会员体验
专利管家(专利管理)
工作空间(专利管理)
风险监控(情报监控)
数据分析(专利分析)
侵权分析(诉讼无效)
联系我们
交流群
官方交流:
QQ群: 891211   
微信请扫码    >>>
现在联系顾问~
热词
    • 6. 发明授权
    • Method for producing butadiene from n-butane
    • 从正丁烷生产丁二烯的方法
    • US08088962B2
    • 2012-01-03
    • US11813935
    • 2006-01-16
    • Catharina KlannerGötz-Peter SchindlerSven CroneFrieder BorgmeierMark DudaFalk Simon
    • Catharina KlannerGötz-Peter SchindlerSven CroneFrieder BorgmeierMark DudaFalk Simon
    • C07C5/333
    • C07C5/3337C07C7/08C07C11/167
    • A process for preparing butadiene, comprising A) providing a stream (a) comprising n-butane; B) feeding stream (a) comprising into at least one first dehydrogenation zone and nonoxidatively catalytically dehydrogenating n-butane to obtain a stream (b) comprising n-butane, 1-butene, 2-butene, butadiene, hydrogen and low-boiling secondary constituents; C) feeding stream (b) and an oxygenous gas into at least one second dehydrogenation zone and oxidatively dehydrogenating n-butane, 1-butene and 2-butene to obtain a stream (c) comprising n-butane, 2-butene, butadiene, low-boiling secondary constituents, carbon oxides and steam, wherein stream (c) has a higher content of butadiene than stream (b); D) removing the low-boiling secondary constituents and steam to obtain a stream (d) substantially consisting of n-butane, 2-butene and butadiene; E) separating stream (d) into a stream (e1) consisting substantially of n-butane and 2-butene and a stream (e2) consisting substantially of butadiene by extractive distillation; F) recycling stream (e1) into the first dehydrogenation zone.
    • 一种制备丁二烯的方法,包括A)提供包含正丁烷的料流(a); B)将包含至少一个第一脱氢区和非氧化催化脱氢的正丁烷的料流(a)进料,以获得包含正丁烷,1-丁烯,2-丁烯,丁二烯,氢和低沸点二级 成分; C)将进料流(b)和氧气送入至少一个第二脱氢区,并使正丁烷,1-丁烯和2-丁烯氧化脱氢得到包含正丁烷,2-丁烯,丁二烯, 低沸点次级成分,碳氧化物和蒸汽,其中物流(c)具有比物流(b)更高的丁二烯含量; D)除去低沸点二次成分和蒸汽,得到基本上由正丁烷,2-丁烯和丁二烯组成的料流(d); E)通过萃取蒸馏将料流(d)分离成基本上由正丁烷和2-丁烯组成的料流(e1)和基本上由丁二烯组成的料流(e2); F)再循环流(e1)进入第一脱氢区。
    • 8. 发明授权
    • Method for producing butadiene from n-butane
    • 从正丁烷生产丁二烯的方法
    • US07495138B2
    • 2009-02-24
    • US11722278
    • 2005-12-19
    • Sven CroneCatharina KlannerGötz-Peter SchindlerMark DudaFrieder Borgmeier
    • Sven CroneCatharina KlannerGötz-Peter SchindlerMark DudaFrieder Borgmeier
    • C07C5/333
    • C07C5/333C07C11/167
    • A process for preparing butadiene, comprising nonoxidatively dehydrogenating n-butane from a stream (a) in a first dehydrogenation zone to obtain stream (b) comprising 1-butene, 2-butene, and butadiene; oxidatively dehydrogenating the 1-butene and 2-butene of (b) in the presence of an oxygenous gas in a second dehydrogenation zone to obtain stream (c) comprising n-butane, butadiene, hydrogen, and steam; compressing and cooling (c) to obtain stream (d2) comprising n-butane, butadiene, hydrogen, and steam; extractively distilling (d2) into stream (e1) comprising butadiene and stream (e2) comprising n-butane, hydrogen, and steam; optionally compressing and cooling (e2) to obtain stream (f1) comprising n-butane and water and stream (f2) comprising n-butane and hydrogen and optionally recycling (f1) into the first dehydrogenation zone; separating (f2) into stream (g1) comprising n-butane and stream (g2) comprising hydrogen by contacting (f2) with a high boiling absorbent and subsequently desorbing the gas constituents dissolved in the absorbent.
