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公开(公告)号:US07232935B2
公开(公告)日:2007-06-19
申请号:US10655533
申请日:2003-09-05
申请人: Juha Jakkula , Vesa Niemi , Jouko Nikkonen , Veli-Matti Purola , Jukka Myllyoja , Pekka Aalto , Juha Lehtonen , Ville Alopaeus
发明人: Juha Jakkula , Vesa Niemi , Jouko Nikkonen , Veli-Matti Purola , Jukka Myllyoja , Pekka Aalto , Juha Lehtonen , Ville Alopaeus
IPC分类号: C07C1/20
CPC分类号: C10G3/45 , C10G3/46 , C10G3/47 , C10G3/48 , C10G3/50 , C10G2300/1014 , C10G2300/1018 , C10G2300/1037 , C10G2300/4081 , C10G2400/04 , Y02P30/20
摘要: The invention relates to a process for producing a hydrocarbon component of biological origin. The process comprises at least two steps, the first one of which is a HDO step and the second one is an isomerization step operated using the counter-current flow principle. A biological raw material containing fatty acids and/or fatty acid esters serves as the feed stock.
摘要翻译: 本发明涉及一种用于生产生物来源的烃组分的方法。 该方法包括至少两个步骤,其中第一步是HDO步骤,第二步是使用逆流原理操作的异构化步骤。 含有脂肪酸和/或脂肪酸酯的生物原料用作原料。
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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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公开(公告)号:US20110015459A1
公开(公告)日:2011-01-20
申请号:US12837627
申请日:2010-07-16
IPC分类号: C07C1/207
CPC分类号: C10G47/16 , C10G3/45 , C10G3/46 , C10G3/47 , C10G3/49 , C10G3/50 , C10G45/02 , C10G45/12 , C10G45/58 , C10G45/64 , C10G47/00 , C10G65/043 , C10G65/12 , C10G2300/1011 , C10G2300/4018 , C10G2400/02 , C10G2400/28 , Y02P30/20
摘要: In the process of the invention, an aliphatic C2-C14 hydrocarbon product is prepared from natural fats or derivatives thereof. The process comprises the steps of: (i) providing a natural fat or derivative thereof, (ii) deoxygenating a natural fat or derivative thereof originating from step (i) to yield an aliphatic C9-C28 hydrocarbon, (iii) hydrocracking an aliphatic C9-C28 hydrocarbon originating from step (ii) to yield a product comprising an aliphatic C2-C14 hydrocarbon, (iv) isomerising an aliphatic C2-C14 hydrocarbon originating from step (iii) into an isomerised aliphatic C2-C14 hydrocarbon, and optionally (v) recovering an isomerised C2-C14 hydrocarbon originating from step (iv) as said C2-C14 hydrocarbon product. Pure and high quality light fuel is easily obtained in sufficient amounts.
摘要翻译: 在本发明的方法中,由天然脂肪或其衍生物制备脂族C 2 -C 14烃产物。 该方法包括以下步骤:(i)提供天然脂肪或其衍生物,(ii)脱氧源自步骤(i)的天然脂肪或其衍生物以产生脂族C 9 -C 28烃,(iii)加氢裂化脂族C 9 来源于步骤(ii)的-C28烃产生包含脂族C 2 -C 14烃的产物,(iv)将由步骤(iii)衍生的脂族C 2 -C 14烃异构化成异构化的脂族C 2 -C 14烃,和任选地(v )从所述C2-C14烃产物回收源自步骤(iv)的异构化的C 2 -C 14烃。 能够容易地获得纯净和高质量的轻质燃料。
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公开(公告)号:US09005429B2
公开(公告)日:2015-04-14
申请号:US12495263
申请日:2009-06-30
申请人: Varpu Markkanen , Petri Lindqvist , Elina Harlin , Pekka Aalto , Jukka Myllyoja , Ville Alopaeus
发明人: Varpu Markkanen , Petri Lindqvist , Elina Harlin , Pekka Aalto , Jukka Myllyoja , Ville Alopaeus
CPC分类号: C10G65/043 , C10G3/46 , C10G3/50 , C10G45/64 , C10G2300/1014 , C10G2300/1018 , C10G2300/1055 , C10G2300/4081 , C10G2400/02 , C10G2400/04 , C10G2400/08 , Y02P30/20
摘要: The present invention relates to hydrocarbons and particularly to the manufacture of hydrocarbon components suitable as aviation fuels or jet fuels and as blending stocks for aviation fuels. The process comprises the stages, wherein in the first stage an oil feed of biological origin and hydrogen gas are subjected to conditions sufficient to effect hydrodeoxygenation in the presence of a hydrodeoxygenation catalyst to yield n-paraffins; in the second stage the n-paraffins and hydrogen gas are subjected to conditions sufficient to effect isomerization in the presence of an isomerization catalyst to yield isoparaffins and separating fractions; and recycling the fraction boiling at a temperature above 200° C. under atmospheric pressure obtained from the second stage to reisomerization, where isomerization is effected in the presence of an isomerization catalyst.
