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公开(公告)号:US09909075B2
公开(公告)日:2018-03-06
申请号:US14501516
申请日:2014-09-30
Inventor: Benjamin Klein , Odette Eng
CPC classification number: C10G55/04 , C10G7/00 , C10G7/02 , C10G7/06 , C10G7/12 , C10G9/005 , C10G2300/1033 , C10G2300/1077 , C10G2300/301 , C10G2400/02 , C10G2400/04 , C10G2400/06 , C10G2400/08
Abstract: Systems and methods for refining conventional crude and heavy, corrosive, contaminant-laden carbonaceous crude (Opportunity Crude) in partially or totally separated streams or trains.
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公开(公告)号:US20180030359A1
公开(公告)日:2018-02-01
申请号:US15729927
申请日:2017-10-11
Applicant: Saudi Arabian Oil Company
Inventor: Esam Zaki HAMAD , Yuguo X. WANG
CPC classification number: C10G25/12 , C10G25/003 , C10G25/05 , C10G67/06 , C10G2300/1033 , C10G2300/202 , C10G2300/207 , C10G2300/4093 , C10G2300/44
Abstract: A whole crude oil desulfurization system and process includes a combination of an adsorption zone and a hydroprocessing zone. This combined process and system reduces the requisite throughput for the hydroprocessing unit, conventionally a very costly and process both in terms of energy expenditures and catalyst depletion. By first contacting the whole crude oil feedstock with an adsorbent for the sulfur-containing compounds, the adsorption effluent having a relatively lower sulfur content can be collected and provided to refiners without further treatment. The adsorbates, including adsorbed organosulfur compounds, are solvent desorbed resulting in a stream containing high levels of organosulfur compounds and a solvent. Following recovery of the solvent, the volume of the sulfur-containing feedstream that remains to be desulfurized in the hydroprocessing zone is substantially less than the original amount of whole crude oil feedstock.
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公开(公告)号:US09873838B2
公开(公告)日:2018-01-23
申请号:US15090157
申请日:2016-04-04
Applicant: William Dale Storey , Norman L. Arrison , Dale R. Schadeck
Inventor: William Dale Storey , Norman L. Arrison , Dale R. Schadeck
IPC: C09K8/528 , C10G31/08 , B01D53/78 , B01D53/52 , B01D53/62 , B01D53/48 , B01D53/14 , C10L3/10 , C10G29/20 , B01D53/40
CPC classification number: C10G31/08 , B01D53/1456 , B01D53/1493 , B01D53/40 , B01D2251/108 , B01D2251/306 , B01D2252/103 , B01D2252/2021 , B01D2252/204 , B01D2252/20405 , B01D2252/20421 , B01D2252/20484 , B01D2256/24 , B01D2257/304 , B01D2257/306 , B01D2257/308 , B01D2257/504 , C09K8/528 , C09K2208/20 , C10G29/20 , C10G2300/1025 , C10G2300/1033 , C10G2300/207 , C10G2300/805 , C10L3/103 , C10L3/104 , C10L2290/545 , Y02P20/152
Abstract: The invention is directed to a treatment fluid comprising electrolyzed water and an amine, and methods for producing and using same in the treatment of a gas or liquid containing a contaminant such as an acid gas or a sulphur compound.
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公开(公告)号:US09872343B2
公开(公告)日:2018-01-16
申请号:US14705182
申请日:2015-05-06
Applicant: HARRIS CORPORATION
Inventor: Francis Eugene Parsche
CPC classification number: H05B6/106 , C10G1/00 , C10G1/02 , C10G2300/1033 , H05B6/80 , H05B2214/03
Abstract: A method for heating materials by application of radio frequency (“RF”) energy is disclosed. For example, the disclosure concerns a method for RF heating of petroleum ore, such as bitumen, oil sands, oil shale, tar sands, or heavy oil. Petroleum ore is mixed with a substance comprising susceptor particles that absorb RF energy. A source is provided which applies RF energy to the mixture of a power and frequency sufficient to heat the susceptor particles. The RF energy is applied for a sufficient time to allow the susceptor particles to heat the mixture to an average temperature greater than about 212° F. (100° C.). Optionally, the susceptor particles can be removed from the mixture after the desired average temperature has been achieved. The susceptor particles may provide for anhydrous processing, and temperatures sufficient for cracking, distillation, or pyrolysis.
