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    • 4. 发明申请
    • Method for the production of butadiene
    • 生产丁二烯的方法
    • US20070167661A1
    • 2007-07-19
    • US10584758
    • 2004-12-30
    • Thorsten JohannGotz-Peter SchindlerAndreas BrodhagenSven CroneRegina BenferThomas HillMark Duda
    • Thorsten JohannGotz-Peter SchindlerAndreas BrodhagenSven CroneRegina BenferThomas HillMark Duda
    • C07C5/327
    • C07C5/333C07C5/48C07C11/167
    • The invention relates to a process for preparing butadiene from n-butane having 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, low-boiling secondary constituents and in some cases 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 1-butene and 2-butene to obtain a product gas stream c comprising n-butane, 2-butene, butadiene, hydrogen, low-boiling secondary constituents and steam, said product gas stream c having a higher content of butadiene than the product gas stream b; D) removing hydrogen, 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 recycle stream e1 consisting substantially of n-butane and 2-butene and a stream e2 consisting substantially of butadiene by extractively distilling and recycling the stream e1 into the first dehydrogenation zone; F) if desired, feeding some or all of the stream e2 consisting substantially of butadiene into a selective hydrogenation zone and selectively hydrogenating butadiene to 1- and/or 2-butene to obtain a stream f comprising 1-butene and 2-butene; G) if desired, feeding the stream f comprising 1-butene and 2-butene into a distillation zone and removing a product of value stream g1 consisting substantially of 1-butene to leave a stream g2 comprising 2-butene; H) if desired, recycling the stream g2 comprising 2-butene into the first dehydrogenation zone.
    • 本发明涉及一种从正丁烷制备丁二烯的方法,该方法具有以下步骤: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, 低沸点次生成分,有时还有蒸汽; 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1-丁烯和2-丁烯氧化脱氢得到包含正丁烷,2-丁烯, 丁二烯,氢,低沸点二次成分和蒸汽,所述产物气流c具有比产物气流b更高含量的丁二烯; D)除去氢气,低沸点次级组分和蒸汽,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)将C 4 H 4产物气流d分离成基本上由正丁烷和2-丁烯组成的循环流e1和基本上由丁二烯组成的物流e2,通过萃取蒸馏并将流e1再循环到 第一个脱氢区; F)如果需要,将基本上由丁二烯组成的一些或全部流e2加入到选择性氢化区中,并将丁二烯选择性氢化为1-和/或2-丁烯,以获得包含1-丁烯和2-丁烯的料流f; 如果需要,将包含1-丁烯和2-丁烯的料流f加入到蒸馏区中并除去基本上由1-丁烯组成的物流g1的产物以留下包含2-丁烯的料流g2; H)如果需要,将包含2-丁烯的料流g2再循环到第一脱氢区中。
    • 5. 发明申请
    • Method for the production of butadiene and 1-butene
    • 制备丁二烯和1-丁烯的方法
    • US20070161842A1
    • 2007-07-12
    • US10584783
    • 2004-12-30
    • Thorsten JohannGotz-Peter SchindlerAndreas BrodhagenSven CroneRegina BenferMarcus SiglMark Duda
    • Thorsten JohannGotz-Peter SchindlerAndreas BrodhagenSven CroneRegina BenferMarcus SiglMark Duda
    • C07C5/327C07C1/00
    • C07C5/327C07C5/333C07C5/48C07C11/167
    • The invention relates to a process for preparing butadiene from n-butane having 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, low-boiling secondary constituents and in some cases 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 and steam, said product gas stream c having a higher content of butadiene than the 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) feeding the stream e1 consisting substantially of n-butane and 2-butene and a cycle stream g comprising 1-butene and 2-butene into a distillation zone and separating into a 1-butene-rich product of value stream f1, a recycle stream f2 comprising 2-butene and n-butane and a stream f3 comprising 2-butene, and recycling the recycle stream f2 into the first dehydrogenation zone; G) feeding the stream f3 comprising 2-butene into an isomerization zone and isomerizing 2-butene to 1-butene to obtain a cycle stream g comprising 1-butene and 2-butene, and recycling the cycle gas stream g into the distillation zone.
