Systems and methods for maximizing recovery in membrane distillation

Patent metadata

Field	Value
Publication number	US-10569223-B2
Application number	US-201715628205-A
Country	US
Kind code	B2
Filing date	Jun 20, 2017
Priority date	Jun 23, 2016
Publication date	Feb 25, 2020
Grant date	Feb 25, 2020

Abstract

Membrane distillation (MD) systems include at least two MD modules arranged in series, each of at least two MD modules including a condensing media inlet operable to receive a condensing media and a condensing media outlet, a feed inlet operable to receive a feed media and a feed outlet, and a first heating element positioned and operable to heat a feed prior to or upon introduction of the feed to a first of the at least two MD modules, wherein a stream exiting the feed outlet of the first of the at least two MD modules is introduced to the second of the at least two MD modules. Other MD systems include at least two MD modules arranged in parallel.

First claim

What is claimed is:

1. A membrane distillation (MD) system comprising at least two MD modules arranged in series, each of the at least two MD modules comprising at least one membrane, a condensing media inlet or a surface operable to receive a condensate and a condensing media outlet, a feed inlet operable to receive a feed media and a feed outlet, and at least one external heating element positioned and operable to heat the feed media to a first temperature prior to introduction of the feed media to a first of the at least two MD modules, and to heat a stream exiting the feed outlet of the first of the at least two MD modules to at least a higher temperature prior to the stream being introduced to a second of the at least two MD modules, wherein the at least one external heating element and the condensing media or a surface are operable to maintain a high temperature gradient between feed media entering and permeate in the at least two MD modules, and
wherein temperature on a feed side of the at least two MD modules is maintained at a high value to enhance membrane flux and water recovery by increasing temperature of the stream exiting the feed outlet of each of the at least two MD modules to a higher temperature.

2. The MD system of claim 1 comprising more than two MD modules.

3. The MD system of claim 1 further comprising a second external heating element positioned and operable to heat the stream exiting the first of the at least two MD modules to at least the first temperature.

4. The MD system of claim 1 comprising more than two MD modules arranged serially and plural external heating elements in addition to the at least one external heating element, wherein each of the plural external heating elements is positioned and operable to heat a stream exiting each of the more than two MD modules to a high temperature prior to the stream being introduced to a successive MD module.

5. The MD system of claim 1 , wherein the at least one external heating element is a central heat exchanger positioned and operable to also heat the stream exiting the feed outlet of the first of the at least two MD modules to at least the first temperature.

6. The MD system of claim 1 comprising more than two MD modules, wherein the at least one external heating element is a central heat exchanger positioned and operable to also heat a stream exiting each of the more than two MD modules to at least the first temperature prior to the stream being introduced to a successive MD module.

7. The MD system of claim 1 wherein each of the MD modules is independently selected from the group consisting of a hollow fiber membrane module, a flat membrane module and a spiral wound membrane module.

8. The MD system of claim 1 wherein each of the MD modules is independently selected from the group consisting of a direct contact membrane distillation (DCMD) module, a sweep gas membrane distillation (SGMD) module, a vacuum membrane distillation (VMD) module and an air gap membrane distillation (AGMD) module.

9. The MD system of claim 1 wherein at least one of the at least two MD modules comprises at least one heating element positioned therein.

10. The MD system of claim 1 wherein at least one of the at least two MD modules comprises a spiral wound membrane module or a hollow fiber module.

11. A method for purifying a feed stream comprising the steps of providing a plurality of MD modules arranged in series, circulating a condensing media through each of the plurality of MD modules, heating the feed stream to a first temperature prior to introduction of the feed stream to the first of the plurality of MD modules using at least one external heating element, subsequently heating each stream exiting each MD module to a higher temperature using the at least one external heating element prior to introducing each stream to a successive MD module, maintaining a high temperature gradient between feed stream entering and permeate of the at least two MD modules, and maintaining temperature on a feed side of the at least two MD modules to enhance membrane flux by increasing temperature of the stream exiting the feed outlet of each of the at least two MD modules to the first temperature.

12. The method of claim 11 wherein at least one of the plurality of MD modules comprises at least one heating element positioned therein.

13. The method of claim 11 wherein at least one of the plurality of MD modules comprises a spiral wound membrane module comprising at least one baffle positioned in the hot feed channel and an external steam jacket.

14. The method of claim 11 wherein each of the plurality of MD modules is independently selected from the group consisting of a hollow fiber membrane module, a flat membrane module and a spiral wound membrane module.

15. The method of claim 11 wherein each of the plurality of MD modules is independently selected from the group consisting of a direct contact membrane distillation (DCMD) module, a sweep gas membrane distillation (SGMD) module, a vacuum membrane distillation (VMD) module and an air gap membrane distillation (AGMD) module.

16. A membrane distillation (MD) system comprising at least two MD modules arranged in series, each of the at least two MD modules comprising at least one membrane, a condensing media inlet operable to receive a condensing media and a condensing media outlet, a feed inlet operable to receive a feed media and a feed outlet, and at least one external heating element positioned and operable to heat the feed media to a first temperature prior to introduction of the feed media to a first of the at least two MD modules, and to heat a stream exiting the feed outlet of the first of the at least two MD modules to at least the first temperature prior to the stream being introduced to a second of the at least two MD modules, wherein the at least one external heating element and the condensing media are operable to maintain a consistent temperature gradient between feed media entering and exiting the at least two MD modules, and
wherein temperature on a feed side of the at least two MD modules is maintained at a high value to enhance membrane flux and water recovery by increasing temperature of the stream exiting the feed outlet of each of the at least two MD modules to the first temperature.

Assignees

• New Jersey Inst Technology

Inventors

• Mitra Somenath
• Roy Sagar

Classifications

• B01D2317/04

  Elements in parallel · CPC title

• C02F2103/08

  Seawater, e.g. for desalination · CPC title

• B01D2317/022

  Reject series · CPC title

• C02F1/447

  by membrane distillation (distillation and evaporation without the use of membranes C02F1/04) · CPC title

• B01D61/58

  Multistep processes · CPC title