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公开(公告)号:US09340734B2
公开(公告)日:2016-05-17
申请号:US13513385
申请日:2010-11-30
IPC分类号: C01B39/02 , C01B39/20 , C01B39/24 , C10G47/16 , B01J29/08 , B01J37/10 , B01J23/888 , B01J37/02 , B01J37/06 , C10G47/18 , C10G47/20
CPC分类号: C10G47/16 , B01J23/888 , B01J29/084 , B01J37/0201 , B01J37/0207 , B01J37/06 , B01J37/10 , B01J2029/081 , B01J2229/126 , B01J2229/16 , B01J2229/36 , B01J2229/37 , B01J2229/42 , C01B39/026 , C01B39/20 , C01B39/24 , C10G47/18 , C10G47/20
摘要: Disclosed is a process for the preparation of a faujasite zeolite. A starting zeolite of the faujasite structure having a silica to alumina ratio of from 4.5 to 6.5 and an alkali level of less than 1.5% wt is steam calcined to produce an intermediate zeolite. The intermediate zeolite is treated with an acidified solution having specificately defined characteristics.
摘要翻译: 公开了一种制备八面沸石的方法。 二氧化硅与氧化铝之比为4.5至6.5并且碱含量低于1.5重量%的八面沸石结构的起始沸石被蒸汽煅烧以产生中间沸石。 中间沸石用具有特定限定特征的酸化溶液处理。
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公开(公告)号:US09199228B2
公开(公告)日:2015-12-01
申请号:US13266713
申请日:2010-04-15
申请人: László Domokos , Cornelis Ouwehand
发明人: László Domokos , Cornelis Ouwehand
IPC分类号: B01J29/06 , B01J29/16 , B01J29/08 , B01J29/14 , B01J29/80 , C10G47/16 , C10G47/18 , C10G47/20 , B01J29/70 , B01J29/78 , B01J35/10
CPC分类号: B01J29/166 , B01J29/084 , B01J29/146 , B01J29/7007 , B01J29/7815 , B01J29/80 , B01J35/1038 , B01J35/1061 , B01J35/1085 , B01J37/0009 , B01J37/0201 , B01J2229/16 , B01J2229/18 , B01J2229/20 , B01J2229/40 , B01J2229/42 , C10G47/16 , C10G47/18 , C10G47/20 , C10G2300/70
摘要: Process of preparing a hydrocracking catalyst carrier comprising amorphous binder and zeolite Y, which process comprises subjecting zeolite Y having a silica to alumina molar ratio of at least 10 to calcination at a temperature of from 700 to 1000° C., hydrocracking catalyst carrier comprising amorphous binder and zeolite Y having a silica to alumina molar ratio of at least 10, the infrared spectrum of which catalyst has a peak at 3690 cm−1, substantially reduced peaks at 3630 cm−1 and 3565 cm−1 and no peak at 3600 cm−1, hydrocracking catalyst carrier comprising an amorphous binder and zeolite Y having a silica to alumina molar ratio of at least 10, which catalyst has an acidity as measured by exchange with perdeuterated benzene of at most 20 micro-mole/gram, hydrocracking catalyst derived from such carrier and hydrocracking process with the help of such catalyst.
摘要翻译: 制备包含无定形粘合剂和沸石Y的加氢裂化催化剂载体的方法,该方法包括将二氧化硅与氧化铝摩尔比至少为10的沸石Y在700至1000℃的温度下煅烧,加氢裂化催化剂载体包含非晶态 粘结剂和二氧化硅与氧化铝摩尔比至少为10的沸石Y,其催化剂在3690cm -1处具有峰值的红外光谱,在3630cm-1和3565cm -1处基本上减少的峰,在3600cm处没有峰 -1,包含无定形粘合剂的加氢裂化催化剂载体和二氧化硅与氧化铝摩尔比至少为10的沸石Y,该催化剂具有通过与每氘代苯交换至多20微摩尔/克的加氢裂化催化剂得到的酸度 从这种载体和加氢裂化过程中借助于这种催化剂。
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公开(公告)号:US08834710B2
公开(公告)日:2014-09-16
申请号:US12743477
申请日:2008-11-19
IPC分类号: B01J37/20 , C10G49/24 , C10G45/08 , B01J37/00 , B01J23/883
CPC分类号: C10G49/24 , B01J23/883 , B01J37/0045 , B01J37/20 , C10G45/08 , Y10S585/906 , Y10S585/951
摘要: A process for starting up a hydrotreating process using a bulk metal catalyst. The process comprises the steps of providing a hydrocarbon feed stream containing less than 100 ppmw nitrogen containing species; and adding a nitrogen-containing compound to the hydrocarbon feed stream followed by contacting the resulting feed stream with the bulk metal catalyst in the presence of hydrogen and a sulfur-containing species.
