JPS61249509A - Extremely high efficiency water washing separator - Google Patents

Extremely high efficiency water washing separator

Info

Publication number
JPS61249509A
JPS61249509A JP9103185A JP9103185A JPS61249509A JP S61249509 A JPS61249509 A JP S61249509A JP 9103185 A JP9103185 A JP 9103185A JP 9103185 A JP9103185 A JP 9103185A JP S61249509 A JPS61249509 A JP S61249509A
Authority
JP
Japan
Prior art keywords
water
washing
liq
washed
trichlorotrifluoroethane
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
JP9103185A
Other languages
Japanese (ja)
Other versions
JPH0252521B2 (en
Inventor
Kuniyoshi Ohashi
大橋 国美
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.)
Canon Inc
Original Assignee
Canon Inc
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 Canon Inc filed Critical Canon Inc
Priority to JP9103185A priority Critical patent/JPS61249509A/en
Publication of JPS61249509A publication Critical patent/JPS61249509A/en
Publication of JPH0252521B2 publication Critical patent/JPH0252521B2/ja
Granted legal-status Critical Current

Links

Abstract

PURPOSE:To separate by washing with water with high efficiency and with a small amt. of water by providing in stages plural washing vessels provided with a water injection nozzle and furnishing a separation layer at the lowermost stage in the titled separator for separating a water-insoluble solvent contg. a water-soluble solvent by washing with water. CONSTITUTION:A liq. mixture 2 flowing in from a liq. mixture inflow part 9 is charged into the first washing vessel 7a, brought into contact with washing water and washed. The washing water after extracting alkyl alcohol is transferred to the upper water vessel. Liq. trichlorotrifluoroethane is charged in the second washing vessel 7b at the oblique lower part which is one stage lower than the first washing vessel 7a, washed and then further washed in the third washing vessel 7c. The washed trichlorotrifluoroethane flows out from a washed liq. outlet 13, falls into the first liq. storage 14, passes through partition plates 15a and 15b and transfers to the second liq. storage 14b then to the third liq. storage 14. The liq. is taken out from a discharge valve 5, distilled and dried.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、超動率水洗分離装置に関し、更に詳しくは、
水溶性溶剤を含有する非水溶性溶剤を非常に高効率で水
洗分離し得る装置に関する。
[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a hypermobility water washing separation device, and more specifically,
The present invention relates to a device that can wash and separate water-insoluble solvents containing water-soluble solvents with extremely high efficiency.

[従来の技術] 光学部品を洗浄するに当っては、脱水工程でアルキルア
ルコールが使用される。この脱水剤としてのアルキルア
ルコールは光学部品から除去する必要があり、そのため
に乾燥ペーパ一槽内でトリクロロトリフルオロエタンの
凝縮液により光学部品に付着したフルキルアルコールを
洗浄除去する(これは蒸留乾燥と称される工程である)
、ここで洗浄により生じた混合液は、乾燥受皿工程から
排出され、次いで水洗分離槽内に入り、水と接触させて
水洗することにより、アルキルアルコールは水に溶解し
、水との混合液として水洗分離槽から排出され公害処理
工程に送られ、一方のトリクロルフルオロエタンは非水
溶性物質で比重がと水より重く、水洗分離槽の2液分離
液層のうちの下層液相となる。この下層液相のトリクロ
ルフルオロエタンは再び蒸留乾燥用に使用されるが。
[Prior Art] When cleaning optical components, alkyl alcohol is used in the dehydration process. It is necessary to remove this alkyl alcohol as a dehydrating agent from the optical components, and for this purpose, the alkyl alcohol adhering to the optical components is washed and removed with a condensate of trichlorotrifluoroethane in a tank of drying paper (this is done by distillation drying). (This is a process called
The mixed liquid generated by washing here is discharged from the drying tray process, then enters the washing separation tank, and is brought into contact with water and washed with water, whereby the alkyl alcohol is dissolved in water and becomes a mixed liquid with water. Trichlorofluoroethane is discharged from the water washing separation tank and sent to a pollution treatment process, and trichlorofluoroethane is a water-insoluble substance with a specific gravity heavier than water and becomes the lower liquid phase of the two-liquid separated liquid layer in the washing separation tank. This lower liquid phase trichlorofluoroethane is used again for distillation drying.

