption refrigerator including nitrate and / or nitrite in an absorption solution,
The refrigerant circuit from the condenser in the absorption refrigerator to the evaporator is provided with a synthetic adsorbent containing an ion exchange type aluminum compound and a silicon compound that adsorbs ammonium ions in the refrigerant liquid in the refrigerant circuit. Ammonia removal device in absorption refrigerator.
JP1991011366U 1991-03-05 1991-03-05 Ammonia removal device in absorption refrigerator Expired - Lifetime JP2584728Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1991011366U JP2584728Y2 (en) 1991-03-05 1991-03-05 Ammonia removal device in absorption refrigerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1991011366U JP2584728Y2 (en) 1991-03-05 1991-03-05 Ammonia removal device in absorption refrigerator

Publications (2)

Publication Number Publication Date
JPH04110350U JPH04110350U (en) 1992-09-24
JP2584728Y2 true JP2584728Y2 (en) 1998-11-05

Family

ID=31900737

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1991011366U Expired - Lifetime JP2584728Y2 (en) 1991-03-05 1991-03-05 Ammonia removal device in absorption refrigerator

Country Status (1)

Country Link
JP (1) JP2584728Y2 (en)

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5093281A (en) * 1973-12-24 1975-07-25
JPS5522412B2 (en) * 1974-03-13 1980-06-17
JPS52148959A (en) * 1976-06-04 1977-12-10 Asahi Chem Ind Co Ltd Treating method of ammoniacal nitrogen compound contained in a solution
JPS52154792A (en) * 1976-06-08 1977-12-22 Asahi Chemical Ind Process for purifying stowing water for live fish and shellfishes
JPS5325313A (en) * 1976-08-20 1978-03-09 Mitsubishi Electric Corp Relay circuit
JPS5418714A (en) * 1977-08-17 1979-02-13 Mansei Kogyo Kk Device for reproducing digital information from audio cassette tape
JPH01312368A (en) * 1988-06-10 1989-12-18 Hitachi Ltd Absorptive type refrigerator, ammonia removing method, ammonia removing device and ammonia gas removing agent

Also Published As

Publication number Publication date
JPH04110350U (en) 1992-09-24

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