Syngas conversion and catalyst system employed therefor
AssigneeConocoPhillips Company
InventorsAn-hsiang Wu, Jianhua Yao, Charles A. Drake
Life of this patent
Estimating the term…
Loading patent…
AssigneeConocoPhillips Company
InventorsAn-hsiang Wu, Jianhua Yao, Charles A. Drake
Estimating the term…
A process for the conversion of syngas by contact of syngas under conversion conditions with catalyst having as components zinc oxide, copper oxide, aluminum oxide, Y zeolite and clay in which (A) in a one step process for conversion of syngas to dimethyl ether, the catalyst has as components an extruded mixture of zinc oxide, copper oxide, gamma aluminum oxide, Y zeolite and clay; (B) in a two step process for conversion of syngas to light olefins, a catalyst system is employed that has in the first step a catalyst mixture of zinc oxide, copper oxide, aluminum oxide, Y zeolite and clay and the catalyst employed in the second step is SAPO-34; SAPO-34 modified with lanthanum(III) nitrate hexahydrate; SAPO-34 modified with magnesium nitrate hexahydrate; SAPO-34 modified with tributyl borate or SAPO-34 modified with triethyl phosphate or (C) in a two step process for conversion of syngas to light olefins, the pressure on the effluent from the contact of syngas with a mixture of zinc oxide, copper oxide, aluminum oxide, Y zeolite and clay is reduced before contact with a second catalyst of SAPO-34. The catalyst systems employed in the processes herein.
A catalyst suitable for the conversion of syngas comprising zinc oxide, copper oxide, aluminum oxide, Y zeolite and clay.
A catalyst suitable for the conversion of syngas to light olefins comprising (A) a first catalyst bed comprising zinc oxide, copper oxide, aluminum oxide, Y zeolite and clay arranged to emit effluent into (B) a second catalyst bed comprising a SAPO.
Dependencies are inferred from the claim text.