JP2006272136A5 - - Google Patents

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JP2006272136A5
JP2006272136A5 JP2005094335A JP2005094335A JP2006272136A5 JP 2006272136 A5 JP2006272136 A5 JP 2006272136A5 JP 2005094335 A JP2005094335 A JP 2005094335A JP 2005094335 A JP2005094335 A JP 2005094335A JP 2006272136 A5 JP2006272136 A5 JP 2006272136A5
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membrane module
membrane
microfiltration
ultrafiltration
reverse osmosis
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JP2005094335A
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JP4923428B2 (en
JP2006272136A (en
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次に、逆浸透膜モジュールで得られた濃縮水の少なくとも一部を精密ろ過膜モジュールまたは限外ろ過膜モジュールの洗浄水とする洗浄方法について説明する。この洗浄方法も、逆浸透膜モジュールの運転を継続しつつ実施するものであるため、バルブV3、V6は開のままである。洗浄は、バルブV4、V7を閉とし、ポンプ4を停止してからバルブV1、V2を閉とした後、バルブV5を開とし、逆浸透膜モジュールで得られた濃縮水の少なくとも一部を濃縮水返送手段12を通して精密ろ過膜モジュールまたは限外ろ過膜モジュールへ逆流させることで行う。 Next, a cleaning method will be described in which at least a part of the concentrated water obtained by the reverse osmosis membrane module is used as cleaning water for the microfiltration membrane module or the ultrafiltration membrane module. Since this washing method is also performed while continuing the operation of the reverse osmosis membrane module, the valves V3 and V6 remain open. For cleaning, the valves V4 and V7 are closed, the pump 4 is stopped, the valves V1 and V2 are closed, the valve V5 is opened, and at least a part of the concentrated water obtained by the reverse osmosis membrane module is concentrated. It carried out by causing reverse flow into the microfiltration membrane module or ultrafiltration membrane module through the water return feed unit 12.

Claims (5)

塩分を含有する原水を精密ろ過膜モジュールまたは限外ろ過膜モジュールで処理して得られた処理水を、逆浸透膜モジュールで逆浸透処理する膜分離方法において、前記精密ろ過膜モジュールまたは限外ろ過膜モジュールで処理して得られた処理水を洗浄水として、前記精密ろ過膜モジュールに用いられる精密ろ過膜または前記限外ろ過膜モジュールに用いられる限外ろ過膜の逆流洗浄を定期的に行うとともに、前記逆浸透膜モジュールで得られた透過水の少なくとも一部を洗浄水として、1ヶ月に1回〜1日に10回の範囲で、前記精密ろ過膜または前記限外ろ過膜の洗浄を行うことを特徴とする膜分離方法。   In the membrane separation method of treating raw water containing salt with a microfiltration membrane module or an ultrafiltration membrane module, reverse osmosis treatment with a reverse osmosis membrane module, the microfiltration membrane module or ultrafiltration The treated water obtained by treating with the membrane module is used as washing water, and the backwashing of the microfiltration membrane used in the microfiltration membrane module or the ultrafiltration membrane used in the ultrafiltration membrane module is periodically performed. The microfiltration membrane or the ultrafiltration membrane is washed in the range of once a month to 10 times a day using at least a part of the permeated water obtained by the reverse osmosis membrane module as washing water. A membrane separation method. 前記逆浸透膜モジュールで得られた濃縮水で前記精密ろ過膜モジュールに用いられる精密ろ過膜または前記限外ろ過膜モジュールに用いられる限外ろ過膜を洗浄する洗浄手段Aと、前記逆浸透膜モジュールで得られた透過水で前記精密ろ過膜モジュールに用いられる精密ろ過膜または前記限外ろ過膜モジュールに用いられる限外ろ過膜を洗浄する洗浄手段Bとを、前記洗浄手段Aの次に洗浄手段Bの順序で、もしくは、前記洗浄手段Bの次に洗浄手段Aの順序で行うことを特徴とする請求項1に記載の膜分離方法。 Cleaning means A for cleaning the microfiltration membrane used in the microfiltration membrane module or the ultrafiltration membrane used in the ultrafiltration membrane module with the concentrated water obtained by the reverse osmosis membrane module, and the reverse osmosis membrane module A cleaning means B for cleaning the microfiltration membrane used in the microfiltration membrane module or the ultrafiltration membrane used in the ultrafiltration membrane module with the permeated water obtained in step 1 above, and the cleaning means A next to the cleaning means A The membrane separation method according to claim 1, wherein the membrane separation method is performed in the order of B or in the order of the cleaning means A after the cleaning means B. 前記逆浸透膜モジュールで得られた透過水および/または濃縮水のpHが5以下であることを特徴とする請求項1又は2に記載の膜分離方法。 Membrane separation method according to claim 1 or 2, wherein the pH of the permeate and / or retentate obtained in the reverse osmosis membrane module is 5 or less. 塩分を含有する原水を膜分離処理するための装置であって、精密ろ過膜モジュールまたは限外ろ過膜モジュールと、前記精密ろ過膜モジュールまたは前記限外ろ過膜モジュールで得られた処理水を逆浸透処理する逆浸透膜モジュールと、前記精密ろ過膜モジュールまたは前記限外ろ過膜モジュールで得られた処理水を洗浄水として、前記精密ろ過膜モジュールに用いられる精密ろ過膜または前記限外ろ過膜モジュールに用いられる限外ろ過膜の逆流洗浄用に返送する手段と、前記逆浸透膜モジュールで得られた透過水の少なくとも一部を、前記精密ろ過膜または前記限外ろ過膜の洗浄水として返送する手段とを有することを特徴とする膜分離装置。   A device for membrane separation treatment of raw water containing salt, reverse osmosis of microfiltration membrane module or ultrafiltration membrane module and treated water obtained by the microfiltration membrane module or ultrafiltration membrane module The reverse osmosis membrane module to be treated and the treated water obtained by the microfiltration membrane module or the ultrafiltration membrane module are used as washing water, to the microfiltration membrane used in the microfiltration membrane module or the ultrafiltration membrane module Means for returning the ultrafiltration membrane used for backflow cleaning, and means for returning at least part of the permeated water obtained by the reverse osmosis membrane module as washing water for the microfiltration membrane or the ultrafiltration membrane And a membrane separation device. 前記逆浸透膜モジュールへ供給される水のpHを5以下にするための酸添加装置を有することを特徴とする請求項4に記載の膜分離装置。 5. The membrane separation apparatus according to claim 4, further comprising an acid addition device for adjusting the pH of the water supplied to the reverse osmosis membrane module to 5 or less.
JP2005094335A 2005-03-29 2005-03-29 Membrane separation method and membrane separation apparatus Active JP4923428B2 (en)

