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1.发明申请公开(公告)号：US20150307417A1
公开(公告)日：2015-10-29
申请号：US14420643
申请日：2013-08-01
发明人： Gunther Schmidt , Stefanie Walter , Helmut Fritz
IPC分类号： C07C4/04
CPC分类号： C07C4/04 , C10G9/36 , C10G2400/20
摘要： The invention relates to a process for converting hydrocarbon feeds by thermal steamcracking to at least one olefin-containing product stream comprising at least ethylene and propylene, with at least partial conversion of a first hydrocarbon feed in at least one first cracking furnace (1) and of a second hydrocarbon feed in at least one second cracking furnace (2). According to the invention, the second hydrocarbon feed comprises predominantly hydrocarbons having a carbon number of 5 or/and 4 and consists for the most part of one or more recycled fractions (P, T) which are obtained from the product stream, and the second hydrocarbon is converted in the second cracking furnace (2) with cracking conditions that lead to a ratio of propylene to ethylene of 0.7 to 1.6 kg/kg.
摘要翻译： 本发明涉及一种通过热蒸汽裂化将烃进料转化成至少一种至少包含乙烯和丙烯的含烯烃产物流，至少部分转化至少一个第一裂解炉（1）中的第一烃进料和 的第二烃进料在至少一个第二裂解炉（2）中。 根据本发明，第二烃进料主要包含碳数为5或/和4的烃，并且大部分由从产物流获得的一种或多种再循环馏分（P，T）组成，第二烃进料 在第二裂解炉（2）中使用导致丙烯与乙烯的比例为0.7至1.6kg / kg的裂化条件转化烃。
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公开(公告)号：US09630892B2
公开(公告)日：2017-04-25
申请号：US14420643
申请日：2013-08-01
发明人： Gunther Schmidt , Stefanie Walter , Helmut Fritz
CPC分类号： C07C4/04 , C10G9/36 , C10G2400/20
摘要： The invention relates to a process for converting hydrocarbon feeds by thermal steamcracking to at least one olefin-containing product stream comprising at least ethylene and propylene, with at least partial conversion of a first hydrocarbon feed in at least one first cracking furnace (1) and of a second hydrocarbon feed in at least one second cracking furnace (2). According to the invention, the second hydrocarbon feed comprises predominantly hydrocarbons having a carbon number of 5 or/and 4 and consists for the most part of one or more recycled fractions (P, T) which are obtained from the product stream, and the second hydrocarbon is converted in the second cracking furnace (2) with cracking conditions that lead to a ratio of propylene to ethylene of 0.7 to 1.6 kg/kg.
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公开(公告)号：US09630891B2
公开(公告)日：2017-04-25
申请号：US14420633
申请日：2013-08-01
发明人： Gunther Schmidt , Helmut Fritz , Stefanie Walter
CPC分类号： C07C4/04 , C10G9/36 , C10G2400/20
摘要： The invention relates to a process for converting feeds composed of hydrocarbons by thermal steamcracking to at least one olefin-containing product stream comprising at least ethylene and propylene, with at least partial conversion of the feeds in at least one first cracking furnace (1) and in at least one second cracking furnace (2). According to the invention, a fresh feed (B) is fractionated into at least one first and one second fresh feed fraction (B1, B2), and the first fresh feed fraction (B1) is conducted at least partly into the first cracking furnace (1) and the second fresh feed fraction (B2) at least partly into the second cracking furnace (2).
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公开(公告)号：US10344226B2
公开(公告)日：2019-07-09
申请号：US14440704
申请日：2013-11-07
发明人： Gunther Schmidt , Boris Banovsky , Stefanie Walter
摘要： A process for preparing olefinic products by thermal steam cracking of a first furnace feed composed of hydrocarbons in at least one first cracking furnace and of a second furnace feed composed of hydrocarbons in at least one second cracking furnace. The first furnace feed is at least partly converted into a first product stream in the first cracking furnace and the second furnace feed is at least partly converted into a second product stream in the second cracking furnace. A first pyrolysis oil is isolated from the first product stream and is at least partly treated chemically. The first pyrolysis oil is at least partly recirculated as furnace feed from downstream of the chemical treatment to the first cracking furnace. The first cracking furnace and the second cracking furnace are operated under different cracking conditions.
