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1. 发明申请

WO2022164868A1 PROCESS FOR MAKING HEAVY GRADE BASE OIL PRODUCTS 审中-公开
公开(公告)号：WO2022164868A1
公开(公告)日：2022-08-04
申请号：PCT/US2022/013855
申请日：2022-01-26
申请人： CHEVRON U.S.A. INC.
发明人： TREVINO, Horacio , ZHANG, Minghui , LEI, Guan-Dao , VO, Luyen T.
IPC分类号： C10G65/12 , C10G65/14 , C10G47/00 , C10G45/58 , C10G45/44 , C10M101/02
摘要： An improved process for making a heavy base oil from a base oil feedstream comprising an atmospheric resid feedstock, and, optionally, a base oil feedstock, via hydroprocessing. The process generally involves subjecting a base oil feedstream comprising the atmospheric resid to hydrocracking and dewaxing steps, and optionally to hydrofinishing, to produce base oil product(s) including a heavy grade base oil product having a viscosity of at least about 12.7 cSt at 100°C. The invention is useful to make heavy grade base oil products, as well as Group II and/or Group III/III+ base oils.

2. 发明申请

WO2020043758A1 PROCESS FOR PRODUCTION OF HYDROCARBON FUELS FROM TWO HEAVY FEEDSTOCKS 审中-公开
公开(公告)号：WO2020043758A1
公开(公告)日：2020-03-05
申请号：PCT/EP2019/072919
申请日：2019-08-28
申请人： HALDOR TOPSØE A/S
发明人： ANDERSEN, Stefan , HUNTER, Michael Glenn
IPC分类号： C10G45/08 , C10G47/14 , C10G47/18 , C10G65/12 , C10G11/18 , C10G69/04 , C10G69/14 , C10G65/14
摘要： The present disclosure relates to a process and a process plant for conversion of a first hydrocarbonaceous feedstock and a second hydrocarbonaceous feedstock by hydroprocessing, in which said first hydrocarbonaceous feedstock is characterized by demanding a higher process severity compared to said second hydrocarbonaceous feedstock, said process comprising the steps of combining said first hydrocarbonaceous feedstock with a first gas stream comprising hydrogen forming a hydrotreatment feed, directing said hydrotreatment feed to a hydrotreatment section under hydrotreatment conditions, withdrawing a hydrotreated product from said hydrotreatment section, separating said hydrotreated product in a first vapor/liquid separator forming a liquid-phase hydrotreated product and a hydrotreated vapor stream, directing an amount of said liquid-phase hydrotreated product to a stripping step providing at least a stripper light ends stream and a stripped liquid hydrotreated product, forming a hydrocracker feed comprising said second hydrocarbonaceous feedstock and a second gas stream comprising hydrogen, directing said hydrocracker feed to a hydrocracking section under hydrocracking conditions forming a hydrocracked product, and directing said hydrocracked product to a fractionation section from which at least a light product comprising a vapor phase, a heavy distillate product and an unconverted oil product are produced, wherein an amount of said hydrotreated vapor stream is directed to said hydrocracking section, either for being combined with said hydrocracker feed upstream the hydrocracking section, or for being combined with the hydrocracked product up- stream fractionation, and wherein the combined stream optionally is further treated in a further hydrotreatment section upstream said fractionation, with the associated benefit of providing a process in which a demanding hydrocarbonaceous feedstock and a less demanding hydrocarbonaceous feedstock may be treated independently, in a way where the most demanding feedstock is only treated by hydrotreatment and the least demanding feedstock is treated by hydrocracking, and the products may be segregated for independent downstream treatment while reducing capital and operational costs by integrating the sub-processes, and reducing hydrogen consumption according to the requirements