再使用にあたっては、このトリクロロトリフルオロエタ
ンの水洗分離純度(アルキルアルコールとトリクロロト
リフルオロエタンの分離純度)は約100%近くである
必要がある。
For reuse, the water washing separation purity (separation purity of alkyl alcohol and trichlorotrifluoroethane) of this trichlorotrifluoroethane needs to be close to about 100%.

従来の水洗分離方式では、第2図に示すように水洗分離
槽底側のトリクロロトリフルオロエタン溶液層に蛇管形
状のシャワー管lを設け、2液層のうち上層で分離でき
ないアルキルアルコールを溶存したトリクロロフルオロ
エタン溶液を下層部においてシャワー水洗することによ
りアルキルアルコールを除去していた。
In the conventional water washing separation method, as shown in Figure 2, a serpentine shower pipe l is installed in the trichlorotrifluoroethane solution layer at the bottom of the washing separation tank, and the alkyl alcohol that cannot be separated is dissolved in the upper layer of the two liquid layers. The alkyl alcohol was removed by washing the trichlorofluoroethane solution in the lower layer with shower water.

なお、第2図において、Aは水洗浄により生じた水とア
ルキルアルコールの混合液の領域を示し、Cは水洗領域
であり、2は蒸留乾燥工程から流入してくるトリクロロ
トリフルオロエタンとアルキルアルコールとの混合液で
あり、3は洗浄水供給弁、4は取出口、5は取出弁、6
は洗浄排水出口である。
In Fig. 2, A indicates a region of a mixture of water and alkyl alcohol produced by water washing, C indicates a water washing region, and 2 indicates a region of a mixture of water and alkyl alcohol generated from the distillation drying process. 3 is a cleaning water supply valve, 4 is a take-out port, 5 is a take-out valve, 6
is the cleaning drainage outlet.

[発明が解決しようとする問題点] ところが、上記従来の水洗分離ではアルキルアルコール
を100%分離する必要性から、洗浄機一台当り約8交
/日のトリクロロフルオルエタンとアルキルアルコール
の混合液を処理するのに約5■3/日の洗浄水が必要で
あり、また、工場に7〜8台の洗浄機を設置した場合に
は、その排水量は35〜40ta37日にものぼるとい
う問題点があった。
[Problems to be Solved by the Invention] However, in the conventional water washing separation described above, it is necessary to separate 100% of the alkyl alcohol, so the mixture of trichlorofluoroethane and alkyl alcohol is used approximately 8 times per day per washing machine. Approximately 5 x 3 days of washing water is required to process the water, and if 7 to 8 washing machines are installed in a factory, the amount of waste water will reach 35 to 40 ta per 37 days. was there.

また、ここで発生する排水はアルキルアルコールを溶存
しているため、公害防止面から有機排水に指定されてお
り、この排水処理には困難がつきまとい、その処理経費
は膨大なものであった。
Furthermore, since the wastewater generated here contains dissolved alkyl alcohol, it is designated as organic wastewater from a pollution prevention perspective, and the treatment of this wastewater is fraught with difficulties and the processing costs are enormous.

従って、少量の洗浄水でアルキルアルコールの分離が可
能な装置が、公害防止面及び公害処理経費の点から強く
要望されていた。
Therefore, there has been a strong demand for an apparatus capable of separating alkyl alcohols with a small amount of washing water from the viewpoint of pollution prevention and pollution treatment costs.

本発明は以上の問題点を解決し、水溶性溶剤を含有する
非水溶性溶剤を非常に高効率で水洗分離し得る装置を提
供するためになされたものである。
The present invention has been made in order to solve the above problems and provide an apparatus that can wash and separate water-insoluble solvents containing water-soluble solvents with extremely high efficiency.

