公开(公告)号：US20100076236A1

公开(公告)日：2010-03-25

申请号：US12527475

申请日：2008-02-20

申请人： Auke Antoinette Van Heuzen ,  Hans De Lang ,  Patrick Moureaux ,  Donald Reinalda ,  Marcello Stefano Rigutto

发明人： Auke Antoinette Van Heuzen ,  Hans De Lang ,  Patrick Moureaux ,  Donald Reinalda ,  Marcello Stefano Rigutto

IPC分类号： C07C1/20

CPC分类号： C10L1/08 ,  C10G3/46 ,  C10G3/49 ,  C10G3/50 ,  C10G2300/1014 ,  C10G2300/1018 ,  C10G2400/04 ,  C11C3/123 ,  Y02E50/13 ,  Y02P30/20

摘要： Process for producing paraffinic hydrocarbons, the process comprising the following steps: (a) contacting hydrogen and a feedstock comprising triglycerides, diglycerides, monoglycerides and/or fatty acids with a hydrogenation catalyst under hydro-deoxygenation conditions; and (b) contacting the whole effluent of step (a) with a hydroprocessing catalyst comprising sulphided Ni and sulphided W or Mo as hydrogenation components on a carrier comprising amorphous silica-alumina and/or a zeolitic compound under hydro-isomerisation conditions.

摘要翻译： 所述方法包括以下步骤：（a）在加氢脱氧条件下，使氢和包含甘油三酸酯，甘油二酯，甘油单酯和/或脂肪酸的原料与氢化催化剂接触; 和（b）在加氢异构化条件下，将包含硫化Ni和硫化W或Mo作为氢化组分的加氢处理催化剂与包含无定形二氧化硅 - 氧化铝和/或沸石化合物的载体接触。

公开(公告)号：US08912374B2

公开(公告)日：2014-12-16

申请号：US12527475

申请日：2008-02-20

申请人： Auke Antoinette Van Heuzen ,  Hans De Lang ,  Patrick Moureaux ,  Donald Reinalda ,  Marcello Stefano Rigutto

发明人： Auke Antoinette Van Heuzen ,  Hans De Lang ,  Patrick Moureaux ,  Donald Reinalda ,  Marcello Stefano Rigutto

IPC分类号： C07C1/00 ,  C10G3/00 ,  C10L1/08 ,  C11C3/12

CPC分类号： C10L1/08 ,  C10G3/46 ,  C10G3/49 ,  C10G3/50 ,  C10G2300/1014 ,  C10G2300/1018 ,  C10G2400/04 ,  C11C3/123 ,  Y02E50/13 ,  Y02P30/20

摘要： Process for producing paraffinic hydrocarbons, the process comprising the following steps: (a) contacting hydrogen and a feedstock comprising triglycerides, diglycerides, monoglycerides and/or fatty acids with a hydrogenation catalyst under hydrodeoxygenation conditions; and (b) contacting the whole effluent of step (a) with a hydroprocessing catalyst comprising sulphided Ni and sulphided W or Mo as hydrogenation components on a carrier comprising amorphous silica-alumina and/or a zeolitic compound under hydro-isomerization conditions.

摘要翻译： 用于生产链烷烃的方法，该方法包括以下步骤：（a）在加氢脱氧条件下使氢和包含甘油三酯，甘油二酯，甘油单酯和/或脂肪酸的原料与氢化催化剂接触; 和（b）在加氢异构化条件下，将包含硫化Ni和硫化W或Mo作为氢化组分的加氢处理催化剂与包含无定形二氧化硅 - 氧化铝和/或沸石化合物的载体接触，使步骤（a）的全部流出物接触。

公开(公告)号：US20110257447A1

公开(公告)日：2011-10-20

申请号：US12972134

申请日：2010-12-17

申请人： Carolina Botella-Franco ,  Hans De Lang ,  Lavanya Meesala ,  Argi Joachim Antonio Moppi ,  Colin John Schaverien

发明人： Carolina Botella-Franco ,  Hans De Lang ,  Lavanya Meesala ,  Argi Joachim Antonio Moppi ,  Colin John Schaverien

