公开(公告)号：US20190233746A1

公开(公告)日：2019-08-01

申请号：US15885554

申请日：2018-01-31

申请人： UOP LLC

发明人： Jagannathan Govindhakannan ,  Hans G. Lefebvre

IPC分类号： C10G53/06

CPC分类号： C10G53/06 ,  C10G2300/206

摘要： Solvent deasphalting (SDA) is used to extract deasphalted oil from heavier hydrocarbons in series. The pitch stream from solvent deasphalting is calcined to recover volatile hydrocarbon vapor products and calcined solids. The hydrocarbon vapors can be fractionated to recover valuable transportation range fuel products. The pitch stream can be first fed to the fractionation column before calcination.

公开(公告)号：US20170355655A1

公开(公告)日：2017-12-14

申请号：US15540821

申请日：2015-12-24

申请人： SHELL OIL COMPANY

发明人： Jean Paul Andre Marie Joseph Ghislain LANGE ,  Guus VAN ROSSUM ,  Sascha Reinier Aldegonda KERSTEN ,  Shushil KUMAR

IPC分类号： C07C7/10 ,  C10G1/00 ,  C10G1/06 ,  B01D11/04

CPC分类号： C07C7/10 ,  B01D11/0492 ,  C10G1/002 ,  C10G1/04 ,  C10G1/06 ,  C10G1/065 ,  C10G3/00 ,  C10G21/12 ,  C10G21/28 ,  C10G53/06 ,  C10G2300/1011 ,  C10G2300/1014 ,  C10G2300/44 ,  Y02P30/20 ,  C07C9/00

摘要： A process for liquid-liquid extraction of an oil-blend of non-uniform oligomeric and polymeric components comprising: (a) preselecting a desired molecular weight (Mw) boundary between heavy and light components; (b) selecting an extractive solvent or an extractive mixture of solvents, which form essentially a single phase with the light components; (c) mixing the oil-blend and the extractive solvent or extractive mixture of solvents selected in step (b) at elevated temperature, which is at least at or above said fractionation temperature, and wherein the extractive solvent/mixture of solvents to oil-blend ratio is from 1:2 to 100:1; (d) allowing a phase split to form between the heavy components fraction and the light components/extractive solvent fraction at the fractionation temperature or at most 10° C. below the fractionation temperature; (e) followed by separation of said fractions.

公开(公告)号：US20170130143A1

公开(公告)日：2017-05-11

申请号：US15416069

申请日：2017-01-26

申请人： PNG Gold Corporation

发明人： Martin R. MacDonald

IPC分类号： C10G53/04 ,  C10G53/08 ,  C10G53/06

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 recovering synthetic oils from a feed stream, the method comprising separating at least a portion of the non-synthetic oil constituents from a commingled stream to produce a partially purified synthetic oil stream and one or more contaminant streams. Extracting at least a portion of the synthetic oil from the partially purified synthetic oil stream to produce a synthetic oil stream and a second contaminant stream.

公开(公告)号：US20170081595A1

公开(公告)日：2017-03-23

申请号：US15369369

申请日：2016-12-05

申请人： PT PERTAMINA (PERSERO) ,  PT PURA BARUTAMA

发明人： Meliana YANA ,  Supriyantini NUNIK ,  Joseph TUNDANG ,  Sudiyatmoko BAMBANG

IPC分类号： C10G21/16 ,  C10G21/02

CPC分类号： C10G21/16 ,  C10G21/02 ,  C10G53/06 ,  C10G2300/302 ,  C10G2300/308 ,  C10G2300/4025 ,  C10G2300/44 ,  C10G2300/802 ,  C10G2400/18 ,  C10G2400/30

摘要： Process for TDAE-1 and TDAE-2 production is initiated with production of DAE Feeds which have kinematic viscosity at 100° C. ranges 24-67 cSt, followed by mixing them with solvent to yield Mixture of DAE Feed with density ranges 0.75-0.85 kg/liter and further contacting the Mixture of DAE Feed with solvent, like furfural, NMP and DMSO to facilitate a counter current liquid-liquid extraction, wherein the TDAE-1 and TDAE-2 are produced at ratio of polar solvent to Mixture of DAE Feed ranges 1.7-2.0 and 0.5-1.7, respectively. The PCA content of TDAE-1 and TDAE-2 are less than 3% weight and 3-20% weight. The amount of 8 Grimmer polyaromatics hydrocarbon content in the TDAE-1 and TDAE-2 are the same, that is, less than 10 mg/kg including Benzo (a) pyrene substance as much as less than 1 mg/kg.

公开(公告)号：US20160288014A1

公开(公告)日：2016-10-06

申请号：US15085582

申请日：2016-03-30

申请人： COUNCIL OF SCIENTIFIC & INDUSTRIAL RESEARCH

发明人： MADHUKAR ONKARNATH GARG ,  PRASENJIT GHOSH ,  SUNIL KUMAR ,  SHRIKANT MADHUSUDAN NANOTI ,  BHAGAT RAM NAUTIYAL

IPC分类号： B01D3/40 ,  B01D3/10 ,  B01D3/00 ,  C07C7/08 ,  C10G7/06

CPC分类号： B01D3/40 ,  B01D3/007 ,  B01D3/10 ,  C07C7/08 ,  C10G21/20 ,  C10G21/28 ,  C10G53/06 ,  C10G55/06 ,  C10G2400/02 ,  C10G2400/30

摘要： Disclosed is a process for simultaneous production of benzene lean gasoline and recovery of high purity aromatics from narrow boiling light cracked gasoline fractions. The present invention provides a vacuum based two stage extractive distillation process, with pure NMP, for production of benzene lean gasoline (benzene content less than 0.4 Weight %) by recovery of high purity aromatics (purity more than 99 Weight %) from cracked gasoline fractions (boiling in the range of 40-90° C.) comprising benzene in the range of 10-30 weight % and close-boiling non-aromatic hydrocarbons like paraffins, iso-paraffins, olefins, di-olefins (including conjugated di-olefins), and naphthenes in the range of 70-90 weight % along with impurities containing but not limited to oxygenates, metals, chlorides, sulphur compounds, nitrogen compounds and organic peroxides.The present invention provides an improved extractive distillation process for simultaneous production of benzene lean gasoline and benzene rich product from cracked gasoline fraction, with higher recovery of better quality products along with lower utility requirements and investment costs.

