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1. 发明公开

US20240352356A1 METHOD AND SYSTEM FOR PRODUCING REFINED HYDROCARBONS FROM WASTE PLASTICS 审中-公开
公开(公告)号：US20240352356A1
公开(公告)日：2024-10-24
申请号：US18636273
申请日：2024-04-16
申请人： SK INNOVATION CO., LTD. , SK GEO CENTRIC CO., LTD.
发明人： Yong Woon KIM , Seo Yeong KANG , Soo Kil KANG , Min Gyoo PARK , Young Moo PARK , Min Woo SHIN , Jae Hwan LEE , Jin Seong JANG , Sang Hwan JO
IPC分类号： C10G67/14 , B01D17/04 , B01D17/06 , B01D37/00 , C10B53/07
CPC分类号： C10G67/14 , B01D17/047 , B01D17/06 , B01D37/00 , C10B53/07 , C10G2300/1003 , C10G2300/202
摘要： The embodiments of the present disclosure relate to a method and system for producing refined hydrocarbons from waste plastics. The method and system for producing refined hydrocarbons from waste plastics according to the present disclosure may minimize formation of an ammonium chloride salt (NH4Cl) and may prevent an adhesion phenomenon of impurity particles in a reactor in a refining process of waste plastic pyrolysis oil containing impurities including chlorine and nitrogen. In addition, the method and system for producing refined hydrocarbons from waste plastics according to the present disclosure may have excellent refining efficiency and may implement a long-term operation of a process because deactivation of a catalyst used in the process is prevented, and may produce refined hydrocarbons having a low content of impurities and a low content of olefins, and solid coke.

2. 发明授权

US11999914B2 Process and a system for production of multiple grade de-aromatized solvents from hydrocarbon streams 有权
公开(公告)号：US11999914B2
公开(公告)日：2024-06-04
申请号：US17481077
申请日：2021-09-21
申请人： INDIAN OIL CORPORATION LIMITED
发明人： Vasamsetty Naga Veera Hima Bindu , Mainak Sarkar , Ganesh Vitthalrao Butley , Ramesh Karumanchi , Sarvesh Kumar , Madhusudan Sau , Gurpreet Singh Kapur , Sankara Sri Venkata Ramakumar
IPC分类号： C10G67/06 , C10G7/00 , C10G25/00 , C10G31/00 , C10G45/08 , C10G45/50 , C10G67/14
CPC分类号： C10G67/14 , C10G7/00 , C10G25/00 , C10G31/00 , C10G45/08 , C10G45/50 , C10G67/06 , C10G2300/1037 , C10G2300/202 , C10G2300/207 , C10G2300/302 , C10G2300/308 , C10G2300/4006 , C10G2300/4012 , C10G2300/4018 , C10G2300/80 , C10G2400/30
摘要： A process and a system are used for production of multiple grades of ultralow aromatic solvents/chemicals having preferred boiling range, flash point and viscosity from different hydrocarbon streams. A plurality of hydrotreating steps are used to hydrotreat a plurality of hydrocarbon feedstocks in the presence of a hydrogen gas stream and a catalyst system. Further, at least one dissolved gas stripping step, at least one adsorption step, and a distillation step are included in the process. Desired iso-paraffin molecules are thereby preserved, and the undesired aromatic molecules are converted into desired naphthene molecules.

3. 发明申请

US20170342330A1 PRODUCTION OF UPGRADED EXTRACT AND RAFFINATE 审中-公开
公开(公告)号：US20170342330A1
公开(公告)日：2017-11-30
申请号：US15599636
申请日：2017-05-19
申请人： ExxonMobil Research and Engineering Company
发明人： Benjamin S. Umansky , Keith K. Aldous , James W. Gleeson , Edward J. Blok , Richard A. Demmin
IPC分类号： C10G45/10 , C10G45/22 , C10G47/02 , C10G49/26 , C10G45/72
CPC分类号： C10G45/10 , C10G21/00 , C10G45/02 , C10G45/22 , C10G45/58 , C10G45/72 , C10G47/02 , C10G49/26 , C10G67/0418 , C10G67/14 , C10G2300/10 , C10G2300/202 , C10G2300/301 , C10G2300/304 , C10G2400/04 , C10G2400/30
摘要： Systems and methods are provided for producing upgraded raffinate and extract products from lubricant boiling range feeds and/or other feeds having a boiling range of 400° F. (204° C.) to 1500° F. (816° C.) or more. The upgraded raffinate and/or extract products can have a reduced or minimized concentration of sulfur, nitrogen, metals, or a combination thereof. The reduced or minimized concentration of sulfur, nitrogen, and/or metals can be achieved by hydrotreating a suitable feed under hydrotreatment conditions corresponding to relatively low levels of feed conversion. Optionally, the feed can also dewaxed, such as by catalytic dewaxing or by solvent dewaxing. Because excessive aromatic saturation is not desired, the pressure for hydrotreatment (and optional dewaxing) can be 500 psig (˜3.4 MPa) to 1200 psig (˜8.2 MPa).

