专利快速检索-快速检索全球专利，免费商用专利数据库-IPRDB

1. 发明申请

WO2016161199A1 PARAFFIN PROCESSING USING IONIC MICRO-EMULSIONS 审中-公开
标题翻译：使用离子微乳的PARAFFIN加工
公开(公告)号：WO2016161199A1
公开(公告)日：2016-10-06
申请号：PCT/US2016/025414
申请日：2016-03-31
申请人： UOP LLC
发明人： BUCHBINDER, Avram M. , TOWLER, Gavin P. , ABREVAYA, Hayim
IPC分类号： B01J31/22 , B01J31/18 , B01J31/02 , B01J35/12 , C07C5/22 , C07C6/00 , B01F3/08
CPC分类号： C10G50/00 , B01F17/0007 , C10G9/00 , C10G29/205 , C10G45/58 , C10L1/04
摘要： A process utilizing a micro-emulsion is described. The micro-emulsion is formed by contacting an ionic liquid, a co-solvent, a hydrocarbon, an optional surfactant, and an optional catalyst promoter. The micro-emulsion comprises a hydrocarbon component comprising the hydrocarbon, and an ionic liquid component comprising the ionic liquid. The ionic liquid comprises a halometallate anion and a cation. The hydrocarbon comprises at least one paraffin having from 4 to about 50 carbon atoms. The co-solvent has a polarity greater than the polarity of the hydrocarbon. The ionic liquid is present in an amount of about 0.05 wt% to about 40 wt% of the micro-emulsion. A product mixture comprising a product is produced in a process zone containing the micro-emulsion. The product comprises at least one of an isomerized paraffin, a disproprtionated paraffin, and a reverse disproportionated paraffin.
摘要翻译：描述了利用微乳液的方法。微乳液通过使离子液体，共溶剂，烃，任选的表面活性剂和任选的催化剂促进剂接触而形成。微乳液包含含烃的烃组分和包含离子液体的离子液体组分。离子液体包含卤代金属阴离子和阳离子。烃包含至少一种具有4至约50个碳原子的链烷烃。共溶剂的极性大于烃的极性。离子液体以微乳液的约0.05重量％至约40重量％的量存在。包含产物的产品混合物在含有微乳液的处理区中产生。该产物包括异构化石蜡，不饱和石蜡和反向歧化石蜡中的至少一种。

2. 发明申请

WO2016107914A1 PROCESS FOR PREPARING A BASE OIL HAVING A REDUCED CLOUD POINT 审中-公开
标题翻译：用于制备具有减少云点的基础油的方法
公开(公告)号：WO2016107914A1
公开(公告)日：2016-07-07
申请号：PCT/EP2015/081445
申请日：2015-12-30
申请人： SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ B.V. , SHELL OIL COMPANY
发明人： DEN BOESTERT, Johannes, Lenndert, Willem, Cornelis , KIEFFER, Eduard, Philip , RENKEMA, Duurt
IPC分类号： C10G31/11 , C10G45/58 , C10G67/14 , C10M177/00
CPC分类号： C10G57/00 , B01D61/022 , B01D71/70 , B01D2311/2669 , B01D2319/025 , B01D2325/023 , B01J29/7469 , C10G31/11 , C10G45/58 , C10G67/14 , C10G2300/1022 , C10G2300/304 , C10G2400/10 , C10M101/00 , C10M177/00 , C10M2203/003 , C10M2205/173 , C10N2220/023 , C10N2270/00
摘要： The present invention relates to a process for preparing a base oil fraction having a reduced cloud point from a hydrocarbon feed which is derived from a Fischer-Tropsch process, the process comprises the steps of: (a) providing a hydrocarbon feed which is derived from a Fischer-Tropsch process; (b) subjecting the hydrocarbon feed of step (a) to a catalytic dewaxing treatment to obtain an at least partially isomerised product; (c) separating at least part of the at least partially isomerised product as obtained in step (b) into one or more light hydrocarbon fractions and one or more heavy base oil fractions; (d) separating at least one of the heavy base oil fractions as obtained in step (c) by means of a first membrane into a first permeate which comprises a base oil having a reduced cloud point and a first retentate which comprises a base oil containing haze compounds, wherein the membrane separation is carried out at a temperature in the range of from the pour point of the base oil and up to 120°C and a pressure in the range of from 5-60 bar; and (e) separating at least part of the first permeate as obtained in step (d) by means of a second membrane into a second permeate which comprises a base oil having a further reduced cloud point and a second retentate which comprises a base oil containing haze compounds, wherein the membrane separation is carried out at a temperature in the range of from the pour point of the base oil and up to 120°C and a pressure in the range of from 5-60 bar; and (f) recovering the second permeate as obtained in step (e).
摘要翻译：本发明涉及一种制备基烃油馏分的方法，该馏分具有源自费 - 托方法的烃原料的浊点减少，该方法包括以下步骤：（a）提供烃源自费 - 托法（b）使步骤（a）的烃进料进行催化脱蜡处理以获得至少部分异构化的产物; （c）将步骤（b）中获得的至少部分异构化的产物的至少一部分分离成一种或多种轻质烃馏分和一种或多种重质基础油馏分; （d）通过第一膜将步骤（c）中获得的重质基础油馏分中的至少一种分离成包含具有降低的浊点的基础油和第一渗余物的第一渗透物，所述第一渗透物包含含有雾状化合物，其中膜分离在从基础油的倾点至120℃的温度和5-60巴的压力范围内进行; 和（e）通过第二膜将步骤（d）中获得的至少部分第一渗透物分离成第二渗透物，所述第二渗透物包含具有进一步降低的浊点的基础油和第二滞留物，所述第二渗透物包含含有雾状化合物，其中膜分离在从基础油的倾点至120℃的温度和5-60巴的压力范围内进行; 和（f）回收步骤（e）中获得的第二渗透物。

