Batch pressure-driven membrane separation with closed-flow loop and reservoir

Patent metadata

Field	Value
Publication number	US-10166510-B2
Application number	US-201615350064-A
Country	US
Kind code	B2
Filing date	Nov 13, 2016
Priority date	Feb 22, 2016
Publication date	Jan 1, 2019
Grant date	Jan 1, 2019

Abstract

A feed of at least one of (a) a source liquid including a solvent with a dissolved impurity and (b) a retentate of the source liquid is pumped in a substantially closed loop through a liquid-separation module. The liquid-separation module includes a membrane that passes at least partially purified solvent to a permeate side of the membrane while diverting the impurity in a retentate on the retentate side of the membrane. The purified solvent is extracted from the permeate side of the membrane; and the retentate from the liquid-separation module is pumped to or through a pressurized reservoir with a variable volume for the feed component and recirculated as a component of the feed. Over time, the volume for the feed is reduced and the pressure applied to the feed in the reservoir is increased to balance against an increasing difference in osmotic pressure across the membrane.

First claim

What is claimed is:

1. A method for batch pressure-driven membrane separation, comprising:
a) pumping a feed of at least one of (i) a source liquid including a solvent with a dissolved impurity and (ii) a retentate of the source liquid into a substantially closed loop through a liquid-separation module, wherein the liquid-separation module comprises a membrane that passes at least partially purified solvent as filtrate to a permeate side of the membrane while diverting at least a portion of the impurity in a retentate on a retentate side of the membrane;
b) extracting the purified solvent from the permeate side of the membrane;
c) pumping the retentate as feed component from the liquid-separation module to or through a pressurized reservoir with a variable volume for the feed component;
d) recirculating the retentate as feed component via steps (a)-(e) and reducing the volume for the feed in the pressurized reservoir, in the conduits and in the liquid-separation module and increasing the pressure applied to the feed in the reservoir over time to balance against an increasing difference in osmotic pressure across the membrane as the feed increases in osmotic pressure; and
e) after a plurality of iterations through the above steps, discharging a concentrated impurity stream from the liquid-separation module and supplying new source liquid to the substantially closed loop.

2. The method of claim 1 , wherein feed flows continuously and simultaneously through steps (a)-(d).

3. The method of claim 1 , wherein the solvent comprises water.

4. The method of claim 3 , wherein the liquid-separation module is a reverse-osmosis or nano-filtration module.

5. The method of claim 1 , further comprising pumping pressurizing fluid into or through the reservoir to control the volume of feed in the reservoir and the pressure applied to the feed in the reservoir.

6. The method of claim 5 , wherein the pressurizing fluid is passed into or through the reservoir tank on an opposite side of a movable wall, membrane, bladder, or diaphragm from the feed in the reservoir.

7. The method of claim 5 , wherein the pressurizing fluid includes the purified solvent from the liquid-separation module.

8. The method of claim 5 , wherein both the liquid-separation module and a storage tank are inside a pressure vessel, and wherein the pressure vessel defines the pressurized reservoir, the method further comprising:
pumping the pressurizing fluid into the storage tank;
pumping the feed in the substantially closed loop through the pressure vessel to release additional purified solvent from the feed through the membrane; and
controlling the flow of pressurizing fluid into the storage tank to increase the volume of the storage tank and to decrease the volume for the feed while increasing the pressure applied to the feed over time.

9. The method of claim 8 , wherein the pressurizing fluid includes purified solvent from the liquid-separation module.

10. The method of claim 8 , further comprising injecting additional pressurizing fluid into the storage tank or releasing pressurizing fluid from the storage tank to counter-balance a change in density of the feed.

11. The method of claim 8 , wherein the storage tank is a bladder or flexible tank.

Assignees

• Massachusetts Inst Technology

Inventors

• Warsinger David Elan Martin
• Lienhard V John H
• Tow Emily Winona
• Mcgovern Ronan Killian
• Thiel Gregory Parker

Classifications

• C02F2209/03

  Pressure · CPC title

• B01D2315/14

  Batch-systems · CPC title

• B01D2311/14

  Pressure control · CPC title

• B01D61/025

  Reverse osmosis; Hyperfiltration · CPC title

• B01D2311/25

  Recirculation, recycling or bypass, e.g. recirculation of concentrate into the feed · CPC title