Production of renewable fuels and energy by steam/CO2 reforming of wastes
This invention relates to a power recovery process in waste steam/CO 2 reformers in which a waste stream can be made to release energy without having to burn the waste or the syngas. This invention in some embodiments does not make use of fuel cells as a component but makes use of exothermic chemical reactors using syngas to produce heat, such as Fischer-Tropsch synthesis. It also relates to control or elimination of the emissions of greenhouse gases in the power recovery process of this invention with the goal of producing energy in the future carbonless world economy.
1. A method of reforming of organic waste material, comprising:
producing a first stream of synthesized hydrocarbon gas;
providing to a waste reforming conversion system a supply of organic waste;
mixing the organic waste with a first portion of the first stream;
reforming the mixture of the first stream and the waste with steam and carbon dioxide and producing a second stream of synthesized hydrocarbon gas and heat; and
using a second portion from the second stream for said producing a first stream.
2. The method of claim 1 wherein said reforming does not include burning the waste or the portion of the first stream.
3. The method of claim 1 wherein said reforming is without the use of a catalyst.
4. The method of claim 1 which further comprises using the heat from said reforming to drive a heat engine and generator to produce electricity.
5. The method of claim 1 wherein said producing a first stream is with a hydrocarbon synthesis reactor.
6. The method of claim 5 wherein the hydrocarbon synthesis reactor further produces a carbon-containing liquid or solid product.
7. The method of claim 6 wherein the carbon-containing liquid or solid product is paraffin.
8. The method of claim 6 wherein the organic waste includes carbon and wherein substantially all of the carbon in the organic waste is sequestered in the carbon-containing liquid or solid product.
9. The method of claim 1 wherein said reforming is at a temperature not greater than one thousand eight hundred degrees F.
10. The method of claim 1 wherein said using a second portion includes cooling the second portion prior to said producing a first stream.
11. The method of claim 1 wherein said using a second portion includes pressurizing the second portion prior to said producing a first stream.
12. The method of claim 1 wherein the first stream of synthesized hydrocarbon gas includes hydrogen and carbon monoxide, and wherein mixing the organic waste with a first portion of the first stream comprises mixing the organic waste with the hydrogen and carbon monoxide from the first stream.
13. The method of claim 1 wherein the first stream of synthesized hydrocarbon gas includes hydrogen and carbon monoxide, and which further comprises controlling said producing the first stream to maintain a ratio of hydrogen to carbon monoxide from about one and one half to about three and two tenths.
14. The method of claim 1 wherein the first stream of synthesized hydrocarbon gas includes hydrogen and carbon monoxide, and which further comprises controlling said producing the first stream to maintain a ratio of hydrogen to carbon monoxide of about 0.7.
15. The method of claim 14 wherein the ratio of hydrogen to carbon monoxide is about 0.73.