JPH08143851A - Recycling system for anti-freezing solution - Google Patents

Recycling system for anti-freezing solution

Info

Publication number
JPH08143851A
JPH08143851A JP28476894A JP28476894A JPH08143851A JP H08143851 A JPH08143851 A JP H08143851A JP 28476894 A JP28476894 A JP 28476894A JP 28476894 A JP28476894 A JP 28476894A JP H08143851 A JPH08143851 A JP H08143851A
Authority
JP
Japan
Prior art keywords
membrane
antifreeze
component
reverse osmosis
solution
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.)
Pending
Application number
JP28476894A
Other languages
Japanese (ja)
Inventor
Kunihisa Uruno
邦久 宇留野
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 Ltd
Hitachi Automotive Systems Engineering Co Ltd
Original Assignee
Hitachi Automotive Engineering Co Ltd
Hitachi Ltd
Hitachi Car Engineering 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 Automotive Engineering Co Ltd, Hitachi Ltd, Hitachi Car Engineering Co Ltd filed Critical Hitachi Automotive Engineering Co Ltd
Priority to JP28476894A priority Critical patent/JPH08143851A/en
Publication of JPH08143851A publication Critical patent/JPH08143851A/en
Pending legal-status Critical Current

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  • Separation Using Semi-Permeable Membranes (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

PURPOSE: To provide a anti-freezing solution-recycling system of high efficiency which can minimize the time loss needed for cleaning and exchanging the membrane because the membrane can be cleaned in parallel with the recycling treatment of the antifreezing solution. CONSTITUTION: In this recycling system, a plurality of reverse osmotic membranes 5 are used as a means for recycling a used antifreezing solution 9 containing (A) ethylene glycol, (B) additives, (C) oxidized products of component A, (D) deteriorated products of component B, (E) dissolved metal components and (F) insoluble solids, while the other reverse osmotic membranes 5 are cleaned, preferably by using a detergent-circulating pump 12 to circulate the detergent in a tank 11 for detergent. For example, relatively large component F is removed from the antifreezing solution 9 using filters 3a, 3b, then water and components A-E are separated with membrane 5a, further fed to an ion-exchange resin 6 to give a treated solution 10.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、不凍液の再生処理方法
および再生処理装置に係り、特に、内燃機関の冷却用不
凍液を回収処理する方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method and apparatus for reprocessing antifreeze liquid, and more particularly to a method for recovering antifreeze liquid for cooling an internal combustion engine.

【0002】[0002]

【従来の技術】従来の技術は、例えば、SAEペーパ92
1635Fig.6にて開示されているように逆浸透膜を用いた
ものがあるが1セットしか使用していないため膜が汚染
された場合、膜を洗浄するために処理の中断が必要であ
り処理効率が良くなかった。
2. Description of the Related Art A conventional technique is, for example, SAE paper 92.
1635 There are some that use reverse osmosis membrane as disclosed in Fig. 6, but since only one set is used, if the membrane is contaminated, it is necessary to interrupt the treatment to clean the membrane. It wasn't very efficient.

【0003】[0003]

【発明が解決しようとする課題】上記従来技術は、汚染
物質や添加剤を除去することにより逆浸透膜の汚染が進
み処理性能および処理速度の低下が発生した場合に、処
理を中断して逆浸透膜の洗浄が必要であり処理効率が悪
かった。
SUMMARY OF THE INVENTION In the above-mentioned prior art, when the reverse osmosis membrane is contaminated due to the removal of pollutants and additives, and the treatment performance and the treatment speed are lowered, the treatment is interrupted and the reverse treatment is performed. It was necessary to clean the osmotic membrane and the treatment efficiency was poor.

【0004】[0004]

【課題を解決するための手段】上記目的は、逆浸透膜を
複数本用い、逆浸透膜洗浄機能を持たせることにより常
に洗浄された膜を確保しておき、膜が汚染されて処理効
率が低下した場合に直ちに他方の洗浄された膜に切り換
えることにより達成される。
[Means for Solving the Problems] The above-mentioned object is to use a plurality of reverse osmosis membranes and to ensure a washed membrane at all times by providing a reverse osmosis membrane washing function. This is achieved by switching to the other washed membrane immediately if it drops.

