IP Library Granted Patent US 8,523,985
Granted Patent B2
US 8,523,985 · App. 13/548,166 · Granted Sep 3, 2013

Bubble-column vapor mixture condenser

Inventors: Prakash Narayan Govindan (Cambridge, MA); Gregory P. Thiel (Belmont, MA); Ronan K. McGovern (Cambridge, MA); John H. Lienhard (Cambridge, MA); Mostafa H. Elsharqawy (Dhahran, SA)
Assignees: Massachusetts Institute of Technology; King Fahd University of Petroleum and Minerals
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Quick Facts
Patent No.
US 8,523,985
App. No.
13/548,166
Granted
Sep 3, 2013
Kind
B2
Abstract

In a bubble-column vapor mixture condenser, a fluid source supplies a carrier-gas stream including a condensable fluid in vapor phase. The condensable fluid in liquid form is contained as a bath in a chamber in each stage of the condenser, and the carrier gas is bubbled through the bath to condense the fluid into the bath. Energy from condensation is recovered to a liquid composition in a conduit that passes through the liquid in the stages of the condenser. The bubble-column vapor mixture condenser can be used, e.g., in a humidification-dehumidification system for purifying a liquid, such as water.

Claims (14)

1. A humidification-dehumidification system comprising:

a source of liquid including a vaporizable component;

a humidifier including a carrier-gas inlet and a carrier-gas outlet; a liquid inlet and a liquid outlet, wherein the liquid inlet is coupled with the source of the liquid; and a chamber in which liquid introduced from the liquid inlet can contact a carrier gas containing a condensable fluid in vapor phase that is introduced from the carrier-gas inlet in a counterflow arrangement and in which a portion of the liquid can vaporize into the carrier gas;

a bubble-column vapor mixture condenser including at least a first stage and a second stage, each stage including a carrier-gas inlet, a carrier-gas outlet and a chamber configured to contain a liquid bath in fluid communication with the carrier-gas inlet and the carrier-gas outlet, wherein the carrier-gas inlet of the first stage is in fluid communication with the carrier-gas outlet of the humidifier, wherein the carrier-gas outlet of the first-stage is in fluid communication with the carrier gas inlet of the second stage, and wherein the carrier-gas outlet of the second stage is in fluid communication with the carrier-gas inlet of the humidifier to facilitate flow of the carrier gas from the humidifier through the chamber of the first stage and then through the chamber of the second stage before returning to the humidifier;

a conduit passing from the source of the liquid through the chamber of each stage of the bubble-column condenser to recover energy from condensation; and

an intermediate exchange conduit coupled with (a) the conduit between the first stage and the second stage of the bubble-column vapor mixture condenser and (b) the humidifier chamber at an intermediate stage for transfer of the liquid therebetween.

2. The humidification-dehumidification system of claim 1 , further comprising a bath of the vaporizable component of the liquid in liquid phase filling the chambers of the first and second stages of the bubble-column condenser.

3. The humidification-dehumidification system of claim 2 , further comprising a bubble generator coupled with the inlet of each stage to generate bubbles of the carrier gas in the liquid.

4. The humidification-dehumidification system of claim 1 , wherein the liquid includes water.

5. The humidification-dehumidification system of claim 1 , wherein the chamber configured to contain the liquid bath has a height-to-diameter aspect ratio less than 1.

6. The humidification-dehumidification system of claim 1 , wherein the chambers configured to contain the liquid baths are at an angle to the vertical.

7. The humidification-dehumidification system of claim 1 , further comprising surfaces extending from the conduit, wherein the surfaces are configured to increase the rate of heat transfer between the conduit and liquid in the chamber.

8. The humidification-dehumidification system of claim 3 , wherein the bubble generator is selected from (a) a sieve plate and (b) a radial, ring, spider, and wheel-type sparger.

9. The humidification-dehumidification system of claim 2 , wherein the bath in the first stage is at least 5° C. warmer than the bath in the second stage.

Assignments (2)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 12, 2012
From: ELSHARQAWY, MOSTAFA H.
To: KING FAHD UNIVERSITY OF PETROLEUM AND MINERALS
Reel/Frame 028540/0673 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 12, 2012
From: GOVINDAN, PRAKASH NARAYAN; THIEL, GREGORY P.; MCGOVERN, RONAN K.; LIENHARD, JOHN H.
To: MASSACHUSETTS INSTITUTE OF TECHNOLOGY
Reel/Frame 028540/0677 →
Continuity (2)
Continuation 13241907 · Sep 23, 2011
Related Publication 20130075940A1 · Mar 28, 2013