摘要翻译: 使用本体金属催化剂启动加氢处理工艺的方法。 该方法包括提供含有少于100ppmw含氮物质的烃进料流的步骤; 并向烃进料流中加入含氮化合物,随后在氢气和含硫物质的存在下使所得进料流与本体金属催化剂接触。
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公开(公告)号:US20130197290A1
公开(公告)日:2013-08-01
申请号:US13641710
申请日:2011-04-18
IPC分类号: B01J29/44
CPC分类号: B01J29/44 , B01J29/40 , B01J29/405 , B01J35/0006 , B01J35/002 , B01J35/023 , B01J35/10 , B01J35/1019 , B01J35/1042 , B01J37/0009 , B01J37/0207 , B01J37/04 , B01J37/08 , B01J37/30 , B01J2229/16 , B01J2229/186 , B01J2229/20 , B01J2229/32 , B01J2229/42 , C07C4/18 , C07C15/04 , C07C2529/40 , C07C2529/44 , C10G35/065 , C10G35/09 , C10G2300/1096 , C10G2400/30 , Y02P20/52
摘要: Process for preparing a catalyst support which process comprises a) mixing pentasil zeolite having a bulk silica to alumina molar ratio in the range of from 20 to 150 with water, a silica source and an alkali metal salt, b) extruding the mixture obtained in step (a), c) drying and calcining the extrudates obtained in step (b), d) subjecting the calcined extrudates obtained in step (c) to ion exchange to reduce the alkali metal content, and e) drying the extrudates obtained in step (d); process for preparing a catalyst by furthermore impregnating such support with platinum in an amount in the range of from 0.001 to 0.1 wt % and tin in an amount in the range of from 0.01 to 0.5 wt %, each on the basis of total catalyst; ethylbenzene dealkylation catalyst obtainable thereby and a process for dealkylation of ethylbenzene which process comprises contacting feedstock containing ethylbenzene with such catalyst.
摘要翻译: 制备催化剂载体的方法,该方法包括:a)将水分二氧化硅源和碱金属盐与本体二氧化硅与氧化铝摩尔比为20-150的pentasil沸石混合,b)将步骤 (a)中,c)干燥和煅烧步骤(b)中获得的挤出物,d)使步骤(c)中获得的煅烧挤出物进行离子交换以降低碱金属含量,和e)干燥步骤 d); 通过进一步用0.001至0.1重量%的量的铂浸渍这种载体并以0.01-0.5重量%的量,锡的总催化剂为基础,制备催化剂的方法; 乙苯脱烷基化催化剂和乙苯的脱烷基化方法,该方法包括使含有乙苯的原料与这种催化剂接触。
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公开(公告)号:US20120319322A1
公开(公告)日:2012-12-20
申请号:US13327395
申请日:2011-12-15
申请人: Rene Georges Ernst BARTHEL , Maria Johanna Wilhelmina VAN WIERINGEN , Leonardus Maria VAN DER SMAN , László DOMOKOS
发明人: Rene Georges Ernst BARTHEL , Maria Johanna Wilhelmina VAN WIERINGEN , Leonardus Maria VAN DER SMAN , László DOMOKOS
CPC分类号: B01J35/026 , B01J21/063 , B01J23/8892 , B01J35/1014 , B01J37/0009 , B01J37/0018 , B01J37/0072 , B01J37/08 , B29B9/06 , B29B9/10 , B29B9/12 , B29C48/04 , B29C48/05 , B29C48/06 , B29C48/12 , B29C48/13 , B29C48/131 , B29C48/30 , B29C48/3001 , B29C48/345 , B29C48/87 , B29K2105/251 , C10G2/32 , C10G2/50
摘要: A die is provided for extruding elongate particles suitable for use in catalysis. The die comprises a plurality of channels extending from an inlet to an outlet. From the inlet to the outlet each channel comprises a first section with a helical bore with a non-circular cross-section, and a second section with a cylindrical bore. The cylindrical bore of the second section which has a diameter equal or greater than that of the first section. The second section is at least twice as long as a diameter of the first section.