【0005】[0005]

【作用】本発明による不凍液再生処理装置は、逆浸透膜
を複数本用い、不凍液処理と並行してもう一方の膜を洗
浄しておくことができるので、膜の洗浄および交換に要
する時間的ロスを最小限にでき、効率の良い不凍液の再
生が可能になる。
In the antifreeze regenerating apparatus according to the present invention, a plurality of reverse osmosis membranes can be used and the other membrane can be washed in parallel with the antifreeze treatment. Therefore, the time loss required for washing and replacement of the membrane can be reduced. It is possible to minimize the heat generation and to efficiently regenerate the antifreeze liquid.

【0006】[0006]

【実施例】以下、本発明の一実施例について、添付の図
を参照して説明する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to the accompanying drawings.

【0007】図1は、本発明による一実施例の不凍液の
再生処理方法および再生処理装置の概略を示した系統図
である。
FIG. 1 is a system diagram showing an outline of a method and apparatus for regenerating an antifreeze solution according to an embodiment of the present invention.

【0008】不凍液再生処理装置1は、第一工程として
の第一フィルタ3aと第二フィルタ3b,第二工程とし
ての逆浸透膜5a,第三工程としてのイオン交換樹脂6
の各処理手段による汚染物質除去工程から成り、それぞ
れの手段が、第一ポンプ2,第二ポンプ4,透過液配管
8a,残渣液配管8bおよび各種配管で接続されてお
り、さらに予備の逆浸透膜5bが洗浄剤タンク11と第
三ポンプ12に接続されている。
The antifreeze regenerating apparatus 1 comprises a first filter 3a and a second filter 3b as a first step, a reverse osmosis membrane 5a as a second step, and an ion exchange resin 6 as a third step.
Each of the processing means comprises a pollutant removal step, and each means is connected by a first pump 2, a second pump 4, a permeate pipe 8a, a residual liquid pipe 8b and various pipes, and a spare reverse osmosis. The membrane 5b is connected to the cleaning agent tank 11 and the third pump 12.

【0009】そして、使用済み不凍液9は不凍液再生処
理装置1で再生処理され、エチレングリコールと水の処
理液10が得られる。
Then, the used antifreeze liquid 9 is regenerated by the antifreeze liquid regeneration treatment apparatus 1 to obtain a treatment liquid 10 of ethylene glycol and water.

【0010】一般に、使用前の不凍液は、エチレングリ
コールに水を加えた溶液である。
Generally, the antifreeze solution before use is a solution prepared by adding water to ethylene glycol.

【0011】そして、各種装置や、内燃機関より抜き取
られた使用済み不凍液9は、上記のものに汚染物質の混
在したものである。
The used antifreeze liquid 9 extracted from various devices and the internal combustion engine is a mixture of the above substances and pollutants.

【0012】内燃機関より抜き取られた使用済み不凍液
の汚染物質として、通常、エチレングリコールの酸化成
分と添加剤の劣化成分と溶解した金属成分と溶解しない
固形物とがある。特に、この使用済み不凍液の金属成分
には、公害で問題になるPb,Cuなどの重金属が含ま
れている。
As pollutants of the used antifreeze liquid extracted from the internal combustion engine, there are usually an oxidizing component of ethylene glycol, a deterioration component of an additive, a dissolved metal component and a solid substance which is not dissolved. In particular, the metal components of the used antifreeze liquid contain heavy metals such as Pb and Cu which are problematic due to pollution.

【0013】まず、この使用済み不凍液9が、第一工程
として第一ポンプ2により第一フィルタ3aと第二フィ
ルタ3bに送られる。ここで、水酸化した金属類や塵埃
などのような、比較的大きな溶解しない固形物が除去さ
れる。
First, the used antifreeze liquid 9 is sent to the first filter 3a and the second filter 3b by the first pump 2 as a first step. Here, relatively large undissolved solids such as metal hydroxides and dust are removed.

