IP Library Granted Patent US 9,023,211
Granted Patent B2
US 9,023,211 · App. 13/716,662 · Granted May 5, 2015

Vacuum membrane distillation (VMD) using aspirator to generate vacuum pressure

Inventor: Hassan Ali Arafat (Abu Dhabi, AE)
Assignee: Masdar Institute of Science and Technology
B01D61/366B01D61/364B01D2311/04B01D2313/243
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Quick Facts
Patent No.
US 9,023,211
App. No.
13/716,662
Granted
May 5, 2015
Kind
B2
Abstract

A VMD system and method uses an aspirator to generate a vacuum pressure for drawing permeate from a membrane module. The aspirator generates the vacuum pressure by receiving and passing a circulating liquid and combines the permeate with the circulating liquid such that the permeate condensates in the circulating liquid. Using an aspirator (e.g., instead of a vacuum pump) allows a more efficient and cost-effective operation of the VMD system and method, particularly in a desalination application. A VMD system and method using an aspirator may be used in desalination and other applications including, without limitation, environmental cleanup (e.g., removal of volatile organic chemicals from water) and food and medical applications.

Claims (34)

1. A vacuum membrane distillation (VMD) system comprising:

a membrane module configured to receive a feed solution and including a membrane configured to separate a permeate from a retentate in the feed solution;

an aspirator configured to generate a vacuum pressure to draw the permeate from the membrane module, wherein the aspirator is configured to generate the vacuum pressure by receiving and passing a circulating liquid, and wherein the aspirator is configured to combine the permeate with the circulating liquid such that the permeate condensates in the circulating liquid;

a circulation system configured to circulate the circulating liquid through the aspirator;

a permeate collection system configured to collect the permeate condensated in the circulating liquid, and wherein the permeate collection system is configured to supply the permeate together with the circulating liquid to the circulation system; and

wherein the circulation system circulates the circulating liquid and the collected permeate between the aspirator and the permeate collection system tank without heating or cooling the circulating liquid between the aspirator and the permeate collection system tank.

2. The VMD system of claim 1 further comprising a heat transfer system for transferring heat from the permeate collection system to preheat the feed solution.

3. The VMD system of claim 1 wherein the circulation system includes a circulation pump for circulating the circulating liquid including the permeate through the aspirator.

4. The VMD system of claim 1 wherein the circulation system includes a flow control apparatus for controlling a flow of the circulating liquid and thereby controlling the vacuum pressure.

5. The VMD system of claim 1 further comprising a heater configured to heat the feed solution.

6. The VMD system of claim 1 further comprising a feed solution tank for holding the feed solution.

7. The VMD system of claim 1 wherein the membrane module includes a hydrophobic membrane.

8. A vacuum membrane distillation (VMD) method comprising:

circulating a circulating water through an aspirator to generate a vacuum pressure in response to the circulating water using the Venturi effect;

receiving a feed solution in a membrane module;

separating a permeate water vapor from a retentate in the feed solution in the membrane module;

drawing the permeate water vapor from the membrane module using the vacuum pressure generated by the circulating water; and

combining the permeate water vapor with the circulating water such that the permeate water vapor condensates in the circulating water and is circulated together with the circulating water.

9. The VMD method of claim 8 wherein the feed solution is salt water and the retentate is brine.

10. The VMD method of claim 8 further comprising:

heating the feed solution.

11. The VMD method of claim 8 further comprising:

pre-heating the feed solution with heat accumulated in the circulating water due to condensation of the permeate water vapor.

12. The VMD method of claim 8 further comprising:

controlling the flow of the circulating water to control the vacuum pressure.

13. The VMD method of claim 8 wherein the circulating water is circulated with a flow rate through the aspirator sufficient to provide a vacuum pressure of at least about −0.1 bar (gauge).

14. A desalination system comprising:

a source of salt water;

a heater configured to heat the salt water;

a membrane module configured to receive the salt water and including a membrane configured to separate water vapor from brine in the salt water;

an aspirator configured to generate a vacuum pressure to draw the water vapor from the membrane module, wherein the aspirator is configured to generate the vacuum pressure by receiving and passing circulating water through the aspirator, and wherein the aspirator is configured to combine the water vapor with the circulating water such that the permeate condensates in the circulating water; and

a circulation pump configured to circulate the circulating water through the aspirator.

15. The desalination system of claim 14 further comprising a permeate collection tank configured to collect water received from the aspirator.

16. The desalination system of claim 14 further comprising a flow control apparatus configured to control flow of the circulating liquid to control the vacuum pressure.

Assignments (2)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 16, 2018
From: MASDAR INSTITUTE OF SCIENCE AND TECHNOLOGY
To: KHALIFA UNIVERSITY OF SCIENCE AND TECHNOLOGY
Reel/Frame 045356/0428 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Dec 31, 2012
From: ARAFAT, HASSAN ALI
To: MASDAR INSTITUTE OF SCIENCE AND TECHNOLOGY
Reel/Frame 029547/0616 →
Continuity (2)
Provisional Application 61570923 · Dec 15, 2011
Related Publication 20130153497A1 · Jun 20, 2013