    • 本发明涉及一种从正丁烷制备丁二烯的方法,该方法具有以下步骤: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, 低沸点次生成分,有时还有蒸汽; 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,低沸点二次成分和蒸汽,所述产物气流c具有比产物气流b更高含量的丁二烯; 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)将C 4 H 4产物气流d分离成基本上由正丁烷和2-丁烯组成的物流e1和通过萃取蒸馏基本上由丁二烯组成的价值流e2的产物; F)将基本上由正丁烷和2-丁烯组成的流e1和包含1-丁烯和2-丁烯的循环流g加入到蒸馏区中并分离成价值流f1的富含1-丁烯的产物,再循环 包含2-丁烯和正丁烷的料流f2和包含2-丁烯的料流f3,并将再循环料流f2再循环到第一脱氢区中; G)将包含2-丁烯的料流f3进料到异构化区并将2-丁烯异构化成1-丁烯,得到包含1-丁烯和2-丁烯的循环流g,并将循环气流g再循环到蒸馏区中。
    • 6. 发明申请
    • Method for the production of butadiene
    • 生产丁二烯的方法
    • US20070179330A1
    • 2007-08-02
    • US10584785
    • 2004-12-30
    • Thorsten JohannGotz-Peter SchindlerAndreas BrodhagenSven CroneMark Duda
    • Thorsten JohannGotz-Peter SchindlerAndreas BrodhagenSven CroneMark Duda
    • C07C5/333C07C2/00
    • C07C5/333C07C5/48C07C11/167
    • The invention relates to a process for preparing butadiene from n-butane having 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, low-boiling secondary constituents and in some cases 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 1-butene and 2-butene to obtain a product gas stream c comprising n-butane, 2-butene, butadiene, hydrogen, low-boiling secondary constituents and steam, said product gas stream c having a higher content of butadiene than the product gas stream b; D) removing hydrogen, 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) feeding the C4 product gas stream d into a distillation zone and removing a butadiene/butane mixture as the product of value stream e1, to leave a stream e2 consisting substantially of n-butane and 2-butene; F) recycling the stream e2 into the first dehydrogenation zone.
    • 本发明涉及一种从正丁烷制备丁二烯的方法,该方法具有以下步骤: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, 低沸点次生成分,有时还有蒸汽; 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1-丁烯和2-丁烯氧化脱氢得到包含正丁烷,2-丁烯, 丁二烯,氢,低沸点二次成分和蒸汽,所述产物气流c具有比产物气流b更高含量的丁二烯; D)除去氢气,低沸点次级组分和蒸汽,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)将C 4 H 4产物气流d进料到蒸馏区中并除去作为值流e1的产物的丁二烯/丁烷混合物,以留下基本上由正丁烷和2- 丁烯 F)将流e2再循环到第一脱氢区。
    • 7. 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. 发明授权
    • Method for the production of butadine from n-butane
    • 从正丁烷生产丁二烯的方法
    • US07435860B2
    • 2008-10-14
    • US11721240
    • 2005-12-07
    • Sven CroneCatharina KlannerGötz-Peter SchindlerMark DudaFrieder Borgmeier
    • Sven CroneCatharina KlannerGötz-Peter SchindlerMark DudaFrieder Borgmeier
    • C07C5/333
    • C07C11/167C07C5/48
    • 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 and 2-butene; 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, carbon dioxide, and steam; compressing and cooling (c) to obtain stream (d2) comprising n-butane, butadiene, hydrogen, carbon dioxide, and steam; extractively distilling (d2) into stream (e1) comprising butadiene and stream (e2) comprising n-butane, hydrogen, carbon dioxide, and steam; compressing and cooling (e2) to obtain stream (f1) comprising n-butane and water and stream (f2) comprising n-butane, hydrogen, and carbon dioxide; cooling (f2) to obtain stream (g1) comprising n-butane and stream (g2) comprising carbon dioxide and hydrogen; phase separating water from (f1) to obtain stream (h1) comprising n-butane; and recycling (h1) into the first dehydrogenation zone.
