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

Inactive Publication Date: 2005-08-04
REACTION 35 LLC
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

[0011] The present invention addresses the need for an efficient way to convert methane and other hydrocarbons into higher hydrocarbons. In one embodiment, a hydrocarbon having a carbon number Cn, where n ≧2, is prepared by allowing a reactant hydrocarbon having a carbon number Cm, where m<n, to react with a halogenating agent, thereby forming a halogenated hydrocarbon; allowing the halogenated hydrocarbon to contact a metal-oxygen cataloreactant, thereby forming a product hydrocarbon having an carbon number Cn, where n≧2; recovering the product hydrocarbon; and regenerating the cataloreactant. Often, a mixture of hydrocarbons is obtained, but careful selection of the reactant hydrocarbon, halogenating agent, metal-oxygen cataloreactant, and reaction conditions allow a tailored approach to hydrocarbon product formation. Methane (i.e., natural gas) as well as other light hydrocarbons, e.g., C2 to C6 hydrocarbons, are envisioned as preferred feedstocks. More generally, the invention contemplates the use of feedstocks having carbon numbers as high as C10. Laboratory observations have thus far focused on methane oligomerization and methyl bromide coupling, with detection of C2-C10 species, including alkanes, alkenes, branched hydrocarbons, and aromatic compounds.

Problems solved by technology

The light hydrocarbons can be recycled for further processing over the oxyhydrochlorination catalyst.” All of these techniques for making higher alkanes from C1 feedstocks suffer from the disadvantage that the hydrocarbon stream must be separated from an aqueous hydrohalic acid stream, and the hydrohalic acid stream must be recycled.
The process does not incorporate reactive neutralization of hydrogen halide, and appears to suffer from slow kinetics.
Liquid phase chemistry, however, typically suffers from such disadvantages as the requirement of solvent, corrosion, and lower rates of reaction than gas-phase chemistry.
In addition, such a process consumes energy required to produce the magnesium metal needed for the energetic and reducing Grignard reagents.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

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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Abstract

A method of synthesizing hydrocarbons from smaller hydrocarbons includes the steps of hydrocarbon halogenation, simultaneous oligomerization and hydrogen halide neutralization, and product recovery, with a metal-oxygen cataloreactant used to facilitate carbon-carbon coupling. Treatment with air or oxygen liberates halogen and regenerates the cataloreactant.

Description

CROSS-REFERENCE TO RELATED APPLICATION(S) [0001] This application is a continuation-in-part, and claims priority of U.S. patent application Ser. No. 10 / 893,418, filed Jul. 15, 2004, currently pending, which claims the benefit of U.S. Provisional Patent Application No. 60 / 487,364, filed Jul. 15, 2003, the entire contents of both applications being incorporated by reference herein.FIELD OF THE INVENTION [0002] This invention relates generally to hydrocarbon oligomerization, and more particularly to a method of making hydrocarbons using cataloreactants. BACKGROUND OF THE INVENTION [0003] Scientists have long sought efficient ways to convert methane and other alkanes into higher hydrocarbons, including light olefins and gasoline-range materials. Efficient processes could create value in a number of ways, including: facilitating the utilization of remotely located stranded natural gas through its conversion into more easily transportable liquid fuels and feedstocks, and allowing the use ...

Claims

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Application Information

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Patent Type & Authority Applications(United States)
IPC IPC(8): C07C1/26
CPCC07C1/26C07C2521/10C07C2523/02C07C2529/18C07C2529/40C10G27/00C10G2400/22C10G2400/02C10G2400/20C10G2400/30Y10S585/943Y10S585/935C10G50/00Y02P20/52C07C11/04C07C11/06C07C2/00
Inventor LORKOVIC, IVAN M.
Owner REACTION 35 LLC
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