【0014】本実施例の場合は、前方に目の粗い第一フ
ィルタ3aと,後方に目の細かい第二フィルタ3bとを
設けたものである。
In the case of the present embodiment, a coarse first filter 3a is provided in the front and a fine second filter 3b is provided in the rear.

【0015】次に、第一工程で処理された不凍液は、第
二工程として第二ポンプ4により逆浸透膜5aに圧送さ
れる。そして、水と,エチレングリコールと,添加剤
と,エチレングリコールの酸化成分や添加剤の劣化成分
と,重金属を含む溶解した金属成分とが、逆浸透膜5a
の膜を境にして分離される。
Next, the antifreeze solution treated in the first step is pressure-fed to the reverse osmosis membrane 5a by the second pump 4 in the second step. Then, water, ethylene glycol, an additive, an oxidizing component of ethylene glycol or a deterioration component of the additive, and a dissolved metal component including a heavy metal are contained in the reverse osmosis membrane 5a.
Are separated by the membrane of.

【0016】一方、逆浸透膜5aで、使用済み不凍液9
を一度に多量に短時間に処理することは、装置やポンプ
圧力の大きさの点で問題である。従って、処理されずに
滞留する使用済み不凍液9と透過しなかった成分とを含
む液、即ち、残渣液を、残渣液配管8bから回収し、元
の使用済み不凍液9の入った容器に帰還させる。そし
て、再び、第一および第二工程の処理を繰り返す。
On the other hand, in the reverse osmosis membrane 5a, the used antifreeze liquid 9
It is a problem in terms of the size of the apparatus and the pump pressure to process a large amount of the same at a short time. Therefore, the liquid containing the used antifreeze liquid 9 that remains untreated and the component that has not permeated, that is, the residual liquid, is recovered from the residual liquid pipe 8b and returned to the container containing the original used antifreeze liquid 9. . Then, the processes of the first and second steps are repeated again.

【0017】最後に、第二工程で処理された不凍液、即
ち逆浸透膜5aを透過した透過液は、第三工程として透
過液配管8aを通り、イオン交換樹脂6に送られる。
Finally, the antifreeze solution treated in the second step, that is, the permeate that has permeated the reverse osmosis membrane 5a is sent to the ion exchange resin 6 through the permeate pipe 8a as the third step.

【0018】第三工程では、エチレングリコールの分子
よりも小さい添加剤およびエチレングリコールの酸化成
分および添加剤の劣化成分が主に除去される。
In the third step, the additive smaller than the molecule of ethylene glycol, the oxidizing component of ethylene glycol and the deteriorated component of the additive are mainly removed.

【0019】そして、第二工程で処理しきれずに逆浸透
膜5aを透過させた、残りのエチレングリコールの分子
よりも小さい添加剤およびエチレングリコールの酸化成
分および添加剤の劣化成分も、第三工程で除去される。
Then, the additive smaller than the remaining ethylene glycol molecules and the oxidizing component of ethylene glycol and the deteriorated component of the additive, which have not been completely processed in the second step and permeate through the reverse osmosis membrane 5a, are also added. Will be removed.

【0020】そして、汚染物質が取り除かれ、エチレン
グリコールと水の処理液10が得られる。
Then, contaminants are removed, and a treatment liquid 10 of ethylene glycol and water is obtained.

【0021】このように使用済み不凍液を処理していく
のであるが、処理を進めていくうちに不凍液内の汚染物
質により逆浸透膜が汚染され、それが膜の詰まりとなっ
て透過液流量の低下がイオン交換樹脂後流の流量計7に
現れるようになる。
The used antifreeze solution is treated in this way. As the treatment proceeds, the reverse osmosis membrane is contaminated by contaminants in the antifreeze solution, which causes the membrane to become clogged and the permeate flow rate. The decrease comes to appear in the flowmeter 7 downstream of the ion exchange resin.

【0022】その時は逆浸透膜5aと予備の逆浸透膜5
bを交換して不凍液の処理を続ける。
At that time, the reverse osmosis membrane 5a and the spare reverse osmosis membrane 5
Replace b and continue antifreeze treatment.

