The present invention relates to a process for preparing and
processing of synthesis gas, the process particularly comprising the steps of preparing a first gas
stream comprises H2 and CO2; feeding said gas
stream into a first reactor comprising a reverse
water gas shift catalyst, wherein said gas
stream is fed into the first reactor at a gas hourly
space velocity (GHSV) in the range of from 1,000 to 100,000 h-1, wherein the reverse
water gas shift reaction is conducted at a temperature in the range of from 650 to 1,000 °C, wherein in a time interval Δt, wherein Δt is in the range of from 1 to 60 minutes, the GHSV of said gas stream displays a gradient in the range of from 2,000 to 60,000 h-1, obtaining a second gas stream; feeding the second gas stream into a second reactor, wherein the second reactor comprises one or more of a
methanol synthesis catalyst, a
dimethyl ether synthesis catalyst, an oxo synthesis or
hydroformylation catalyst, a Fischer-Tropsch synthesis catalyst, a
formic acid synthesis catalyst, and a
phosgene synthesis catalyst, obtaining a product stream.