Carbon dioxide recovery device

Patent metadata

Field	Value
Publication number	US-12364950-B2
Application number	US-202117917510-A
Country	US
Kind code	B2
Filing date	Apr 26, 2021
Priority date	May 1, 2020
Publication date	Jul 22, 2025
Grant date	Jul 22, 2025

Abstract

A carbon dioxide recovery device provided with a separation device that separates carbon dioxide from to-be-separated gas (for example, combustion exhaust gas) containing carbon dioxide, wherein: in order from the upstream side where the to-be-separated gas is supplied, the separation device and carbon dioxide sublimators, which sublimate (solidify) carbon dioxide that was separated in the separation device, are connected in series, refrigerant circuits in which a fluid having cold heat serves as the refrigerant, are connected to the carbon dioxide sublimators, and the refrigerant is used to sublimate (solidify) the carbon dioxide; and when the carbon dioxide is sublimated (solidified), the carbon dioxide sublimators are depressurized and set to negative pressure so as to draw in the carbon dioxide separated at the separation device.

First claim

The invention claimed is:

1. A carbon dioxide recovery device comprising a separation device to separate carbon dioxide from to-be-separated gas including the carbon dioxide, wherein
the separation device and a carbon dioxide desublimator to desublimate (solidify) the carbon dioxide having been separated by the separation device are connected in series in order from an upstream side of supplying the to-be-separated gas,
the carbon dioxide desublimator is connected with a refrigerant circuit in which a fluid having cold heat is utilized as a refrigerant, and the carbon dioxide is desublimated (solidified) by the refrigerant, and
wherein the device is configured so that when the carbon dioxide is desublimated (solidified), the carbon dioxide desublimator is depressurized to be under negative pressure so that the carbon dioxide having been separated by the separation device is sucked.

2. The carbon dioxide recovery device according to claim 1 , wherein
the separation device is provided with an absorption tower configured to bring to-be-separated gas including carbon dioxide and absorbing liquid for absorbing the carbon dioxide into gas-liquid contact to absorb the carbon dioxide by the absorbing liquid and a regeneration tower configured to emit the carbon dioxide with water vapor from the absorbing liquid that has absorbed the carbon dioxide,
the regeneration tower, a water vapor condenser configured to condense the water vapor having been emitted in the regeneration tower, and a carbon dioxide desublimator configured to desublimate (solidify) the carbon dioxide having been emitted in the regeneration tower are successively connected in series,
the water vapor condenser and the carbon dioxide desublimator are connected to a refrigerant circuit using a fluid having cold heat as a refrigerant, and the water vapor is condensed and the carbon dioxide is desublimated (solidified) by the refrigerant, and
the water vapor condenser and the carbon dioxide desublimator are depressurized to be under negative pressure when the water vapor is condensed and the carbon dioxide is desublimated (solidified), so that the water vapor and the carbon dioxide both having been emitted in the regeneration tower are sucked.

3. The carbon dioxide recovery device according to claim 2 , wherein the refrigerant circuit is connected as being communicated with the carbon dioxide desublimator, the water vapor condenser, and the absorption tower, and the refrigerant flows through the carbon dioxide desublimator, the water vapor condenser, and the absorption tower in this order.

4. The carbon dioxide recovery device according to claim 2 , wherein the regeneration tower is connected in parallel with at least two carbon dioxide recovery lines configured with the water vapor condenser and the carbon dioxide desublimator which are connected in series.

5. The carbon dioxide recovery device according to claim 2 , wherein the regeneration tower is connected with one water vapor condenser, and the water vapor condenser is connected in parallel with at least two carbon dioxide desublimators.

6. The carbon dioxide recovery device according to claim 2 , wherein a decompression valve is provided between the regeneration tower and the water vapor condenser.

7. The carbon dioxide recovery device according to claim 1 , wherein the separation device storing an adsorbent to adsorb carbon dioxide is configured to separate carbon dioxide from the to-be-separated gas in a manner that the adsorbent adsorbs carbon dioxide included in the to-be-separated gas that has been supplied to the separation device.