3. 发明申请

WO2018005184A1 MODULAR CRUDE REFINING PROCESS 审中-公开
标题翻译：模块化原油精炼工艺
公开(公告)号：WO2018005184A1
公开(公告)日：2018-01-04
申请号：PCT/US2017/038470
申请日：2017-06-21
申请人： UOP LLC
发明人： CARTER, Elizabeth A. , ACIKGOZ, Saadet Ulas , BRIDGE, Nicholas W. , GOSLING, Christopher D. , TOWLER, Gavin P.
IPC分类号： C10G7/00 , C10G45/00 , C10G47/00 , C10G65/14 , C10G70/04
摘要： A crude distillation and refining process and apparatus enables modular supply of the crude distillation column. Crude oil may be heated and then separated into only two liquid products in the crude distillation column. The separation between the light and heavy products may be controlled by the overhead product flow rate. Heat is recovered from an overhead stream and a bottoms stream by pre-heating the incoming crude oil stream by heat exchange with overhead stream and the bottoms stream. In an embodiment, a diesel-range distillate fraction may be condensed from an overhead stream in a first heat exchanger and a naphtha-range fraction may be condensed from the gas stream uncondensed by the first heat exchanger in a second heat exchanger.
摘要翻译：原油蒸馏和精炼过程和装置能够模块化地供应原料蒸馏塔。原油可以被加热，然后在原油蒸馏塔中分离成仅两种液体产物。轻质和重质产品之间的分离可以通过塔顶产品流量来控制。通过与塔顶物流和底部物流进行热交换来预热进入的原油物流，从顶部物流和底部物流中回收热量。在一个实施方案中，柴油馏分馏分可以在第一热交换器中从顶部料流中冷凝，石脑油馏分馏分可以在第二热交换器中由未被第一热交换器冷凝的气体料流冷凝。 >

4. 发明申请

WO2016019403A3 PRODUCTION OF OILFIELD HYDROCARBONS 审中-公开
标题翻译：生产油田油气
公开(公告)号：WO2016019403A3
公开(公告)日：2016-10-06
申请号：PCT/ZA2015050002
申请日：2015-07-22
申请人： SASOL TECH PTY LTD
发明人： DE WET EWALD WATERMEYER
IPC分类号： C10G57/02 , C10G47/00 , C10G65/00 , C10G65/12 , C10G65/14
CPC分类号： C10G57/00 , C10G47/00 , C10G57/02 , C10G65/00 , C10G65/12 , C10G65/14 , C10G2300/1022
摘要： A process (20) to produce olefinic products suitable for use as or conversion to oilfield hydrocarbons includes separating (42) an olefins-containing Fischer-Tropsch condensate (64) into a light fraction (68), an intermediate fraction (82) and a heavy fraction (94), oligomerising (44) at least a portion of the light fraction (68) to produce a first olefinic product (72) which includes branched internal olefins, and carrying out either one or both of the steps of (i) dehydrogenating (50) at least a portion of the intermediate fraction (82) to produce an intermediate product (84) which includes internal olefins and alpha-olefins, and synthesising (52) higher olefins from the intermediate product which includes internal olefins and alpha-olefins to produce a second olefinic product (86), and (ii) dimerising (52) at least a portion of the intermediate fraction to produce a second olefinic product (86). At least a portion of the heavy fraction (94) is dehydrogenated (58) to produce a third olefinic product (96) which includes internal olefins. Also provided is a process (30) to produce paraffinic products suitable for use as or conversion to oilfield hydrocarbons which includes separating (110) a Fischer-Tropsch wax (124) into at least a lighter fraction (126, 128) and a heavier fraction (130), hydrocracking (120) the heavier fraction (130) to provide a cracked intermediate (144), and separating (122) the cracked intermediate (144) into at least a naphtha fraction (148), a heavier than naphtha paraffinic distillate fraction (150) suitable for use as or conversion to oilfield hydrocarbons, and a bottoms fraction (152) which is heavier than the paraffinic distillate fraction (150).
摘要翻译：生产适用作油田烃或转化为油田烃的烯烃产物的方法（20）包括将含烯烃的费 - 托合并物（64）分离（42）成轻馏分（68），中馏分（82）和（94），低聚（44）至少一部分轻馏分（68）以产生包含支链内烯烃的第一烯烃产物（72），并且进行（i）的步骤（50）将所述中间馏分（82）的至少一部分脱氢以产生包含内烯烃和α-烯烃的中间产物（84），并由所述中间产物合成（52）更高级烯烃，所述中间产物包含内烯烃和α-烯烃，制备第二烯烃产物（86），和（ii）将至少一部分中间馏分二聚（52）以产生第二烯烃产物（86）。至少一部分重馏分（94）被脱氢（58）以产生包含内烯烃的第三烯烃产物（96）。还提供了生产适用作油田烃或转化为油田烃的链烷烃产物的方法（30），其包括将（110）费 - 托蜡（124）分离成至少较轻馏分（126,128）和较重馏分（130），加氢裂化（120）较重馏分（130）以提供裂化中间产物（144），和将裂化中间产物（144）分离（122）成至少一种石脑油馏分（148）适合用作油田烃或转化为油田烃的馏分（150），以及比石蜡馏分馏分（150）重的塔底馏分（152）。