3. 发明申请

WO2016081305A1 PRODUCTION OF LUBRICANT BASE STOCKS WITH CONTROLLED AROMATIC CONTENTS 审中-公开
标题翻译：生产具有控制的芳香含量的润滑剂基础库存
公开(公告)号：WO2016081305A1
公开(公告)日：2016-05-26
申请号：PCT/US2015/060604
申请日：2015-11-13
申请人： EXXONMOBIL RESEARCH AND ENGINEERING COMPANY
发明人： LYON, Kristen, S. , JOSECK, Eric, D. , SCHLEICHER, Gary, P. , DOUGHERTY, Richard, C. , HORTON, Angela
IPC分类号： C10G45/02 , C10G45/58 , C10G47/00 , C10G65/04 , C10G65/12 , C10G67/04
CPC分类号： C10G69/02 , C10G45/02 , C10G45/58 , C10G47/00 , C10G65/04 , C10G65/12 , C10G67/04 , C10G2400/10 , C10M101/00 , C10M101/02 , C10M2203/1006 , C10M2203/1045 , C10M2205/223 , C10N2220/022 , C10N2230/43
摘要： Methods are provided for producing Group II and Group III base stocks with a controlled or consistent aromatics content. An aromatics-rich base stock, such as a Group I base stock or an alkylated aromatic base stock, can be added to the catalytically treated base stock in a minimal amount after the final catalytic treatment step but prior to fractionation. At the beginning of a processing run for forming lubricant base stock products, about 0.25 wt% to about 1.25 wt% of the Group I base stock can be added to a catalytically processed feed after the final catalytic processing stage but prior to fractionation to form the Group II and/or Group III base stock. During the course of the processing run, the amount of Group I base stock added can be reduced roughly in correspondence with the increase in aromatics caused by catalyst deactivation. This can allow a catalytically processed lubricant base stock product to be generated that contains at least about a threshold (minimum) aromatics content during the course of a processing run. Alternatively, this can allow a catalytically processed lubricant base stock product to be generated that has consistent aromatics content during the course of the processing run.
摘要翻译：提供了用于生产具有受控或一致的芳烃含量的II类和III类基础油料的方法。可以在最终催化处理步骤之后但在分馏之前以最小的量将富含芳烃的基础油料如I类基础油料或烷基化芳族基础油料加入催化处理的原料中。在用于形成润滑剂基础产品的加工运行开始时，可以在最终催化处理阶段之后但在分馏之前将约0.25重量％至约1.25重量％的第I族原料加入催化加工的进料中，以形成 II类和/或III类基础油。在加工过程中，加入的I类原料的量可以与催化剂失活引起的芳族化合物的增加大致相当。这可以允许在处理运行过程中产生含有至少约一个阈值（最小）芳烃含量的催化加工的润滑剂基础原料产品。或者，这可以允许在处理运行过程中生成具有一致的芳族化合物含量的催化加工的润滑剂基础原料产品。