摘要翻译: 提供用于挤出适合用于催化的细长颗粒的模具。 模具包括从入口延伸到出口的多个通道。 从入口到出口,每个通道包括具有非圆形横截面的螺旋孔的第一部分和具有圆柱形孔的第二部分。 第二部分的圆柱形孔具有等于或大于第一部分直径的直径。 第二部分至少是第一部分直径的两倍。
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公开(公告)号:US20100217057A1
公开(公告)日:2010-08-26
申请号:US12677009
申请日:2008-09-10
申请人: László Domokos , Ralph Haswell , Hong-Xin Li
发明人: László Domokos , Ralph Haswell , Hong-Xin Li
CPC分类号: B01J29/46 , B01J29/40 , B01J29/405 , B01J29/44 , B01J37/0009 , B01J2229/16 , B01J2229/20 , B01J2229/42 , C01B39/38 , C01B39/40 , C07C4/18 , C07C2529/40 , C07C2529/42 , C07C2529/44 , C07C2529/46 , C07C2529/48 , Y02P20/52 , C07C15/08
摘要: A new configuration of ZSM-5 is provided whereby the crystals have a higher average silica to alumina ratio at the edges of each crystallite than in the centre as determined from a narrow slit line scan profile obtained from SEM/EDX or TEM/EDX elemental analysis. Such ZSM-5 crystals are obtained by a preparation process using L-tartaric acid. The new configuration ZSM-5 provides significantly reduced xylene losses in ethylbenzene dealkylation, especially when combined with silica as binder, and one or more hydrogenation metals selected from platinum, tin, lead, silver, copper, and nickel. Further advantages are found if used in combination with a small crystal size ZSM-5.
摘要翻译: 提供了一种ZSM-5的新结构,由此,从SEM / EDX或TEM / EDX元素分析得到的窄缝线扫描轮廓确定,晶体在每个微晶边缘处的平均二氧化硅与氧化铝之比高于中心 。 通过使用L-酒石酸的制备方法获得这样的ZSM-5晶体。 新配置ZSM-5在乙苯脱烷基化中显着降低二甲苯损失,特别是当与二氧化硅作为粘合剂组合时,以及一种或多种选自铂,锡,铅,银,铜和镍的氢化金属。 如果与小型晶体尺寸的ZSM-5结合使用,可以发现更多的优点。
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公开(公告)号:US10543479B2
公开(公告)日:2020-01-28
申请号:US13881070
申请日:2011-10-20
申请人: László Domokos , Laurent Georges Huve , Hermanus Jongkind , Aan Hendrik Klazinga , Marcello Stefano Rigutto
发明人: László Domokos , Laurent Georges Huve , Hermanus Jongkind , Aan Hendrik Klazinga , Marcello Stefano Rigutto
IPC分类号: B01J29/06 , B01J29/74 , B01J29/78 , B01J29/76 , B01J29/72 , B01J37/30 , B01J37/00 , B01J29/70 , B01J35/10 , B01J29/80 , B01J37/02 , C10G65/12
摘要: A hydrocarbon conversion catalyst composition which comprises ZSM-48 and/or EU-2 zeolite particles and refractory oxide binder essentially free of alumina in which the average aluminium concentration of the ZSM-48 and/or EU-2 zeolite particles is at least 1.3 times the aluminium concentration at the surface of the particles, processes for preparing such catalyst compositions and processes for converting hydrocarbon feedstock with the help of such compositions.
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公开(公告)号:US08835516B2
公开(公告)日:2014-09-16
申请号:US13327436
申请日:2011-12-15
申请人: Rene Georges Ernst Barthel , Maria Johanna Wilhelmina Van Wieringen , Leonardus Maria Van Der Sman , László Domokos
发明人: Rene Georges Ernst Barthel , Maria Johanna Wilhelmina Van Wieringen , Leonardus Maria Van Der Sman , László Domokos
IPC分类号: C07C27/00
CPC分类号: B29C47/30 , B01J21/063 , B01J23/75 , B01J23/8892 , B01J23/8913 , B01J35/026 , B01J35/1014 , B01J37/0018 , B29C47/0035 , B29K2105/251 , C10G2/33 , C10G2300/4006 , C10G2300/4012
摘要: A process for performing a Fischer Tropsch reaction comprising (a) providing syngas to a reactor, said reactor comprising catalyst particles that have been produced by extruding a paste using a die comprising a plurality of channels extending from an inlet to an outlet, wherein from the inlet to the outlet each channel comprises a first section with a helical bore with a non-circular cross-section, and a second section with a cylindrical bore which has a diameter equal or greater than that of the first section, wherein the second section is at least twice as long as a diameter of the first section; (b) providing the following process conditions in the reactor: a temperature from 125 to 350° C., and a pressure from 5 to 150 bar absolute, and a gaseous hourly space velocity from 500 to 10000 Nl/l/h; and (c) removing Fischer Tropsch product from the reactor.