摘要翻译： 本发明提供了一种改进的萃取蒸馏方法，用于同时生产来自裂化汽油馏分的苯稀汽油和富苯产物，具有更高质量产品的回收率以及更低的效用要求和投资成本。

公开(公告)号：US20020157989A1

公开(公告)日：2002-10-31

申请号：US10128066

申请日：2002-04-23

申请人： Clearwater, Inc.

发明人： Larry W. Gatlin ,  Wayne Mueller

IPC分类号： C10G029/00 ,  C10G029/04

CPC分类号： C10G53/06 ,  C02F1/58 ,  C02F1/683 ,  C02F2303/02 ,  C10G27/06 ,  C10G29/06 ,  C10G29/08 ,  C10G29/205 ,  C10G31/08 ,  C10G33/04

摘要： Potassium formate is used together with a sulfide scavenger to remove and otherwise treat sulfhydryl compounds such as hydrogen sulfide present in hydrocarbons and aqueous substrates

摘要翻译： 甲酸钾与硫化物清除剂一起使用以除去和以其他方式处理巯基化合物，例如烃和含水基质中存在的硫化氢

公开(公告)号：US06375802B1

公开(公告)日：2002-04-23

申请号：US09553697

申请日：2000-04-20

申请人： Joseph C. Gentry ,  Fu-Ming Lee

发明人： Joseph C. Gentry ,  Fu-Ming Lee

IPC分类号： B01D1100

CPC分类号： C10G21/00 ,  C10G53/00 ,  C10G53/06 ,  C10G53/16

摘要： An improved process for the recovery of aromatic compounds from a mixture containing aromatic and non-aromatic compounds and method for retrofitting existing equipment for the same is provided. The improved process comprises the steps of recovering aromatic compounds via parallel operation of a hybrid extractive distillation/liquid-liquid extractor operation and variations thereof. Methods of quickly and economically retrofitting existing recovery process equipment for use with the improved aromatics recovery process are also disclosed.

摘要翻译： 提供了一种用于从含有芳族和非芳香族化合物的混合物中回收芳族化合物的改进方法以及用于改造现有设备的方法。 改进的方法包括通过混合萃取蒸馏/液 - 液萃取器操作及其变化的并行操作来回收芳族化合物的步骤。 还公开了快速和经济地改造用于改进的芳烃回收方法的现有回收工艺设备的方法。

公开(公告)号：US5009772A

公开(公告)日：1991-04-23

申请号：US315489

申请日：1989-02-27

申请人： Stephen R. Nelson ,  Richard L. Hood

发明人： Stephen R. Nelson ,  Richard L. Hood

IPC分类号： C10G21/00 ,  C10G53/06

CPC分类号： C10G53/06 ,  C10G21/003

摘要： A solvent extraction process for separating a heavy hydrocarbon feedstock material into its various component parts. The process comprises the utilization of pressure reduction to enhance the separation and recovery of a deasphalted oil product comprising substantially the lower molecular weight hydrocarbon components present in the original heavy hydrocarbon feedstock material.

摘要翻译： 用于将重质烃原料分离成其各种组分部分的溶剂萃取方法。 该方法包括利用减压来增强脱沥青油产品的分离和回收，所述脱沥青油产品基本上包含存在于原始重质烃原料中的较低分子量烃成分。

公开(公告)号：US2690417A

公开(公告)日：1954-09-28

申请号：US13375349

申请日：1949-12-19

申请人： STANDARD OIL CO

发明人： HAROLD SHALIT ,  DETERS JOHN F ,  LIEN ARTHUR P

IPC分类号： C10G53/06 ,  C10G53/10

CPC分类号： C10G53/06 ,  C10G53/10

公开(公告)号：US20190016648A1

公开(公告)日：2019-01-17

申请号：US16034572

申请日：2018-07-13

申请人： IFP Energies nouvelles

发明人： Beatrice FISCHER ,  Vincent COUPARD

IPC分类号： C07C2/76 ,  C07C7/11 ,  C07C7/00 ,  F25J3/02 ,  B01D53/04

CPC分类号： C07C2/76 ,  B01D53/0423 ,  C07C7/005 ,  C07C7/11 ,  C10G11/18 ,  C10G21/00 ,  C10G50/00 ,  C10G53/04 ,  C10G53/06 ,  C10G55/06 ,  C10G57/02 ,  C10G70/048 ,  C10G70/06 ,  C10G2400/02 ,  C10G2400/20 ,  C10G2400/30 ,  F25J3/0209 ,  F25J3/0242 ,  F25J3/0247 ,  F25J2215/64 ,  F25J2215/66

摘要： The present invention describes a process for fractionating the gaseous fraction leaving overhead from the fractionation column of a catalytic cracking unit (FCC) using a unit for the conversion of ethylene into propylene, in order to upgrade the ethylene contained in the fuel gas.