Method for producing long-chain hydrocarbons from natural gas
View Patent ↗Natural gas is reacted with steam for generating carbon monoxide and hydrogen in a first catalytic reactor. The resulting gas mixture is used to perform Fischer-Tropsch synthesis in a second catalytic reactor. After performing Fischer-Tropsch synthesis, the remaining hydrogen is separated from a hydrocarbon-rich stream using a hydrogen-permeable membrane, and the hydrocarbon-rich stream is returned to be subjected to steam reforming. Preferable, the hydrogen-rich stream is supplied to a combustion channel for providing heat for the endothermic steam-reforming reaction. The overall process converts natural gas to longer-chain hydrocarbons and can provide a carbon conversion of more than 80%.
1. A process for generating longer-chain hydrocarbons from natural gas, said process including the steps of:
subjecting natural gas to steam reforming for generating a mixture of carbon monoxide and hydrogen,
subjecting said mixture to Fischer-Tropsch synthesis for producing a resultant mixture,
using a non-refrigerated coolant for cooling and separating said resultant mixture into a liquid phase comprised of longer-chain hydrocarbons and a gas phase,
using a hydrogen-permeable membrane for separating said gas phase into a hydrogen-rich stream and a hydrocarbon-rich stream, and
combining said hydrocarbon-rich stream with natural gas and steam for subjecting to catalytic methanation in a prereformer prior to steam reforming.
2. A process as defined in claim 1 including the step of supplying said hydrogen-rich stream to a combustion channel for providing heat to said steam reforming reaction.
3. A process as defined in claim 1 including the step of maintaining said prereformer at a temperature of about 400° C.
4. A process as defined in claim 1 including the step of using a platinum/rhodium catalyst during said step of steam reforming.
5. A process as claimed in claim 1 wherein said non-refrigerated coolant is water at about 20° C. (68° F.).