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公开(公告)号:US20220402837A1
公开(公告)日:2022-12-22
申请号:US17777256
申请日:2021-07-12
Applicant: LG CHEM, LTD.
Inventor: In Seop KIM , Sang Beom LEE , Doo Wook KIM , Man Woo SON
Abstract: Provided is a method for preparing 1-butene and propylene including: supplying a C4 mixture stream to a first hydrogenation reactor to convert 1,3-butadiene into 1-butene; supplying a discharge stream from the first hydrogenation reactor to a first distillation column, supplying a lower discharge stream from the first distillation column including 2-butene and n-butane to a metathesis reactor, and supplying an upper discharge stream from the first distillation column including 1-butene and i-butane to a second distillation column; recovering an upper discharge stream the second distillation column including i-butane and recovering 1-butene from a lower discharge stream from the second distillation column; and producing propylene in the metathesis reactor, supplying a discharge stream from the metathesis reactor to a purification unit to recover propylene, and recycling an unreacted material to the metathesis reactor.
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公开(公告)号:US20200263095A1
公开(公告)日:2020-08-20
申请号:US16645647
申请日:2019-07-02
Applicant: LG CHEM, LTD.
Inventor: In Seop KIM , Seok Goo LEE , Sung Kyu LEE , Tae Woo KIM , Joon Ho SHIN
Abstract: A method for quenching a pyrolysis product, including: supplying a discharge stream from a liquid decomposition furnace to a first quench tower; supplying an upper discharge stream from the first quench tower to a second quench tower; supplying a discharge stream from a first gas decomposition furnace to the second quench tower; and supplying a discharge stream from a second gas decomposition furnace to the second quench tower.
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公开(公告)号:US20200216373A1
公开(公告)日:2020-07-09
申请号:US16647828
申请日:2019-07-04
Applicant: LG CHEM, LTD.
Inventor: Tae Woo KIM , Sung Kyu LEE , In Seop KIM , Joon Ho SHIN , Yeon Uk CHOO
Abstract: A method for preparing ethylene including: feeding a thermally cracked compressed stream to a first distillation apparatus selectively operating as a first deethanizer or a depropanizer; and feeding an overhead discharge stream of the first distillation apparatus to a second distillation apparatus. When the first distillation apparatus is operated as the first deethanizer, a bottom discharge stream of the second distillation apparatus is fed to a C2 separator. When the first distillation apparatus is operated as the depropanizer, the bottom discharge stream of the second distillation apparatus is passed through a third distillation apparatus and fed to the C2 separator.
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