5. 发明申请

WO2013087942A1 INTEGRATED GAS-TO-LIQUID CONDENSATE PROCESS AND APPARATUS 审中-公开
标题翻译：集成气 - 液体冷凝过程和装置
公开(公告)号：WO2013087942A1
公开(公告)日：2013-06-20
申请号：PCT/EP2012/075865
申请日：2012-12-17
申请人： SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ B.V. , SHELL OIL COMPANY
发明人： HOEK, Arend , SCHOLTEN, Wilhelmus, Johannes, Franciscus , AL-SHARSHANI, Ali Mohammed, Ali Shahab
IPC分类号： C10G2/00 , C10G45/02 , C10G47/00 , C10G65/14
CPC分类号： C10G55/02 , C10G2/332 , C10G45/02 , C10G47/00 , C10G65/14 , C10G2300/1025 , C10G2400/04 , C10G2400/06 , C10G2400/08 , C10L1/04
摘要： A process is provided for production of a middle distillate fraction from a gas-to-liquid (GTL) conversion comprising the steps of: (a) providing a feed stream comprising a natural gas and a condensate and separating a condensate from the natural gas feed stream to produce a condensate feed stream and a natural gas feed stream; (b) preparing a mixture of carbon monoxide and hydrogen from the natural gas feed stream obtained in step (a); (c) preparing a long chain hydrocarbon product stream by performing a Fischer-Tropsch reaction using carbon monoxide and hydrogen obtained in step (b); (d) Subjecting the long chain hydrocarbon product stream to a hydrocracking/hydroisomerization step to obtain a hydrocracked/hydroisomerised Fischer-Tropsch (FT) product stream; (e) treating the condensate stream of step (a) with a desulfurization step to generate a condensate product stream; (f) combining the hydrocracked/hydroisomerised FT product stream of step (d) with the condensate product stream of step (e) in order to provide a distillation feed stream; and (g) performing a distillation step on the distillation feed stream, wherein the distillation step provides for isolation of middle distillate products; wherein the steps (c) to (d) occur substantially concurrently with step (e). Middle distillate fractions and fuel/fuel blends obtained according to the process are also provided.
摘要翻译：提供一种用于从气 - 液（GTL）转化器生产中间馏分馏分的方法，包括以下步骤：（a）提供包含天然气和冷凝物的进料流，并从天然气进料中分离出冷凝物流以产生冷凝物进料流和天然气进料流; （b）从步骤（a）中获得的天然气进料流中制备一氧化碳和氢气的混合物; （c）通过使用步骤（b）中获得的一氧化碳和氢进行费 - 托反应制备长链烃产物流; （d）使长链烃产物流进行加氢裂化/加氢异构化步骤以获得加氢裂化/加氢异构化费 - 托（FT）产物流; （e）用脱硫步骤处理步骤（a）的冷凝物流以产生冷凝物产物流; （f）将步骤（d）的加氢裂化/加氢异构化的FT产物流与步骤（e）的冷凝物产物流混合，以提供蒸馏进料流; 和（g）对所述蒸馏进料流进行蒸馏步骤，其中所述蒸馏步骤提供中间馏分产物的分离; 其中步骤（c）至（d）基本上与步骤（e）同时发生。还提供了根据该方法获得的中间馏分馏分和燃料/燃料混合物。

