JP2009247977A5 - - Google Patents

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Publication number
JP2009247977A5
JP2009247977A5 JP2008098428A JP2008098428A JP2009247977A5 JP 2009247977 A5 JP2009247977 A5 JP 2009247977A5 JP 2008098428 A JP2008098428 A JP 2008098428A JP 2008098428 A JP2008098428 A JP 2008098428A JP 2009247977 A5 JP2009247977 A5 JP 2009247977A5
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Japan
Prior art keywords
concentrate
circulation
flow rate
waste liquid
filtration system
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JP2008098428A
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Japanese (ja)
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JP4896917B2 (en
JP2009247977A (en
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Priority to JP2008098428A priority Critical patent/JP4896917B2/en
Priority claimed from JP2008098428A external-priority patent/JP4896917B2/en
Publication of JP2009247977A publication Critical patent/JP2009247977A/en
Publication of JP2009247977A5 publication Critical patent/JP2009247977A5/ja
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Publication of JP4896917B2 publication Critical patent/JP4896917B2/en
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Claims (8)

塗装機器を洗浄する際に前記塗装機器から排出される洗浄廃液を循環させる循環ラインと、
前記循環ライン上に設けられると共に、前記洗浄廃液を、前記循環ライン上を循環する濃縮液と透過液とに分離するクロスフロー膜部と、
前記濃縮液の循環流量を検出する循環流量検出部と、
前記クロスフロー膜部への前記洗浄廃液の供給圧を一定に保持すると共に、前記循環流量検出部で検出された循環流量に基づいて前記濃縮液の循環を停止させる制御部と、
を備えることを特徴とする膜濾過システム。
A circulation line for circulating the washing waste liquid discharged from the coating device when cleaning painting equipment,
A cross-flow membrane part that is provided on the circulation line and separates the cleaning waste liquid into a concentrate and a permeate that circulate on the circulation line;
A circulating flow rate detection unit for detecting the circulating flow rate of the concentrate;
A control unit that keeps the supply pressure of the cleaning waste liquid to the crossflow membrane unit constant, and that stops the circulation of the concentrate based on the circulation flow rate detected by the circulation flow rate detection unit;
A membrane filtration system comprising:
前記制御部は、前記濃縮液の循環流量が所定の閾値以下になると前記濃縮液の循環を停止させることを特徴とする請求項1記載の膜濾過システム。   2. The membrane filtration system according to claim 1, wherein the control unit stops the circulation of the concentrate when the circulation flow rate of the concentrate becomes a predetermined threshold value or less. 前記制御部は、前記濃縮液の循環流量と、単位膜面積当りの前記透過液の透過流量とを乗じた値が、所定の閾値以下になると前記濃縮液の循環を停止させる事を特徴とする請求項1記載の膜濾過システム。   The controller is configured to stop circulation of the concentrate when a value obtained by multiplying a circulation flow rate of the concentrate and a permeation flow rate of the permeate per unit membrane area becomes a predetermined threshold value or less. The membrane filtration system according to claim 1. 前記洗浄廃液は、水性シンナーを用いて前記塗装機器を洗浄した際に排出される水性シンナー廃液であることを特徴とする請求項1〜3のいずれか一項記載の膜濾過システム。   The membrane filtration system according to any one of claims 1 to 3, wherein the cleaning waste liquid is an aqueous thinner waste liquid that is discharged when the coating equipment is cleaned using an aqueous thinner. 塗装機器を洗浄する際に前記塗装機器から排出される洗浄廃液を循環させる循環ラインと、前記循環ライン上に設けられると共に、前記洗浄廃液を、前記循環ライン上を循環する濃縮液と透過液とに分離するクロスフロー膜部とを備える膜濾過システムの運転方法において、
前記クロスフロー膜部への前記洗浄廃液の供給圧を一定に保持すると共に、前記濃縮液の循環流量を検出し、検出された前記濃縮液の循環流量に基づいて前記濃縮液の循環を停止させることを特徴とする膜濾過システムの運転方法。
A circulation line for circulating the washing waste liquid discharged from the coating device when cleaning painting equipment, with is provided on the circulation line, the washing waste liquid, and concentrate circulating through the circulation line on the permeate In a method of operating a membrane filtration system comprising a crossflow membrane part to be
While maintaining the supply pressure of the cleaning waste liquid to the cross-flow membrane part constant, the circulation flow rate of the concentrate is detected, and the circulation of the concentrate is stopped based on the detected circulation flow of the concentrate. A method for operating a membrane filtration system.
前記濃縮液の循環流量が所定の閾値以下になると前記濃縮液の循環を停止させることを特徴とする請求項5記載の膜濾過システムの運転方法。   6. The method of operating a membrane filtration system according to claim 5, wherein the circulation of the concentrate is stopped when the circulation flow rate of the concentrate becomes a predetermined threshold value or less. 前記濃縮液の循環流量と、単位膜面積当りの前記透過液の透過流量とを乗じた値が、所定の閾値以下になると前記濃縮液の循環を停止させる事を特徴とする請求項5記載の膜濾過システムの運転方法。   6. The circulation of the concentrate is stopped when a value obtained by multiplying the circulation flow rate of the concentrate and the permeate flow rate of the permeate per unit membrane area becomes a predetermined threshold value or less. Operation method of membrane filtration system. 前記洗浄廃液は、水性シンナーを用いて前記塗装機器を洗浄した際に排出される水性シンナー廃液であることを特徴とする請求項5〜7のいずれか一項記載の膜濾過システムの運転方法。   The method for operating a membrane filtration system according to any one of claims 5 to 7, wherein the cleaning waste liquid is an aqueous thinner waste liquid that is discharged when the coating apparatus is cleaned using an aqueous thinner.
JP2008098428A 2008-04-04 2008-04-04 Membrane filtration system and method of operating the membrane filtration system Expired - Fee Related JP4896917B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2008098428A JP4896917B2 (en) 2008-04-04 2008-04-04 Membrane filtration system and method of operating the membrane filtration system