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JP2006272136A JP2006272136A (en) 2006-10-12
JP2006272136A5 true JP2006272136A5 (en) 2009-08-06
JP4923428B2 JP4923428B2 (en) 2012-04-25

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JP5582740B2 (en) * 2009-07-29 2014-09-03 三菱重工業株式会社 Desalination apparatus and method for cleaning pretreatment membrane of desalination apparatus
KR101206618B1 (en) 2010-06-28 2012-11-29 효성굿스프링스 주식회사 Apparatus and Method of Cleaning Reverse Osmosis for Sea Water Desalination
CN103328079B (en) * 2011-01-20 2016-06-29 东丽株式会社 The washing methods of membrane module, method of making water and fresh water generator
CA2840475A1 (en) * 2011-06-29 2013-01-03 Toray Industries, Inc. Washing method for separation membrane module
JP2015077530A (en) * 2012-01-24 2015-04-23 東レ株式会社 Water production method and water production device
JP5802580B2 (en) * 2012-03-12 2015-10-28 株式会社東芝 Membrane filtration device
JP6183213B2 (en) * 2012-07-10 2017-08-23 東レ株式会社 Fresh water generation method and fresh water generation apparatus
JP6141610B2 (en) * 2012-09-07 2017-06-07 旭化成株式会社 Method for operating water treatment apparatus and method for producing potable water
JP6087667B2 (en) * 2013-03-06 2017-03-01 水ing株式会社 Desalination method and desalination apparatus
JP6441808B2 (en) * 2013-09-30 2018-12-19 水ing株式会社 Desalination apparatus and desalination method
CN104098155A (en) * 2014-07-03 2014-10-15 大庆兰德石油科技有限公司 Deep treatment device for oil-containing and polymer-containing sewage adopting carbon compound composite film
CN105645518A (en) * 2015-12-31 2016-06-08 杭州仁顺环保科技有限公司 Technology for recycling wastewater produced by copper valve welding based on ultrafiltration and reverse osmosis
WO2017168720A1 (en) * 2016-03-31 2017-10-05 三菱重工業株式会社 Reverse osmosis membrane processing method and reverse osmosis membrane processing equipment
CN106178977B (en) * 2016-07-29 2018-08-07 新乡学院 A kind of synthetic method of graphene reverse osmosis composite membrane
CN109970273B (en) * 2018-10-26 2024-06-21 中国林业科学研究院林业新技术研究所 Membrane separation coupling evaporation treatment process and device for chemi-mechanical pulp wastewater

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JPH10263539A (en) * 1997-03-28 1998-10-06 Japan Organo Co Ltd Member treating method of water to be treated and membrane treating device
JP2003181247A (en) * 2001-12-17 2003-07-02 Nitto Denko Corp Treatment system having spiral membrane element and its operating method

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