The patent badge is an abbreviated version of the USPTO patent document. The patent badge does contain a link to the full patent document.

The patent badge is an abbreviated version of the USPTO patent document. The patent badge covers the following: Patent number, Date patent was issued, Date patent was filed, Title of the patent, Applicant, Inventor, Assignee, Attorney firm, Primary examiner, Assistant examiner, CPCs, and Abstract. The patent badge does contain a link to the full patent document (in Adobe Acrobat format, aka pdf). To download or print any patent click here.

Date of Patent:
Oct. 27, 2015

Filed:

Jan. 15, 2014
Applicant:

Primus Green Energy Inc., Hillsborough, NJ (US);

Inventors:

Howard L. Fang, Bridgewater, NJ (US);

Moshe Ben-Reuven, Princeton, NJ (US);

Richard E. Boyle, Philadelphia, PA (US);

Robert M. Koros, Westfield, NJ (US);

Assignee:

Primus Green Energy Inc., Hillsborough, NJ (US);

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C07C 1/04 (2006.01); B01J 8/04 (2006.01); C10G 3/00 (2006.01); C10G 45/58 (2006.01);
U.S. Cl.
CPC ...
C07C 1/041 (2013.01); B01J 8/0449 (2013.01); C10G 3/42 (2013.01); C10G 3/49 (2013.01); C10G 45/58 (2013.01); B01J 2219/0004 (2013.01); C10G 2300/1022 (2013.01); C10G 2300/304 (2013.01); C10G 2300/4025 (2013.01); C10G 2300/4081 (2013.01); C10G 2400/02 (2013.01); C10G 2400/04 (2013.01); C10G 2400/08 (2013.01); C10G 2400/30 (2013.01);
Abstract

Synthetic fuels are produced from synthesis gas in a four-stage reactor system with a single recycle loop providing the requisite thermal capacity to moderate the high heat release of the reactions and to provide the reactants and reaction environments for the efficient operation of the process. The first reactor converts a portion of the synthesis gas to methanol; the second reactor converts the methanol to dimethylether; the third reactor converts the methanol and dimethylether to fuel; and the fourth reactor converts the high melting point component, durene, and other low volatility aromatic components such as tri- and tetra-methylbenzenes to high octane branched paraffins. A large part of the gas stream of the fourth reactor is recycled to the inlet of the first stage and mixed with the fresh synthesis gas stream. Alternatively, the fresh synthetic gas stream is mixed with the product of the second stage.


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