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    • 86. 发明申请
    • PROCESS FOR RECOVERING 3-METHYLBUT-3-EN-1-OL
    • WO2019030386A1
    • 2019-02-14
    • PCT/EP2018/071771
    • 2018-08-10
    • BASF SE
    • WERNER, AlbertBRU ROIG, MiriamPARVULESCU, Andrei-NicolaeMINGES, RolandKELLER, AndreasMAURER, StephanMUELLER, UlrichSIEGEL, Wolfgang
    • C07C29/38C07C29/80C07C33/025
    • The present invention relates to a process for recovering 3-methylbut-3-en-1 -ol from a feed stream F1 comprising 3-methylbut-3-en-1 -ol, one or more solvents, water, and isobutene, wherein 3-methylbut-3-en-1 -ol, the one or more solvents and water are separated from isobutene by distillation, the process comprising subjecting the feed stream F1 to distillation conditions in a distillation unit, obtaining a bottoms stream B1 which is enriched in -methylbut-3-en-1 -ol, in the one or more solvents and in water compared to the feed stream F1 subjec The present invention relates to a process for recovering 3-methylbut-3-en-1 -ol from a feed stream F1 comprising 3-methylbut-3-en-1 -ol, one or more solvents, water, and isobutene, wherein 3-methylbut-3-en-1 -ol, the one or more solvents and water are separated from isobutene by distillation, the process comprising subjecting the feed stream F1 to distillation conditions in a distillation unit, obtaining a bottoms stream B1 which is enriched in -methylbut-3-en-1 - ol, in the one or more solvents and in water compared to the feed stream F1 subjected to distillation conditions, and a top stream T1 which is enriched in isobutene, further subjecting the bottoms stream B1 to distillation conditions in a second distillation unit and obtaining a bottoms stream B2 which is enriched in 3-methylbut-3-en-1-ol compared to the bottoms stream B1 and a top stream T2 which is enriched in water compared to the bottoms stream B1, further subjecting the bottoms stream B2 to distillation conditions in a third distillation unit and obtaining a top stream T3 which is enriched in 3-methylbut-3-en-1-ol compared to the bottoms stream B2 and a bottoms stream B3. ted to distillation conditions, and a top stream T1 which is enriched in isobutene, further subjecting the bot- toms stream B1 to distillation conditions in a second distillation unit and obtaining a bottoms stream B2 which is enriched in 3-methylbut-3-en-1-ol compared to the bottoms stream B1 and a top stream T2 which is enriched in water compared to the bottoms stream B1, further subjecting the bottoms stream B2 to distillation conditions in a third distillation unit and obtaining a top stream T3 which is enriched in 3-methylbut-3-en-1-ol compared to the bottoms stream B2 and a bottoms stream B3.
    • 90. 发明申请
    • A PROCESS FOR PURIFYING PROPYLENE OXIDE
    • 一种纯化氧化丙烯的方法
    • WO2018015435A1
    • 2018-01-25
    • PCT/EP2017/068228
    • 2017-07-19
    • BASF SE
    • TELES, Joaquim H.KRAMP, MarvinMUELLER, ChristianWOERZ, Nicolai TonioMETZEN, BerndKELLER, TobiasRIEDEL, DominicWEBER, MarkusURBANCZYK, DanielPARVULESCU, Andrei-NicolaeWEGERLE, UlrikeMUELLER, Ulrich
    • C07D301/32C07D303/02
    • The present invention is related to a process for purifying propylene oxide, comprising (i) providing a stream S0 comprising propylene oxide, acetonitrile, water, and an organic compound comprising a carbonyl group -C(=O)-, wherein said organic compound comprising a carbonyl group -C(=O)- comprises one or more of acetone and propionaldehyde; (ii) separating propylene oxide from the stream S0 by distillation, comprising subjecting the stream S0 to distillation conditions in a distillation column, obtaining a gaseous top stream S1c which is enriched in propylene oxide compared to the stream S0, a liquid bottoms stream S1 a which is enriched in acetonitrile and water compared to the stream S0, and a side stream S1b comprising propylene oxide which is enriched in the carbonyl compound compared to the stream S0; wherein the distillation column is operated at an absolute pressure at the top of the distillation column in the range of from 0.1 to 2.0 bar and an internal reflux ratio in the range of from 2.0 to 6.0; wherein the distillation column exhibits at least 100 theoretical trays, the rectifying section of the distillation column consists of from 30 to 70 % of the theoretical trays and the stripping section of the distillation column consists of from 70 to 30 % of the theoretical trays.
    • 本发明涉及纯化环氧丙烷的方法,包括(i)提供包含环氧丙烷,乙腈,水和包含羰基-C(= O)的有机化合物的物流S 0, ) - ,其中所述包含羰基-C(= O) - 的有机化合物包含丙酮和丙醛中的一种或多种; (ii)通过蒸馏从物流S0分离环氧丙烷,包括使物流S0在蒸馏塔中经受蒸馏​​条件,获得富集环氧丙烷的气态顶部物流S1c,与物流S0相比,液态底部物流S1a 其与流S0相比富含乙腈和水,以及包含富含羰基化合物的环氧丙烷的侧流S1b与流S0相比; 其中所述蒸馏塔在所述蒸馏塔顶部的绝对压力下操作,所述蒸馏塔的压力范围为0.1-2.0巴,内回流比为2.0-6.0; 其中蒸馏塔表现出至少100个理论塔板,蒸馏塔的精馏段由理论塔板的30-70%组成,蒸馏塔的汽提段由理论塔板的70-30%组成。 / p>