Fluidized bed water gas shift catalyst
The present invention relates to an aqueous gas-converting catalyst composition comprising: an active component; a support; an inorganic binder; at least one accelerator selected from the group consisting of cobalt oxide, molybdenum oxide, nickel oxide, calcium oxide, barium oxide, strontium oxide, magnesium oxide, zirconium oxide, manganese oxide and barium titania; and at least one stabilizer selected from the group consisting of magnesium oxide, zirconium oxide, stabilized zirconia, and hydrotalcite. The catalyst according to the present invention can effectively capture and separate carbon dioxide due to the excellent physical properties thereof such as packing density and abrasion resistance, and high CO conversion. Also, according to the present invention, mass production is facilitated by applying a spraying technique, and overall costs are lowered because of high yield. Thus, the present invention can be applied as a low cost pre-combustion CO2 capturing technique to an integrated gasification combined cycle, fuel cells, coal liquefaction, compound production, and the like.
1. A water gas shift reaction catalyst composition comprising:
an active component including copper oxide (CuO) and cerium oxide (CeO 2 ), and including at least one selected from the group consisting of cobalt oxide, nickel oxide, molybdenum oxide and barium titania;
at least one support selected from the group consisting of alumina having a specific surface area of 150 m 2 /g to 250 m 2 /g, and hydrotalcite comprising 30 parts by weight to 60 parts by weight of magnesium hydroxide;
at least one inorganic binder selected from the group consisting of bentonite, kaolin, an alumina sol, a silica sol, and boehmite; and
a stabilizer formed of hydrotalcite comprising 30 parts by weight to 60 parts by weight of magnesium hydroxide.
2. The water gas shift reaction catalyst composition of claim 1 , wherein the active component is included in a range of 10 parts by weight to 90 parts by weight based on 100 parts by weight of the water gas shift reaction catalyst composition.
3. The water gas shift reaction catalyst composition of claim 1 , wherein the support is included in a range of 3 parts by weight to 70 parts by weight based on 100 parts by weight of the water gas shift reaction catalyst composition.
4. The water gas shift reaction catalyst composition of claim 1 , wherein the inorganic binder is included in a range of 3 parts by weight to 70 parts by weight based on 100 parts by weight of the water gas shift reaction catalyst composition.
5. The water gas shift reaction catalyst composition of claim 1 , wherein a promoter and the stabilizer are included in a range of 3 parts by weight to 70 parts by weight based on 100 parts by weight of the water gas shift reaction catalyst composition.
6. A slurry composition comprising: 25 parts by weight to 50 parts by weight of the water gas shift reaction catalyst composition of claim 1 ; and a solvent.
7. The slurry composition of claim 6 , further comprising at least one organic additive selected from the group consisting of a dispersant, a defoamer, and an organic binder.
8. The slurry composition of claim 7 , wherein the dispersant comprises at least one selected from the group consisting of anionic dispersants, cationic dispersants, amphoteric dispersants, and nonionic dispersants.
9. The slurry composition of claim 7 , wherein the defoamer comprises a metallic soap-based or polyester-based nonionic surfactant.
10. The slurry composition of claim 7 , wherein the organic binder comprises at least one selected from the group consisting of polyvinyl alcohols, polyglycols, and methylcellulose.
11. A method of preparing a water gas shift reaction catalyst, the method comprising:
(A) forming solid particles by spraying and drying the slurry composition of claim 6 ; and
(B) drying and firing the solid particles.
12. The method of claim 11 , wherein the slurry composition is prepared by:
preparing a mixture of a solvent and a solid raw material;
adding an organic additive to the mixture, the additive comprising at least one selected from the group consisting of dispersants, defoamers, and organic binders; and
agitating and pulverizing the mixture.
13. The method of claim 12 , wherein after the agitating and pulverizing of the mixture, the mixture has an average particle diameter of 0.01 gm to 3 pm.
14. The method of claim 12 , further comprising removing foreign substances from the slurry composition after the agitating and pulverizing.
15. The method of claim, 11 , wherein the drying of the solid particles of (B) is performed in an air atmosphere at a temperature of 110° C. to 150° C.
16. The method of claim 11 , wherein the firing of the solid particles of (B) is performed at a temperature of 350° C. to 1000° C. in an atmosphere of air, nitrogen, helium, hydrogen, steam, or a reducing gas.
17. The water gas shift reaction catalyst comprising the water gas shift reaction catalyst composition of claim 1 , wherein the water gas shift reaction catalyst has an average particle size of 60 μm to 180 pm, a particle size distribution of 30 gm to 330 pm, a filling density of 0.5 g/cc to 2.0 g/cc, a wear resistance of 70% or less, and a CO conversion ratio of 60% or higher.
18. The water gas shift reaction catalyst composition of claim 1 , wherein the active component is included in a range of 10 parts by weight to 70 parts by weight based on 100 parts by weight of the water gas shift reaction catalyst composition.
19. The water gas shift reaction catalyst composition of claim 1 , wherein the at least one support is included in a range of 5 parts by weight to 60 parts by weight based on 100 parts by weight of the water gas shift reaction catalyst composition.