    • 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-丁烯和2-丁烯的料流(b) 在第二脱氢区中在有氧气体存在下使(b)的1-丁烯和2-丁烯氧化脱氢以得到包含正丁烷,丁二烯,氢,二氧化碳和蒸汽的流(c) 压缩并冷却(c)以获得包含正丁烷,丁二烯,氢气,二氧化碳和蒸汽的流(d2); 将包含丁二烯的流(e1)和包含正丁烷,氢气,二氧化碳和蒸汽的物流(e2)萃取蒸馏(d2) 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,氢气和二氧化碳的物流(f2); 冷却(f2)以获得包含正丁烷的流(g1)和包含二氧化碳和氢气的流(g2); 将(f1)的水相分离以获得包含正丁烷的流(h1); 和再循环(h1)进入第一个脱氢区。
    • 10. 发明授权
    • Method for producing butadiene from n-butane
    • 从正丁烷生产丁二烯的方法
    • US07417173B2
    • 2008-08-26
    • US11718814
    • 2005-11-11
    • Sven CroneCatharina KlannerGötz-Peter SchindlerMark DudaFrieder Borgmeier
    • Sven CroneCatharina KlannerGötz-Peter SchindlerMark DudaFrieder Borgmeier
    • C07C5/333
    • C07C7/09C07C5/333C07C11/167
    • Processes for producing butadiene from n-butane comprising: (a) providing a feed gas stream comprising n-butane; (b) non-oxidatively dehydrogenating the feed gas stream in the presence of a catalyst in a first dehydrogenation zone to form a first intermediate gas stream comprising n-butane, 1-butene, 2-butene, butadiene and hydrogen; (c) oxidatively dehydrogenating the first intermediate gas stream in the presence of an oxygenous gas having an oxygen content of at least 75% by volume in a second dehydrogenation zone to form a second intermediate gas stream comprising n-butane, butadiene, hydrogen, carbon dioxide and steam; (d) compressing and cooling the second intermediate gas to form a first condensate stream comprising water and a third intermediate gas stream comprising n-butane, butadiene, hydrogen, carbon dioxide and steam; (e) compressing and cooling the third intermediate gas to form a second condensate stream comprising n-butane, butadiene and water and a fourth intermediate gas stream comprising n-butane, butadiene, hydrogen and carbon dioxide; (1) cooling the fourth intermediate gas stream to form a third condensate stream comprising n-butane and butadiene, and an offgas stream comprising carbon dioxide and hydrogen; (g) removing water from the second condensate stream and combining the second condensate stream and third condensate stream to form a C4 hydrocarbon stream comprising n-butane and butadiene; and (h) separating the C4 hydrocarbon stream to form a recylce stream comprising n-butane and a product stream comprising butadiene; wherein at least a portion of the recycle stream is fed to the first dehydrogenation zone.
    • 用于从正丁烷生产丁二烯的方法包括:(a)提供包含正丁烷的进料气流; (b)在催化剂存在下在第一脱氢区中使进料气流非氧化脱氢,以形成包含正丁烷,1-丁烯,2-丁烯,丁二烯和氢的第一中间气流; (c)在第二脱氢区中在氧含量至少为75体积%的氧气存在下,使第一中间气流氧化脱氢以形成包含正丁烷,丁二烯,氢,碳的第二中间气流 二氧化碳和蒸汽; (d)压缩和冷却第二中间气体以形成包含水的第一冷凝物流和包含正丁烷,丁二烯,氢气,二氧化碳和蒸汽的第三中间气流; (e)压缩和冷却第三中间气体以形成包含正丁烷,丁二烯和水的第二冷凝物流和包含正丁烷,丁二烯,氢气和二氧化碳的第四中间气流; (1)冷却第四中间气流以形成包含正丁烷和丁二烯的第三冷凝物流和包含二氧化碳和氢气的废气流; (g)从第二冷凝物流中除去水并将第二冷凝物流和第三冷凝物流合并以形成包含正丁烷和丁二烯的C 4烃流; 和(h)分离C 4 O 4烃流以形成包含正丁烷和包含丁二烯的产物流的回流; 其中所述再循环流的至少一部分被供给到所述第一脱氢区。