Multi-stage bubble-column vapor mixture condensation

Patent metadata

Field	Value
Publication number	US-11007455-B2
Application number	US-201916405496-A
Country	US
Kind code	B2
Filing date	May 7, 2019
Priority date	Sep 23, 2011
Publication date	May 18, 2021
Grant date	May 18, 2021

Abstract

A multi-stage bubble-column vapor mixture condenser comprises at least a first stage and a second stage. Each stage includes a carrier-gas inlet and a carrier-gas outlet, as well as a condenser chamber containing a condensing bath in fluid communication with the carrier-gas inlet and the carrier-gas outlet. The carrier-gas inlet is positioned to bubble carrier gas from the carrier-gas inlet up through the condensing bath, overcoming a hydrostatic head of the condensing bath. The carrier-gas outlet is positioned with an opening for carrier-gas extraction above the condensing bath, wherein the first-stage carrier-gas outlet is in fluid communication with the carrier-gas inlet of the second stage to facilitate flow of the carrier gas through the condensing bath in the condenser chamber of the first stage and then through the condensing bath in the condenser chamber of the second stage.

First claim

What is claimed is:

1. A method for multi-stage bubble-column vapor mixture condensation using a multi-stage bubble-column vapor mixture condenser, comprising: at least a first stage and a second stage, wherein each stage includes:
a carrier-gas inlet;
a carrier-gas outlet; and
a condenser chamber containing a condensing bath in fluid communication with the carrier-gas inlet and the carrier-gas outlet, wherein the carrier-gas inlet is positioned to bubble carrier gas from the carrier-gas inlet up through the condensing bath, overcoming a hydrostatic head of the condensing bath, wherein the carrier-gas outlet is positioned with an opening for carrier-gas extraction above the condensing bath, wherein the first-stage carrier-gas outlet is in fluid communication with the carrier-gas inlet of the second stage to facilitate flow of the carrier gas through the condensing bath in the condenser chamber of the first stage and then through the condensing bath in the condenser chamber of the second stage, and wherein the condenser chamber is configured with a height-to-diameter aspect ratio, an orientation angle, and is sufficiently free of impediments to establish a natural and regular liquid circulation loop in the condensing bath that maintains a temperature difference of no greater than 1%, measured in Kelvin, from top-to-bottom of the bath,

the method comprising:
introducing a carrier gas including a vaporized component through the carrier-gas inlet of the first stage;
bubbling the carrier gas up through the first-stage condensing bath while condensing a portion of the vaporized component of the carrier gas into the first-stage condensing bath;
extracting the carrier gas from the carrier-gas outlet of the first stage;
passing the carrier gas from the carrier-gas outlet of the first stage through the carrier-gas inlet of the second stage;
bubbling the carrier gas up through the condensing bath of the second stage while condensing an additional portion of the vaporized component of carrier gas into the second-stage condensing bath;
extracting the carrier gas from the carrier-gas outlet of the second stage; and
establishing the natural and regular liquid circulation loop in each condensing bath to thereby maintain the temperature difference of no greater than 1%, measured in Kelvin, from top-to-bottom of each bath.

2. The method of claim 1 , wherein the condensing bath in the first stage is at least 5° C. warmer than the condensing bath in the second stage.

3. The method of claim 1 , further comprising adding the vaporized component to the carrier gas by vaporizing the vaporized component from a feed liquid into the carrier gas in a humidifier.

4. The method of claim 3 , wherein the vaporized component is water.

5. The method of claim 4 , wherein the condensing bath in each stage consists essentially of water, and the method further comprising extracting the water from the condensing baths.

6. The method of claim 1 , wherein the carrier gas is extracted from the carrier-gas outlet of each stage with a concentration of vaporized component that is lower than that of the carrier gas as it entered the stage.

7. The method of claim 1 , further comprising transferring the carrier gas through an intermediate exchange conduit between intermediate stages of the bubble-column vapor mixture condenser and of the humidifier.

8. The method of claim 1 , further comprising directing coolant through an internal conduit in counterflow to carrier-gas flow through the condenser chamber and recovering energy from condensation with the coolant.

9. The method of claim 8 , wherein the coolant is in a liquid phase.

10. The method of claim 9 , wherein the coolant includes water.

11. The method of claim 1 , wherein the condensing bath has a height-to-diameter aspect ratio less than 0.5.

Assignees

• Massachusetts Inst Technology
• Univ King Fahd Pet & Minerals

Inventors

• Govindan Prakash Narayan
• Thiel Gregory P
• Mcgovern Ronan K
• Lienhard John H
• Elsharqawy Mostafa H

Classifications

• Y02A20/131

  Reverse-osmosis · CPC title

• B01F2101/55

  Mixing liquid air humidifiers with air · CPC title

• B01F23/2321

  by moving liquid and gas in counter current · CPC title

• B01F23/231

  by bubbling (mixers with gas or liquid agitation, e.g. with air supply tubes B01F33/40) · CPC title

• B01D3/205

  Bubble caps · CPC title