4. 发明申请

WO2016073394A1 PROCESSES FOR MAXIMIZING HIGH QUALITY DISTILLATE 审中-公开
标题翻译：最大化高品质蒸馏过程
公开(公告)号：WO2016073394A1
公开(公告)日：2016-05-12
申请号：PCT/US2015/058703
申请日：2015-11-03
申请人： UOP LLC
发明人： THAKKAR, Vasant P.
IPC分类号： C10G65/12 , C10G69/02 , C10G69/10
CPC分类号： C10G67/02 , C10G45/02 , C10G45/08 , C10G45/12 , C10G45/58 , C10G45/64 , C10G2300/104 , C10G2300/1044 , C10G2300/1048 , C10G2400/02 , C10G2400/04 , C10G2400/06 , C10G2400/08
摘要： A process for producing a high quality distillate that meets the ultralow sulfur, cold flow, and distillation requirements. The feed stream is first hydrotreated and dewaxed in the same reactor to provide a hydrotreated and dewaxed effluent. The hydrotreated and dewaxed effluent is separated in a separation zone into a liquid and a vapor phase, the vapor phase comprising a hydrogen containing gas that can be recycled. The liquid phase is separated into at least a diesel stream and a heavy hydrocarbon stream. The heavy hydrocarbon stream is hydrocracked and the hydrocracked effluent may be passed to the reactor for hydrotreating and dewaxing or passed to the separation zone with the hydrotreated and dewaxed effluent.
摘要翻译：生产符合超低硫，冷流和蒸馏要求的高品质馏出物的方法。首先在同一反应器中将进料物流加氢处理和脱蜡以提供加氢处理和脱蜡的流出物。将加氢处理和脱蜡的流出物在分离区中分离成液体和气相，气相包含可再循环的含氢气体。液相被分离成至少柴油流和重质烃流。将重质烃流加氢裂化，并将加氢裂化的流出物送入反应器进行加氢处理和脱蜡，或者与加氢处理和脱蜡的流出物一起进入分离区。

5. 发明申请

WO2016062868A1 METHOD FOR KETONISATION OF BIOLOGICAL MATERIAL 审中-公开
标题翻译：生物材料鉴定方法
公开(公告)号：WO2016062868A1
公开(公告)日：2016-04-28
申请号：PCT/EP2015/074622
申请日：2015-10-23
申请人： NESTE OIL OYJ
发明人： MYLLYOJA, Jukka , PIILOLA, Rami , KETTUNEN, Mika
IPC分类号： C10G3/00 , C07C45/48 , B01J23/04 , C10G65/04
CPC分类号： C07C45/48 , B01J21/063 , B01J23/04 , B01J23/42 , B01J23/883 , B01J29/85 , B01J35/0006 , C10G3/42 , C10G3/46 , C10G3/47 , C10G3/50 , C10G45/58 , C10G65/043 , C10G2300/1011 , C10G2400/10 , Y02P30/20 , C07C49/04
摘要： The present invention relates to a method for producing ketones which method comprises the steps of: a) providing a feedstock of biological origin comprising fatty acids and/or fatty acid derivatives having an average chain length of 24 C-atoms or less, b) subjecting said feedstock to a catalytic ketonisation reaction in the presence of a K 2 O/TiO 2 -catalyst, c) obtaining from said ketonisation reaction a product stream comprising ketones, which ketones have a longer average hydrocarbon chain length than the average hydrocarbon chain length in said feedstock, wherein step b) is carried out directly on said feedstock and in the presence of said K 2 O/TiO 2 -catalyst as the sole catalyst applied in said ketonisation reaction.
摘要翻译：本发明涉及一种生产酮的方法，该方法包括以下步骤：a）提供生物来源的原料，其包含平均链长为24个C原子或更少的脂肪酸和/或脂肪酸衍生物，b）所述原料在K 2 O / TiO 2 - 催化剂存在下进行催化酮化反应，c）从所述酮化反应获得包含酮的产物流，所述酮具有比所述原料中的平均烃链长更长的平均烃链长度，其中步骤b）直接在所述原料上并在所述K 2 O / TiO 2催化剂存在下作为在所述酮化反应中应用的唯一催化剂进行。