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Application Number Priority Date Filing Date Title
JP2008098428A JP4896917B2 (en) 2008-04-04 2008-04-04 Membrane filtration system and method of operating the membrane filtration system

Publications (3)

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JP2009247977A JP2009247977A (en) 2009-10-29
JP2009247977A5 true JP2009247977A5 (en) 2011-01-06
JP4896917B2 JP4896917B2 (en) 2012-03-14

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103787461A (en) * 2012-11-05 2014-05-14 苏州卓融水处理科技有限公司 Environment-friendly water treatment system
CN106823817A (en) * 2017-04-06 2017-06-13 杭州瑞裕通膜技术有限公司 A kind of filtering and purifying and its application method containing solid oil product inferior

Family Cites Families (9)

* Cited by examiner, † Cited by third party
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JPH03165820A (en) * 1989-11-24 1991-07-17 Shibaura Eng Works Co Ltd Device for backwashing filter membrane module
JP3089702B2 (en) * 1991-04-26 2000-09-18 栗田工業株式会社 Membrane separation device
JPH09164363A (en) * 1995-12-18 1997-06-24 Kansai Paint Co Ltd Coating method
JP3473309B2 (en) * 1997-02-04 2003-12-02 栗田工業株式会社 Operation control device for membrane separation device
JP2000161848A (en) * 1998-11-24 2000-06-16 Sumitomo Chem Co Ltd Spray drying method and spray drier
JP2002079153A (en) * 2000-09-04 2002-03-19 Nippon Paint Co Ltd Operation control method in recycling system fo water based coating material
JP2002113334A (en) * 2000-10-05 2002-04-16 Mitsubishi Rayon Co Ltd Hollow fiber membrane module and method for treating liquid using the same
JP3942904B2 (en) * 2002-01-30 2007-07-11 日本ペイント株式会社 Water paint recovery method and recovery system
JP4536482B2 (en) * 2004-10-25 2010-09-01 旭化成ケミカルズ株式会社 Operation method of membrane filtration device

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