Abstract:
Recycle of a stream comprising C8 oligomers to an oligomerization zone to be oligomerized with C4 olefins can produce diesel range oligomers. A diesel stream can be separated from a gasoline stream which can be recycled to the oligomerization zone.
Abstract:
A process provides oligomerization feed stream comprising C5 hydrocarbons and olefins along with C4 olefins to an oligomerization zone. The oligomerization feed stream may be obtained from cracked FCC products. Unreacted C5 hydrocarbons can be recycled to the oligomerization zone to maintain the liquid phase therein.
Abstract:
A first oligomerization stream is oligomerized over a first catalyst in a first oligomerization reactor zone to make oligomerate. An oligomerate stream is separated to provide a heavy oligomerate boiling in the diesel range and a second oligomerization feed stream. The latter is fed to a second oligomerization reactor zone with a second different catalyst to produce the heavy oligomerate.
Abstract:
To bias an oligomerization reaction toward C9 olefin production, C5 olefins are split and fed to a C4 olefin feed stream at a downstream location, so the C4 olefins are in stoichiometric excess over the C5 olefins. The result is greater oligomerization to C9 olefins. C9 olefins fed to an FCC unit have a carbon number divisible by three and thus produces a greater proportion of propylene.
Abstract:
Distillate cracks to propylene more readily than VGO. Additionally, less branched hydrocarbons crack to propylene more readily than more branched hydrocarbons. Oligomerization to diesel range oligomers followed by catalytic cracking with less branched oligomers can provide more propylene.
Abstract:
Disclosed is a process and apparatus for switching oligomerization feed between a first oligomerization zone that includes a uni-dimensional small pore zeolite to make more diesel and a second oligomerization zone that includes SPA catalyst for making more gasoline. The diesel can be recycled to make more propylene. The process and apparatus will provide refiners with flexibility to produce the most valuable product commensurate with fluctuating market conditions.
Abstract:
Disclosed is the addition of C5 olefins to oligomerization feed stream has the counterintuitive effect of reducing the production of heavier oligomers over a uni-dimensional, ten-ring pore zeolite. Consequently, C5 olefins can be added to C4 olefins in an oligomerization feed stream to produce more gasoline and less distillate.
Abstract:
A process for separating an oligomerate stream into a vaporous oligomerate stream and a liquid oligomerate bottom stream is followed by recycling the liquid oligomerate bottom stream to an oligomerization zone to maintain the liquid phase therein and to provide unreacted olefins to the oligomerization zone.
Abstract:
Oligomerizing C4 and C5 olefins over a SPA catalyst provides an oligomerate product stream comprising C6+ olefins that meets a gasoline T-90 specification of 380° F. The oligomerate product stream can be taken to the gasoline pool without further upgrading.
Abstract:
An olefinic composition has a moderate concentration of Type 2 C8 olefins. The oligomerate composition has hydrocarbon molecules with minimal branching which make excellent diesel and can also be readily cracked to propylene. Consequently, oligomerate product can be sent to the diesel pool or fed or recycled to an FCC unit to increase production of propylene.