US2024247199A1PendingUtilityA1
Process for converting olefins to jet fuel with dealkanizer
Est. expiryJan 20, 2043(~16.5 yrs left)· nominal 20-yr term from priority
C10G 2400/08C10G 2300/4081C10G 2300/1092C10G 69/126C10G 50/00
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Claims
Abstract
A process for oligomerizing olefins to distillate fuels which oligomerizes a recycle olefin stream with charge olefin streams in a first-stage oligomerization reactor. The first-stage oligomerate is oligomerized in a second-stage oligomerization reactor to provide a second-stage oligomerate stream. A recycle olefin stream is taken from said second-stage oligomerate stream. A dealkanizer column can be used to remove light alkanes that would be inert and accumulate in a recycle loop. The second-stage oligomer product stream is hydrogenated to produce fuels.
Claims
exact text as granted — not AI-modified1 . A process for oligomerizing an olefin stream comprising:
oligomerizing a charge olefin stream over a first-stage oligomerization catalyst to produce a first-stage oligomerized stream; oligomerizing said first-stage oligomerized stream over a second-stage oligomerization catalyst to provide a second-stage oligomerized stream; and dealkanizing said second-stage oligomerized stream to provide a light alkane stream and a dealkanized stream.
2 . The process of claim 1 further comprising oligomerizing said charge olefin streams with a recycle olefin stream over said first-stage oligomerization catalyst and taking said recycle olefin stream from said dealkanized stream.
3 . The process of claim 2 wherein taking said recycle olefin stream from said dealkanized stream further comprises splitting said dealkanized stream into a light olefin stream and a heavy olefin stream and taking said recycle olefin stream from said light olefin stream.
4 . The process of claim 3 wherein taking said recycle olefin stream from said light olefin stream further comprises separating said light olefin stream to provide a light off-gas stream and a light liquid overhead stream and taking said recycle olefin stream from said light liquid overhead stream.
5 . The process of claim 1 further comprising splitting said dealkanized stream into a light olefin stream and a heavy olefin stream.
6 . The process of claim 5 further comprising recycling a recycle olefin stream taken from said light olefin stream to said oligomerizing step over said first-stage oligomerization catalyst.
7 . The process of claim 6 further comprising separating said light olefin stream to provide a light olefin condensate stream and taking a portion of said light olefin condensate stream as said recycle olefin stream.
8 . The process of claim 7 wherein taking said recycle olefin stream further comprises separating said light olefin stream to provide a light off-gas stream and a light liquid overhead stream and taking said recycle olefin stream from said light liquid overhead stream.
9 . The process of claim 1 wherein said recycle olefin stream comprises C4 to C8 olefins.
10 . The process of claim 3 wherein said recycle olefin stream is obtained by separating said light alkane stream to provide an off-gas stream and a light alkane condensate stream and taking said recycle olefin stream from said light alkane condensate stream.
11 . The process of claim 1 further comprising combusting said off-gas stream to provide heating requirements in said process.
12 . A process for oligomerizing an olefin stream comprising:
oligomerizing a charge olefin stream and a recycle olefin stream over a first-stage oligomerization catalyst to produce a first-stage oligomerized stream; oligomerizing said first-stage oligomerized stream over a second-stage oligomerization catalyst to provide a second-stage oligomerized stream; dealkanizing said second-stage oligomerized stream to provide a light alkane stream and a dealkanized stream; and taking said recycle olefin stream from said dealkanized stream.
13 . The process of claim 12 wherein taking said recycle olefin stream from said dealkanized stream further comprises splitting said dealkanized stream into a light olefin stream and a heavy olefin stream and taking said recycle olefin stream from said light olefin stream.
14 . The process of claim 13 wherein taking said recycle olefin stream from said light olefin stream further comprises separating said light olefin stream to provide a light off-gas stream and a light liquid overhead stream and taking said recycle olefin stream from said light liquid overhead stream.
15 . The process of claim 14 further comprising splitting said dealkanized stream into a light olefin stream and a heavy olefin stream.
16 . The process of claim 15 further comprising recycling a recycle olefin stream taken from said light olefin stream to said oligomerizing step over said first-stage oligomerization catalyst.
17 . The process of claim 16 further comprising separating said light olefin stream to provide a light olefin condensate stream and taking a portion of said light olefin condensate stream as said recycle olefin stream.
18 . The process of claim 17 wherein taking said recycle olefin stream further comprises separating said light olefin stream to provide a light off-gas stream and a light liquid overhead stream and taking said recycle olefin stream from said light liquid overhead stream.
19 . A process for oligomerizing an olefin stream comprising:
oligomerizing a charge olefin stream and a recycle olefin stream over a first-stage oligomerization catalyst to produce a first-stage oligomerized stream; oligomerizing said first-stage oligomerized stream over a second-stage oligomerization catalyst to provide a second-stage oligomerized stream; dealkanizing said second-stage oligomerized stream to provide a light alkane stream and a dealkanized stream; separating said light alkane stream to provide an off-gas stream and a light alkane condensate stream and taking said recycle olefin stream from said light alkane condensate stream.
20 . The process of claim 1 further comprising combusting said off-gas stream to provide heating requirements in said process.Join the waitlist — get patent alerts
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