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filingDate 2011-11-09-04:00^^<http://www.w3.org/2001/XMLSchema#date>
grantDate 2015-11-25-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationDate 2015-11-25-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber CN-103270139-B
titleOfInvention Single loop multistage fuel production
abstract In the four stage reactor assemblies with single loop loop, produce synthol by synthetic gas, described in there is single loop loop four stage reactor assemblies provide necessary thermal capacity to regulate the high Thermal release that reacts and to provide reactant and reaction environment for the Effec-tive Function of method.A part of Synthetic holography is methyl alcohol by the first stage, methanol conversion is dme by subordinate phase, methyl alcohol and dimethyl ether conversion are fuel by the phase III, and high melting point component durene and other low volatility aromatic component (such as Three methyl Benzene and tetramethyl-benzene) are converted into the paraffinic hydrocarbons of higher octane branching by fourth stage.Four-stage catalyst for hydrotreatment has tolerance to CO is poisoning.This reaction produces water as by product, and it is carried into high-pressure separator after fourth stage.Stream from separator is liquid fuel flow, current and comprise the air-flow of light hydrocarbon gas and unreacted synthetic gas.The major part of this air-flow is recycled to the entrance of first stage and mixes with fresh synthesis gas stream.Or fresh synthesis gas stream mixes with the product of subordinate phase.Smaller portions from the air-flow of separator be sent to hydrocarbon reclaim and fuel gas for providing the preheating of multiple stream.Liquid fuel is sent to fuel Products (such as, gasoline, rocket engine fuel or diesel oil) blended, and current such as can be delivered to synthetic gas produce equipment be used for stream produce.
priorityDate 2010-11-09-04:00^^<http://www.w3.org/2001/XMLSchema#date>
type http://data.epo.org/linked-data/def/patent/Publication

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