[問題点を解決するための手段] 本発明によれば、水溶性溶剤と水より高比重の非水溶性
溶剤との混合液に水を接触させて水溶性溶剤を水で抽出
することにより水洗し非水溶性溶剤を分離する装置であ
って、底部に水噴出ノズルを備えた複数の水洗槽を階段
状に備え・るとともに最下段の水洗槽の下方に非水溶性
溶剤層と水層を分離するだめの分離槽を設けてなること
を特徴とする超動率水洗分離装置が提供されるものであ
る。
[Means for Solving the Problems] According to the present invention, water washing is performed by bringing water into contact with a mixture of a water-soluble solvent and a water-insoluble solvent having a higher specific gravity than water and extracting the water-soluble solvent with water. This equipment separates non-water-soluble solvents, and is equipped with a plurality of washing tanks equipped with water jet nozzles at the bottom in a stepped manner, and a non-water-soluble solvent layer and a water layer below the bottom washing tank. A super-mobility water washing separation device is provided, which is characterized by being provided with a separation tank for separation.

[実施例] 次に図面に示す実施例を挙げて本発明を説明する。[Example] Next, the present invention will be described with reference to embodiments shown in the drawings.

なお、以下の実施例では水より高比重の非水溶性溶剤と
してトリクロロトリフルオロエタンを、そして水溶性溶
剤としてアルキルアルコールを例にとって説明する。
In the following examples, trichlorotrifluoroethane is used as a water-insoluble solvent having a specific gravity higher than water, and alkyl alcohol is used as a water-soluble solvent.

第1図は本発明の超動率水洗分離装置を示す概略説明図
である。
FIG. 1 is a schematic explanatory diagram showing a supermobility water washing separation apparatus of the present invention.

第1図において、2はアルキルアルコールとトリクロロ
トリフルオロエタンの混合液であり、こ。
In FIG. 1, 2 is a mixture of alkyl alcohol and trichlorotrifluoroethane.

の混合液2は蒸留乾燥工程より排出されてくるものであ
る。 7a、 ?b、 ?cは水洗槽であり、 ?aは
第1水洗槽、7bは第2水洗槽、7Cは第3水洗槽であ
る。水洗槽?a、 7b、 ?cは、中央部が深く形成
された中央傾斜型であり、底部に各々水噴出ノズル8a
、 8b、 8c備えてなるものである。水洗槽は。
The mixed liquid 2 is discharged from the distillation drying process. 7a, ? b.? c is a washing tank, and ? A is a first washing tank, 7b is a second washing tank, and 7C is a third washing tank. Wash tank? a, 7b, ? c is a centrally inclined type with a deep central part, and each has a water jet nozzle 8a at the bottom.
, 8b, and 8c. The washing tank.

at★%浦?l11m9★%jl17h  筑*★件k
ll 7 eの順に階段状に設けである。
at★%ura? l11m9★%jl17h Chiku*★item k
They are arranged in a stepwise manner in the order of ll 7 e.