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公开(公告)号:US09856727B2
公开(公告)日:2018-01-02
申请号:US14889039
申请日:2014-12-31
Applicant: Halliburton Energy Services, Inc.
Inventor: Sanja Natali , Jason D. Dykstra , Yuzhen Xue , Zhijie Sun
CPC classification number: E21B43/34 , C09K8/52 , C09K8/584 , C10G33/04 , C10G2300/1033 , C10G2300/201 , C10G2300/4037 , E21B21/068 , E21B49/086
Abstract: Systems comprising a main tubular coupled to a pump and extending from a surface into a subterranean formation, wherein produced bulk fluid is pumped to the surface, and wherein the bulk fluid comprises at least water and a hydrocarbon, and has certain constituent parameters; a storage container for retaining the bulk fluid; a sampling tubular in fluid communication with the main tubular for sampling the bulk fluid, thereby forming at least one sampled fluid; and a dosing system coupled to the sampling tubular and configured to receive the sampled fluid, the dosing system configured to determine a constituent parameter of the sampled fluid, identify a type and concentration of separating surfactant to include in the bulk fluid to obtain a hydrophilic-lipophilic deviation (HLD) substantially equal to 0, and introduce the identified type and concentration of the separating surfactant into the storage container retaining the bulk fluid.
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公开(公告)号:US09856422B2
公开(公告)日:2018-01-02
申请号:US13989154
申请日:2011-11-23
Applicant: Christopher Hardacre , Peter Goodrich , Azlan Hussain , David Rooney
Inventor: Christopher Hardacre , Peter Goodrich , Azlan Hussain , David Rooney
CPC classification number: C10G21/16 , C07C51/48 , C07C211/63 , C10G19/02 , C10G21/27 , C10G21/28 , C10G2300/1033 , C10G2300/104 , C10G2300/1051 , C10G2300/1055 , C10G2300/1059 , C10G2300/203 , Y02P20/582 , C07C63/36
Abstract: The present invention relates to a process for the removal of naphthenic acids from crude oils and crude oil distillates by use of supported basic ionic liquids.
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公开(公告)号:US20170368484A1
公开(公告)日:2017-12-28
申请号:US15545592
申请日:2015-01-23
Applicant: NORWEGIAN FIELD INDUSTRY AS
Inventor: Marius Armann NILO
CPC classification number: B01D36/003 , B01D1/16 , B01D1/20 , B01D17/042 , B01D17/044 , B01D29/111 , B01D29/906 , B01D35/005 , C10G31/06 , C10G31/09 , C10G33/06 , C10G2300/1033 , C10G2300/1062 , C10G2300/208 , C10G2400/10
Abstract: A Filter for the removal of water from oil, the filter includes a distillation element having an inlet pipe that in one end is to be fluidly connectable to a reservoir of oil to be filtered, and in the other end being fluidly connected to a distillation head, said distillation head including a plurality of compressing tubes for injecting under pressure said oil into an evaporation chamber, whereby eventual water within the oil droplet evaporates from said decompressed oil, the filter further including a tubular core with a plurality of apertures and a hollow interior, said core having an open end for fluid communication with the hollow interior, a length of yarn wound around an outer surface of the core, wherein the filter further includes a device for blowing air or an inert gas into the evaporation chamber for removal of the water vapor during use of the filter. A method of manufacturing such a filter, as well as a method of removing water of is also disclosed. The water removal unit is part of a modular system, which makes the whole filter unit scalable within fixed steps. When water removing block with attached start block and end block, are stacked upon each other, and connected to filter unit, it becomes scalable complete cleaning equipment. Pump and motor must be adapted to each configuration.