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5.发明授权公开(公告)号：US09505679B2
公开(公告)日：2016-11-29
申请号：US14420630
申请日：2013-08-06
发明人： Helmut Fritz , Stefanie Walter , Gunther Schmidt
CPC分类号： C07C4/04 , C10G9/36 , C10G2400/20
摘要： The invention relates to a process for converting hydrocarbon feeds by thermal steamcracking to at least one olefin-containing product stream comprising at least ethylene and propylene, with at least partial conversion of a first hydrocarbon feed in at least one first cracking furnace (1) and of a second hydrocarbon feed in at least one second cracking furnace (2). According to the invention, the second hydrocarbon feed is converted in the second cracking furnace (2) with cracking conditions that lead to a ratio of propylene to ethylene of 0.7 to 1.6 kg/kg, and the first hydrocarbon feed is converted in the first cracking furnace (1) with cracking conditions that lead to a ratio of propylene to ethylene of 0.25 to 0.85 kg/kg at the cracking furnace exit, the value for the ratio of propylene to ethylene for the second hydrocarbon feed being above the value for the ratio of propylene to ethylene for the first hydrocarbon feed.
摘要翻译： 本发明涉及一种通过热蒸汽裂化将烃进料转化成至少一种至少包含乙烯和丙烯的含烯烃产物流，至少部分转化至少一个第一裂解炉（1）中的第一烃进料和 的第二烃进料在至少一个第二裂解炉（2）中。 根据本发明，第二烃进料在第二裂解炉（2）中被转化为具有导致丙烯与乙烯的比例为0.7至1.6kg / kg的裂化条件，并且第一烃进料在第一裂化 炉子（1）具有在裂解炉出口处导致丙烯与乙烯的比例为0.25至0.85kg / kg的裂化条件，第二烃进料的丙烯与乙烯的比值高于比率值 的丙烯至乙烯用于第一烃进料。
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公开(公告)号：US20160194259A1
公开(公告)日：2016-07-07
申请号：US14916161
申请日：2014-09-03
发明人： Stefanie Walter , Helmut Fritz , Gunther Schmidt
CPC分类号： C07C4/04 , C07C5/03 , C07C5/13 , C07C5/333 , C07C7/14891 , C07C41/06 , C07C41/34 , C10G9/36 , C10G45/58 , C10G65/04 , C10G69/06 , C10G70/041 , C10G2300/104 , C10G2300/20 , C10G2300/4081 , C07C11/167 , C07C11/08
摘要： The invention relates to a method for producing hydrocarbon products which comprises preparing a hydrocarbon stream (C4) which predominantly comprises branched and unbranched hydrocarbons each having four carbon atoms. A first and a second partial stream (i-C4, n-C4) are obtained from this stream (C4), the first partial stream (i-C4) predominantly comprising branched hydrocarbons with four carbon atoms and the second partial stream (n-C4) predominantly comprising unbranched hydrocarbons with four carbon atoms. The method further comprises the steam cracking of at least part of the first partial stream (i-C4) at a first, higher cracking severity and at least part of the second partial stream (n-C4), at a second, lower, cracking severity.
摘要翻译： 本发明涉及一种用于生产烃产物的方法，其包括制备主要包含具有四个碳原子的支链和非支链烃的烃流（C 4）。 从该流（C4）获得第一和第二部分流（i-C4，n-C4），主要包含具有四个碳原子的支链烃的第一部分流（i-C4）和第二部分流 C4）主要包含具有四个碳原子的无支链烃。 该方法还包括在第一较高裂化强度下至少部分第一部分流（i-C4）和至少部分第二部分流（n-C4）的蒸汽裂化，在第二较低裂化 严重程度
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7.发明申请公开(公告)号：US20150218065A1
公开(公告)日：2015-08-06
申请号：US14420630
申请日：2013-08-06
发明人： Helmut Fritz , Stefanie Walter , Gunther Schmidt
IPC分类号： C07C4/04
CPC分类号： C07C4/04 , C10G9/36 , C10G2400/20
摘要： The invention relates to a process for converting hydrocarbon feeds by thermal steamcracking to at least one olefin-containing product stream comprising at least ethylene and propylene, with at least partial conversion of a first hydrocarbon feed in at least one first cracking furnace (1) and of a second hydrocarbon feed in at least one second cracking furnace (2). According to the invention, the second hydrocarbon feed is converted in the second cracking furnace (2) with cracking conditions that lead to a ratio of propylene to ethylene of 0.7 to 1.6 kg/kg, and the first hydrocarbon feed is converted in the first cracking furnace (1) with cracking conditions that lead to a ratio of propylene to ethylene of 0.25 to 0.85 kg/kg at the cracking furnace exit, the value for the ratio of propylene to ethylene for the second hydrocarbon feed being above the value for the ratio of propylene to ethylene for the first hydrocarbon feed.
