초록 ▼

Synthesis gas for a Fischer-Tropsch process is obtained by primary steam reforming a hydrocarbon feedstock in tubes in a heat exchange reformer, subjecting the primary reformed gas to secondary reforming and using the hot secondary reformed gas to heat the tubes in the heat exchange reformer. The r

Synthesis gas for a Fischer-Tropsch process is obtained by primary steam reforming a hydrocarbon feedstock in tubes in a heat exchange reformer, subjecting the primary reformed gas to secondary reforming and using the hot secondary reformed gas to heat the tubes in the heat exchange reformer. The resultant reformed gas is cooled, de-watered and used to form hydrocarbons in the Fischer-Tropsch process. At least part of the tail gas from the Fischer-Tropsch process is combusted in a gas turbine to provide power for the reforming process.

대표청구항 ▼

The invention claimed is: 1. A process for the production of hydrocarbons by the Fischer-Tropsch reaction comprising a. subjecting a mixture of a gaseous desulphurised hydrocarbon feedstock and steam to steam reforming by: i. passing the mixture over a catalyst disposed in heated tubes in a heat ex

The invention claimed is: 1. A process for the production of hydrocarbons by the Fischer-Tropsch reaction comprising a. subjecting a mixture of a gaseous desulphurised hydrocarbon feedstock and steam to steam reforming by: i. passing the mixture over a catalyst disposed in heated tubes in a heat exchange reformer, ii. subjecting the resultant primary reformed gas to secondary reforming by partially combusting the primary reformed gas with oxygen provided by an oxygen-rich gas comprising >90% oxygen and bringing the resultant partially combusted gas towards equilibrium over a secondary reforming catalyst, and iii. using the resultant secondary reformed gas to heat the tubes of the heat exchange reformer, thereby producing a partially cooled reformed gas, b. further cooling the partially cooled reformed gas to below the dew point of the steam therein to condense water and separating condensed water to give a de-watered synthesis gas, c. passing said de-watered synthesis gas through a hydrocarbon synthesis reaction to form a reaction products stream, d. separating at least a part of said reaction products stream into a hydrocarbons product stream and a tail gas stream, e. combusting at least a part of said tail gas to produce a combustion gas, and f. using said combustion gas to drive a turbine, thereby to produce power from said turbine. 2. A process as claimed in claim 1, wherein said oxygen rich gas is provided by an air separation unit and wherein nitrogen generated by said air separation unit is fed to said turbine. 3. A process as claimed in claim 1, wherein said turbine is a part of an integrated gas turbine apparatus comprising an air compressor for supplying compressed air for use in said gas turbine apparatus, a combustion chamber and said turbine. 4. A process as claimed in claim 3, wherein a portion of the compressed air is supplied to an air separation unit. 5. A process as claimed in claim 1 wherein the exhaust gases from the gas turbine are passed through a heat exchanger to recover heat for use in the process.