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1. 发明申请

US20170145318A1 PROCESS FOR THE MANUFACTURE OF DIESEL RANGE HYDROCARBONS 审中-公开
公开(公告)号：US20170145318A1
公开(公告)日：2017-05-25
申请号：US15428080
申请日：2017-02-08
申请人： NESTE OIL OYJ
发明人： Jukka MYLLYOJA , Pekka AALTO , Pekka SAVOLAINEN , Veli-Matti PUROLA , Ville ALOPAEUS , Johan GRONQVIST
IPC分类号： C10G3/00 , C10G45/58
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.

2. 发明授权

US09533291B2 Method for production of hydrocarbons by increasing hydrocarbon chain length 有权
标题翻译：通过增加烃链长度来生产碳氢化合物的方法
公开(公告)号：US09533291B2
公开(公告)日：2017-01-03
申请号：US14375733
申请日：2012-11-01
申请人： Neste Oil Oyj
发明人： Jukka Myllyoja , Pekka Aalto , Rami Piilola
IPC分类号： C07C5/27 , C07C1/20 , C07C1/24 , C10G3/00 , B01J27/051 , C11C3/12 , C10L1/04 , B01J35/00 , B01J23/04 , B01J23/883 , C11C1/00 , C07C45/54 , C10M105/24 , B01D3/00 , B01J23/887 , C07C1/22 , C07C45/41 , C10M105/04 , C10M177/00 , B01J37/20 , B01J21/06
CPC分类号： B01J27/0515 , B01D3/009 , B01J21/063 , B01J23/04 , B01J23/883 , B01J23/8872 , B01J35/0006 , B01J37/20 , C07C1/22 , C07C1/24 , C07C5/2735 , C07C5/2737 , C07C45/41 , C07C45/54 , C07C2523/16 , C07C2523/42 , C07C2523/44 , C07C2523/46 , C07C2523/745 , C07C2523/75 , C07C2523/755 , C10G3/42 , C10G3/44 , C10G3/45 , C10G3/46 , C10L1/04 , C10L2200/0484 , C10M105/04 , C10M105/24 , C10M177/00 , C11C1/005 , C11C3/123 , Y02P30/20
摘要： The present invention provides a method for increasing hydrocarbon chain length. The method comprises providing a feedstock comprising fatty acids and/or fatty acid esters with hydrocarbon chain length below C23 into a reaction zone in which ketonization is conducted in the presence of a hydrotreatment catalyst under hydrogen pressure. The obtained ketones have a hydrocarbon chain length of from C24 to C43. The present invention further provides a method for simultaneous production of base oil components and fuel components.
摘要翻译：本发明提供了增加烃链长度的方法。该方法包括将烃链长度低于C23的脂肪酸和/或脂肪酸酯的原料提供到在氢气压力下在加氢处理催化剂存在下进行酮化的反应区。所得酮的烃链长度为C24至C43。本发明还提供了一种用于同时生产基础油组分和燃料组分的方法。

3. 发明申请

US20140042367A1 METHOD OF PURIFYING GAS STREAMS 有权
标题翻译：净化气流的方法
公开(公告)号：US20140042367A1
公开(公告)日：2014-02-13
申请号：US13962618
申请日：2013-08-08
申请人： Neste Oil Oyj
发明人： Juhani Aittamaa , Kari Keskinen , Jukka Keyriläinen
IPC分类号： C01B3/52
CPC分类号： C01B3/52 , B01D53/52 , B01D2251/50 , C01B2203/0485 , C10G3/50 , C10G70/006 , Y02P30/20
摘要： A method of purifying a gas stream formed from a process wherein a glyceride containing raw material is converted to hydrocarbon paraffins. The gas stream contains hydrogen or carbon dioxide as a major component and at least one sulphurous component selected from sulphide compounds as an impurity. The gas is contacted with an acidic aqueous wash solution of transition metal ions capable of binding to sulphide ions. A significant portion of the sulphide compounds contained in the gas are bound into practically insoluble transition metal sulphide compounds to remove sulphide compounds from the gas to produce a purified gas. The obtained purified gas is recovered. The method efficiently lowers sulphide concentrations to ppm or sub-ppm level and it can be implemented on an industrial scale with low investment costs. The metal can be recovered.
摘要翻译：一种纯化由其中含有甘油酯的原料转化为烃链烷烃的方法形成的气流的方法。气流含有作为主要成分的氢或二氧化碳和选自硫化物作为杂质的至少一种亚硫酸成分。气体与能够结合硫化物离子的过渡金属离子的酸性水溶液接触。包含在气体中的大部分硫化物化合物被结合到几乎不溶的过渡金属硫化物化合物中以从气体中除去硫化物以产生净化气体。回收得到的净化气体。该方法有效地将硫化物浓度降低到ppm或亚ppm水平，并且可以以低投资成本在工业规模上实施。金属可以回收。

