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.

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.

公开(公告)号：US09163183B2

公开(公告)日：2015-10-20

申请号：US13683181

申请日：2012-11-21

申请人： REG SYNTHETIC FUELS, LLC

发明人： Peter Havlik

IPC分类号： C10G17/02 ,  C10G17/04 ,  C10G21/16 ,  C10G25/00 ,  C10G45/00 ,  C10G45/58 ,  C10G53/04 ,  C10G53/08 ,  C10G53/10 ,  C10G67/04 ,  C10G67/06 ,  C10G67/08 ,  C10G21/00 ,  C10G21/20 ,  C10G21/24

CPC分类号： C10G17/04 ,  C10G21/00 ,  C10G21/16 ,  C10G25/00 ,  C10G45/00 ,  C10G45/58 ,  C10G53/04 ,  C10G53/08 ,  C10G53/10 ,  C10G67/04 ,  C10G67/06 ,  C10G67/08 ,  C10G2300/1022 ,  C10G2300/202 ,  C10G2300/205

摘要： The present disclosure is directed to a method and system of removing solubilized metals from a Fischer-Tropsch (FT) reactor product. The FT reactor product is contacted with a chelating agent to form metal complexes. The FT reactor product containing metal complexes are subjected to centrifugal separation to form a heavy phase and a light phase containing less than 500 wppb solubilized metals.

摘要翻译： 本公开涉及从费 - 托（FT）反应器产物中除去溶解的金属的方法和系统。 使FT反应器产物与螯合剂接触以形成金属络合物。 将含有金属络合物的FT反应器产物进行离心分离以形成含有小于500wppb的溶解金属的重相和轻相。

公开(公告)号：US20140001100A1

公开(公告)日：2014-01-02

申请号：US13877706

申请日：2011-10-05

申请人： Mahpuzah Abai ,  Martin P. Atkins ,  Kuah Y. Cheun ,  John Holbrey ,  Peter Nockemann ,  Ken Seddon ,  Geetha Srinivasan ,  Yiran Zou

发明人： Mahpuzah Abai ,  Martin P. Atkins ,  Kuah Y. Cheun ,  John Holbrey ,  Peter Nockemann ,  Ken Seddon ,  Geetha Srinivasan ,  Yiran Zou

IPC分类号： C10G21/24 ,  C10G21/20 ,  C10G21/22

CPC分类号： C10G21/20 ,  B01D2252/30 ,  B01D2256/24 ,  B01D2257/602 ,  C10G21/06 ,  C10G21/22 ,  C10G21/24 ,  C10G25/003 ,  C10G29/06 ,  C10G2300/1025 ,  C10G2300/104 ,  C10G2300/1044 ,  C10G2300/1051 ,  C10G2300/1055 ,  C10G2300/205 ,  C10G2400/02 ,  C10G2400/04 ,  C10G2400/08 ,  C10L3/101 ,  C10L2290/542

摘要： The present invention relates to a process for the removal of mercury from a mercury-containing hydrocarbon fluid feed using specifically selected ionic liquids comprising, contacting the mercury-containing hydrocarbon fluid feed with an ionic liquid having the formula [Cat+][M+][X−] and separating from the ionic liquid a hydrocarbon fluid product having a reduced mercury content compared to the mercury-containing fluid feed.

摘要翻译： 本发明涉及一种使用特定选择的离子液体从含汞烃流体进料中除去汞的方法，该方法包括：使含汞烃流体进料与具有式[Cat +] [M +] [X - ]并与离子液体分离，与含汞流体进料相比，具有降低的汞含量的烃流体产物。

公开(公告)号：US08608952B2

公开(公告)日：2013-12-17

申请号：US12945786

申请日：2010-11-12

申请人： Manuela Serban ,  Alakananda Bhattacharyya ,  Beckay J. Mezza ,  Kurt M. Vanden Bussche ,  Christopher P. Nicholas ,  Warren K. Bennion

发明人： Manuela Serban ,  Alakananda Bhattacharyya ,  Beckay J. Mezza ,  Kurt M. Vanden Bussche ,  Christopher P. Nicholas ,  Warren K. Bennion

IPC分类号： C10G21/06 ,  C10G67/04 ,  C10G29/20 ,  C10G21/20 ,  C10G21/24 ,  C10G21/28

CPC分类号： C10G21/24 ,  C10G21/28 ,  C10G33/04 ,  C10G2300/1033 ,  C10G2300/203 ,  C10G2300/4081 ,  C10G2300/805

摘要： A process for de-acidifying a hydrocarbon feed includes contacting the hydrocarbon feed containing an organic acid with a feed-immiscible phosphonium ionic liquid to produce a hydrocarbon and feed-immiscible phosphonium ionic liquid mixture and separating the mixture to produce a hydrocarbon effluent having a reduced organic acid content relative to the hydrocarbon feed. Optionally, a de-emulsifier is added to at least one of the contacting and separating steps.

