Apparatus and method for reverse osmosis

Patent metadata

Field	Value
Publication number	US-11097223-B2
Application number	US-201515128890-A
Country	US
Kind code	B2
Filing date	Mar 31, 2015
Priority date	Mar 31, 2014
Publication date	Aug 24, 2021
Grant date	Aug 24, 2021

Abstract

An apparatus for reverse osmosis, the apparatus comprising: a single-stage reverse osmosis (SSRO) unit; and a counter-current membrane cascade with recycle (CMCR) unit comprising a plurality of stages of reverse osmosis including at least a first stage and a second stage wherein permeate from the first stage is configured to be introduced as feed to the second stage; wherein retenate from the SSRO unit is configured to be introduced as feed to the first stage, and wherein product obtained using the apparatus comprises permeate from the SSRO unit and permeate from a last stage of the CMCR unit.

First claim

The invention claimed is:

1. An apparatus for reverse osmosis, the apparatus comprising:
a single-stage reverse osmosis (SSRO) unit; and
a counter-current membrane cascade with recycle (CMCR) unit comprising a plurality of stages of reverse osmosis including at least a first stage, a second stage, and a third stage, wherein each of the plurality of stages in the CMCR unit consists of a plurality of reverse osmosis membrane modules, and wherein the CMCR unit comprises no interstage pumping on retentate sides of the membrane cascade in the CMCR unit;
wherein a first combined stream consisting of retentate from the SSRO unit and retentate from the second stage is configured to be introduced as feed without use of a pump to the first stage,
wherein a second combined stream consisting of retentate from the third stage and permeate from the first stage is configured to be introduced as feed to the second stage without use of a pump,
wherein the first stage is a stage at which concentration of the combined flows of the retentate from the second stage and the permeate from the first stage is closest to concentration of the retentate from the SSRO unit,
wherein the SSRO unit is configured to have a same osmotic pressure differential (OPD) as OPD in each of the plurality of reverse osmosis stages of the CMCR unit, and
wherein product obtained using the apparatus comprises permeate from the SSRO unit and permeate from a last stage of the CMCR unit.

2. The apparatus for reverse osmosis of claim 1 , wherein the last stage of the CMCR unit is the third stage, and wherein permeate from the second stage is configured to be introduced as feed to the third stage.

3. The apparatus for reverse osmosis of claim 1 , wherein the SSRO unit comprises a plurality of reverse osmosis membrane modules connected in parallel.

4. The apparatus for reverse osmosis of claim 1 , wherein membrane rejection in each of the plurality of stages in the CMCR unit decreases in the direction of retentate flow in the CMCR unit.

5. The apparatus for reverse osmosis of claim 1 , wherein one of the plurality of stages in the CMCR is configured to have a safety factor of less than one.

6. A method of reverse osmosis, the method comprising the steps of:
a) introducing feed of an aqueous solution into a single-stage reverse osmosis (SSRO) unit;
b) introducing retentate from the SSRO unit as feed to a counter-current membrane cascade with recycle (CMCR) unit, the CMCR unit comprising a plurality of stages of reverse osmosis including at least a first stage, a second stage, and a third stage, wherein each of the plurality of stages in the CMCR unit consists of a plurality of reverse osmosis membrane modules, and wherein the CMCR unit comprises no interstage pumping on retentate sides of the membrane cascade in the CMCR unit;
c) introducing a first combined stream consisting of the retentate from the SSRO unit and retentate from the second stage as feed to the first stage without use of a pump;
d) introducing a second combined stream consisting of retentate from the third stage and permeate from the first stage as feed to the second stage without use of a pump; and
e) collecting as product permeate from the SSRO unit and permeate from a last stage of the CMCR unit, wherein the first stage is a stage at which concentration of the combined flows of the retentate from the second stage and the permeate from the first stage is closest to concentration of the retentate from the SSRO unit, and wherein osmotic pressure differential (OPD) in the SSRO unit is the same as OPD in each of the plurality of reverse osmosis stages of the CMCR unit.

7. The method for reverse osmosis of claim 6 , wherein the last stage of the CMCR unit is the third stage and further comprises introducing permeate from the second stage as feed to the third stage.

8. The method of reverse osmosis of claim 6 , wherein safety factor for one of the plurality of stages in the CMCR is less than one.

9. The apparatus for reverse osmosis of claim 1 , further comprising the retentate from the SSRO unit, the retentate from the second, and the first combined stream, wherein the first combined stream has a concentration closest to a concentration of the retentate from the SSRO unit, and wherein the first combined stream has a concentration such that the OPD in the first stage is the same as the OPD in the SSRO unit.

10. The apparatus for reverse osmosis of claim 9 , further comprising the retentate from the third stage, the permeate from the first stage, and the second combined stream, wherein the second combined stream has a concentration such that the OPD in the second stage is the same as the OPD in the first stage.

Assignees

• Univ Nanyang Tech

Inventors

• Chong Tzyy Haur
• Krantz William B
• Loo Siew Leng

Classifications

• B01D61/12

  Controlling or regulating · CPC title

• Y02A20/131

  Reverse-osmosis · CPC title

• B01D61/08

  Apparatus therefor · CPC title

• B01D61/026 Primary

  comprising multiple reverse osmosis steps · CPC title

• C02F1/441

  by reverse osmosis · CPC title