【0023】そしてこの汚染された膜は、第三ポンプ1
2により洗浄剤タンク11内の洗浄剤を循環させて洗浄
しておき次回の交換に備える。
This contaminated membrane is then used by the third pump 1
In step 2, the cleaning agent in the cleaning agent tank 11 is circulated for cleaning to prepare for the next replacement.

【0024】[0024]

【発明の効果】本発明によれば、不凍液の再生処理と並
行して膜の洗浄ができるようになり、従来の再生処理を
中断して膜の洗浄をするという時間的ロスを最小限にす
ることができ、効率の良い作業が行える。
According to the present invention, the membrane can be washed in parallel with the antifreeze regenerating treatment, and the time loss of washing the membrane by interrupting the conventional regenerating treatment is minimized. It is possible to perform efficient work.

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

【図1】本発明による不凍液再生処理システムの機器配
置を示す系統図。
FIG. 1 is a system diagram showing a device layout of an antifreeze liquid reclamation processing system according to the present invention.

【符号の説明】[Explanation of symbols]

1…不凍液再生処理装置、2…第一ポンプ、3a…第一
フィルタ、3b…第二フィルタ、4…第二ポンプ、5…
逆浸透膜、6…イオン交換樹脂、7…流量計、8a…透
過液配管、8b…残渣液配管、9…使用済み不凍液、1
0…処理液、11…洗浄剤タンク、12…第三ポンプ。
DESCRIPTION OF SYMBOLS 1 ... Antifreeze reclaiming apparatus, 2 ... 1st pump, 3a ... 1st filter, 3b ... 2nd filter, 4 ... 2nd pump, 5 ...
Reverse osmosis membrane, 6 ... Ion exchange resin, 7 ... Flowmeter, 8a ... Permeate pipe, 8b ... Residual liquid pipe, 9 ... Used antifreeze liquid, 1
0 ... Treatment liquid, 11 ... Cleaning agent tank, 12 ... Third pump.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 // C07C 31/20 A 9155−4H ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Office reference number FI technical display location // C07C 31/20 A 9155-4H

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】エチレングリコールと,添加剤と,前記エ
チレングリコールの酸化成分と,前記添加剤の劣化成分
と,溶解した金属成分と,溶解しない固形物とを含む使
用済み不凍液を再生するための手段として逆浸透膜を用
いた不凍液再生処理装置において、逆浸透膜を複数本用
い、一方を使用しているときにもう他方の逆浸透膜が洗
浄できる機能を持たせることを特徴とする不凍液再生処
理装置。
1. Regenerating a used antifreeze liquid containing ethylene glycol, an additive, an oxidizing component of the ethylene glycol, a deterioration component of the additive, a dissolved metal component, and an insoluble solid substance. In an antifreeze reclaiming apparatus using a reverse osmosis membrane as a means, a plurality of reverse osmosis membranes are used, and when one is used, the other reverse osmosis membrane has a function of washing the other antifreeze Processing equipment.
【請求項2】請求項1において、前記洗浄機能が、洗浄
剤タンクと洗浄剤循環用ポンプから成る不凍液再生処理
装置。
2. The antifreeze reclaiming apparatus according to claim 1, wherein the cleaning function comprises a cleaning agent tank and a cleaning agent circulating pump.
JP28476894A 1994-11-18 1994-11-18 Recycling system for anti-freezing solution Pending JPH08143851A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP28476894A JPH08143851A (en) 1994-11-18 1994-11-18 Recycling system for anti-freezing solution

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP28476894A JPH08143851A (en) 1994-11-18 1994-11-18 Recycling system for anti-freezing solution

Publications (1)

Publication Number Publication Date
JPH08143851A true JPH08143851A (en) 1996-06-04

Family

ID=17682767

Family Applications (1)

Application Number Title Priority Date Filing Date
JP28476894A Pending JPH08143851A (en) 1994-11-18 1994-11-18 Recycling system for anti-freezing solution

Country Status (1)

Country Link
JP (1) JPH08143851A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9598618B2 (en) 2011-11-18 2017-03-21 Byk-Chemie Gmbh Solid amine adducts

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9598618B2 (en) 2011-11-18 2017-03-21 Byk-Chemie Gmbh Solid amine adducts

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