4. 发明授权

US09783748B2 Process for producing diesel fuel 有权
公开(公告)号：US09783748B2
公开(公告)日：2017-10-10
申请号：US14481461
申请日：2014-09-09
申请人： UOP LLC
发明人： Craig Harvey , Haiyan Wang , B. Daniel Thomas , Brian Ganyu , Jagannathan Govindhakannan
IPC分类号： C10G67/06 , C10G67/04 , C10G67/14 , C10L1/02
CPC分类号： C10G67/049 , C10G67/0454 , C10G67/14 , C10G2400/04 , C10L1/026
摘要： One exemplary embodiment can be a process for producing a diesel fuel. The process can include providing a hydrocarbon feed to a residue processing unit. Generally, the residue processing unit includes a solvent deasphalting zone, a hydroprocessing zone, and a hydroprocessing fractionation zone. The process can further include recycling at least a portion of an unconverted oil stream from the hydroprocessing fractionation zone, and sending one part of the at least a portion of the recycled unconverted oil stream to the unconverted oil fractionation zone providing a light unconverted oil stream downstream of the solvent deasphalting zone and a heavy unconverted oil stream to the solvent deasphalting zone.

5. 发明授权

US09783738B2 Hydrocarbon recovery from Fischer-Tropsch off-gas 有权
公开(公告)号：US09783738B2
公开(公告)日：2017-10-10
申请号：US14415123
申请日：2013-07-22
申请人： SHELL OIL COMPANY
发明人： Harold Boerrigter , Andreas Kustosz , Andres Eduardo Leonardi , Lionel Paul Ramone , Wilhelmus Hendrikus Johannes Balk , Pascal Edzo Armin Rots
IPC分类号： C10G2/00 , C01B3/52 , C10G67/04 , C10K1/18 , C10G21/14 , C01B3/34 , C01B3/48 , C10G45/58 , C10G47/00 , C10G67/14
CPC分类号： C10G2/00 , C01B3/34 , C01B3/48 , C01B3/52 , C01B2203/0216 , C01B2203/0233 , C01B2203/0244 , C01B2203/0283 , C01B2203/043 , C01B2203/0475 , C01B2203/065 , C10G2/30 , C10G2/32 , C10G21/14 , C10G45/58 , C10G47/00 , C10G67/049 , C10G67/14 , C10K1/18 , Y02C10/06 , Y02P30/40
摘要： The invention pertains to a method for processing a Fischer-Tropsch off-gas wherein Fischer-Tropsch off-gas is contacted with a wash fluid in a scrubber, and wherein the wash fluid is recycled in a closed loop with a dedicated scrubber, stripper and splitter. The wash fluid preferably is kerosene or LDF. The C3+ hydrocarbons that are recovered from the off-gas are, together with other Fischer-Tropsch product, subjected to hydrocracking or hydrocracking/hydroisomerization. Additionally, hydrogen is recovered from the off-gas.