摘要翻译： 用于使烃进料脱酸的方法包括将含有机酸的烃进料与进料不混溶的鏻离子液体接触以产生烃和进料不混溶的鏻离子液体混合物，并分离混合物以产生具有还原的 有机酸含量相对于烃进料。 任选地，将去乳化剂加入到至少一个接触和分离步骤中。

公开(公告)号：US4529503A

公开(公告)日：1985-07-16

申请号：US405645

申请日：1982-08-05

申请人： Semyon G. Kukes

发明人： Semyon G. Kukes

IPC分类号： C10G21/24 ,  C10G25/00 ,  C10G29/02

CPC分类号： C10G21/24

摘要： Metals contained in a hydrocarbon containing feed stream are removed by contacting the hydrocarbon containing feed stream with a phosphorous compound selected from the group consisting of phosphine, hydrocarbylphosphines, hydrocarbylphosphites, hydrocarbylphosphonates, hydrocarbylphosphates, hydrocarbylphosphine oxides, hydrocarbylthiophosphites, and hydrocarbylphosphine sulfides to convert the metals to oil insoluble compounds which can be removed from the hydrocarbon containing feed stream by conventional methods.

摘要翻译： 通过使含烃进料流与选自磷化氢，烃基膦，烃基亚磷酸酯，烃基膦酸酯，烃基磷酸酯，烃基氧化膦，烃基硫代亚磷酸酯和烃基膦硫化物的磷化合物接触将含有烃的进料流中的金属转化为 可通过常规方法从含烃进料流中除去的油不溶性化合物。

公开(公告)号：US11739273B2

公开(公告)日：2023-08-29

申请号：US17250858

申请日：2019-11-09

申请人： GREENOVEL INC.

发明人： Mai Attia ,  Sherif Farag ,  Jamal Chaouki

IPC分类号： C10G17/04 ,  C10G21/16 ,  C10G21/20 ,  C10G21/24 ,  C10G21/28 ,  C10G32/02

CPC分类号： C10G17/04 ,  C10G21/20 ,  C10G32/02 ,  C10G2300/205 ,  C10G2300/4081

摘要： A process for removing metals in a petroleum oil material. The process comprises causing the petroleum oil material to react with a removing agent which comprises a phosphoric acid ester. A microwave irradiation environment was created during the reaction to provide the required energy essential for separating such contaminations from the oil chemical network. The process of the invention is applied at ambient pressure and low temperature compared to the conventional metal removal processes. The process of the invention can be readily scaled up and integrated into an industrial facility.

公开(公告)号：US10920157B2

公开(公告)日：2021-02-16

申请号：US15861044

申请日：2018-01-03

申请人： Saudi Arabian Oil Company

发明人： Omer Refa Koseoglu

IPC分类号： C10G67/06 ,  C10G55/06 ,  B01D3/14 ,  C10G7/00 ,  C10G21/20 ,  B01D11/04 ,  C10G21/24 ,  C10G53/04 ,  C10G67/14 ,  C10G67/04 ,  C10G53/08

摘要： A process for the treatment of a hydrocracking unit bottoms recycle stream, and preferably the fresh hydrocracker feed to remove heavy poly-nuclear aromatic (HPNA) compounds and HPNA precursors employs, in the alternative, an adsorption step which removes most of the HPNA compounds followed by an ionic liquid extraction step to remove the remaining HPNA compounds, or a first ionic liquid extraction step which removes most of the HPNA compounds followed by an adsorption step to remove the remaining HPNA compounds. Ionic liquids of the general formula Q+A− are identified for use in the process; organic polar solvents are identified for removal of the HPNA compounds in solution. Suitable adsorbents are identified for use in packed bed or slurry bed columns that operate within specified temperature and pressure ranges.

公开(公告)号：US09677013B2

公开(公告)日：2017-06-13

申请号：US14201165

申请日：2014-03-07

申请人： PNG GOLD CORPORATION

发明人： Martin R. MacDonald

IPC分类号： C10G67/04 ,  C10G53/04 ,  C07C5/02 ,  C07C7/00 ,  C10G21/16 ,  C10G21/18 ,  C10G21/20 ,  C10G21/24 ,  C10G45/04 ,  C10G67/14 ,  C10G21/02 ,  C10G7/00 ,  C10G21/00

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 oil 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.

公开(公告)号：US08608943B2

公开(公告)日：2013-12-17

申请号：US12945253

申请日：2010-11-12

申请人： Manuela Serban ,  Alakananda Bhattacharyya ,  Beckay J. Mezza ,  Kurt M. Vanden Bussche ,  Christopher P. Nicholas ,  Joseph A. Kocal ,  Warren K. Bennion

发明人： Manuela Serban ,  Alakananda Bhattacharyya ,  Beckay J. Mezza ,  Kurt M. Vanden Bussche ,  Christopher P. Nicholas ,  Joseph A. Kocal ,  Warren K. Bennion

IPC分类号： C10G21/06 ,  C10G67/04 ,  C10G29/20 ,  C10G21/20 ,  C10G21/24 ,  C10G21/28

CPC分类号： C10G21/28 ,  C10G21/24 ,  C10G55/06 ,  C10G67/02 ,  C10G2300/1074 ,  C10G2300/202 ,  C10G2300/4081 ,  C10G2300/805 ,  C10G2400/06

摘要： A process for removing a nitrogen compound from a vacuum gas oil feed includes contacting the vacuum gas oil feed comprising the nitrogen compound with a VGO-immiscible phosphonium ionic liquid to produce a vacuum gas oil and VGO-immiscible phosphonium ionic liquid mixture, and separating the mixture to produce a vacuum gas oil effluent having a reduced nitrogen content relative to the vacuum gas oil feed.

摘要翻译： 从真空瓦斯油进料中除去氮化合物的方法包括将包含氮化合物的减压瓦斯油进料与VGO不混溶的鏻离子液体接触以产生真空瓦斯油和VGO不混溶的鏻离子液体混合物， 混合物以产生相对于减压瓦斯油进料具有降低的氮含量的减压瓦斯油流出物。