4. 发明授权

US09598327B2 Process for the manufacture of diesel range hydrocarbons 有权
公开(公告)号：US09598327B2
公开(公告)日：2017-03-21
申请号：US14477758
申请日：2014-09-04
申请人： NESTE OIL OYJ
发明人： Jukka Myllyoja , Pekka Aalto , Pekka Savolainen , Veli-Matti Purola , Ville Alopaeus , Johan Gronqvist
IPC分类号： C07C1/24 , C10G45/02 , C10G3/00 , C10L1/08 , C10G45/62 , C10G45/64 , C10G45/58 , C10G65/04 , C07C5/03 , C07C5/27 , C07C7/10 , C07C7/12 , C07C7/13
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.

5. 发明申请

US20150251168A1 Simultaneous Production of Base Oil and Fuel Components from Renewable Feedstock 有权
公开(公告)号：US20150251168A1
公开(公告)日：2015-09-10
申请号：US14717107
申请日：2015-05-20
申请人： NESTE OIL OYJ
发明人： Mika Kettunen , Jukka Myllyoja , Rami Piilola , Goran Sandstrom , Pekka Aalto
IPC分类号： B01J27/051 , B01J23/883 , B01J23/04 , B01J35/00
CPC分类号： B01J27/0515 , B01D3/009 , B01J21/063 , B01J23/04 , B01J23/883 , B01J23/8872 , B01J35/0006 , B01J37/20 , C07C1/22 , C07C1/24 , C07C5/2735 , C07C5/2737 , C07C45/41 , C07C45/54 , C07C2523/16 , C07C2523/42 , C07C2523/44 , C07C2523/46 , C07C2523/745 , C07C2523/75 , C07C2523/755 , C10G3/42 , C10G3/44 , C10G3/45 , C10G3/46 , C10L1/04 , C10L2200/0484 , C10M105/04 , C10M105/24 , C10M177/00 , C11C1/005 , C11C3/123 , Y02P30/20
摘要： The present invention provides a method for simultaneous production of components suitable for production of base oil and fuel components. In the method a feedstock comprising fatty acids and/or fatty acid esters is entered into a reaction zone and subjected to a ketonisation reaction in the presence of a dual catalyst system. This system is configured to perform a ketonisation reaction and a hydrotreatment reaction, under hydrogen pressure. Subsequently ketones are obtained.

6. 发明授权

US09120713B2 Simultaneous production of base oil and fuel components from renewable feedstock 有权
标题翻译：从可再生原料同时生产基础油和燃料成分
公开(公告)号：US09120713B2
公开(公告)日：2015-09-01
申请号：US14375732
申请日：2012-11-01
申请人： Neste Oil Oyj
发明人： Mika Kettunen , Jukka Myllyoja , Rami Piilola , Goran Sandstrom , Pekka Aalto
IPC分类号： C07C45/41 , C07C1/22 , B01J23/00 , C07C1/24 , C11C3/12 , C10L1/04 , C10G3/00 , B01J23/883 , C11C1/00 , C07C45/54 , C10M105/24 , B01D3/00 , B01J23/887 , C07C5/27 , C10M105/04 , C10M177/00 , B01J37/20 , B01J35/00 , B01J21/06 , B01J23/04
CPC分类号： B01J27/0515 , B01D3/009 , B01J21/063 , B01J23/04 , B01J23/883 , B01J23/8872 , B01J35/0006 , B01J37/20 , C07C1/22 , C07C1/24 , C07C5/2735 , C07C5/2737 , C07C45/41 , C07C45/54 , C07C2523/16 , C07C2523/42 , C07C2523/44 , C07C2523/46 , C07C2523/745 , C07C2523/75 , C07C2523/755 , C10G3/42 , C10G3/44 , C10G3/45 , C10G3/46 , C10L1/04 , C10L2200/0484 , C10M105/04 , C10M105/24 , C10M177/00 , C11C1/005 , C11C3/123 , Y02P30/20
摘要： The present invention provides a method for simultaneous production of components suitable for production of base oil and fuel components. In the method a feedstock comprising fatty acids and/or fatty acid esters is entered into a reaction zone and subjected to a ketonization reaction in the presence of a dual catalyst system. This system is configured to perform a ketonization reaction and a hydrotreatment reaction, under hydrogen pressure. Subsequently ketones are obtained.
摘要翻译：本发明提供了一种用于同时生产适用于生产基础油和燃料组分的组分的方法。在该方法中，包含脂肪酸和/或脂肪酸酯的原料进入反应区并在双重催化剂体系的存在下进行酮化反应。该系统配置为在氢气压力下进行酮化反应和加氢处理反应。随后得到酮。

