Method for recovering hydrocarbon compounds and a hydrocarbon recovery apparatus from a gaseous by-product
There is provided a method for recovering hydrocarbon compounds from a gaseous by-products generated in the Fisher-Tropsch synthesis reaction, the method comprising a pressurizing step in which the gaseous by-products are pressurized, a cooling step in which the pressurized gaseous by-products are pressurized to liquefy hydrocarbon compounds in the gaseous by-products, and a separating step in which the hydrocarbon compounds liquefied in the cooling step are separated from the remaining gaseous by-products.
1. A method for recovering hydrocarbon compounds from gaseous by-products generated in the Fisher-Tropsch synthesis reaction, the method comprising:
a discharging step in which the gaseous by-products are discharged from an FT synthesis reactor;
a heat exchanging step in which the gaseous by-products discharged from the FT synthesis reactor are cooled by exchanging heat with a recycled gaseous by-products;
a pressurizing step in which the gaseous by-products cooled in the heat exchanging step are pressurized;
a cooling step in which the pressurized gaseous by-products are cooled down to liquefy hydrocarbon compounds in the gaseous by-products;
a separating step in which the hydrocarbon compounds liquefied in the cooling step are separated from the remaining gaseous by-products; and
a recycling step in which at least a portion of the remaining gaseous by-products are recycled to the FT synthesis reactor as a feedstock gas for the Fisher-Tropsch synthesis reaction, wherein the portion of the remaining gaseous by-products recycled to the FT synthesis reactor also serves as the recycled gaseous by-products in the heat exchanging step for cooling the gaseous by-products discharged from the FT synthesis reactor.
2. The method for recovering hydrocarbon compounds according to claim 1 , wherein the recycling step comprises a pressure adjusting step in which the pressure of the portion of the remaining gaseous by-products is adjusted to the pressure in a feedstock gas inlet port of the FT synthesis reactor.