US2009039020A1PendingUtilityA1

Methods for reducing boron concentration in high salinity liquid

Assignee: HYDRANAUTICSPriority: Jun 13, 2002Filed: Oct 20, 2008Published: Feb 12, 2009
Est. expiryJun 13, 2022(expired)· nominal 20-yr term from priority
C02F 1/66C02F 2101/10C02F 2209/06C02F 1/5236C02F 1/441C02F 1/444Y02A20/131B01D 61/04C02F 5/08C02F 2103/08B01D 2311/04C02F 9/00B01D 61/026
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Claims

Abstract

Methods of treating a high salinity liquid, such as seawater, containing boron are provided, including adjusting the pH of the liquid to about 8 to about 9.5, optionally adding a scale inhibitor to the liquid, passing the liquid through a reverse osmosis device, and recovering a permeate having a boron concentration less than about 2 ppm. One embodiment includes removing colloidal matter from the liquid using a membrane filtration system, such as ultrafiltration or microfiltration, prior to passing the liquid through the reverse osmosis device, and preferably prior to adjusting the pH of the liquid.

Claims

exact text as granted — not AI-modified
1 . A method of reducing boron concentration in a high-salinity, boron-containing liquid comprising the following steps:
 (a) increasing a pH of a non-softened, high salinity liquid to about 8 to 9.5;   (b) passing the pH-increased, non-softened high salinity liquid through at least one reverse osmosis device; and   (c) recovering a permeate from the at least one reverse osmosis device wherein the permeate has a boron concentration of less than about 2 ppm,   
     further comprising at least before step (b) adding at least one coagulant chemical to the high salinity liquid and treating the high salinity liquid with a membrane filtration system to remove at least one suspended solid from the liquid. 
   
   
       2 . The method of  claim 1 , wherein the high salinity liquid is seawater. 
   
   
       3 . The method of  claim 1 , wherein the seawater comprises about 4 to about 7 ppm boron. 
   
   
       4 . The method of  claim 1 , wherein the pH of the high salinity liquid is increased to about 8 to about 9.3. 
   
   
       5 . The method of  claim 1 , wherein step (a) comprises adding a base to the high salinity liquid. 
   
   
       6 . The method of  claim 5 , wherein the base is selected from the group consisting of calcium hydroxide, sodium hydroxide, and lime. 
   
   
       7 . The method of  claim 1 , wherein the at least one reverse osmosis device comprises an array comprising at least one reverse osmosis membrane. 
   
   
       8 . The method of  claim 7 , wherein the at least one reverse osmosis membrane is a polyamide-type membrane. 
   
   
       9 . The method of  claim 7 , wherein the at least one reverse osmosis membrane is selected from the group consisting of a spiral wound membrane and a hollow fiber membrane. 
   
   
       10 . The method of  claim 1 , wherein the method further comprises adding a scale inhibitor to the high salinity liquid before step (b). 
   
   
       11 . The method of  claim 1 , wherein the permeate has a boron concentration of less than about 1 ppm. 
   
   
       12 . The method of  claim 1 , wherein the permeate has a boron concentration of less than about 0.5 ppm. 
   
   
       13 . The method of  claim 1 , wherein the membrane filtration system is selected from the group consisting of an ultrafiltration system and a microfiltration system. 
   
   
       14 . The method of  claim 13 , wherein the membrane filtration system comprises a membrane module selected from the group consisting of an ultrafiltration membrane module and a microfiltration membrane module. 
   
   
       15 . The method of  claim 14 , wherein the ultrafiltration or microfiltration membrane module comprises a membrane selected from the group consisting of spiral wound and capillary type membranes. 
   
   
       16 . The method of  claim 1 , wherein the pH of the high salinity liquid is increased to about 8.5 to 9.5 in step (a). 
   
   
       17 . The method of  claim 16 , wherein the pH of the high salinity liquid is increased to about 8.5 to about 9.3. 
   
   
       18 . The method of  claim 1 , wherein the at least one reverse osmosis device is a high pressure reverse osmosis device. 
   
   
       19 . The method of  claim 1 , wherein step (b) comprises passing the pH-increased, non-softened, high salinity liquid through two reverse osmosis devices. 
   
   
       20 . A desalination treatment method for high salinity, boron-containing liquid, including reducing a boron concentration in the high salinity, boron-containing liquid, the method comprising the following steps:
 (a) treating a non-softened, high salinity liquid with a membrane filtration system to remove at least one suspended solid from the liquid;   (b) subsequently increasing a pH of the non-softened, high salinity liquid to about 8 to 9.5;   (c) passing the pH-increased, non-softened, high salinity liquid through at least one reverse osmosis device; and   (d) recovering a permeate from the at least one reverse osmosis device wherein the permeate has a boron concentration of less than about 2 ppm.

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