7. 发明申请

US20130072583A1 METHOD OF PRODUCING A HYDROCARBON COMPOSITION 审中-公开
标题翻译：生产油料组合物的方法
公开(公告)号：US20130072583A1
公开(公告)日：2013-03-21
申请号：US13675720
申请日：2012-11-13
申请人： Neste Oil Oyj
发明人： Jukka KOSKINEN , Jan Wahlström , Isto Eilos , Sebastian Johansson , Sami Toppinen , Marianne Pettersson
IPC分类号： C10G2/00
CPC分类号： C10G2/30 , C01B3/38 , C01B3/48 , C01B2203/0233 , C01B2203/0244 , C01B2203/0261 , C01B2203/0283 , C01B2203/0405 , C01B2203/0415 , C01B2203/043 , C01B2203/0475 , C01B2203/062 , C01B2203/1241 , C01B2203/147 , C01B2203/148 , C10G2300/1014 , C10G2300/1018 , C10G2300/1025 , C10G2300/4043 , C10G2300/42 , C10G2400/10 , C10J3/463 , C10J3/54 , C10J2300/0916 , C10J2300/0956 , C10J2300/0959 , C10J2300/0976 , C10J2300/0993 , C10J2300/0996 , C10J2300/1659 , C10K3/006 , C10K3/023 , C10K3/026 , Y02E50/32 , Y02P20/145 , Y02P20/146 , Y02P30/20 , Y02P30/446 , Y02T50/678
摘要： A method of producing a hydrocarbon composition, the method including providing a biomass raw-material; gasifying the raw-material in the presence of oxygen to produce a gas containing carbon monoxide, carbon dioxide, hydrogen and hydrocarbons possibly together with inert components; separately increasing the hydrogen-to-carbon monoxide ratio of the gas to a value of about 2; feeding the gas to a Fischer-Tropsch reactor; converting in the Fischer-Tropsch reactor at least a significant part of the carbon monoxide and hydrogen contained in the gas into a hydrocarbon composition containing C4-C90 hydrocarbons; and recovering the hydrocarbon composition. Fresh external hydrogen is introduced into the gas before feeding into the Fischer-Tropsch reactor. By using external hydrogen feed, the capacity of a biomass gasification process can be increased and any need for a Water Gas Shift for producing hydrogen from carbon monoxide and steam can be eliminated.
摘要翻译：一种生产烃组合物的方法，所述方法包括提供生物质原料; 在氧气存在下气化原料以产生含有一氧化碳，二氧化碳，氢气和烃的气体，可能与惰性组分一起; 分别将气体的氢气与一氧化碳的比率增加到约2的值; 将气体送入费 - 托反应器; 在费 - 托反应器中将包含在气体中的至少一部分一氧化碳和氢气转化成含C4-C90烃的烃组合物; 并回收烃组合物。在进入费 - 托反应器之前，将新鲜的外部氢气引入气体中。通过使用外部氢气进料，可以提高生物质气化过程的能力，并且可以消除从一氧化碳和蒸汽产生氢气的水煤气变换的任何需要。

