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Methods for reducing boron concentration in high salinity liquid

a technology of high salinity liquid and boron concentration, which is applied in the direction of multi-stage water/sewage treatment, membranes, separation processes, etc., can solve the problems of high boron rejection by ro membranes, increased operating costs, and effective filtration of feed water, so as to reduce boron concentration and high salinity

Inactive Publication Date: 2009-02-12
HYDRANAUTICS +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

This method significantly increases boron rejection rates in reverse osmosis systems, reducing boron concentration to less than 0.5 ppm without scaling issues, while minimizing operating costs by eliminating the need for pre-softening and acid neutralization.

Problems solved by technology

Such an approach would result in both effective filtration of feed water and higher boron rejection by RO membranes.
However, the use of acid for pH reduction, followed by caustic for acid neutralization, would result in additional operating costs.
However, during periods of stormy weather, media filters could not cope with the increasing load of suspended matter.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

example 1

[0035]A second sample of seawater having a boron concentration of 5.89 ppm was treated with sodium hydroxide in-line to raise the pH to 9.24. Approximately 28 ppm of 100% NaOH were added to achieve a pH in the desired range. Approximately 4 ppm of a commercial anti-scalant was added to the liquid. The seawater, at a temperature of 23.4° C., was fed through the same pressure vessel as in Comparative Example 1. After passing through the pressure vessel, the permeate was analyzed and found to have a boron concentration of 0.48 ppm. The data from the two Examples are tabulated below.

WaterWaterInitial boron con-Final boron con-ExampleTemp (° C.)pHcentration (ppm)centration (ppm)123.18.146.021.27223.49.245.890.48

[0036]These Examples demonstrate that the pH of the high salinity liquid has a significant effect on the final boron concentration in the permeate recovered from the reverse osmosis device. When the pH is about 8 to about 9.5, the boron concentration may be reduced to less than ab...

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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.

Description

CROSS-REFERENCE TO RELATED APPLICATIONS[0001]This application is a continuation of U.S. patent application Ser. No. 10 / 460,697, filed Jun. 12, 2003, which is a continuation-in-part of application Ser. No. 10 / 188,476, filed Jul. 3, 2002, and which claims the benefit of U.S. Provisional Application No. 60 / 388,256, filed Jun. 13, 2002, and U.S. Provisional Application No. 60 / 443,363, filed Jan. 29, 2003, all of the disclosures of which are incorporated herein by reference.BACKGROUND OF THE INVENTION[0002]Seawater typically contains about 4 to 7 ppm boron, in addition to a variety of water-soluble salts. Traditional methods for purifying (desalinating) seawater for drinking and irrigation purposes utilize reverse osmosis (RO) membranes, which are effective at significantly reducing the concentrations of all dissolved ions in the seawater. Although the reduction of the majority of dissolved ions by polyamide reverse osmosis membranes is about 98% to about 99%, the rejection rate of boron...

Claims

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Application Information

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Patent Type & Authority Applications(United States)
IPC IPC(8): C02F1/44C02F1/66C02F103/08C02F101/10B01D61/02B01D61/04C02F1/52C02F5/08C02F9/00
CPCB01D61/022B01D61/04C02F2209/06C02F2103/08C02F2101/10C02F9/00C02F5/08C02F1/66C02F1/5236B01D2311/04C02F1/441C02F1/444B01D2311/18Y02A20/131B01D61/026
Inventor WILF, MARKBARTELS, CRAIG R.HIROSE, MASAHIKO
Owner HYDRANAUTICS