IP Library Patent Application 10898491
Patent Application
App. No. 10/898,491

Method for reducing exhaust carbon dioxide

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Quick Facts
Patent No.
US None
App. No.
10/898,491
Abstract

A method for effectively absorbing and removing CO 2 in an exhaust gas generated during an industrial process for reducing the amount of CO 2 that is exhausted into the atmosphere. The exhaust gas containing CO 2 is blown into an agglomerate of solid particles containing CaO and/or Ca(OH) 2 so that the CO 2 is in contact with the agglomerate for fixing the CO 2 in the exhaust gas as CaCO 3 , thereby reducing the CO 2 concentration in the exhaust gas. Preferably, the solid particles contain water, and more preferably, the solid particles contain surface adhesive water.

Claims (24)

1 . A method for reducing an exhaust carbon dioxide comprising:

preparing agglomerates of solid particles containing at least one compound selected from the group consisting of CaO and Ca(OH) 2 ;

contacting an exhaust gas containing CO 2 with the agglomerates of the solid particles in a reaction chamber, the solid particles having a film of adhesive water on a surface of the solid particles; and

fixing CO 2 in the exhaust gas as CaCO 3 in the solid particles to reduce CO 2 in the exhaust gas.

2 . The method according to claim 1 , wherein the agglomerates of the solid particles are obtained by pulverizing materials containing CaO and/or Ca(OH) 2 into grain and/or rough grain.

3 . The method according to claim 1 , wherein the step of contacting the exhaust gas comprises contacting an exhaust gas containing CO 2 with the agglomerates of the solid particles by blowing the exhaust gas into the agglomerates of the solid particles.

4 . The method according to claim 3 , wherein the exhaust gas containing CO 2 is blown into the agglomerates of the solid particles from one direction.

5 . The method according to claim 1 , wherein the water content in the agglomerates of the solid particles is from 3 wt. % to 20 wt. %.

6 . The method according to claim 1 , wherein a grain size of the solid particles is substantially 5 mm or less.

7 . The method according to claim 1 , wherein the exhaust gas introduced into the reaction chamber is at a temperature corresponding to the boiling point of water or lower, within the reaction chamber.

8 . The method according to claim 1 , wherein the reaction chamber is at a temperature corresponding to the boiling point of water or lower.

9 . The method according to claim 1 , wherein a temperature of the agglomerates of the solid particles is at a temperature corresponding to the boiling point of water or lower, within the reaction chamber.

10 . The method according to claim 1 , wherein the step of contacting the exhaust gas containing CO 2 with the agglomerates of the solid particles comprises contacting a pressurized exhaust gas with the agglomerates of the solid particles.

11 . The method according to claim 1 , further comprising saturating H 2 O in the exhaust gas, prior to contacting the exhaust gas with the agglomerates of the solid particles.

12 . The method according to claim 1 , wherein the water content in the agglomerates of the solid particles is a range of from 3 to 20 wt. %, and the exhaust gas is blown into the agglomerates of the solid particles, to contact the exhaust gas with the agglomerates of the solid particles.

13 . The method according to claim 12 , wherein the exhaust gas introduced into the reaction chamber is at a temperature corresponding to the boiling point of water or lower, within the reaction chamber, the reaction chamber is at a temperature corresponding to the boiling point of water or lower, and the agglomerates of the solid particles to be contacted with the exhaust gas is at a temperature corresponding to the boiling point of water or lower, within the reaction chamber.

14 . The method according to claim 13 , further comprising saturating H 2 O in the exhaust gas prior to contacting the exhaust gas with the agglomerates of the solid particles.

15 . The method according to claim 1 , wherein the agglomerates of the solid particles are at least one material selected from the group consisting of a slag generated in an iron and steel making process and a concrete.

16 . The method according to claim 1 , wherein the solid particles of the agglomerates are at least one material selected from the group consisting of a slag generated in an iron and steel making process and a concrete.

17 . The method according to claim 1 , wherein the agglomerates of the solid particles are at least one material selected from the group consisting of a slag generated in an iron-steel making process, a concrete, a mortar, a glass, an alumna cement and a CaO containing refractory.

18 . A method of creating a seaweed bed comprising:

temporarily immersing a heavy material in an existing seaweed bed so that marine algae adhere and grow on a surface of the material;

recovering the heavy material and transporting the heavy material as a seed material in a place for creating the seaweed bed; and

arranging an adhering material for adhering the marine algae around the seed material so that the marine algae on the seed material is proliferated onto another seed material.

Assignments (3)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 24, 2004
From: JFE ENGINEERING CORPORATION
To: JFE STEEL CORPORATION
Reel/Frame 015408/0129 →
CHANGE OF NAME Recorded Nov 23, 2004
From: NKK CORPORATION
To: JFE ENGINEERING CORPORATION
Reel/Frame 015402/0850 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 19, 2004
From: TAKAHASHI, TATSUHITO; ISOO, TSUNEO; KATO, MAKOTO; TANABE, HARUYOSHI
To: NKK CORPORATION
Reel/Frame 015392/0489 →