Abstract
The invention describes a method for the selective (hydro) cracking of petroleum materials, containing normal straight-chained and/or slightly branched-chained hydrocarbons. The mixture is brought into contact with a selective, crystalline alumino silicate zeolite cracking catalyst housing a silicon oxide/aluminum oxide ratio of at least about 12 and a constraint index of about 1 to 12 under cracking conditions. A zeolite catalyst with a crystal size of up to 0.05 ..mu.. is used. Solidification point and viscosity in particular of oils are to be lowered through the catalytic dewaxing.
Citation Formats
Gorring, R L, and Shipman, G F.
Process for the selective cracking of straight-chained and slightly branched hydrocarbons.
Germany: N. p.,
1975.
Web.
Gorring, R L, & Shipman, G F.
Process for the selective cracking of straight-chained and slightly branched hydrocarbons.
Germany.
Gorring, R L, and Shipman, G F.
1975.
"Process for the selective cracking of straight-chained and slightly branched hydrocarbons."
Germany.
@misc{etde_6775943,
title = {Process for the selective cracking of straight-chained and slightly branched hydrocarbons}
author = {Gorring, R L, and Shipman, G F}
abstractNote = {The invention describes a method for the selective (hydro) cracking of petroleum materials, containing normal straight-chained and/or slightly branched-chained hydrocarbons. The mixture is brought into contact with a selective, crystalline alumino silicate zeolite cracking catalyst housing a silicon oxide/aluminum oxide ratio of at least about 12 and a constraint index of about 1 to 12 under cracking conditions. A zeolite catalyst with a crystal size of up to 0.05 ..mu.. is used. Solidification point and viscosity in particular of oils are to be lowered through the catalytic dewaxing.}
place = {Germany}
year = {1975}
month = {Jan}
}
title = {Process for the selective cracking of straight-chained and slightly branched hydrocarbons}
author = {Gorring, R L, and Shipman, G F}
abstractNote = {The invention describes a method for the selective (hydro) cracking of petroleum materials, containing normal straight-chained and/or slightly branched-chained hydrocarbons. The mixture is brought into contact with a selective, crystalline alumino silicate zeolite cracking catalyst housing a silicon oxide/aluminum oxide ratio of at least about 12 and a constraint index of about 1 to 12 under cracking conditions. A zeolite catalyst with a crystal size of up to 0.05 ..mu.. is used. Solidification point and viscosity in particular of oils are to be lowered through the catalytic dewaxing.}
place = {Germany}
year = {1975}
month = {Jan}
}