Facility for cooling a gas flow containing co2 and method using such a facility

Patent metadata

Field	Value
Publication number	US-2025050268-A1
Application number	US-202218721185-A
Country	US
Kind code	A1
Filing date	Nov 22, 2022
Priority date	Dec 17, 2021
Publication date	Feb 13, 2025
Grant date	—

Abstract

A facility for cooling a gas flow containing CO2, water and at least one other component includes a scrubbing tower, a pipe for conveying the gas flow at a first temperature to the bottom of the tower, a pipe for conveying water at a second temperature, which is lower than the first temperature, to a first level at the top of the scrubbing tower, a pump, a pipe being connected to the tank of the column for removing tank water and to the pump for pressurizing the water removed from the tank, and means for withdrawing water downstream of the pump, these means being connected to the tower thereby conveying the pressurized water at a third temperature to an indirect heat exchanger located in the tower at the second level above the first level, the third temperature being higher than the second temperature, but lower than the first temperature.

First claim

1 - 10 . (canceled)

11 . An installation for cooling a gas stream, containing CO 2 , water and at least one other component, comprising:
a scrubbing tower, a duct configured to send the gas stream at a first temperature to the bottom of the tower, a duct configured to send water at a second temperature, which is lower than the first temperature, to a first level at the top of the scrubbing tower, a pump, a duct being connected to the bottom end of the column and configured to remove the bottom water and to the pump so as to pressurize the water removed from the bottom end,. a withdrawing means for withdrawing water downstream of the pump, the withdrawing means being connected to the tower and configured to send the pressurized water at a third temperature to an indirect heat exchanger located in the tower at a second level above the first level, the third temperature being higher than the second temperature but lower than the first temperature.

12 . The installation as claimed in claim 11 , further comprising a heater, the withdrawing means being connected to the heater and configured to send water pressurized by the pump thereto and configured to send the water heated in the heater to the indirect heat exchanger.

13 . The installation as claimed in claim 11 , wherein the tower comprises mass and heat exchange elements disposed below the first level and between the first and second levels.

14 . A method for cooling a gas stream, containing CO 2 , water and at least one other component, comprising.
sending the gas stream at a first temperature to the bottom of a scrubbing tower,. scrubbing the stream with water sent to a first level at the top of the scrubbing tower at a second temperature, which is lower than the first temperature,. removing gas at least partially purified of water at the top of the tower at a temperature lower than the first temperature, water is removed at the bottom end of the scrubbing tower and pressurized in a pump,. the water pressurized by the pump is sent, without having been cooled, at a third temperature to an indirect heat exchanger located in the tower at a second level above the first level,
wherein the third temperature is higher than the second temperature but lower than the first temperature, and
wherein the first portion of the water is cooled in the indirect heat exchanger in order to introduce heat at the top of the scrubbing tower.

15 . The method as claimed in claim 14 , wherein at least a portion of the water cooled in the heat exchanger is mixed with water pressurized and cooled in a cooler.

16 . The method as claimed in claim 14 , wherein the gas removed at the top of the tower is sent to a filter thereby removing solid impurities.

17 . The method as claimed in claim 14 , wherein the water sent to the heat exchanger is not heated downstream of the pressurization so as to reach the third temperature.

18 . The method as claimed in claim 14 , wherein the water sent to the heat exchanger is heated downstream of the pressurization so as to reach the third temperature.

19 . The method as claimed in claim 16 , wherein the water sent to the heat exchanger is heated by indirect heat exchange with the gas filtered in the filter and then compressed in a compressor.

20 . The method as claimed in claim 18 , wherein the water sent to the heat exchanger is heated by indirect heat exchange with the gas stream upstream of the tower.

Assignees

• Lair Liquide Sa Pour Letude Et L’Exploitation Des Procedes Georges Claude

Inventors

• Tran Michael
• Leclerc Mathieu
• Caloro Gian Luigi
• Harbal Achraf

Classifications

• B01D2259/65

  Employing advanced heat integration, e.g. Pinch technology · CPC title

• B01D2256/22

  Carbon dioxide · CPC title

• B01D2252/103

  Water · CPC title

• B01D53/1418

  Recovery of products · CPC title

• B01D46/0036

  by adsorption or absorption · CPC title