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公开(公告)号:US06897347B2
公开(公告)日:2005-05-24
申请号:US10134475
申请日:2002-04-30
申请人: Veli-Matti Purola , Sami Toppinen , Antti Pyhälahti , Marina Lindblad , Johan Grönqvist , Pirjo Siira
发明人: Veli-Matti Purola , Sami Toppinen , Antti Pyhälahti , Marina Lindblad , Johan Grönqvist , Pirjo Siira
CPC分类号: C07C2/28 , C07C2531/10 , Y02P20/127
摘要: The invention relates to a method for dimerizing isobutene, wherein, in dimerizing conditions, the isobutene is brought into contact with a porous cation exchange resin comprising a styrene polymer, which is cross-linked with divinyl benzene, and any sulphonic acid groups adhering to the polymer. The harmful deactivation of this catalyst, which is caused by the accumulation of the oligomers and polymers of isobutene and other C4-olefins in the cation exchange resin catalyst, is essentially decreased by selecting the cation exchange resin from a group including cation exchange resins, the acid capacity of which is 4.7 equivalents/kg at a minimum, and the portion of divinyl benzene units of which is 5% by weight at a minimum and smaller than 20% by weight.
摘要翻译: 本发明涉及异丁烯二聚的方法,其中在二聚条件下,使异丁烯与包含与二乙烯基苯交联的苯乙烯聚合物的多孔阳离子交换树脂和与二乙烯基苯粘合的任何磺酸基团接触 聚合物。 由阳离子交换树脂催化剂中异丁烯和其它C 4 - 烯烃的低聚物和聚合物的积聚引起的该催化剂的有害失活通过从阳离子交换树脂催化剂中选择阳离子交换树脂 包含阳离子交换树脂的基团,其酸容量最小为4.7当量/ kg,二乙烯基苯单元的部分最小为5重量%且小于20重量%。
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公开(公告)号:US08212094B2
公开(公告)日:2012-07-03
申请号:US13107146
申请日:2011-05-13
申请人: Jukka Myllyoja , Pekka Aalto , Pekka Savolainen , Veli-Matti Purola , Ville Alopaeus , Johan Grönqvist
发明人: Jukka Myllyoja , Pekka Aalto , Pekka Savolainen , Veli-Matti Purola , Ville Alopaeus , Johan Grönqvist
IPC分类号: C07C1/00
CPC分类号: C10G3/50 , C07C1/24 , C07C5/03 , C07C5/2775 , C07C7/10 , C07C7/12 , C07C7/13 , C07C2529/076 , C10G3/46 , C10G3/47 , C10G45/02 , C10G45/58 , C10G45/62 , C10G45/64 , C10G65/043 , C10G2300/1011 , C10G2300/1014 , C10G2300/1018 , C10G2300/202 , C10G2300/205 , C10G2300/207 , C10G2300/4006 , C10G2300/4081 , C10G2300/802 , C10G2400/04 , C10L1/08 , Y02E50/13 , Y02P30/20
摘要: The invention relates to a process for the manufacture of diesel range hydrocarbons wherein a feed is hydrotreated in a hydrotreating step and isomerized in an isomerization step, and a feed comprising fresh feed containing more than 5 wt % of free fatty acids and at least one diluting agent is hydrotreated at a reaction temperature of 200-400° C., in a hydrotreating reactor in the presence of catalyst, and the ratio of the diluting agent/fresh feed is 5-30:1.
摘要翻译: 本发明涉及一种用于制造柴油范围烃的方法,其中将进料在加氢处理步骤中加氢处理并在异构化步骤中异构化,以及包含含有大于5重量%游离脂肪酸和至少一个稀释的新鲜原料的进料 在催化剂存在下,在加氢处理反应器中,在200-400℃的反应温度下加氢处理试剂,稀释剂/新鲜进料的比例为5-30:1。
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公开(公告)号:US08859832B2
公开(公告)日:2014-10-14
申请号:US13491182
申请日:2012-06-07
申请人: Jukka Myllyoja , Pekka Aalto , Pekka Savolainen , Veli-Matti Purola , Ville Alopaeus , Johan Grönqvist
发明人: Jukka Myllyoja , Pekka Aalto , Pekka Savolainen , Veli-Matti Purola , Ville Alopaeus , Johan Grönqvist
CPC分类号: C10G3/50 , C07C1/24 , C07C5/03 , C07C5/2775 , C07C7/10 , C07C7/12 , C07C7/13 , C07C2529/076 , C10G3/46 , C10G3/47 , C10G45/02 , C10G45/58 , C10G45/62 , C10G45/64 , C10G65/043 , C10G2300/1011 , C10G2300/1014 , C10G2300/1018 , C10G2300/202 , C10G2300/205 , C10G2300/207 , C10G2300/4006 , C10G2300/4081 , C10G2300/802 , C10G2400/04 , C10L1/08 , Y02E50/13 , Y02P30/20
摘要: The invention relates to a process for the manufacture of diesel range hydrocarbons wherein a feed is hydrotreated in a hydrotreating step and isomerized in an isomerization step, and a feed comprising fresh feed containing more than 5 wt % of free fatty acids and at least one diluting agent is hydrotreated at a reaction temperature of 200-400° C., in a hydrotreating reactor in the presence of catalyst, and the ratio of the diluting agent/fresh feed is 5-30:1.
