초록 ▼

A multistep process is disclosed for the manufacture of synthetic lubricants from the C8 to C24 linear olefin components of below liquid fuel value petroleum distillate fractions derived via the high temperature thermal cracking of petroleum residua. Such feeds contain major amounts of 1-n-olefins,

A multistep process is disclosed for the manufacture of synthetic lubricants from the C8 to C24 linear olefin components of below liquid fuel value petroleum distillate fractions derived via the high temperature thermal cracking of petroleum residua. Such feeds contain major amounts of 1-n-olefins, n-paraffins and greater than 0.1% concentration of sulfur mostly in the form aromatic, thiophene type sulfur compounds. In the first step of the present process such feeds are enriched in the straight chain aliphatic hydrocarbon components by one or more separation processes, preferably via urea adduction or by crystallization. In the second step, the olefin components are oligomerized to sulfur containing C30 to C60 polyolefins, preferably in the presence of BF3 complex catalysts. In the third step, the polyolefins are hydrogenated to novel isoparaffin lubricants in the presence of sulfur resistant catalysts, preferably transition metal sulfides.

대표청구항 ▼

A multistep process for the manufacture of polyolefin lubricants, derived mostly from C8 to C24 linear olefin components of coker distillate fractions containing more than 0.1% sulfur which are produced by the high temperature thermal cracking of petroleum residua, comprising the following three ste

A multistep process for the manufacture of polyolefin lubricants, derived mostly from C8 to C24 linear olefin components of coker distillate fractions containing more than 0.1% sulfur which are produced by the high temperature thermal cracking of petroleum residua, comprising the following three steps: (a) enrichment of coker distillate feed in 1-n-olefin and n-paraffin components by one or more separation processes including urea adduction or crystallization, (b) oligomerization of the C8 to C24 olefin components of an enriched coker distillate fraction to produce sulfur containing C30 to C60 polyolefins, (c) hydrogenation of sulfur containing polyolefins to isoparaffins with the simultaneous removal of the sulfur.