混合液流入部9より流入した混合液2は、第1水洗槽7
aに入り、水噴出ノズル8aから噴出する洗浄水10と
接触し、水洗が行なわれ、トリクロロトリフルオロエタ
ン−アルキルアルコール混合物からアルキルアルコール
が水中に抽出される。ここで水噴出ノズル8a、 8b
、 8cとしては、水と被洗浄液との接触効率を良くす
るために、細い孔が多数設けられたシャワーノズルと称
されるノズルが好適に用いられる。3は洗浄水供給弁、
11は流量計であり、流量計11で測定される流量をフ
ィードバックしつつ洗浄水供給弁3の開閉を調節して、
所定の流量で洗浄水を水噴出ノズル8a、 8b、 8
cに供給する。水洗量としては1.251 /Hである
。アルキルアルコールを抽出した洗浄水はトリクロロト
リフルオロエタン液層を通過して上方の水層に移動し、
第1水洗槽3aで水洗されたトリクロロトリフルオロエ
タン液は、第1水洗槽3aよりも1段斜め下方に設けら
れた第2水洗槽3bに出口12aを通じて流入し、ここ
で水噴出ノズル8bから噴出する洗浄水で洗浄される。
The mixed liquid 2 flowing from the mixed liquid inlet 9 flows into the first washing tank 7.
a and comes into contact with the washing water 10 ejected from the water ejection nozzle 8a, washing with water is performed, and alkyl alcohol is extracted from the trichlorotrifluoroethane-alkyl alcohol mixture into water. Here, water jet nozzles 8a, 8b
, 8c, a nozzle called a shower nozzle provided with a large number of thin holes is suitably used in order to improve the contact efficiency between water and the liquid to be cleaned. 3 is a wash water supply valve;
Reference numeral 11 denotes a flow meter, which adjusts the opening and closing of the cleaning water supply valve 3 while feeding back the flow rate measured by the flow meter 11.
Water jet nozzles 8a, 8b, 8 spray cleaning water at a predetermined flow rate.
supply to c. The amount of water washing is 1.251/H. The washing water from which the alkyl alcohol has been extracted passes through the trichlorotrifluoroethane liquid layer and moves to the upper water layer.
The trichlorotrifluoroethane liquid washed in the first washing tank 3a flows through the outlet 12a into the second washing tank 3b, which is provided one stage diagonally below the first washing tank 3a, and there, from the water jet nozzle 8b. It is washed with a jet of washing water.

以後第3水洗槽?Cにおいても同様の水洗が行なわれる
。水洗が完了したトリクロロトリフルオロエタンは水洗
完了出口13より流出する。水洗完了出口13は、第3
水洗槽7Cの壁の所定レベル位置に孔を穿設することに
形成されているが1mの上級を所定巾で所定高さまで切
欠して形成したものであってもよい(このことは出口1
2a、 12bについても同様である。)。
After that, the third washing tank? Similar water washing is performed in C. The trichlorotrifluoroethane that has been washed with water flows out from the water washing completion outlet 13. The water washing completion outlet 13 is the third
It is formed by drilling a hole at a predetermined level position on the wall of the water washing tank 7C, but it may also be formed by cutting out a 1 m upper part with a predetermined width and a predetermined height.
The same applies to 2a and 12b. ).

水洗完了出口13より流出したトリクロロトリフルオロ
エタンは、第1液溜14aに落下し、開口部(図示省略
)を有する仕切板15a、 15bを通過することによ
り、第2液溜14b、次いで第3液溜14cに移り、第
3液溜14cに設けられた取出弁5から取出し、再生ト
リクロロトリフルオロエタンとして蒸留乾燥工程で使用
される。
Trichlorotrifluoroethane flowing out from the water washing completion outlet 13 falls into the first liquid reservoir 14a, passes through partition plates 15a and 15b having openings (not shown), and is then transferred to the second liquid reservoir 14b and then to the third liquid reservoir 14a. The liquid is transferred to the liquid reservoir 14c, taken out from the take-out valve 5 provided in the third liquid reservoir 14c, and used as recycled trichlorotrifluoroethane in the distillation drying process.

なお、第1図中、Aは洗浄本領域で、Bは純粋トリクロ
ロトリフルオロエタン領域である。アルキルアルコール
を溶存した水は洗浄排水出口6からオーバーフローし、
公害処理に付される。
In FIG. 1, A is the main cleaning area, and B is the pure trichlorotrifluoroethane area. The water containing dissolved alkyl alcohol overflows from the washing drain outlet 6,
Subjected to pollution treatment.