8. The carbon dioxide recovery device according to claim 7 , wherein
the separation device is configured to emit water vapor with the carbon dioxide,
the carbon dioxide recovery device includes a water vapor condenser to condense the water vapor,
the separation device, the water vapor condenser, and the carbon dioxide desublimator are connected in series in order from an upstream side of supplying the to-be-separated gas, and
the refrigerant circuit is connected to the water vapor condenser and the carbon dioxide, desublimator, and the water vapor is condensed and the carbon dioxide is desublimated (solidified) by the refrigerant.

9. The carbon dioxide recovery device according to claim 1 , wherein
the separation device is provided with a permeable membrane to selectively transmit carbon dioxide, and the permeable membrane is configured to transmit carbon dioxide included in the to-be-separated gas that has been supplied to the separation device to separate carbon dioxide from the to-be-separated gas, and
the carbon dioxide desublimator is connected on a transmission side of the permeable membrane of the separation device.

10. The carbon dioxide recovery device according to claim 9 , wherein
the separation device is configured to emit water vapor with the carbon dioxide,
the carbon dioxide recovery device includes a water vapor condenser to condense the water vapor,
the separation device ( 70 A, 70 B), the water vapor condenser, and the carbon dioxide desublimator are connected in series in order from an upstream side of supplying the to-be-separated gas, and
the refrigerant circuit is connected to the water vapor condenser and the carbon dioxide desublimator, and the water vapor is condensed and the carbon dioxide is desublimated (solidified) by the refrigerant.

11. The carbon dioxide recovery device according to claim 1 , wherein
the to-be-separated gas is combustion exhaust gas from an iron manufacturing plant or a cement plant, and
the carbon dioxide desublimator is cooled down by the refrigerant to minus 85 degrees centigrade or below.

12. The carbon dioxide recovery device according to claim 1 , wherein
the to-be-separated gas is combustion exhaust gas from a power plant, and
the carbon dioxide desublimator is cooled down by the refrigerant to minus 96 degrees centigrade or below.

13. The carbon dioxide recovery device according to claim 1 , wherein
the to-be-separated gas is the atmosphere, and
the carbon dioxide desublimator is cooled down by the refrigerant to minus 140 degrees centigrade or below.

14. The carbon dioxide recovery device according to claim 1 , wherein
the carbon dioxide desublimator is provided with a heating medium,
carbon dioxide is liquefied and recovered by heating inside the carbon dioxide desublimator to a temperature equal to or higher than a triple point of carbon dioxide by the heating medium, and
heating by the heating medium is to be stopped at a timing when a temperature of liquefied carbon dioxide is minus 56.6 degrees centigrade or more and minus 50 degrees centigrade or below or at a timing when a pressure inside the carbon dioxide desublimator becomes 518 kPa or more and 800 kPa or less.

15. The carbon dioxide recovery device according to claim 14 , wherein the carbon dioxide desublimator is configured to desublimate (solidify) carbon dioxide until a volume ratio of the desublimated (solidified) carbon dioxide to a volume of the carbon dioxide desublimator is in a range of 0.1 to 0.3 inclusive.

16. The carbon dioxide recovery device according to claim 14 , wherein the carbon dioxide desublimator is connected with a gas-liquid separator, and carbon dioxide is recovered from the carbon dioxide desublimator via the gas-liquid separator.

17. The carbon dioxide recovery device according to claim 14 , wherein the carbon dioxide desublimator is connected with a solid-liquid separator, and carbon dioxide is recovered from the carbon dioxide desublimator via the solid-

Assignees

• Toho Gas Kk
• National Univ Corporation Tokai National Higher Education And Research System

Inventors

• Umeda Yoshito
• Machida Hiroshi
• Norinaga Koyo
• Yamashita Hiroshi
• Yamaguchi Tsuyoshi

Classifications

• B01D2257/504

  Carbon dioxide · CPC title

• B01D53/78

  with gas-liquid contact · CPC title

• B01D53/22

  by diffusion (manufacturing semi-permeable membranes B01D67/00; form, structure or properties of semi-permeable membranes B01D69/00; material for semi-permeable membranes B01D71/00) · CPC title

• B01D53/18

  Absorbing units; Liquid distributors therefor (B01D3/16, B01D3/26, B01D3/30 take precedence; packing elements B01J19/30, B01J19/32) · CPC title

• B01D53/1475

  Removing carbon dioxide · CPC title