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公开(公告)号:US09815750B2
公开(公告)日:2017-11-14
申请号:US14466444
申请日:2014-08-22
Applicant: JX Nippon Oil & Energy Corporation
Inventor: Shinichiro Yanagawa , Masahide Kobayashi , Yuko Aoki , Kazuaki Hayasaka
CPC classification number: C07C4/06 , B01J29/061 , B01J29/405 , B01J37/28 , B01J2229/37 , C07C2529/06 , C07C2529/40 , C07C2529/85 , C07C2529/87 , C10G2300/1033 , C10G2300/1044 , C10G2300/1048 , C10G2300/1051 , C10G2300/1055 , C10G2300/1059 , C10G2300/301 , C10G2400/30
Abstract: A catalyst for producing monocyclic aromatic hydrocarbons, used for producing monocyclic aromatic hydrocarbons of 6 to 8 carbon number from a feedstock oil having a 10 volume % distillation temperature of at least 140° C. and an end point temperature of not more than 400° C., wherein the catalyst contains a crystalline aluminosilicate, gallium and/or zinc, and phosphorus, the molar ratio between silicon and aluminum (Si/Al ratio) in the crystalline aluminosilicate is not more than 100, the molar ratio between the phosphorus supported on the crystalline aluminosilicate and the aluminum of the crystalline aluminosilicate (P/Al ratio) is not less than 0.01 and not more than 1.0, and the amount of gallium and/or zinc is not more than 1.2% by mass based on the mass of the crystalline aluminosilicate.
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公开(公告)号:US09745520B2
公开(公告)日:2017-08-29
申请号:US14969019
申请日:2015-12-15
Applicant: Phillips 66 Company
Inventor: Zhenhua Mao
CPC classification number: C10G25/003 , C10G25/06 , C10G25/12 , C10G31/00 , C10G31/09 , C10G2300/1033 , C10G2300/201 , C10G2300/208
Abstract: The invention relates to removing contaminants from oil using solid sorbents that are comprised primarily of carbon and preferably of coke particles. The coke particles have an affinity for contaminants in oil and are sized to be filtered from oil without plugging. Most contaminants have such a small size that they tend to plug up filters. As the contaminants agglomerate onto the solid sorbent, the resulting particles form a filter cake on conventional filter materials in such a way as to allow the oil to pass on through without significant pressure drop or delay.
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公开(公告)号:US09701914B2
公开(公告)日:2017-07-11
申请号:US11983078
申请日:2007-11-07
Applicant: M. Rashid Khan , Othman A. Taha
Inventor: M. Rashid Khan , Othman A. Taha
CPC classification number: C10G11/187 , B01J23/10 , B01J29/084 , B01J29/40 , B01J29/80 , C10G11/05 , C10G2300/1033 , C10G2300/1044 , C10G2300/1059 , C10G2300/1074 , C10G2300/4006 , C10G2300/4081 , C10G2400/20 , G05D21/02
Abstract: With an aim to optimize propylene production, petroleum oil such as gas oil is catalytically cracked by contacting the oil with catalyst mixture consisting of a base cracking catalyst containing an stable Y-type zeolite and small amounts of rare-earth metal oxide, and an additive containing a shape-selective zeolite, in a down-flow type fluid catalytic cracking apparatus having a regeneration zone, a separation zone, and a stripping zone, wherein conversion of hydrocarbon occurs under relatively severe conditions. According to this fluid catalytic cracking process, the production of light-fraction olefins such as propylene is maximized by applying appropriate process control, monitoring, and optimizing systems. Process model and historical data to test a predictive system can provide early warning of potential performance degradation and equipment failure in the FCC unit.
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