水洗完了出口13より分離流出したトリクロロトリフル
オロエタンの分離純度はアルキルアルコールを含まず、
100%近い純度であった。また、第1液溜14aでの
トリクロロトリフルオロエタン領域の同液を分析した結
果、アルキルアルコールを含まず、上記同様100%で
あった。なお1以上に示された値は、洗浄水中のアルキ
ルアルコールの溶解限界量(ある濃度からトリクロロト
リフルオロエタン中に溶は込むアルキルアルコールの量
)を約25%に設定し、また、蒸留乾燥工程から本発明
の分離装置に流入するトリクロロトリフルオロエタン−
アルキルアルコール混合液中のアルキルアルコール含有
量が60重量%の場合の値である。
The separation purity of trichlorotrifluoroethane separated and flowing out from the water washing completion outlet 13 is that it does not contain alkyl alcohol.
The purity was close to 100%. Further, as a result of analyzing the same liquid in the trichlorotrifluoroethane region in the first liquid reservoir 14a, it was found that it did not contain alkyl alcohol and was 100% as above. The values shown above are based on the fact that the solubility limit amount of alkyl alcohol in washing water (the amount of alkyl alcohol that dissolves into trichlorotrifluoroethane from a certain concentration) is set at approximately 25%, and the dissolution limit amount of alkyl alcohol in washing water is set at approximately 25%. trichlorotrifluoroethane flowing into the separation device of the present invention from
This is a value when the alkyl alcohol content in the alkyl alcohol mixture is 60% by weight.

[発明の効果] 本発明の超動率水洗分離装置は上記のように、底部に水
噴出ノズルを備えた複数の水洗槽を階段状に備えである
から、水溶性溶剤を含んだ水より高比重の非水溶性溶剤
は上段から下段の水洗槽に流下する間に各段で水洗を受
け、極めて高効率で水洗が行なわれる。また、最下段の
水洗槽の下方に非水溶性溶剤層と水層を分離するための
分離槽を設けであるから、この分離槽において水洗槽で
の水洗を完了した水より高比重の非水溶性溶剤が下側の
層として確実に分離される。このように本発明の装置に
よれば、高効率で水洗が行なわれるために洗浄水の使用
量は少量で済み、洗浄排水の量も少なくなるために洗浄
排水の処理も極めて容易に行なえるようになり、工業的
意義は大である。
[Effects of the Invention] As described above, the hypermobility water washing separator of the present invention is equipped with a plurality of washing tanks equipped with water jet nozzles at the bottom in a stepped manner, so that it has a higher water content than water containing a water-soluble solvent. The water-insoluble solvent having a specific gravity is washed with water at each stage while flowing down from the upper stage to the lower stage of the water washing tank, and water washing is performed with extremely high efficiency. In addition, since a separation tank is provided below the lowest washing tank to separate the non-water-soluble solvent layer and the water layer, the non-aqueous solvent in this separation tank has a higher specific gravity than the water that has been washed in the washing tank. The solvent is ensured to be separated as the lower layer. As described above, according to the apparatus of the present invention, since water washing is performed with high efficiency, the amount of washing water used is small, and the amount of washing waste water is also reduced, so that the treatment of washing waste water can be performed extremely easily. This is of great industrial significance.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明の超動率水洗分離装置を示す概略説明図
、第2図法従来の水洗分離装置を示す概略説明図である
。 l・・・シャワー管 2・・・混合液 3・・・洗浄水供給弁 4・・・取出口 5・・・取出弁 6・・・洗浄排水出口 アa・・・第1水洗槽 7b・・・第2水洗槽 7c・・・第3水洗槽 8a、 8b、 8c・・・水噴出ノズル9・・・混合
液流入部 1G・・・洗浄水 11・・・流量計 12a、 12b−−−出口 13・・・水洗完了出口 14a・・・第1液溜 14b・・・第2液溜 14c・・・第3液溜 15a、 15b−−−仕切板 A・・・洗浄水領域 B・・・純粋トリクロロトリフルオロエタン領域C・・
・水洗領域
FIG. 1 is a schematic explanatory diagram showing a super-mobility water washing separator according to the present invention, and FIG. 2 is a schematic explanatory diagram showing a conventional water washing separator. l...Shower pipe 2...Mixed liquid 3...Washing water supply valve 4...Outlet port 5...Outlet valve 6...Washing drain outlet aa...First washing tank 7b. ...Second washing tank 7c...Third washing tank 8a, 8b, 8c...Water jet nozzle 9...Mixed liquid inlet 1G...Washing water 11...Flowmeter 12a, 12b-- - Outlet 13...Washing completion outlet 14a...First liquid reservoir 14b...Second liquid reservoir 14c...Third liquid reservoir 15a, 15b---Partition plate A...Washing water area B・...Pure trichlorotrifluoroethane region C...
・Washing area

