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 waste reformation system comprising:
a synthesis reactor for producing a first stream of synthesized gas;
a waste reforming conversion system for receiving at least organic waste and for producing a second stream of synthesized gas, the waste reforming conversion system including a rotatable outer wall including a helical spiral flight affixed to an interior of the outer wall and a non-rotatable reactor containing a steam reformer, the non-rotatable reactor located within the rotatable outer wall; and
a heat engine in fluid communication with the waste reforming conversion system, wherein gases from the heat engine are supplied to the waste reforming conversion system;
wherein the synthesis reactor is in fluid communication with the waste reforming conversion system such that a first portion of the first stream is mixed with the organic waste prior to the organic waste being received by the waste reforming conversion system; and
wherein the waste reforming conversion system is in fluid communication with the synthesis reactor such that the second stream is used for producing the first stream.
2. The waste reformation system of claim 1 , wherein the synthesis reactor is one of a Fischer-Tropsch reactor, a methanol synthesis reactor, and a methanation reactor.
3. The waste reformation system of claim 1 , wherein the waste reformation system further comprises a shift converter in fluid communication with the waste reforming conversion system.
4. The waste reformation system of claim 3 , further comprising a pressure swing adsorption (PSA) unit in fluid communication with the shift converter, the PSA unit for producing hydrogen fuel.
5. The waste reformation system of claim 2 , wherein the waste reformation system further comprises a shift converter in fluid communication with the waste reforming conversion system.
6. The waste reformation system of claim 5 , further comprising a pressure swing adsorption (PSA) unit in fluid communication with the shift converter, the PSA unit for producing hydrogen fuel.
7. The waste reformation system of claim 1 , wherein operation of the waste reforming conversion system does not include burning the waste or the first portion of the first stream.
8. The waste reformation system of claim 1 , wherein the synthesis reactor additionally produces a carbon-containing liquid or solid product.
9. The waste reformation system of claim 8 , wherein the organic waste includes carbon and wherein substantially all of the carbon in the organic waste is retained within the waste reformation system or sequestered in the carbon-containing liquid or solid product.
10. The waste reformation system of claim 1 , wherein the first stream of synthesized gas includes hydrogen and carbon monoxide.
11. The waste reformation system of claim 1 , wherein the waste reforming conversion system is configured to operate at a temperature from about one thousand five hundred degrees fahrenheit to about one thousand eight hundred degrees fahrenheit.
12. The waste reformation system of claim 1 , wherein the second stream includes hydrogen and carbon monoxide.
13. The waste reformation system of claim 12 , wherein the second stream has a ratio of hydrogen to carbon monoxide of about 0.7.
14. The waste reformation system of claim 12 ,
wherein the second stream has a ratio of hydrogen to carbon monoxide from about one and one half to about three and two tenths.
15. The waste reformation system of claim 1 ,
wherein the synthesis reactor is in fluid communication with the heat engine; and
wherein steam produced by operation of the synthesis reactor is supplied to the heat engine.
16. The waste reformation system of claim 1 , wherein the waste reforming conversion system further includes two opposing ends with a waste entrance and an exit for the second stream of synthesized gas at one end and and an exit for solid waste at the other end.
17. The waste reformation system of claim 1 , wherein the gases from the heat engine are supplied to the waste reforming conversion system to heat the waste reforming conversion system and are not in fluid communication with the first stream of synthesized gas.
18. The waste reformation system of claim 1 , wherein the non-rotatable reactor includes one or more vanes configured to direct gaseous flow within waste reforming conversion system toward a bottom of the waste reforming conversion system.
19. The waste reformation system of claim 1 , wherein the non-rotatable reactor includes a filter configured to hinder solids within the waste reforming conversion system from entering the steam reformer.
20. The waste reformation system of claim 1 , further comprising a hollow truss supporting the non-rotatable reactor and configured to convey steam and, optionally, carbon dioxide, into the steam reformer through the hollow truss.
21. The waste reformation system of claim 1 ,
wherein the steam former is electrically heated;
wherein the heat engine powers a generator; and
wherein the generator supplies electrical power to heat the steam reformer.
22. A waste reformation system comprising:
a synthesis reactor for producing a first stream of synthesized gas;
a waste reforming conversion system for receiving at least organic waste and for producing a second stream of synthesized gas, the waste reforming conversion system including
two opposing ends with a waste entrance and an exit for the second stream of synthesized gas at one end and a reactor containing a steam reformer and an exit for solid waste at the other end, and
a rotatable outer wall including a helical spiral flight affixed to an interior of the outer wall,
wherein the spiral flight and the rotatable outer wall combine to create an internal gas passage for flowing the second stream of synthesized gas from the reactor to the exit for the second stream of synthesized gas; and
a heat engine in fluid communication with the waste reforming conversion system, wherein gases from the heat engine are supplied to the waste reforming conversion system;
wherein the synthesis reactor is in fluid communication with the waste reforming conversion system such that a first portion of the first stream is mixed with the organic waste prior to the organic waste being received by the waste reforming conversion system; and
wherein the waste reforming conversion system is in fluid communication with the synthesis reactor such that the second stream is used for producing the first stream.