초록 ▼

A process for converting natural gas to liquid hydrocarbons comprising heating the gas through a selected range of temperature for sufficient time and/or combustion of the gas at a sufficient temperature and under suitable conditions for a reaction time sufficient to convert a portion of the gas str

A process for converting natural gas to liquid hydrocarbons comprising heating the gas through a selected range of temperature for sufficient time and/or combustion of the gas at a sufficient temperature and under suitable conditions for a reaction time sufficient to convert a portion of the gas stream to reactive hydrocarbon products, primarily ethylene or acetylene. The gas containing acetylene may be separated such that acetylene is converted to ethylene. The ethylene product(s) may be reacted in the presence of an acidic catalyst to produce a liquid, a portion of which will be predominantly naphtha or gasoline. A portion of the incoming natural gas or hydrogen produced in the process may be used to heat the remainder of the natural gas to the selected range of temperature. Reactive gas components are used in a catalytic liquefaction step and/or for alternate chemical processing.

대표청구항 ▼

What is claimed is: 1. A method for converting at least a portion of the natural gas to reactive hydrocarbon products, by: heating a first portion of the natural gas in a conversion reactor by incomplete combustion of a second portion of the natural gas, the conversion reactor comprising a reaction

What is claimed is: 1. A method for converting at least a portion of the natural gas to reactive hydrocarbon products, by: heating a first portion of the natural gas in a conversion reactor by incomplete combustion of a second portion of the natural gas, the conversion reactor comprising a reaction section operated at conversion promoting conditions, such that the reactive hydrocarbon products, comprising acetylene, and reactive gas products comprising hydrogen, carbon monoxide, and carbon dioxide, are produced, separating a portion of the reactive gas products comprising hydrogen, carbon monoxide, and carbon dioxide for introduction into the conversion reactor by quenching the reactive hydrocarbon products to produce a quenched reactive hydrocarbon products, wherein the separated portion of reactive gas products comprising hydrogen, carbon monoxide, and carbon dioxide control the incomplete combustion temperature of the second portion of the natural gas, converting at least a portion of the quenched reactive hydrocarbon products to hydrocarbon liquids by reacting a liquefaction feed comprising at least a portion of the quenched reactive hydrocarbon products in a catalytic liquefaction reactor operated at liquefaction promoting conditions, such that the hydrocarbon liquids, comprising naphtha, are produced. 2. The method of claim 1, wherein the conversion reactor is a non-catalytic reactor. 3. The method of claim 1, wherein the conversion reactor is configured to be a mixed-stream reactor. 4. The method of claim 1, wherein the reactive hydrocarbon products further comprise ethylene.