摘要翻译： 本发明涉及一种通过热蒸汽裂化将烃进料转化成至少一种至少包含乙烯和丙烯的含烯烃产物流，至少部分转化至少一个第一裂解炉（1）中的第一烃进料和 的第二烃进料在至少一个第二裂解炉（2）中。 根据本发明，第二烃进料在第二裂解炉（2）中被转化为具有导致丙烯与乙烯的比例为0.7至1.6kg / kg的裂化条件，并且第一烃进料在第一裂化 炉子（1）具有在裂解炉出口处导致丙烯与乙烯的比例为0.25至0.85kg / kg的裂化条件，第二烃进料的丙烯与乙烯的比值高于比率值 的丙烯至乙烯用于第一烃进料。
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公开(公告)号：US09670418B2
公开(公告)日：2017-06-06
申请号：US14420636
申请日：2013-08-06
发明人： Gunther Schmidt , Helmut Fritz , Stefanie Walter
IPC分类号： C10G9/36
CPC分类号： C10G9/36 , C10G2400/20
摘要： The invention relates to a process for converting hydrocarbon inputs by thermal steamcracking to give at least one olefin-containing product stream comprising at least ethylene and propylene, by at least partly converting a hydrocarbon input in at least one cracking furnace (2), wherein the hydrocarbon input is converted under mild cracking conditions in the cracking furnace (2), mild cracking conditions meaning that propylene to ethylene are present in a ratio of 0.81 to 1.6 kg/kg at the cracking furnace exit, and the hydrocarbon input comprising predominantly hydrocarbons having a maximum carbon number of 6, preferably a maximum of 5.
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公开(公告)号：US20160194258A1
公开(公告)日：2016-07-07
申请号：US14916157
申请日：2014-09-04
发明人： Stefanie Walter , Helmut Fritz
CPC分类号： C07C4/04 , C07C5/03 , C07C5/13 , C07C5/25 , C07C5/2767 , C07C41/09 , C07C41/34 , C10G9/36 , C10G45/58 , C10G65/04 , C10G69/06 , C10G70/041 , C10G2300/104 , C10G2300/20 , C10G2300/4081 , C07C11/08
摘要： A method for producing hydrocarbon products is proposed which comprises providing a C4 hydrocarbon stream (C4) that predominantly comprises branched and unbranched hydrocarbons each having four carbon atoms, and an n-C4 partial stream (n-C4), which predominantly comprises unbranched hydrocarbons with four carbon atoms and an iso-C4 partial stream (i-C4) which predominantly comprises branched hydrocarbons with four carbon atoms, from the C4 hydrocarbon stream (C4) or a stream derived therefrom. It is envisaged that at least part of the n-C4 partial stream (n-C4) or a stream derived therefrom should be cracked at a cracking severity at which not more than 92% of n-butane contained in the n-C4 partial stream (n-C4) or in the derived stream is converted.
摘要翻译： 提出了一种生产烃产物的方法，其包括提供主要包含具有四个碳原子的支链和非支链烃的C 4烃流（C 4）和主要包含未分支烃的n-C4部分流（n-C4） 四个碳原子和主要包含具有四个碳原子的支链烃，来自C4烃流（C4）或由其衍生的物流的异C4部分流（i-C4）。 设想至少部分n-C4部分流（n-C4）或由其衍生的流应在破坏严重性下破裂，其中在n-C4部分流中包含不超过92％的正丁烷 （n-C4）或在衍生流中转化。
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公开(公告)号：US20150315484A1
公开(公告)日：2015-11-05
申请号：US14420636
申请日：2013-08-06
发明人： Gunther Schmidt , Helmut Fritz , Stefanie Walter
IPC分类号： C10G9/36
CPC分类号： C10G9/36 , C10G2400/20
摘要： The invention relates to a process for converting hydrocarbon inputs by thermal steamcracking to give at least one olefin-containing product stream comprising at least ethylene and propylene, by at least partly converting a hydrocarbon input in at least one cracking furnace (2), wherein the hydrocarbon input is converted under mild cracking conditions in the cracking furnace (2), mild cracking conditions meaning that propylene to ethylene are present in a ratio of 0.81 to 1.6 kg/kg at the cracking furnace exit, and the hydrocarbon input comprising predominantly hydrocarbons having a maximum carbon number of 6, preferably a maximum of 5.
摘要翻译： 本发明涉及一种通过热蒸汽裂化转化烃输入的方法，以至少部分地转化至少一个裂解炉（2）中的烃输入，从而产生至少一种至少包含乙烯和丙烯的含烯烃产物流，其中 碳氢化合物输入在裂解炉（2）中的轻度裂解条件下转化，温和的裂解条件意味着丙烯与乙烯在裂化炉出口处以0.81至1.6kg / kg的比率存在，并且主要包含烃的烃输入物具有 最大碳数为6，最好为5。
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