| CPC C10G 2/31 (2013.01) [C10J 3/005 (2013.01); C10J 3/80 (2013.01); C10J 3/84 (2013.01); C10K 1/004 (2013.01); C10K 1/005 (2013.01); C10K 1/007 (2013.01); C10K 1/022 (2013.01); C10K 1/024 (2013.01); C10K 3/006 (2013.01); C01B 2203/0222 (2013.01); C01B 2203/0283 (2013.01); C01B 2203/061 (2013.01); C01B 2203/062 (2013.01); C01B 2203/1619 (2013.01); C07C 29/1518 (2013.01); C10J 2200/09 (2013.01); C10J 2300/0916 (2013.01); C10J 2300/0989 (2013.01); C10J 2300/1659 (2013.01); C10J 2300/1671 (2013.01); C10J 2300/1675 (2013.01); C10J 2300/1807 (2013.01); C10J 2300/1815 (2013.01); C10J 2300/1884 (2013.01); C10J 2300/1892 (2013.01)] | 22 Claims |

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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.
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