Patent ID: 9206091
Filing Date: 2015-12-08
Classification: B01J,C07C,C10G,F28D,F28F

Abstract:
1. A process for synthesis gas conversion comprising: contacting a synthesis gas feed comprising hydrogen and carbon monoxide having a H in a compact heat exchange reactor comprising a set of reaction passages disposed between a synthesis gas feed header and a products header; and a set of coolant passages disposed between a coolant inlet header and a coolant outlet header; wherein the set of coolant passages conducts a coolant therethrough; and wherein the set of reaction passages conducts synthesis gas and reaction products therethrough and contains the hybrid catalyst therein; at a temperature from 200° C. to 280° C., a pressure from 5 to 40 atmospheres, a recycle ratio from 1 to 3, and a gaseous hourly space velocity less than 20,000 volumes of gas per volume of catalyst per hour; to produce an effluent including a hydrocarbon product containing at least 50 wt % C