摘要翻译: 一种用于进行费托反应的方法,包括(a)向反应器提供合成气,所述反应器包括通过使用包含从入口到出口延伸的多个通道的模头挤出浆料而制备的催化剂颗粒,其中从 每个通道的出口的入口包括具有非圆形横截面的螺旋孔的第一部分和具有等于或大于第一部分的直径的圆柱形孔的第二部分,其中第二部分是 是第一部分的直径的至少两倍; (b)在反应器中提供以下工艺条件:温度为125-350℃,绝对压力为5至150巴,气时空速为500至10000Nl / l / h; 和(c)从反应器中除去费 - 托产物。
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公开(公告)号:US08574542B2
公开(公告)日:2013-11-05
申请号:US12677009
申请日:2008-09-10
申请人: László Domokos , Ralph Haswell , Hong-Xin Li
发明人: László Domokos , Ralph Haswell , Hong-Xin Li
CPC分类号: B01J29/46 , B01J29/40 , B01J29/405 , B01J29/44 , B01J37/0009 , B01J2229/16 , B01J2229/20 , B01J2229/42 , C01B39/38 , C01B39/40 , C07C4/18 , C07C2529/40 , C07C2529/42 , C07C2529/44 , C07C2529/46 , C07C2529/48 , Y02P20/52 , C07C15/08
摘要: A new configuration of ZSM-5 is provided whereby the crystals have a higher average silica to alumina ratio at the edges of each crystallite than in the center as determined from a narrow slit line scan profile obtained from SEM/EDX or TEM/EDX elemental analysis. Such ZSM-5 crystals are obtained by a preparation process using L-tartaric acid. The new configuration ZSM-5 provides significantly reduced xylene losses in ethylbenzene dealkylation, especially when combined with silica as binder, and one or more hydrogenation metals selected from platinum, tin, lead, silver, copper, and nickel. Further advantages are found if used in combination with a small crystal size ZSM-5.
摘要翻译: 提供了一种ZSM-5的新结构,由此,从SEM / EDX或TEM / EDX元素分析得到的窄缝线扫描轮廓确定,晶体在每个微晶边缘处的平均二氧化硅与氧化铝之比高于中心 。 通过使用L-酒石酸的制备方法获得这样的ZSM-5晶体。 新配置ZSM-5在乙苯脱烷基化中显着降低二甲苯损失,特别是当与二氧化硅作为粘合剂组合时,以及一种或多种选自铂,锡,铅,银,铜和镍的氢化金属。 如果与小型晶体尺寸的ZSM-5结合使用,可以发现更多的优点。
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公开(公告)号:US20120055846A1
公开(公告)日:2012-03-08
申请号:US13266713
申请日:2010-04-15
申请人: László Domokos , Cornelis Ouwehand
发明人: László Domokos , Cornelis Ouwehand
CPC分类号: B01J29/166 , B01J29/084 , B01J29/146 , B01J29/7007 , B01J29/7815 , B01J29/80 , B01J35/1038 , B01J35/1061 , B01J35/1085 , B01J37/0009 , B01J37/0201 , B01J2229/16 , B01J2229/18 , B01J2229/20 , B01J2229/40 , B01J2229/42 , C10G47/16 , C10G47/18 , C10G47/20 , C10G2300/70
摘要: Process of preparing a hydrocracking catalyst carrier comprising amorphous binder and zeolite Y, which process comprises subjecting zeolite Y having a silica to alumina molar ratio of at least 10 to calcination at a temperature of from 700 to 1000° C., hydrocracking catalyst carrier comprising amorphous binder and zeolite Y having a silica to alumina molar ratio of at least 10, the infrared spectrum of which catalyst has a peak at 3690 cm−1, substantially reduced peaks at 3630 cm−1 and 3565 cm−1 and no peak at 3600 cm−1, hydrocracking catalyst carrier comprising an amorphous binder and zeolite Y having a silica to alumina molar ratio of at least 10, which catalyst has an acidity as measured by exchange with perdeuterated benzene of at most 20 micro-mole/gram, hydrocracking catalyst derived from such carrier and hydrocracking process with the help of such catalyst.
摘要翻译: 制备包含无定形粘合剂和沸石Y的加氢裂化催化剂载体的方法,该方法包括将二氧化硅与氧化铝摩尔比至少为10的沸石Y在700至1000℃的温度下煅烧,加氢裂化催化剂载体包含非晶态 粘结剂和二氧化硅与氧化铝摩尔比至少为10的沸石Y,其催化剂在3690cm -1处具有峰值的红外光谱,在3630cm-1和3565cm -1处基本上减少的峰,在3600cm处没有峰 -1,包含无定形粘合剂的加氢裂化催化剂载体和二氧化硅与氧化铝摩尔比至少为10的沸石Y,该催化剂具有通过与每氘代苯交换至多20微摩尔/克的加氢裂化催化剂得到的酸度 从这种载体和加氢裂化过程中借助于这种催化剂。
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