6. 发明申请

WO2015181744A1 PROCESS FOR PRODUCING A DIESEL HYDROCARBON FRACTION STARTING FROM A RENEWABLE FEEDSTOCK 审中-公开
标题翻译：生产从可再生饲料开始的柴油机油分离方法
公开(公告)号：WO2015181744A1
公开(公告)日：2015-12-03
申请号：PCT/IB2015/053971
申请日：2015-05-27
申请人： ENI S.P.A.
发明人： BELLUSSI, Giuseppe , MOLINARI, Daniele , DE ANGELIS, Alberto Renato , CALEMMA, Vincenzo
IPC分类号： C11B7/00 , C11C1/00 , C10G45/02 , C10G45/06 , C10G45/12 , C10G45/58 , C10G45/62 , C10G45/64 , C11B3/06 , C10G3/00 , C11B13/00
CPC分类号： C10G3/50 , C10G3/42 , C10G45/02 , C10G45/06 , C10G45/12 , C10G45/58 , C10G45/62 , C10G45/64 , C10G2300/1011 , C10G2300/1014 , C10G2400/04 , C11C1/04 , C11C3/00 , C11C3/14 , Y02E50/13 , Y02P30/20
摘要： The present invention relates to a process for preparing a diesel hydrocarbon fraction, comprising the following steps: (a) reacting at least a renewable feedstock comprising glycerides with ammonia at a temperature within the range of 130–250°C and a pressure within the range of 1-8 MPa, forming at least a mixture of fatty acid amides and glycerine; (b) separating said glycerine from said mixture of amides; (c) subjecting said mixture of amides to catalytic hydrotreatment in the presence of hydrogen, obtaining a reaction product comprising: (i) at least one gaseous effluent comprising ammonia, hydrogen, water vapour and CO, (ii) at least one diesel hydrocarbon fraction comprising a mixture of substantially linear paraffins; (d) separating said diesel hydrocarbon fraction from said reaction product. Said mixture of linear paraffins is advantageously subjected to a further hydroisomerization step for converting the linear paraffins into branched paraffins.
摘要翻译：本发明涉及一种制备柴油烃馏分的方法，包括以下步骤：（a）使至少一种包含甘油酯的可再生原料与氨在130-250℃范围内的温度和在该范围内的压力至少形成脂肪酸酰胺和甘油的混合物; （b）从所述酰胺混合物中分离所述甘油; （c）使所述酰胺混合物在氢的存在下进行催化加氢处理，得到反应产物，其包含：（i）至少一种包含氨，氢，水蒸汽和CO的气态流出物，（ii）至少一种柴油烃馏分包括基本上线性的链烷烃的混合物; （d）从所述反应产物中分离所述柴油烃馏分。所述线性链烷烃的混合物有利地进行进一步的加氢异构化步骤，用于将线性链烷烃转化为支化链烷烃。

7. 发明申请

WO2015181114A1 FISCHER-TROPSCH GASOIL FRACTION 审中-公开
公开(公告)号：WO2015181114A1
公开(公告)日：2015-12-03
申请号：PCT/EP2015/061504
申请日：2015-05-26
申请人： SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ B.V. , SHELL OIL COMPANY
发明人： MORSINK, Johannes Bernardus Wilhelmus , TURFBOER, Johannes , WIERSMA, Rendert Jan , WINTER, Ferry
IPC分类号： C10L1/04
CPC分类号： C10G45/58 , C10G2300/1022 , C10G2300/301 , C10G2300/302 , C10G2400/06 , C10L1/04
摘要： The present invention provides a Fischer-Tropsch gasoil fraction having an initial boiling point of at least 175°C and a final boiling point of at most 285°C. In another aspect the present invention provides a fuel composition and the use of a Fischer-Tropsch gasoil fraction according to the invention.
摘要翻译：本发明提供了一种初始沸点为至少175℃，最终沸点至多为285℃的费 - 托瓦斯油馏分。在另一方面，本发明提供燃料组合物和根据本发明的费 - 托瓦斯油馏分的用途。

8. 发明申请

WO2015101837A3 COMPOSITION COMPRISING PARAFFIN FRACTIONS OBTAINED FORM BIOLOGICAL RAW MATERIALS AND METHOD OF PRODUCING SAME 审中-公开
标题翻译：包含生物形成原料的PARAFFIN分解物的组合物及其生产方法
公开(公告)号：WO2015101837A3
公开(公告)日：2015-09-24
申请号：PCT/IB2014003235
申请日：2014-12-30
申请人： NESTE OIL OYJ
发明人： AALTO PEKKA , SANDBERG KATI , NYMAN TOMI , HAKOLA MAIJA
IPC分类号： C09D7/00 , C07C9/15 , C07C9/16 , C10G3/00 , C10G45/00 , C10L1/16
CPC分类号： C10G3/50 , C07C1/22 , C07C9/14 , C09D7/001 , 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。