    • 一种制备丁二烯的方法,包括在第一脱氢区中从流(a)中非氧化脱氢的正丁烷获得包含1-丁烯,2-丁烯和丁二烯的料流(b) 在第二脱氢区中在有氧气体存在下使(b)的1-丁烯和2-丁烯氧化脱氢,得到包含正丁烷,丁二烯,氢和蒸汽的料流(c) 压缩并冷却(c)以获得包含正丁烷,丁二烯,氢气和蒸汽的流(d2); 将包含丁二烯的流(e1)和包含正丁烷,氢气和蒸汽的物流(e2)萃取蒸馏(d2) 任选地压缩和冷却(e2)以获得包含正丁烷和水的流(f1)和包含正丁烷和氢气的流(f2),并任选地再循环(f1)到第一脱氢区中; 通过使(f2)与高沸点吸收剂接触并随后解吸溶解在吸收剂中的气体组分,将(f2)分离成包含正丁烷和包含氢的流(g2)(g1)的流(g1)。
    • 9. 发明申请
    • Method for Producing Butadiene from N-Butane
    • 从丁烷生产丁二烯的方法
    • US20080183024A1
    • 2008-07-31
    • US11813935
    • 2006-01-16
    • Catharina KlannerGotz-Peter SchindlerSven CroneFrieder BorgmeierMark DudaFalk Simon
    • Catharina KlannerGotz-Peter SchindlerSven CroneFrieder BorgmeierMark DudaFalk Simon
    • C07C5/327
    • C07C5/3337C07C7/08C07C11/167
    • A process for preparing butadiene from n-butane, comprising the steps of A) providing a feed gas stream a comprising n-butane; B) feeding the feed gas stream a comprising n-butane into at least one first dehydrogenation zone and nonoxidatively catalytically dehydrogenating n-butane to obtain a product gas stream b comprising n-butane, 1-butene, 2-butene, butadiene, hydrogen and low-boiling secondary constituents, with or without carbon oxides and with or without steam; C) feeding the product gas stream b of the nonoxidative catalytic dehydrogenation and an oxygenous gas into at least one second dehydrogenation zone and oxidatively dehydrogenating n-butane, 1-butene and 2-butene to obtain a product gas stream c comprising n-butane, 2-butene, butadiene, low-boiling secondary constituents, carbon oxides and steam, said product gas stream c having a higher content of butadiene than product gas stream b; D) removing the low-boiling secondary constituents and steam to obtain a C4 product gas stream d substantially consisting of n-butane, 2-butene and butadiene; E) separating the C4 product gas stream d into a stream e1 consisting substantially of n-butane and 2-butene and a product-of-value stream e2 consisting substantially of butadiene by extractive distillation; F) recycling stream e1 into the first dehydrogenation zone.
    • 一种从正丁烷制备丁二烯的方法,包括以下步骤:A)提供包含正丁烷的进料气流a; B)将包含正丁烷的进料气流a进料到至少一个第一脱氢区和非氧化催化脱氢的正丁烷中,以获得包含正丁烷,1-丁烯,2-丁烯,丁二烯,氢和 低沸点二次成分,有或没有碳氧化物,有或没有蒸汽; C)将非氧化催化脱氢的产物气流b和氧气输送到至少一个第二脱氢区,并使正丁烷,1-丁烯和2-丁烯氧化脱氢得到包含正丁烷的产物气流c, 丁二烯,低沸点二次成分,碳氧化物和蒸汽,所述产物气流c具有比产物气流b更高的丁二烯含量; D)除去低沸点二次成分和蒸汽,得到基本上由正丁烷,2-丁烯和丁二烯组成的C 4 H 4产物气流d; E)通过萃取蒸馏将C 4 S 4产物气流d分离成基本上由正丁烷和2-丁烯组成的流e 1和基本上由丁二烯组成的价值产物流e 2; F)将流e 1再循环到第一脱氢区。
    • 10. 发明申请
    • Method for Producing Butadiene from N-Butane
    • US20080119680A1
    • 2008-05-22
    • US11722278
    • 2005-12-19
    • Sven CroneCatharina KlannerGotz-Peter SchindlerMark DudaFrieder Borgmeier
    • Sven CroneCatharina KlannerGotz-Peter SchindlerMark DudaFrieder Borgmeier
    • C07C5/333
    • C07C5/333C07C11/167
    • A process for preparing butadiene from n-butane, comprising the steps of A) providing a feed gas stream a comprising n-butane; B) feeding the feed gas stream a comprising n-butane into at least one first dehydrogenation zone and nonoxidatively, catalytically dehydrogenating n-butane to obtain a gas stream b comprising n-butane, 1-butene, 2-butene, butadiene and hydrogen, with or without steam, with or without carbon oxides and with or without inert gases; C) feeding the gas stream b and an oxygenous gas into at least one second dehydrogenation zone and oxidatively dehydrogenating 1-butene and 2-butene to obtain a gas stream c comprising n-butane, butadiene, hydrogen, steam, with or without carbon oxides and with or without inert gases; D) compressing in at least one first compression stage and cooling the gas stream c to obtain at least one condensate stream d1 comprising water and a gas stream d2 comprising n-butane, butadiene, hydrogen and steam, with or without carbon oxides and with or without inert gases; E) separating the gas stream d2 by extractive distillation into a product stream e1 consisting substantially of butadiene and a stream e2 comprising n-butane, hydrogen and steam, with or without carbon oxides and with or without inert gases, F) if appropriate compressing in one or more further compression stages and cooling the gas stream e2 to obtain at least one condensate stream f1 comprising n-butane and water, and a gas stream f2 comprising n-butane and hydrogen, with or without carbon oxides and with or without inert gases, and if appropriate recycling the condensate stream f1 into the first dehydrogenation zone; G) separating the gas stream f2 into a recycle stream g1 comprising n-butane and an offgas stream g2 comprising hydrogen, with or without carbon oxides and with or without inert gases, by contacting the gas stream f2 with a high-boiling absorbent and subsequently desorbing the gas constituents dissolved in the absorbent.