Claims (1)

【特許請求の範囲】[Claims] 水溶性溶剤と水より高比重の非水溶性溶剤との混合液に
水を接触させて水溶性溶剤を水で抽出することにより水
洗し非水溶性溶剤を分離する装置であって、底部に水噴
出ノズルを備えた複数の水洗槽を階段状に備えるととも
に最下段の水洗槽の下方に非水溶性溶剤層と水層を分離
するための分離槽を設けてなることを特徴とする超効率
水洗分離装置。
This is a device that separates the non-water-soluble solvent by washing with water by bringing water into contact with a mixture of a water-soluble solvent and a non-water-soluble solvent with a higher specific gravity than water, and extracting the water-soluble solvent with water. Ultra-efficient water washing characterized by having a plurality of washing tanks equipped with jet nozzles in a stepped manner, and a separation tank for separating a water-insoluble solvent layer and a water layer below the lowest washing tank. Separation device.
JP9103185A 1985-04-30 1985-04-30 Extremely high efficiency water washing separator Granted JPS61249509A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9103185A JPS61249509A (en) 1985-04-30 1985-04-30 Extremely high efficiency water washing separator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9103185A JPS61249509A (en) 1985-04-30 1985-04-30 Extremely high efficiency water washing separator

Publications (2)

Publication Number Publication Date
JPS61249509A true JPS61249509A (en) 1986-11-06
JPH0252521B2 JPH0252521B2 (en) 1990-11-13

Family

ID=14015147

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9103185A Granted JPS61249509A (en) 1985-04-30 1985-04-30 Extremely high efficiency water washing separator

Country Status (1)

Country Link
JP (1) JPS61249509A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01155903A (en) * 1987-12-11 1989-06-19 Mitsubishi Electric Corp Purification of incombustible insulating liquid
US5062660A (en) * 1989-04-28 1991-11-05 Nissan Motor Company, Limited Pressure medium fluid circuit for active suspension system with variable fluid source discharge rate depending upon magnitude of stroke in relative displacement between vehicular body and suspension member
US5076606A (en) * 1989-03-27 1991-12-31 Nissan Motor Company, Limited Active suspension system with hydraulic circuit having line pressure dependent flow restriction for working fluid introduced into and drained from working chamber
US5083811A (en) * 1989-04-28 1992-01-28 Nissan Motor Company, Limited Fluid supply circuit for active suspension system with variable fluid source discharge rate depending upon magnitude of lateral acceleration
US5085459A (en) * 1989-03-30 1992-02-04 Nissan Motor Company, Limited Pressure supply network for active suspension system and control therefor

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01155903A (en) * 1987-12-11 1989-06-19 Mitsubishi Electric Corp Purification of incombustible insulating liquid
US5076606A (en) * 1989-03-27 1991-12-31 Nissan Motor Company, Limited Active suspension system with hydraulic circuit having line pressure dependent flow restriction for working fluid introduced into and drained from working chamber
US5085459A (en) * 1989-03-30 1992-02-04 Nissan Motor Company, Limited Pressure supply network for active suspension system and control therefor
US5062660A (en) * 1989-04-28 1991-11-05 Nissan Motor Company, Limited Pressure medium fluid circuit for active suspension system with variable fluid source discharge rate depending upon magnitude of stroke in relative displacement between vehicular body and suspension member
US5083811A (en) * 1989-04-28 1992-01-28 Nissan Motor Company, Limited Fluid supply circuit for active suspension system with variable fluid source discharge rate depending upon magnitude of lateral acceleration

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