摘要翻译: 本发明涉及一种用于制造柴油范围烃的方法,其中将进料在加氢处理步骤中加氢处理并在异构化步骤中异构化,以及包含含有大于5重量%游离脂肪酸和至少一个稀释的新鲜原料的进料 在催化剂存在下,在加氢处理反应器中,在200-400℃的反应温度下加氢处理试剂,稀释剂/新鲜进料的比例为5-30:1。
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公开(公告)号:US08022258B2
公开(公告)日:2011-09-20
申请号:US11477922
申请日:2006-06-30
申请人: Jukka Myllyoja , Pekka Aalto , Pekka Savolainen , Veli-Matti Purola , Ville Alopaeus , Johan Grönqvist
发明人: Jukka Myllyoja , Pekka Aalto , Pekka Savolainen , Veli-Matti Purola , Ville Alopaeus , Johan Grönqvist
IPC分类号: C07C1/00
CPC分类号: C10G3/50 , C07C1/24 , C07C5/03 , C07C5/2775 , C07C7/10 , C07C7/12 , C07C7/13 , C07C2529/076 , C10G3/46 , C10G3/47 , C10G45/02 , C10G45/58 , C10G45/62 , C10G45/64 , C10G65/043 , C10G2300/1011 , C10G2300/1014 , C10G2300/1018 , C10G2300/202 , C10G2300/205 , C10G2300/207 , C10G2300/4006 , C10G2300/4081 , C10G2300/802 , C10G2400/04 , C10L1/08 , Y02E50/13 , Y02P30/20
摘要: The invention relates to a process for the manufacture of diesel range hydrocarbons wherein a feed is hydrotreated in a hydrotreating step and isomerised in an isomerisation step, and a feed comprising fresh feed containing more than 5 wt % of free fatty acids and at least one diluting agent is hydrotreated at a reaction temperature of 200-400° C., in a hydrotreating reactor in the presence of catalyst, and the ratio of the diluting agent/fresh feed is 5-30:1.
摘要翻译: 本发明涉及一种用于制造柴油范围烃的方法,其中进料在加氢处理步骤中加氢处理并在异构化步骤中异构化,并且包含含有大于5重量%游离脂肪酸和至少一个稀释的新鲜原料的进料 在催化剂存在下,在加氢处理反应器中,在200-400℃的反应温度下加氢处理试剂,稀释剂/新鲜进料的比例为5-30:1。
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公开(公告)号:US20130030229A1
公开(公告)日:2013-01-31
申请号:US13491182
申请日:2012-06-07
申请人: Jukka Myllyoja , Pekka Aalto , Pekka Savolainen , Veli-Matti Purola , Ville Alopaeus , Johan Grönqvist
发明人: Jukka Myllyoja , Pekka Aalto , Pekka Savolainen , Veli-Matti Purola , Ville Alopaeus , Johan Grönqvist
IPC分类号: C10G3/00
CPC分类号: C10G3/50 , C07C1/24 , C07C5/03 , C07C5/2775 , C07C7/10 , C07C7/12 , C07C7/13 , C07C2529/076 , C10G3/46 , C10G3/47 , C10G45/02 , C10G45/58 , C10G45/62 , C10G45/64 , C10G65/043 , C10G2300/1011 , C10G2300/1014 , C10G2300/1018 , C10G2300/202 , C10G2300/205 , C10G2300/207 , C10G2300/4006 , C10G2300/4081 , C10G2300/802 , C10G2400/04 , C10L1/08 , Y02E50/13 , Y02P30/20
摘要: The invention relates to a process for the manufacture of diesel range hydrocarbons wherein a feed is hydrotreated in a hydrotreating step and isomerised in an isomerisation step, and a feed comprising fresh feed containing more than 5 wt % of free fatty acids and at least one diluting agent is hydrotreated at a reaction temperature of 200-400° C., in a hydrotreating reactor in the presence of catalyst, and the ratio of the diluting agent/fresh feed is 5-30:1.
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公开(公告)号:US20110282116A1
公开(公告)日:2011-11-17
申请号:US13107146
申请日:2011-05-13
申请人: Jukka MYLLYOJA , Pekka AALTO , Pekka SAVOLAINEN , Veli-Matti PUROLA , Ville ALOPAEUS , Johan GRÖNQVIST
发明人: Jukka MYLLYOJA , Pekka AALTO , Pekka SAVOLAINEN , Veli-Matti PUROLA , Ville ALOPAEUS , Johan GRÖNQVIST
IPC分类号: C10G69/14
CPC分类号: C10G3/50 , C07C1/24 , C07C5/03 , C07C5/2775 , C07C7/10 , C07C7/12 , C07C7/13 , C07C2529/076 , C10G3/46 , C10G3/47 , C10G45/02 , C10G45/58 , C10G45/62 , C10G45/64 , C10G65/043 , C10G2300/1011 , C10G2300/1014 , C10G2300/1018 , C10G2300/202 , C10G2300/205 , C10G2300/207 , C10G2300/4006 , C10G2300/4081 , C10G2300/802 , C10G2400/04 , C10L1/08 , Y02E50/13 , Y02P30/20
摘要: The invention relates to a process for the manufacture of diesel range hydrocarbons wherein a feed is hydrotreated in a hydrotreating step and isomerised in an isomerisation step, and a feed comprising fresh feed containing more than 5 wt % of free fatty acids and at least one diluting agent is hydrotreated at a reaction temperature of 200-400° C., in a hydrotreating reactor in the presence of catalyst, and the ratio of the diluting agent/fresh feed is 5-30:1.
摘要翻译: 本发明涉及一种用于制造柴油范围烃的方法,其中进料在加氢处理步骤中加氢处理并在异构化步骤中异构化,并且包含含有大于5重量%游离脂肪酸和至少一个稀释的新鲜原料的进料 在催化剂存在下,在加氢处理反应器中,在200-400℃的反应温度下加氢处理试剂,稀释剂/新鲜进料的比例为5-30:1。
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