IP Library Patent Application 14520650
Patent Application
App. No. 14/520,650

REJECT RECOVERY REVERSE OSMOSIS (R2RO)

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Patent No.
US None
App. No.
14/520,650
Abstract

A process for the recovery of purified water from a reverse osmosis reject stream includes preconditioning a reject stream to remove scaling ions and provide preconditioned water; separating any precipitate that forms in the preconditioned water to form a feed stream; subjecting the feed stream to high pressure membrane filtration system including a recirculating, high pressure pump generating a permeate stream and a second reject stream; adding a make-up water stream to the feed stream; and separating the permeate stream as purified water. Additional features and embodiments are also provided.

Claims (53)

1 . A process for achieving high salt concentration and/or high permeate recovery from a reject stream from a first reverse osmosis process including a first reverse osmosis permeate stream and first reverse osmosis reject stream, comprising:

preconditioning the first reverse osmosis reject stream to remove scaling ions and provide preconditioned water;

separating any precipitate that forms in the preconditioned water to form a feed stream;

subjecting the feed stream to high pressure reverse osmosis membrane filtration system including a recirculating, high pressure pump generating a second permeate stream and a second reject stream;

adding a make-up water stream to the feed stream; and

separating the second permeate stream as purified water.

2 . The process of claim 1 , further comprising removing at least one member of the group consisting of colloidal impurities and inorganic complexes from the reject stream following the preconditioning step.

3 . The process of claim 2 , wherein said removing step is accomplished by treating the reject stream by at least one of ultrafiltration and microfiltration.

4 . The process of claim 1 , wherein the high pressure membrane filtration is at a pressure between 100 and 150 barg.

5 . The process of claim 1 , wherein the high pressure membrane filtration is at a pressure of more than 140 barg.

6 . The process of claim 1 , wherein the high pressure membrane filtration is conducted in a disk membrane system.

7 . The process of claim 1 , wherein the high pressure membrane filtration is conducted in a plate and frame membrane system.

8 . The process of claim 1 , further comprising heating the feed stream.

9 . The process of claim 1 , further comprising adding an anti-sealant to the feed stream.

10 . The process of claim 1 , further comprising cleaning the membrane filtration system by a low pressure permeate flush.

11 . The process of claim 1 , wherein the second reject stream has a salt concentration up to 12%-15%.

12 . The process of claim 1 , wherein the high pressure membrane filtration system operates between 2000-2100 psi.

13 . The process of claim 1 , wherein the reject stream has a total dissolved solids content of between 120000-150000 mg/l.

14 . The process of claim 1 , wherein total water recovery from an RO system including permeate from the first reverse osmosis and permeate from the second reverse osmosis is at least 98% when it is not limited by TDS.

15 . A combined reverse osmosis process for achieving high salt concentration and/or high permeate recovery from an upstream first reverse osmosis process and a downstream second reverse osmosis process, said first reverse osmosis process including a first reverse osmosis permeate stream and a first reverse osmosis reject stream and said downstream second reverse osmosis process including a second reverse osmosis process permeate stream and a second reverse osmosis reject stream, comprising:

treating cooling tower blowdown in a first reverse osmosis process to produce a first reverse osmosis process permeate stream and a first reverse osmosis process reject stream;

preconditioning the first reverse osmosis reject stream to remove scaling ions and provide preconditioned water;

separating any precipitate that forms in the preconditioned water to form a feed stream;

subjecting the feed stream to the second reverse osmosis process including a recirculating, high pressure pump generating a second reverse osmosis process permeate stream and a second reverse osmosis process reject stream;

adding a make-up water stream to the feed stream; and

separating the second reverse osmosis process permeate stream as treated water.

16 . A combined reverse osmosis process for achieving high salt concentration and/or high permeate recovery from an upstream first reverse osmosis process and a downstream second reverse osmosis process, said first reverse osmosis process including a first reverse osmosis permeate stream and a first reverse osmosis reject stream and said downstream second reverse osmosis process including a second reverse osmosis process permeate stream and a second reverse osmosis reject stream, comprising:

treating recycled and reused refinery water in a first reverse osmosis process to produce a first reverse osmosis process permeate stream and a first reverse osmosis process reject stream;

preconditioning the first reverse osmosis reject stream to remove scaling ions and provide preconditioned water;

separating any precipitate that forms in the preconditioned water to form a feed stream;

subjecting the feed stream to the second reverse osmosis process including a recirculating, high pressure pump generating a second reverse osmosis process permeate stream and a second reverse osmosis process reject stream;

adding a make-up water stream to the feed stream; and

separating the second reverse osmosis process permeate stream as treated water.

