Steady-state conversion of methane to C4+ aliphatic products in high yields using an integrated recycle reactor system Academic Article

abstract

• Conversion of methane in high yields to C4+ nonaromatic hydrocarbons was demonstrated in a recycle system. The principal components of the recycle system included an oxidative coupling reactor with a Mn/Na2WO4/SiO2 catalyst at 800 C for conversion of methane to ethylene, and a reactor with an H-ZSM-5 zeolite at 275 C for subsequent conversion of ethylene to higher hydrocarbons. Total yields of C4+ products were in the range of 60-80%, and yields of C4+ nonaromatic hydrocarbons were in the range of 50-60%. 2000 Kluwer Academic Publishers.

authors

• Rosynek, Michael

published proceedings

• CATALYSIS LETTERS

author list (cited authors)

• Pak, S., Rades, T., Rosynek, M. P., & Lunsford, J. H.

citation count

• 10

complete list of authors

• Pak, S||Rades, T||Rosynek, MP||Lunsford, JH

publication date

• May 2000

publisher

• Springer Nature  Publisher

published in

• Catalysis Letters  Journal

keywords

• ALIPHATIC HYDROCARBONS
• Methane
• Oxidation
• Recycle Reactor
• Zeolite

Digital Object Identifier (DOI)

• 10.1023/A:1019039321142

start page

• 1

end page

• 4

volume

• 66

issue

• 1-2

URL

• http://dx.doi.org/10.1023/a:1019039321142