摘要翻译: 本发明涉及碳氢化合物,特别涉及适用于航空燃料或喷气燃料的烃类组分的制造以及用于航空燃料的混合原料。 该方法包括以下阶段,其中在第一阶段中,在加氢脱氧催化剂存在下,生物来源和氢气的进料经受足以进行加氢脱氧的条件以产生正链烷烃; 在第二阶段中,正链烷烃和氢气在异构化催化剂存在下进行足以实现异构化的条件,得到异链烷烃和分离馏分; 并将在第二阶段获得的大气压下在高于200℃的温度下沸腾的馏分再循环进行再异构化,其中异构化在异构化催化剂存在下进行。
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公开(公告)号:US08592638B2
公开(公告)日:2013-11-26
申请号:US12837627
申请日:2010-07-16
CPC分类号: C10G47/16 , C10G3/45 , C10G3/46 , C10G3/47 , C10G3/49 , C10G3/50 , C10G45/02 , C10G45/12 , C10G45/58 , C10G45/64 , C10G47/00 , C10G65/043 , C10G65/12 , C10G2300/1011 , C10G2300/4018 , C10G2400/02 , C10G2400/28 , Y02P30/20
摘要: In the process of the invention, an aliphatic C2-C14 hydrocarbon product is prepared from natural fats or derivatives thereof. The process comprises the steps of: (i) providing a natural fat or derivative thereof, (ii) deoxygenating a natural fat or derivative thereof originating from step (i) to yield an aliphatic C9-C28 hydrocarbon, (iii) hydrocracking an aliphatic C9-C28 hydrocarbon originating from step (ii) to yield a product comprising an aliphatic C2-C14 hydrocarbon, (iv) isomerising an aliphatic C2-C14 hydrocarbon originating from step (iii) into an isomerised aliphatic C2-C14 hydrocarbon, and optionally (v) recovering an isomerised C2-C14 hydrocarbon originating from step (iv) as said C2-C14 hydrocarbon product. Pure and high quality light fuel is easily obtained in sufficient amounts.
摘要翻译: 在本发明的方法中,由天然脂肪或其衍生物制备脂族C 2 -C 14烃产物。 该方法包括以下步骤:(i)提供天然脂肪或其衍生物,(ii)脱氧源自步骤(i)的天然脂肪或其衍生物以产生脂族C 9 -C 28烃,(iii)加氢裂化脂族C 9 来源于步骤(ii)的-C28烃产生包含脂族C 2 -C 14烃的产物,(iv)将由步骤(iii)衍生的脂族C 2 -C 14烃异构化成异构化的脂族C 2 -C 14烃,和任选地(v )从所述C2-C14烃产物回收源自步骤(iv)的异构化的C 2 -C 14烃。 能够容易地获得纯净和高质量的轻质燃料。
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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:US20100000908A1
公开(公告)日:2010-01-07
申请号:US12495263
申请日:2009-06-30
申请人: Varpu Markkanen , Petri Lindqvist , Elina Harlin , Pekka Aalto , Jukka Myllyoja , Ville Alopaeus
发明人: Varpu Markkanen , Petri Lindqvist , Elina Harlin , Pekka Aalto , Jukka Myllyoja , Ville Alopaeus
IPC分类号: C10G65/02
CPC分类号: C10G65/043 , C10G3/46 , C10G3/50 , C10G45/64 , C10G2300/1014 , C10G2300/1018 , C10G2300/1055 , C10G2300/4081 , C10G2400/02 , C10G2400/04 , C10G2400/08 , Y02P30/20
摘要: The present invention relates to hydrocarbons and particularly to the manufacture of hydrocarbon components suitable as aviation fuels or jet fuels and as blending stocks for aviation fuels. The process comprises the stages, wherein in the first stage an oil feed of biological origin and hydrogen gas are subjected to conditions sufficient to effect hydrodeoxygenation in the presence of a hydrodeoxygenation catalyst to yield n-paraffins;in the second stage the n-paraffins and hydrogen gas are subjected to conditions sufficient to effect isomerisation in the presence of an isomerisation catalyst to yield isoparaffins and separating fractions; and recycling the fraction boiling at a temperature above 200° C. under atmospheric pressure obtained from the second stage to reisomerisation, where isomerisation is effected in the presence of an isomerisation catalyst.
摘要翻译: 本发明涉及碳氢化合物,特别涉及适用于航空燃料或喷气燃料的烃类组分的制造以及用于航空燃料的混合原料。 该方法包括以下阶段,其中在第一阶段中,在加氢脱氧催化剂存在下,生物来源和氢气的进料经受足以进行加氢脱氧的条件以产生正链烷烃; 在第二阶段中,正链烷烃和氢气经历足够的异构化反应在异构化催化剂存在下产生异链烷烃和分离级分的条件; 并将在第二阶段获得的大气压下在高于200℃的温度下沸腾的馏分再循环,其中异构化在异构化催化剂存在下进行。
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