17 . A combined reverse osmosis process for achieving high salt concentration and/or high permeate recovery from an upstream first reverse osmosis process and a downstream second reverse osmosis process, said first reverse osmosis process including a first reverse osmosis permeate stream and a first reverse osmosis reject stream and said downstream second reverse osmosis process including a second reverse osmosis process permeate stream and a second reverse osmosis reject stream, comprising:

treating recycled and reused coal to chemical production water in a first reverse osmosis process to produce a first reverse osmosis process permeate stream and a first reverse osmosis process reject stream;

preconditioning the first reverse osmosis reject stream to remove scaling ions and provide preconditioned water;

separating any precipitate that forms in the preconditioned water to form a feed stream;

subjecting the feed stream to the second reverse osmosis process including a recirculating, high pressure pump generating a second reverse osmosis process permeate stream and a second reverse osmosis process reject stream;

adding a make-up water stream to the feed stream; and

separating the second reverse osmosis process permeate stream as treated water.

18 . A combined reverse osmosis process for achieving high salt concentration and/or high permeate recovery from an upstream first reverse osmosis process and a downstream second reverse osmosis process, said first reverse osmosis process including a first reverse osmosis permeate stream and a first reverse osmosis reject stream and said downstream second reverse osmosis process including a second reverse osmosis process permeate stream and a second reverse osmosis reject stream, comprising:

treating flue gas desulfurization water in a first reverse osmosis process to produce a first reverse osmosis process permeate stream and a first reverse osmosis process reject stream;

preconditioning the first reverse osmosis reject stream to remove scaling ions and provide preconditioned water;

separating any precipitate that forms in the preconditioned water to form a feed stream;

subjecting the feed stream to the second reverse osmosis process including a recirculating, high pressure pump generating a second reverse osmosis process permeate stream and a second reverse osmosis process reject stream;

adding a make-up water stream to the feed stream; and

separating the second reverse osmosis process permeate stream as treated water.

19 . The process of claim 1 , comprising sending said second reject stream to a crystallizer without a brine concentration step.

20 . The process of claim 1 , wherein an internal flow distribution system with the membrane filtration system ensures minimal laminar flow space and therefore minimal fouling.

21 . The process of claim 19 , wherein removal of a brine concentration step decreases operating and capital costs.

22 . An apparatus for practicing the process of claim 1 .

23 . The process of claim 1 , wherein the second reject stream has a salt concentration up to 15%.

24 . The process of claim 1 , wherein total water recovery from an RO system including permeate from the first reverse osmosis and permeate from the second reverse osmosis is up to 99%.

Assignments (5)
RELEASE OF SECURITY INTEREST Recorded May 1, 2026
From: PNC BANK, NATIONAL ASSOCIATION
To: AQUATECH INTERNATIONAL CORPORATION; QUA GROUP, LLC; AQUATECH INTERNATIONAL SALES CORPORATION; AQUATECH INTERNATIONAL, LLC; AQUATECH ENERGY SERVICES, LLC N/K/A AQUATECH ENVIRONMENTAL SERVICES, LLC; ALVEUS HOLDINGS, INC.
Reel/Frame 075312/0234 →
CHANGE OF NAME Recorded Jun 30, 2017
From: AQUATECH INTERNATIONAL CORPORATION
To: AQUATECH INTERNATIONAL, LLC
Reel/Frame 043072/0139 →
AMENDED AND RESTATED PATENT, TRADEMARK AND COPYRIGHT SECURITY AGREEMENT Recorded Jan 17, 2017
From: AQUATECH INTERNATIONAL, LLC; QUA GROUP, LLC; AQUATECH INTERNATIONAL SALES CORPORATION; AQUATECH ENERGY SERVICES, LLC; ALVEUS HOLDINGS, INC.
To: PNC BANK, NATIONAL ASSOCIATION
Reel/Frame 041380/0058 →
ACKNOWLEDGEMENT OF SECURITY INTEREST IN PATENTS Recorded Jul 10, 2015
From: AQUATECH INTERNATIONAL CORPORATION; QUA GROUP, LLC; AQUATECH INTERNATIONAL SALES CORPORATION
To: PNC BANK, NATIONAL ASSOCIATION
Reel/Frame 036089/0047 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Dec 11, 2014
From: CHIDAMBARAN, RAVI; MITTAL, ARUN; SARKAR, AJANTA
To: AQUATECH INTERNATIONAL CORPORATION
Reel/Frame 034476/0155 →