6. 发明申请

US20170283734A1 Method for Producing Base Lubricating Oil from Waste Oil 审中-公开
公开(公告)号：US20170283734A1
公开(公告)日：2017-10-05
申请号：US15628955
申请日：2017-06-21
申请人： Gen III Oil Corporation
发明人： Martin R. MacDonald
IPC分类号： C10M175/00 , C10G21/06 , B01D3/06 , B01D3/10 , B01D3/40 , C10G21/16 , C10G21/18 , C10G21/20 , C10G21/24 , C10G45/04 , C10G53/04 , C10G67/04 , C10G67/14 , C10G7/00 , C10G21/00 , C10G21/02 , C10G71/00 , C10G7/12
CPC分类号： C10M175/005 , B01D3/065 , B01D3/10 , B01D3/40 , C10G7/003 , C10G7/006 , C10G7/12 , C10G21/006 , C10G21/02 , C10G21/06 , C10G21/16 , C10G21/18 , C10G21/20 , C10G21/24 , C10G45/04 , C10G53/04 , C10G67/04 , C10G67/14 , C10G71/00 , C10G2300/1003 , C10G2300/1007 , C10G2300/301 , C10G2300/308 , C10G2300/4081 , C10G2300/44 , C10G2400/10
摘要： A method for recovering base oil from waste lubricating oil by separating base oil range constituents from a waste lubricating oil mixture, thereafter separating higher quality base oil constituents and lower quality base oil constituents from the base oil recovered from the waste lubricating oil mixture and thereafter treating the lower quality base oil constituents to produce marketable base oil. The total base oil produced from a waste lubricating oil mixture by this process is greater than the quantity producible by previous processes using only base oil separation from the waste lubricating oil mixture or processes which use only treatment of the base oil recovered from the waste lubricating oil mixture to produce the product base oil.

7. 发明申请

US20170275538A1 Method for Producing Base Lubricating Oil from Oils Recovered from Combustion Engine Service 审中-公开
公开(公告)号：US20170275538A1
公开(公告)日：2017-09-28
申请号：US15618603
申请日：2017-06-09
申请人： Gen III Oil Corporation
发明人： Martin R. MacDonald
IPC分类号： C10G53/04 , C07C7/00 , C10G21/02 , C10G67/14 , C10G67/04 , C10G45/04 , C10G21/20 , C10G21/18 , C10G21/16 , C10G7/00 , C10G21/00 , C07C5/02 , C10G21/24
CPC分类号： C10G53/04 , C07C5/02 , C07C7/005 , C10G7/00 , C10G7/003 , C10G7/006 , C10G21/006 , C10G21/02 , C10G21/16 , C10G21/18 , C10G21/20 , C10G21/24 , C10G45/04 , C10G53/06 , C10G53/08 , C10G67/04 , C10G67/14 , C10G2300/1007 , C10G2300/44 , C10G2400/22 , C10G2400/30 , C11B3/006
摘要： A method for producing ILSAC GF5 or higher compatible oils from used oil, comprising separating material having a boiling point less than about 350° F. from recovered oil to produce de-volatized fraction and light oil fraction. Separating material with a boiling point greater than about 350° F. and less than about 650° F. from the de-volatized oil fraction to produce fuel oil fraction and heavy oil fraction. Separating material with a boiling point greater than about 1200° F. from the heavy oil fraction to produce partially purified oil fraction and residual fraction. Treating the partially purified oil fraction to separate it into purified oil fraction and contaminant fraction. Hydrogenating the contaminant fraction to remove predetermined compounds, further saturating the fraction and thereby creating a saturated oil fraction. Fractionating the saturated oil stream to produce one or more of naphtha fraction, diesel oil fraction and base oil fraction.

8. 发明申请

US20170114289A1 SELECTIVE SERIES-FLOW HYDROPROCESSING SYSTEM 有权
公开(公告)号：US20170114289A1
公开(公告)日：2017-04-27
申请号：US15400310
申请日：2017-01-06
申请人： Saudi Arabian Oil Company
发明人： Omer Refa Koseoglu
IPC分类号： C10G67/14 , B01J8/04
CPC分类号： C10G67/14 , B01J8/04 , B01J2208/027 , C10G21/00 , C10G65/02 , C10G65/14 , C10G67/0418 , C10G67/0445 , C10G2300/1096 , C10G2300/202 , C10G2300/44 , C10G2400/02 , C10G2400/04
摘要： Aromatic extraction and hydrocracking processes are integrated to optimize the hydrocracking units design and/or performance. By processing aromatics-rich and aromatic-lean fractions separately, the hydrocracking operating severity and or catalyst reactor volume requirement decreases.

