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    • 1. 发明公开
    • VERFAHREN ZUR HERSTELLUNG VON PROPEN AUS PROPAN
    • EP1836146A1
    • 2007-09-26
    • EP06700188.3
    • 2006-01-04
    • BASF AKTIENGESELLSCHAFT
    • CRONE, SvenMACHHAMMER, OttoSCHINDLER, Götz-PeterBORGMEIER, Frieder
    • C07C5/327C07C7/11C07C7/04
    • C07C5/3337C07C7/11C07C11/06
    • A) A feed stream containing propane is prepared, B) the feed stream containing propane, optionally steam and optionally an oxygen-containing gas stream are fed to a dehydrogenation zone and propane undergoes a dehydrogenation to give propene, whereby a product gas stream b is obtained containing propane, propene, methane, ethane, ethene, carbon monoxide, carbon dioxide, steam, optionally hydrogen and optionally oxygen, C) the product gas stream b is cooled, optionally compressed and steam separated off by condensation, to give a product gas stream c stripped of steam, D) the product gas stream c is brought into contact with a selective inert absorption agent which selectively absorbs propene in a first absorption zone, to give an essentially propane-charged absorption agent stream d1 and a gas stream d2 containing propane, methane, ethane, ethene, carbon monoxide, carbon dioxide and hydrogen, E) the absorption agent stream d1 is optionally depressurised in a first desorption zone, to give an essentially propene-charged absorption agent stream e1 and a gas stream e2, containing propene, said gas stream e2 being recycled into the first absorption zone and F) a propene-containing gas stream f1 is released from the essentially propene-charged absorption agent stream d1 and e1 in at least one second desorption zone by depressurization, heating and/or stripping of the absorption agent stream d1 and e1 with recycling of the selective absorption agent.
    • A)制备含有丙烷的进料流,B)将含有丙烷,任选的蒸汽和任选的含氧气流的进料流进料至脱氢区,并将丙烷脱氢生成丙烯,由此产物气流b为 得到含有丙烷,丙烯,甲烷,乙烷,乙烯,一氧化碳,二氧化碳,蒸汽,任选的氢气和任选的氧气,C)将产物气流b冷却,任选压缩并通过冷凝分离出蒸汽,得到产物气体 d)将产物气流c与选择性吸收剂接触,所述选择性惰性吸收剂选择性吸收第一吸收区中的丙烯,得到基本上丙烷加入的吸收剂流d1和含有 丙烷,甲烷,乙烷,乙烯,一氧化碳,二氧化碳和氢气,E)吸收剂料流d1任选地在第一解吸区中减压至g 基本上丙烯的吸收剂流e1和含丙烯的气流e2,所述气流e2被再循环到第一吸收区中,并且F)含丙烯的气流f1从基本上带丙烯的吸收剂释放 在至少一个第二解吸区中通过吸收剂流d1和e1的减压,加热和/或汽提以及选择性吸收剂的再循环来产生流d1和e1。
    • 5. 发明公开
    • VERFAHREN ZUR HERSTELLUNG VON BUTADIEN
    • PROCESS FOR产生丁二烯
    • EP1701928A1
    • 2006-09-20
    • EP04804419.2
    • 2004-12-30
    • BASF Aktiengesellschaft
    • JOHANN, ThorstenSCHINDLER, Götz-PeterBRODHAGEN, AndreasCRONE, SvenDUDA, Mark
    • C07C5/333C07C11/167
    • C07C5/333C07C5/48C07C11/167
    • The invention relates to a method for producing butadiene from n-butane, comprising the steps of A) providing an input gas flow a containing n-butane; B) feeding said input gas flow a containing n-butane into at least one first dehydrogenation zone and dehydrogenating n-butane in a non-oxidative catalytic manner, whereby a product gas flow b containing n-butane, 1-butene, 2-butene, butadiene, hydrogen, low-boiling secondary components, and optional steam is obtained; C) feeding the product gas flow b resulting from the non-oxidative catalytic dehydrogenation process and an oxygen-containing gas into at least one second dehydrogenation zone and oxidatively dehydrogenating 1-butene and 2-butene, whereby a product gas flow c containing n-butane, 2-butene, butadiene, hydrogen, low-boiling secondary components, and steam is obtained, said second product gas flow c having a higher butadiene content than product gas flow b; D) eliminating hydrogen, the low-boiling secondary components, and steam, whereby a C4 product gas flow d essentially comprising n-butane, 2-butene, and butadiene is obtained; E) feeding the C4 product gas flow d into a distillation zone and separating a butadiene/butane mixture as a valuable product flow e1 such that a flow e2 substantially comprising n-butane and 2-butene remains; F) redirecting flow e2 into the first dehydrogenation zone.
    • 10. 发明公开
    • VERFAHREN ZUR HERSTELLUNG VON BUTADIEN
    • EP1708978A1
    • 2006-10-11
    • EP04804421.8
    • 2004-12-30
    • BASF Aktiengesellschaft
    • JOHANN, ThorstenSCHINDLER, Götz-PeterBRODHAGEN, AndreasCRONE, SvenBENFER, ReginaHILL, ThomasDUDA, Mark
    • C07C5/333C07C11/167
    • C07C5/333C07C5/48C07C11/167
    • The invention relates to a method for producing butadiene from n-butane, comprising the steps of A) providing an input gas flow a containing n-butane; B) feeding said input gas flow a containing n-butane into at least one first dehydrogenation zone and dehydrogenating n-butane in a non-oxidative catalytic manner, whereby a product gas flow b containing n-butane, 1-butene, 2-butene, butadiene, hydrogen, low-boiling secondary components, and optional steam is obtained; C) feeding the product gas flow b resulting from the non-oxidative catalytic dehydrogenation process and an oxygen-containing gas into at least one second dehydrogenation zone and oxidatively dehydrogenating 1-butene and 2-butene, whereby a product gas flow c containing n-butane, 2-butene, butadiene, hydrogen, low-boiling secondary components, and steam is obtained, said second product gas flow c having a higher butadiene content than product gas flow b; D) eliminating hydrogen, the low-boiling secondary components, and steam, whereby a C4 product gas flow d essentially comprising n-butane, 2-butene, and butadiene is obtained; E) separating the C4 product gas flow d into a recirculation flow e1 essentially comprising n-butane and 2-butene and a flow e2 substantially comprising butadiene by means of extractive distillation, and redirecting flow e1 into the first dehydrogenation zone.
    • 本发明涉及由正丁烷生产丁二烯的方法,包括以下步骤:A)提供包含正丁烷的输入气流a; B)将所述含有正丁烷的输入气流a送入至少一个第一脱氢区,并以非氧化催化方式使正丁烷脱氢,由此产生含有正丁烷,1-丁烯,2-丁烯 ,丁二烯,氢气,低沸点次要组分和任选的蒸汽; C)将由非氧化催化脱氢方法得到的产物气流b和含氧气体送入至少一个第二脱氢区,并将1-丁烯和2-丁烯氧化脱氢,由此得到含n- 丁烷,2-丁烯,丁二烯,氢气,低沸点次要组分和蒸汽,所述第二产物气流c具有比产物气流b更高的丁二烯含量; D)除去氢气,低沸点次要组分和蒸汽,由此获得主要包含正丁烷,2-丁烯和丁二烯的C4产物气流d; E)通过萃取蒸馏将C4产物气流d分离成基本上包含正丁烷和2-丁烯的再循环流e1和基本上包含丁二烯的流e2,并将流e1重新引导到第一脱氢区中。