9. 发明申请

WO2015129970A1 단일 합성원유 생산용 FT GTL 장치 및 방법 审中-公开
标题翻译： FT GTL设备和生产单一合成原油的方法
公开(公告)号：WO2015129970A1
公开(公告)日：2015-09-03
申请号：PCT/KR2014/007012
申请日：2014-07-30
申请人： 대우조선해양 주식회사
发明人： 권혁 , 문영식 , 최정호 , 김원석 , 박태신 , 고글랜 , 덴흠더글라스
IPC分类号： B63B35/44 , C10G5/00
CPC分类号： C10G5/00 , C10G2/31 , C10G2/32 , C10G45/58 , C10G47/00 , C10G49/00 , C10G67/00 , C10G2300/1025 , C10G2300/4037 , C10G2300/4062
摘要： 단일 합성원유 생산용 FT GTL 장치 및 단일 합성원유 생산용 FT GTL 방법이 개시된다. 본 발명의 단일 합성원유 생산용 FT GTL 장치는 FPSO(Floated Production, Storage, and Off-loading)에서 단일 합성원유 생산을 위한 FT(Fischer-Tropsch) GTL(Gas-to-Liquid) 장치로서, 생산된 천연가스에 대해 안정화를 실행하여 천연가스 콘덴세이트를 생성하는 가스 주입 안정화 유닛; 및 상기 가스 주입 안정화 유닛에서 처리된 천연가스를 개질하여 합성원유 제품을 생성하는 개질 유닛을 포함하는 것을 특징으로 한다.
摘要翻译：公开了用于生产单一合成原油的费 - 托（FT）气 - 液（GTL）装置和用于生产单一合成原油的FT GTL方法。本发明的用于生产单一合成原油的FT GTL装置是用于从浮选生产，储存和卸载（FPSO）生产单一合成原油的FT GTL装置，其特征在于包括：气体注入稳定单元，用于对所生产的天然气进行稳定化以产生天然气冷凝物; 以及用于改变在气体注入稳定单元中处理过的天然气的改性单元，以生产合成原油产品。

10. 发明申请

WO2015094709A1 METHODS AND APPARATUSES FOR ISOMERIZING HYDROCARBONS 审中-公开
标题翻译：用于同位素化的方法和装置
公开(公告)号：WO2015094709A1
公开(公告)日：2015-06-25
申请号：PCT/US2014/068722
申请日：2014-12-05
申请人： UOP LLC
发明人： SHAKUR, Mohamed S.
IPC分类号： C10G53/00
CPC分类号： B01J19/24 , B01D53/228 , B01D53/68 , B01D2257/108 , B01D2257/2045 , C10G45/58 , C10G45/62 , C10G70/045 , C10G2300/104 , C10G2300/305 , C10G2300/4081 , C10G2300/42 , C10G2400/02
摘要： Methods and apparatuses are provided for isomerizing a hydrocarbon stream. The method includes isomerizing a hydrocarbon stream in a reactor to produce an intermediate isomerized stream. The intermediate isomerized stream is fractionated to produce an off gas stream and a heavy isomerized stream, where the off gas stream includes an off gas recycle stream. The off gas recycle stream is dried in an off gas dryer to produce a hydrogen recycle stream, where the off gas drier includes an off gas dryer membrane separating the off gas recycle stream from an off gas purge stream. The off dryer membrane includes a perfluorosulfonated ionomer. The hydrogen recycle stream is then fed into the reactor.
摘要翻译：提供用于使烃流异构化的方法和装置。该方法包括在反应器中异构化烃流以产生中间体异构化的物流。将中间体异构化流分馏以产生废气流和重质异构化流，其中废气流包括废气再循环流。废气再循环流在脱气干燥器中干燥以产生氢再循环流，其中废气干燥器包括将废气再循环流与废气吹扫流分离的脱气干燥器膜。脱水膜包括全氟磺化离聚物。然后将氢循环物流进料到反应器中。

你已经成功收藏专利！

检索式保存成功!

IPRDB

热门服务

关于我们

友情链接

联系方式