IPC分类号： C07C9/00 ,  C07C1/207

CPC分类号： C08H8/00 ,  C08B37/0003 ,  C08B37/0057 ,  C12P19/02 ,  Y02E50/17

摘要： A process for producing hydrocarbons from microbial lipids is provided by contacting a feed comprising microbial lipids with a hydrogenation catalyst and hydrogen at a temperature in the range of from 250 to 380° C. and a total pressure in the range of from 20 to 160 bar (absolute), to obtain an effluent comprising paraffinic hydrocarbons and water; optionally separating a liquid stream rich in paraffinic hydrocarbons from the effluent; contacting the paraffinic hydrocarbons in the liquid stream rich in paraffinic hydrocarbons or the effluent comprising paraffinic hydrocarbons by contacting hydrogen and the liquid stream with hydroisomerisation catalyst at a temperature in the range of from 280 to 450° C. and a total pressure in the range of from 20 to 160 bar (absolute); and separating at least one product fraction from the product stream obtained, wherein the hydrogenation catalyst and/or the hydroisomerisation catalyst comprises a sulfided hydrogenation catalyst.

摘要翻译： 通过使包含微生物脂质的进料与氢化催化剂和氢气在250-380℃的温度和约20至160巴的范围内的总压接触来提供从微生物脂质产生烃的方法 （绝对），以获得包含石蜡烃和水的流出物; 任选地从流出物中分离富含链烷烃的液体物流; 使富含链烷烃的液体物流中的链烷烃与包含链烷烃的流出物接触，通过使氢气和液体流与加氢异构化催化剂在280至450℃的温度范围内接触， 从20到160巴（绝对）; 并从所获得的产物流中分离出至少一种产物级分，其中氢化催化剂和/或加氢异构化催化剂包含硫化氢化催化剂。

公开(公告)号：US20110257446A1

公开(公告)日：2011-10-20

申请号：US12972120

申请日：2010-12-17

申请人： Carolina BOTELLA-FRANCO ,  Hans De Lang ,  Lavanya Meesala ,  Argi Joachim Antonio Moppi ,  Colin John Schaverien

发明人： Carolina BOTELLA-FRANCO ,  Hans De Lang ,  Lavanya Meesala ,  Argi Joachim Antonio Moppi ,  Colin John Schaverien

IPC分类号： C07C9/00 ,  C07C1/207

CPC分类号： C08H8/00 ,  C08B37/0003 ,  C08B37/0057 ,  C12P19/02 ,  Y02E50/17

摘要： A process for producing hydrocarbons from microbial lipids is provided by: contacting a feed comprising microbial lipids, wherein the microbial lipids comprise a triglyceride content in the range of from 40 wt % to 70 wt % and a free fatty acid content in the range of from 10 wt % to 30 wt %, with a hydrogenation catalyst and hydrogen at a temperature in the range of from 250 to 380° C. and a total pressure in the range of from 20 to 160 bar (absolute), to obtain an effluent comprising paraffinic hydrocarbons and water; optionally separating a liquid stream rich in paraffinic hydrocarbons from the effluent; contacting the paraffinic hydrocarbons in the liquid stream rich in paraffinic hydrocarbons or the effluent comprising paraffinic hydrocarbons by contacting hydrogen and the liquid stream with hydroisomerisation catalyst at a temperature in the range of from 280 to 450° C. and a total pressure in the range of from 20 to 160 bar (absolute); and separating at least one product fraction from the product stream.

摘要翻译： 通过以下步骤提供从微生物脂质产生烃的方法：使包含微生物脂质的饲料接触，其中微生物脂质包含40重量％至70重量％范围内的甘油三酯含量，并且游离脂肪酸含量范围为 10重量％至30重量％，加氢催化剂和氢气在250-380℃的范围内，总压力在20至160巴（绝对）范围内，以获得包含 石蜡烃和水; 任选地从流出物中分离富含链烷烃的液体物流; 使富含链烷烃的液体物流中的链烷烃与包含链烷烃的流出物接触，通过使氢气和液体流与加氢异构化催化剂在280至450℃的温度范围内接触， 从20到160巴（绝对）; 并从产物流中分离出至少一种产物级分。