Hydrocarbon synthesis
a technology of hydrocarbons and oligomerization, applied in the direction of hydrocarbon preparation catalysts, hydrocarbon oil treatment products, bulk chemical production, etc., can solve the problems of slow kinetics, no reactive neutralization, and the need to recycle the hydrohalic acid stream
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example 1
[0035] Metal Oxide / Zeolite composite MZ1 was prepared as follows: A solid mixture of a ZSM-5-type zeolite (Zeolyst CBV 8014, Si / Al ratio=80:1, 10 g, 170 mmoles SiO2) and CaNO3 nonahydrate (9 g,=34 mmoles Ca) was prepared and water was added to incipient wetness. After CaNO3 dissolution and stirring, the slurry was dried and calcined in sequence at 115° C. (overnight) and 500° C. (overnight), respectively, in air.
example 2
[0036] Methane at 15 psia was bubbled through bromine at 1° C. at a rate of 5 cc / min. The resulting stream of bromine and methane (1:10 by mole) was passed through a small diameter bromination reactor at 450° C. (1000 h−1) and the mixture of CH4-xBrx (x=0, 1, 2, 3) passed into a reactor containing 5 g of metal oxide / zeolite composite MZ1 (400 C). The output stream from the second reactor contained no brominated products. Based on the methane consumed in the bromination reactor, 10% ethylene, 31% propylene, 3% propane, and 21% butanes / butenes were detected; 65% overall. Trace amounts of C6 species were also detected. After reaction for 5 hours, during which the stream output did not change from the distribution described above, the methane stream was discontinued and the reactor was purged with helium at 5 cc / min for 10 minutes. After He purge, a flow of O2 (2 cc / min) into the second reactor was initiated at 525 C to regenerate the metal oxide from the metal bromide of the partially ...
example 3
[0037] A doped mordenite (Zeolyst CBV 21A, doped with both Ca and Mg) (5 g) was prepared according to Example 1, and used as the cataloreactant in a hydrocarbon synthesis substantially similar to that described above in Example 2. The product output was 30% ethylene, 5% ethane, 10% propylene, 3% propane, 5% butanes / butenes. Multiple runs and cataloreactant regeneration established reproducibility.
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