8. 发明授权

US09545621B2 Dual catalyst system for performing a ketonisation reaction and a hydrotreatment reaction simultaneously 有权
标题翻译：用于同时进行酮化反应和加氢处理反应的双重催化剂体系
公开(公告)号：US09545621B2
公开(公告)日：2017-01-17
申请号：US14717107
申请日：2015-05-20
申请人： Neste Oil Oyj
发明人： Mika Kettunen , Jukka Myllyoja , Rami Piilola , Goran Sandstrom , Pekka Aalto
IPC分类号： C07C45/41 , B01J23/00 , B01J27/051 , C11C3/12 , C10L1/04 , C10G3/00 , B01J35/00 , B01J23/04 , B01J23/883 , C11C1/00 , C07C1/24 , C07C45/54 , C10M105/24 , B01D3/00 , B01J23/887 , C07C1/22 , C07C5/27 , C10M105/04 , C10M177/00 , B01J37/20 , B01J21/06
CPC分类号： B01J27/0515 , B01D3/009 , B01J21/063 , B01J23/04 , B01J23/883 , B01J23/8872 , B01J35/0006 , B01J37/20 , C07C1/22 , C07C1/24 , C07C5/2735 , C07C5/2737 , C07C45/41 , C07C45/54 , C07C2523/16 , C07C2523/42 , C07C2523/44 , C07C2523/46 , C07C2523/745 , C07C2523/75 , C07C2523/755 , C10G3/42 , C10G3/44 , C10G3/45 , C10G3/46 , C10L1/04 , C10L2200/0484 , C10M105/04 , C10M105/24 , C10M177/00 , C11C1/005 , C11C3/123 , Y02P30/20
摘要： The present invention provides a method for simultaneous production of components suitable for production of base oil and fuel components. In the method a feedstock comprising fatty acids and/or fatty acid esters is entered into a reaction zone and subjected to a ketonization reaction in the presence of a dual catalyst system. This system is configured to perform a ketonization reaction and a hydrotreatment reaction, under hydrogen pressure. Subsequently ketones are obtained.
摘要翻译：本发明提供了一种用于同时生产适用于生产基础油和燃料组分的组分的方法。在该方法中，包含脂肪酸和/或脂肪酸酯的原料进入反应区并在双重催化剂体系的存在下进行酮化反应。该系统配置为在氢气压力下进行酮化反应和加氢处理反应。随后得到酮。

9. 发明授权

US09469583B2 Composition comprising paraffin fractions obtained from biological raw materials and method of producing same 有权
$Composition comprising paraffin fractions obtained from biological raw materials and method of producing same$
标题翻译：包含由生物原料获得的石蜡馏分和其制备方法的组合物
公开(公告)号：US09469583B2
公开(公告)日：2016-10-18
申请号：US14147243
申请日：2014-01-03
申请人： Neste Oil Oyj
发明人： Pekka Aalto , Kati Sandberg , Tomi Nyman , Maija Hakola
IPC分类号： C07C6/00 , C07C7/05 , C10G3/00 , C10M105/00 , C10L1/04 , C07C9/14 , C07C1/22 , C09D7/00 , C10G45/58 , C10G65/04 , C10M177/00
CPC分类号： C10G3/50 , C07C1/22 , C07C9/14 , C09D7/20 , C10G3/42 , C10G45/58 , C10G65/043 , C10G2300/1011 , C10G2400/00 , C10L1/04 , C10L2200/0469 , C10L2270/08 , C10M105/00 , C10M105/04 , C10M177/00 , C10M2203/003 , C10M2203/022 , C10N2220/021 , C10N2220/025 , C10N2220/028 , C10N2220/031 , C10N2240/201 , C10N2240/40 , Y02P20/582 , Y02P30/20
摘要： A composition, including 40-50 wt-% C14 paraffins, based on the total weight of the composition, and 35-45 wt-% C15 paraffins, based on the total weight of the composition, wherein the C14 and C15 paraffins are produced from a biological raw material.
摘要翻译：基于组合物的总重量，包含40-50重量％C14链烷烃和基于组合物总重量的35-45重量％C 15链烷烃的组合物，其中C 14和C 15链烷烃由生物原料。

10. 发明申请

US20150057476A1 PROCESS FOR THE MANUFACTURE OF DIESEL RANGE HYDROCARBONS 审中-公开
标题翻译：柴油机油罐的制造工艺
公开(公告)号：US20150057476A1
公开(公告)日：2015-02-26
申请号：US14477758
申请日：2014-09-04
申请人： NESTE OIL OYJ
发明人： Jukka MYLLYOJA , Pekka AALTO , Pekka SAVOLAINEN , Veli-Matti PUROLA , Ville ALOPAEUS , Johan GRONQVIST
IPC分类号： C07C1/24 , C07C5/03 , C07C7/12 , C07C7/13 , C07C5/27 , C07C7/10
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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