US2004168979A1PendingUtilityA1

Scouring method

47
Priority: Dec 20, 1996Filed: Mar 4, 2004Published: Sep 2, 2004
Est. expiryDec 20, 2016(expired)· nominal 20-yr term from priority
B01D 63/0221B01D 2321/16B01D 63/0241B01D 65/02B01D 61/18B01D 2321/04B01D 2321/2058B01D 2321/168B01D 2315/06B01D 63/16B01D 65/08B01D 2321/185
47
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Claims

Abstract

A method and apparatus for removing fouling materials from the surface of a plurality of porous membranes ( 9 ) arranged in a membrane module ( 4 ) by providing, from within the module, by means ( 10 ) other than gas passing through the pores of said membranes, gas bubbles in a uniform distribution relative to the porous membrane array such that the bubbles move past the surfaces of the membranes ( 9 ) to dislodge fouling materials therefrom. The membranes ( 9 ) are arranged in close proximity to one another and mounted to prevent excessive movement therebetween. The bubbles also produce vibration and rubbing together of the membranes to further assist removal of fouling materials.

Claims

exact text as granted — not AI-modified
What is claimed is:  
     
         1 . A method of removing accumulated solids from outer surfaces of porous hollow fiber membranes, wherein the membranes are situated in a vessel, the method comprising the steps of: 
 backwashing the membranes so as to dislodge accumulated solids from the outer surfaces of the membranes;    providing, by means other than gas passing through the pores of the membranes, gas bubbles to the membranes, wherein the gas bubbles scour the outer surfaces of the membranes; and    removing dislodged accumulated solids from the vessel.    
     
     
         2 . The method according to  claim 1 , wherein the removing step comprises draining down liquid from the vessel.  
     
     
         3 . The method according to  claim 2 , wherein the draining down comprises a periodic draindown.  
     
     
         4 . The method according to  claim 2 , wherein the draining down comprises a continuous draindown.  
     
     
         5 . The method according to  claim 1 , wherein the removing step comprises overflowing liquid from the vessel.  
     
     
         6 . The method according to  claim 5 , wherein the overflowing comprises a periodic overflow.  
     
     
         7 . The method according to  claim 5 , wherein the overflowing comprises a continuous overflow.  
     
     
         8 . The method according to  claim 1 , wherein the backwashing comprises backwashing with a gas.  
     
     
         9 . The method according to  claim 1 , wherein the backwashing comprises backwashing with a liquid.  
     
     
         10 . The method of  claim 9 , wherein the liquid comprises a permeate.  
     
     
         11 . The method of  claim 1 , wherein the steps of backwashing and providing gas bubbles to the membrane occur simultaneously.  
     
     
         12 . The method of  claim 1 , wherein the porous hollow fiber membranes extend longitudinally in an array to form a membrane module contained within the vessel.  
     
     
         13 . The method of  claim 1 , wherein the membranes are mounted in a header in close proximity to one another so as to prevent excessive movement therebetween.  
     
     
         14 . The method of  claim 1 , wherein the gas bubbles move past the outer surfaces of the membranes and vibrate the membranes to dislodge the accumulated solids therefrom.  
     
     
         15 . The method of  claim 1 , wherein the membranes are mounted relative to one another so as to produce a rubbing effect between the membranes when vibrated.  
     
     
         16 . The method of  claim 1 , wherein the hollow fiber membranes are arranged in at least one bundle.  
     
     
         17 . The method of  claim 1 , wherein the hollow fiber membranes are surrounded by a perforated cage.  
     
     
         18 . The method of  claim 1 , further comprising providing gas bubbles from within the module through gas distribution holes or gas distribution openings in a header.  
     
     
         19 . The method of  claim 1 , further comprising providing gas bubbles from within the module through at least one tube situated within the module.  
     
     
         20 . The method of  claim 19 , wherein the tube comprises a plurality of holes.  
     
     
         21 . The method of  claim 19 , wherein the tube comprises a comb of tubes.  
     
     
         22 . The method of  claim 1 , further comprising subjecting the membranes to a chemical cleaning.  
     
     
         23 . The method of  claim 1 , further comprising subjecting the membranes to a chemical dosing.  
     
     
         24 . The method of  claim 1 , wherein the gas bubbles are continuously provided.  
     
     
         25 . The method of  claim 1 , wherein the gas bubbles are intermittently provided.  
     
     
         26 . A method of removing accumulated solids from outer surfaces of porous hollow fiber membranes, wherein the membranes are situated in a vessel, the method comprising: 
 backwashing the membranes with a liquid so as to dislodge accumulated solids from the outer surfaces of the membranes;    providing, by means other than gas passing through the pores of the membranes, gas bubbles to the membranes, wherein the gas bubbles scour the outer surfaces of the membranes; and    removing dislodged accumulated solids from the vessel.    
     
     
         27 . A method of removing accumulated solids from outer surfaces of porous hollow fiber membranes, wherein the membranes are situated in a vessel, the method comprising: 
 backwashing the membranes with a gas so as to dislodge accumulated solids from the outer surfaces of the membranes;    providing, by means other than gas passing through the pores of the membranes, gas bubbles to the membranes, wherein the gas bubbles scour the outer surfaces of the membranes; and    removing dislodged accumulated solids from the vessel.    
     
     
         28 . A method of removing accumulated solids from outer surfaces of porous hollow fiber membranes, wherein the membranes are situated in a vessel, the method comprising: 
 backwashing the membranes so as to dislodge accumulated solids from the outer surfaces of the membranes; thereafter    providing, by means other than gas passing through the pores of the membranes, gas bubbles to the membranes, wherein the gas bubbles scour the outer surfaces of the membranes; and thereafter    removing dislodged accumulated solids from the vessel.    
     
     
         29 . A method of removing accumulated solids from outer surfaces of porous hollow fiber membranes, wherein the membranes are situated in a vessel, the method comprising: 
 backwashing the membranes so as to dislodge accumulated solids from the outer surfaces of the membranes, while simultaneously providing, by means other than gas passing through the pores of the membranes, gas bubbles to the membranes, wherein the gas bubbles scour the outer surfaces of the membranes; and thereafter    removing dislodged accumulated solids from the vessel.

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