6. 发明申请

WO2010002545A3 THREE-PHASE HYDROPROCESSING WITHOUT A RECYCLE GAS COMPRESSOR 审中-公开
标题翻译：没有循环气体压缩机的三相氢化
公开(公告)号：WO2010002545A3
公开(公告)日：2010-02-25
申请号：PCT/US2009046534
申请日：2009-06-08
申请人： UOP LLC , KOKAYEFF PETER , PETRI JOHN A
发明人： KOKAYEFF PETER , PETRI JOHN A
IPC分类号： C10G65/14 , C10G45/02
CPC分类号： C10G65/02
摘要： In general, methods of hydroprocessing a hydrocarbonaceous feed stock (12) are provided that do not use a costly recycle gas compressor, but are still able to use the more efficient reaction systems provided in a substantially three-phase hydroprocessing zone (36). The method combines a substantially liquid-phase hydroprocessing zone (20) with the substantially three-phase hydroprocessing zone (36) in a manner so that the hydrogen requirements for both reaction zones (20, 36) can be provided from an external source thereto without the use of a hydrogen recycle or recycle gas compressor to the substantially three-phase reaction zone (36).
摘要翻译：通常，提供加氢处理烃原料（12）的方法，其不使用昂贵的循环气体压缩机，但仍然能够使用在基本上三相的加氢处理区（36）中提供的更有效的反应系统。该方法将基本上液相的加氢处理区域（20）与基本上三相的加氢处理区域（36）结合，使得两个反应区域（20,36）的氢气需求可以从外部来源提供，而没有将氢循环或再循环气体压缩机用于基本上三相的反应区（36）。

7. 发明申请

WO2009106704A3 PROCEDE DE PRODUCTION DE DISTILLATS MOYENS PAR HYDROISOMERISATION ET HYDROCRAQUAGE SEQUENCES D'UN EFFLUENT PRODUIT PAR LE PROCEDE FISCHER-TROPSCH 审中-公开
公开(公告)号：WO2009106704A3
公开(公告)日：2009-09-03
申请号：PCT/FR2008/001744
申请日：2008-12-16
申请人： IFP , ENI S.P.A. , BOUCHY, Christophe , GUILLON, Emmanuelle , MARTENS, Johan
发明人： BOUCHY, Christophe , GUILLON, Emmanuelle , MARTENS, Johan
IPC分类号： C10G65/12 , C10G45/64 , C10G47/18 , B01J21/12 , B01J29/70 , C10G65/14 , B01J23/42 , B01J29/06
摘要： L'invention décrit un procédé de production de distillats moyens à partir d'une charge paraffinique produite par synthèse Fischer-Tropsch, comprenant une séparation d'une fraction lourde à point d'ébullition initial compris entre 120 et 2000C, une hydroisomérisation d'une partie au moins de ladite fraction lourde en présence d'un premier catalyseur d'hydroisomérisation comprenant au moins un métal du groupe VIII et/ou au moins un métal du groupe VIB et au moins un tamis moléculaire, un hydrocraquage d'une partie au moins de l'effluent hydroisomérisé en présence d'un deuxième catalyseur d'hydrocraquage comprenant au moins un métal du groupe VlIl et/ou au moins un métal du groupe VIB et un support silice alumine ou à base de zéolithe Y, et une distillation de l'effluent final pour obtenir des distillats moyens.

8. 发明申请

WO2009019954A1 改質原油の製造方法审中-公开
标题翻译：生产改性原油的方法
公开(公告)号：WO2009019954A1
公开(公告)日：2009-02-12
申请号：PCT/JP2008/062503
申请日：2008-07-10
申请人：出光興産株式会社 , 太田信之
发明人：太田信之
IPC分类号： C10G67/16 , C10G65/14
CPC分类号： C10G67/02 , C10G49/00
摘要：原油からナフサ留分を分離し抜頭原油を得る工程（ナフサ留分分離工程）、該抜頭原油を水素化処理する工程（抜頭原油水素化処理工程）および該ナフサ留分を改質原油の製造に利用する工程（ナフサ留分利用工程）を含む、劣質な原油においても効率よく品質を改善することができる改質原油の製造方法である。
摘要翻译：公开了一种重整原油的制造方法，其特征在于，包括：将石脑油馏分与原油分离，生成顶馏分原油（石脑油馏分分离工序）的工序。氢化顶部原油（顶部原油氢化步骤）的步骤; 以及利用石脑油馏分生产重整原油（石脑油馏分利用步骤）的步骤。该过程能够有效地提高劣质原油的质量。