9. 发明申请

US20160208179A1 TARGETED DESULFURIZATION APPARATUS INTEGRATING OXIDATIVE DESULFURIZATION AND HYDRODESULFURIZATION TO PRODUCE DIESEL FUEL HAVING AN ULTRA-LOW LEVEL OF ORGANOSULFUR COMPOUNDS 有权
标题翻译：集中脱硫装置整合氧化脱硫和加氢脱硫以生产具有超低浓度有机化合物的柴油燃料
公开(公告)号：US20160208179A1
公开(公告)日：2016-07-21
申请号：US15082717
申请日：2016-03-28
申请人： Saudi Arabian Oil Company
发明人： Abdennour BOURANE , Omer Refa KOSEOGLU , Mohammed Ibrahim KATHEERI
IPC分类号： C10G67/14
CPC分类号： C10G67/14 , C10G27/04 , C10G27/12 , C10G45/02 , C10G45/08 , C10G67/16 , C10G69/14 , C10G2300/1055 , C10G2300/1059 , C10G2300/202 , C10G2400/04
摘要： Deep desulfurization of hydrocarbon feeds containing undesired organosulfur compounds to produce a hydrocarbon product having low levels of sulfur, i.e., 15 ppmw or less of sulfur, is achieved by flashing the feed at a target cut point temperature to obtain two fractions. A first fraction contains refractory organosulfur compounds, which boil at or above the target cut point temperature. A second fraction boiling below the target cut point temperature is substantially free of refractory sulfur-containing compounds. The second fraction is contacted with a hydrodesulfurization catalyst in a hydrodesulfurization reaction zone operating under mild conditions to reduce the quantity of organosulfur compounds to an ultra-low level. The first fraction is contacted with an oxidizing agent and an active metal catalyst in an oxidation reaction zone to convert the refractory organosulfur compounds to oxidized organosulfur compounds. The oxidized organosulfur compounds are removed, producing a stream containing an ultra-low level of organosulfur compounds. The two streams can be combined to obtain a full range hydrocarbon product having an ultra-low level of organosulfur compounds.
摘要翻译：通过在目标切割点温度下使进料闪烁以获得两个级分来实现含有不需要的有机硫化合物的烃进料的深度脱硫以产生具有低含量硫的烃产物，即15ppmw或更少的硫。第一部分含有难熔有机硫化合物，其沸点在目标切割点温度以上。沸点低于目标切割点温度的第二部分基本上不含难熔含硫化合物。在温和条件下加氢脱硫反应区，第二馏分与加氢脱硫催化剂接触，将有机硫化合物的量减少到超低水平。将第一级分与氧化反应区中的氧化剂和活性金属催化剂接触，以将难熔有机硫化合物转化为氧化的有机硫化合物。除去氧化的有机硫化合物，产生含有超低含量的有机硫化合物的物流。可以将两股流合并，得到具有超低含量的有机硫化合物的全系列烃产物。

10. 发明授权

US09334451B2 High quality middle distillate production process 有权
标题翻译：优质中间馏分生产工艺
公开(公告)号：US09334451B2
公开(公告)日：2016-05-10
申请号：US12724331
申请日：2010-03-15
申请人： Omer Refa Koseoglu , Adnan Al-Hajji , Ali Mahmood Al-Somali , Hendrik Muller , Mohammed Abdullah Al-Ghamdi
发明人： Omer Refa Koseoglu , Adnan Al-Hajji , Ali Mahmood Al-Somali , Hendrik Muller , Mohammed Abdullah Al-Ghamdi
IPC分类号： C10G67/04 , C10G47/00 , C10G67/06 , C10G67/14
CPC分类号： C10G47/00 , C10G67/04 , C10G67/0409 , C10G67/06 , C10G67/14 , C10G2300/1096
摘要： A hydrocarbon feedstock is hydrocracked in a hydrocracking zone and the effluent is fractioned to recover a light fraction, a middle fraction containing aromatic compounds and a heavy fraction. The heavy fraction is recycled to the hydrocracking zone for further hydrocracking. The middle fraction is introduced to an aromatic separation zone. A product stream is recovered from the aromatic separation zone comprising a middle fraction having a reduced content of aromatic compounds as compared to the middle fraction recovered from the fractionator. Aromatics from the aromatic separation zone are recycled to the hydrocracking zone for further hydrogenation and cracking.
摘要翻译：将碳氢化合物原料在加氢裂化区中加氢裂化，并将流出物分馏以回收轻馏分，含有芳族化合物的中间馏分和重馏分。重馏分被再循环到加氢裂化区用于进一步加氢裂化。将中间馏分引入芳族分离区。与从分馏器回收的中间馏分相比，从芳族分离区回收产物流，其包含具有降低的芳族化合物含量的中间馏分。来自芳族分离区的芳烃被再循环到加氢裂化区以进一步氢化和裂化。

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