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    • 3. 发明专利
    • Integrated microchannel synthesis and separation
    • AU2011213887B2
    • 2015-04-30
    • AU2011213887
    • 2011-08-25
    • VELOCYS INC
    • LITT ROBERT DTONKOVICH ANNA LEE Y
    • B01J8/00C01B31/00C07C27/06
    • A process for carrying out at least two unit operations in series, the process comprising the step of: (a) inputting a feed stream comprising carbon containing molecules and hydrogen containing molecules to a 5 microchannel reactor, the microchannel reactor including a corrugated insert at least partially defining a series of microchannels having an aspect ratio greater than 1.5 and housing a catalyst therein; (b) reacting a portion of the carbon containing molecules with the hydrogen containing molecules within the microchannel reactor to form hydrocarbon molecules 10 flowing in a process stream; (c) removing thermal energy from the microchannel reactor using a first set of cooling microchannels in thermal communication with the microchannel reactor; and, (d) removing at least a portion of the hydrocarbon molecules from the microchannel reactor. REFORMING SECTION 100 ME0H SECTION 14.0 NATRALGASPROUCT COMPRESSOR CO, CH4, H2 + STEAM FROM 300 C 50 ATM ME0H SECTION 50I ME0H EXHAUST -A - SYNTHESIS 117 ~2 ATMND SECTION PHASE SE WTE 13- 2 - - STEAM TO 1i30 SMR FEED WATER CAPTURE SECTION L 3 IC , F/UELFROOMSN COMPRESO CO CH4, H WATER GARSROUT DISTILLATION
    • 5. 发明专利
    • Integrated microchannel synthesis and separation
    • AU2015207908A1
    • 2015-08-20
    • AU2015207908
    • 2015-07-30
    • VELOCYS INC
    • LITT ROBERT DTONKOVICH ANNA LEE Y
    • B01J8/00C01B31/00C07C27/06
    • The present invention relates to a method of carrying out a reaction and concurrent heat exchange within a microchannel unit, comprising: (a) inputting a feed stream of reactants to a microchannel reactor, the microchannel reactor including a waveform sandwiched between opposing process channel shim sheets at least partially defining a series of microchannels having an aspect ratio greater than 1.5 and at least partially housing a particulate catalyst therein, where greater than thirty percent of the available volume of the series of microchannels is occupied by the particulate catalyst; (b) reacting at least a portion of reactants within the microchannel reactor to form product molecules, where the reaction is at least one of methanol synthesis, Fischer-Tropsch, hydrogenation, hydroracking, oligermization, polymerization, alkylation, sulfonation, nitration, ammonia synthesis, oxidation, and hydrogen peroxide synthesis by direct combination; (c) removing thermal energy from the microchannel reactor using a first set of cooling microchannels in thermal communication with the microchannel reactor; and (d) removing at least a portion of the product molecules from the microchannel reactor.
    • 8. 发明专利
    • Integrated microchannel synthesis and separation
    • AU2015207908B2
    • 2017-03-09
    • AU2015207908
    • 2015-07-30
    • VELOCYS INC
    • LITT ROBERT DTONKOVICH ANNA LEE Y
    • B01J8/00C07C27/06
    • The present invention relates to a method of carrying out a reaction and concurrent heat exchange within a microchannel unit, comprising: (a) inputting a feed stream of reactants to a microchannel reactor, the microchannel reactor including a waveform sandwiched between opposing process channel shim sheets at least partially defining a series of microchannels having an aspect ratio greater than 1.5 and at least partially housing a particulate catalyst therein, where greater than thirty percent of the available volume of the series of microchannels is occupied by the particulate catalyst; (b) reacting at least a portion of reactants within the microchannel reactor to form product molecules, where the reaction is at least one of methanol synthesis, Fischer-Tropsch, hydrogenation, hydroracking, oligermization, polymerization, alkylation, sulfonation, nitration, ammonia synthesis, oxidation, and hydrogen peroxide synthesis by direct combination; (c) removing thermal energy from the microchannel reactor using a first set of cooling microchannels in thermal communication with the microchannel reactor; and (d) removing at least a portion of the product molecules from the microchannel reactor.