9. 发明申请

WO2007105400A1 炭化水素油の製造方法および炭化水素油审中-公开
标题翻译：生产石油和油料油的工艺
公开(公告)号：WO2007105400A1
公开(公告)日：2007-09-20
申请号：PCT/JP2007/052618
申请日：2007-02-14
申请人：新日本石油株式会社 , 田中祐一 , 高橋信也 , 千葉善文
发明人：田中祐一 , 高橋信也 , 千葉善文
IPC分类号： C10G65/14 , C10G45/12 , C10G47/16 , C10L1/08
CPC分类号： C10G65/14 , C10G45/12 , C10G47/16 , C10G2300/1022 , C10G2300/301
摘要：炭化水素油の製造方法は、フィッシャー・トロプシュ合成法により得られる合成油を分留し、沸点１５０～３６０°Cの留分の含有量が９０質量％以上であり且つ沸点３５０°C以上の留分の含有量が５質量％以下である中間留分と、当該中間留分よりも重質なワックス分とを得、中間留分およびワックス分を、それぞれ、水素存在下、水素化触媒と接触させた後、混合し分留して沸点１５０～３６０°Cの留分の含有量が８６質量％以上であり且つ沸点３５０°C以上の留分の含有量が５質量％以上である炭化水素油を得ることを特徴とする。
摘要翻译：一种生产烃油的方法，其特征在于包括将通过费 - 托法得到的合成油进行分馏，得到中间馏分，其中沸点为150〜360℃的馏出物的含量为90％质量以上，沸点为350℃以上的馏出物的含量为5质量％以下，蜡成分比中间馏分重，使中间馏分和蜡成分分别与氢化催化剂接触氢化中间馏分与氢化蜡组分混合，并对混合物进行分馏，得到沸点为150〜360℃的馏出物含量为86质量％以上的烃油，沸点为350℃以上的馏出物的含量为5质量％以上。

10. 发明申请

WO2007039047A1 HYDROTREATING AND HYDROCRACKING PROCESS AND APPARATUS 审中-公开
标题翻译：加氢和加氢过程和装置
公开(公告)号：WO2007039047A1
公开(公告)日：2007-04-12
申请号：PCT/EP2006/008868
申请日：2006-09-12
申请人： HALDORE TOPSØE A/S , HUNTER, Michael, Glenn , VIVAS, Angelica, Hidalgo , JENSEN, Lars, Skov , LOW, Gordon, Gongngai
发明人： HUNTER, Michael, Glenn , VIVAS, Angelica, Hidalgo , JENSEN, Lars, Skov , LOW, Gordon, Gongngai
IPC分类号： C10G65/02 , C10G65/12 , C10G65/14
CPC分类号： C10G65/12 , C10G65/02 , C10G65/14 , C10G2300/207 , C10G2400/04
摘要： Partial conversion hydrocracking process comprising the steps of (a) hydrotreating a hydrocarbon feedstock with a hydrogenrich gas to produce a hydrotreated effluent stream comprising a liquid/vapour mixture and separating the liquid/vapour mixture into a liquid phase and a vapour phase, and (b) separating the liquid phase into a controlled liquid portion and an excess liquid portion, and (c) combining the vapour phase with the excess liquid portion to form a vapour plus liquid portion, and (d) separating an FCC feed-containing fraction from the controlled liquid portion and simultaneously hydrocracking the vapour plus liquid portion to produce a dieselcontaining fraction, or hydrocracking the controlled liquid portion to produce a diesel-containing fraction and simultaneously separating a FCC feed-containing fraction from the vapour plus liquid portion. The invention also includes an apparatus for carrying out the partial conversion hydrocracking process.
摘要翻译：部分转化加氢裂化方法包括以下步骤：（a）用富氢气体加氢处理烃原料以产生包含液体/蒸汽混合物的加氢处理流出物流，并将液体/蒸气混合物分离成液相和气相，和（b ）将液相分离成受控的液体部分和过量的液体部分，和（c）将气相与过量的液体部分组合以形成蒸气加液体部分，和（d）将FCC进料的馏分与控制液体部分并同时加氢裂化蒸气加液体部分以产生含柴油馏分，或加氢裂化受控液体部分以产生含柴油馏分，同时将含FCC原料的馏分与蒸气加液体部分分离。本发明还包括用于进行部分转化加氢裂化过程的装置。

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