Method and system for producing a synthesis gas using an oxygen transport membrane based reforming system with secondary reforming and auxiliary heat source
US-9212113-B2 · Dec 15, 2015 · US
US9611438B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9611438-B2 |
| Application number | US-201314428461-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 4, 2013 |
| Priority date | Sep 21, 2012 |
| Publication date | Apr 4, 2017 |
| Grant date | Apr 4, 2017 |
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A steam reformer generates reformed gas by a steam-reforming reaction of hydrocarbon gas such as natural gas. A methanol synthesis column and a gasoline synthesis column synthesize gasoline from the reformed gas via methanol and produce a liquid fuel. A superheater superheats a part of low-pressure steam that has been heat-recovered from the reformed gas with a part of middle-pressure steam that has been heat-recovered by the methanol synthesis column or the gasoline synthesis column, and the steam thereby brought into an unsaturated state is supplied to a low-pressure steam turbine.
Opening claim text (preview).
The invention claimed is: 1. A system for producing a liquid fuel from hydrocarbon gas and for generating power, the system comprising: a steam-reforming device configured to generate reformed gas by performing a steam-reforming reaction with hydrocarbon gas; a synthesis column configured to synthesize gasoline, dimethyl ether, or a diesel fuel from the reformed gas via methanol; a heat exchanging device configured to obtain saturated steam with a temperature of 180° C. or lower by performing heat exchange with the reformed gas before the reformed gas is used by the synthesis column; a superheating device configured to superheat the saturated steam by using a heat source with a temperature of 200° C. or higher generated within the system and obtain superheated steam; and a power generation device configured to generate power by using the superheated steam, wherein the superheating device uses steam generated by an exothermic reaction run in the synthesis column as a heat source. 2. The system according to claim 1 , wherein a part of the reformed gas obtained by the steam-reforming device is used as the heat source for the superheating device. 3. The system according to claim 1 , wherein flue gas generated by from a burning portion of the steam-reforming device is used as the heat source for the superheating device.
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