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41. 发明申请

WO2013019591A1 SELECTIVE SERIES-FLOW HYDROPROCESSING SYSTEM AND METHOD 审中-公开
标题翻译：选择性系列流量加氢系统和方法
公开(公告)号：WO2013019591A1
公开(公告)日：2013-02-07
申请号：PCT/US2012/048472
申请日：2012-07-27
申请人： SAUDI ARABIAN OIL COMPANY , KOSEOGLU, Omer, Refa
发明人： KOSEOGLU, Omer, Refa
IPC分类号： C10G21/16 , C10G65/14 , C10G67/04 , C10G21/00 , C10G65/02
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.
摘要翻译：整合芳香提取和加氢裂化工艺，以优化加氢裂化装置的设计和/或性能。通过分别处理富含芳香族和芳香族馏分，加氢裂化操作严重度和/或催化剂反应器体积要求降低。

42. 发明申请

WO2013019513A1 PROCESS FOR OXIDATIVE DESULFURIZATION WITH INTEGRATED SULFONE DECOMPOSITION 审中-公开
标题翻译：具有综合磺化分解的氧化脱硫方法
公开(公告)号：WO2013019513A1
公开(公告)日：2013-02-07
申请号：PCT/US2012/048167
申请日：2012-07-25
申请人： SAUDI ARABIAN OIL COMPANY , KOSEOGLU, Omer, Refa , BOURANE, Abdennour
发明人： KOSEOGLU, Omer, Refa , BOURANE, Abdennour
IPC分类号： C07C7/00
CPC分类号： B01J23/06 , B01J21/04 , B01J23/007 , B01J37/06 , B01J37/08 , C10G29/04 , C10G29/16
摘要： The process provided herein is concerned with disposal of oxidized sulfur compounds formed by oxidative desulfurization. The process uses solid base catalyst in the presence of a caustic solution or solid base catalyst pretreated with a base and eliminates the need to separate the sulfones from the hydrocarbon streams and recover the hydrocarbons.
摘要翻译：本文提供的方法涉及通过氧化脱硫形成的氧化硫化合物的处理。该方法在用碱处理的苛性碱溶液或固体碱催化剂存在下使用固体碱催化剂，并且不需要将烃与烃流分离并回收烃。

43. 发明申请

WO2013019509A1 INTEGRATED PROCESS TO PRODUCE ASPHALT AND DESULFURIZED OIL 审中-公开
标题翻译：一体化方法生产沥青和脱硫油
公开(公告)号：WO2013019509A1
公开(公告)日：2013-02-07
申请号：PCT/US2012/048145
申请日：2012-07-25
申请人： SAUDI ARABIAN OIL COMPANY , KOSEOGLU, Omer, Refa , BOURANE, Abdennour
发明人： KOSEOGLU, Omer, Refa , BOURANE, Abdennour
IPC分类号： C10G1/00
CPC分类号： C10G1/00 , C10G2300/202 , C10G2300/4006 , C10G2300/4012 , C10G2300/44
摘要： An integrated process is provided to produce asphalt and desulfurized oil. Sulfur molecules contained in heavy petroleum fractions, including organosulfur molecules, and in certain embodiments organonitrogen molecules are oxidized. The polar oxidized sulfur compounds shift from the oil phase to the asphalt phase.
摘要翻译：提供了生产沥青和脱硫油的综合工艺。包含在重质石油馏分中的硫分子，包括有机硫分子，在某些实施方案中，有机硫分子被氧化。极性氧化硫化合物从油相转变为沥青相。

44. 发明申请

WO2013019321A1 SOLVENT-ASSISTED DELAYED COKING PROCESS 审中-公开
标题翻译：溶剂辅助延迟的焦化工艺
公开(公告)号：WO2013019321A1
公开(公告)日：2013-02-07
申请号：PCT/US2012/041897
申请日：2012-06-11
申请人： SAUDI ARABIAN OIL COMPANY , KOSEOGLU, Omer, Refa
发明人： KOSEOGLU, Omer, Refa
IPC分类号： C10B55/00 , C10B57/04 , C10G9/00
CPC分类号： C10B57/045 , C10B55/00 , C10G9/005
摘要： An improved process for the delayed coking of a heavy residual hydrocarbon feedstock to reduce the coking induction period and to enhance the coking process relative to the processes of the prior art is achieved by mixing a sufficient volume of a paraffinic solvent having the formula CnH2n+2, where n = 3 to 8 with the heavy feedstock to disturb the equilibrium of asphaltenes in the solution of maltenes in order to flocculate substantially all of the solid asphaltenes particles to thereby increase the yield and quality of valuable liquid products and minimize undesirable cracking reactions that result in high molecular weight polymers and the formation of coke.
摘要翻译：通过混合足够体积的具有式C n H 2n + 2的链烷烃溶剂来实现重质残余烃原料的延迟焦化以减少焦化诱导期和改进与现有技术方法相关的焦化方法的改进方法，其中n = 3至8，其中重质原料扰乱麦芽糖溶液中沥青质的平衡，以便基本上絮凝所有固体沥青质颗粒，从而提高有价值的液体产物的产率和质量，并使不合需要的开裂反应最小化导致高分子量聚合物和焦炭的形成。

45. 发明申请

WO2012050692A1 INTEGRATED DEASPHALTING AND OXIDATIVE REMOVAL OF HETEROATOM HYDROCARBON COMPOUNDS FROM LIQUID HYDROCARBON FEEDSTOCKS 审中-公开
标题翻译：来自液体烃的异源烃化合物的一体化去除和氧化除去
公开(公告)号：WO2012050692A1
公开(公告)日：2012-04-19
申请号：PCT/US2011/050990
申请日：2011-09-09
申请人： SAUDI ARABIAN OIL COMPANY , KOSEOGLU, Omer, Refa , BOURANE, Abdennour
发明人： KOSEOGLU, Omer, Refa , BOURANE, Abdennour
IPC分类号： C10G61/00
CPC分类号： C10G27/12 , B01J21/063 , B01J23/22 , B01J23/28 , B01J23/30 , C10G2300/202 , C10G2300/206 , C10G2300/44
摘要： A system and process are provided for integrated deasphalting and desulfurization of hydrocarbon feedstock in which the hydrocarbon feedstock, an oxidant, and an oxidation catalyst are mixed prior to passage into a primary settler of a solvent deasphalting unit. Oxidation products, including oxidized organosulfur compounds, are discharged with the asphalt phase.
摘要翻译：提供了一种用于烃原料的综合脱沥青和脱硫的系统和方法，其中烃原料，氧化剂和氧化催化剂在通入溶剂脱沥青装置的初级沉降器之前混合。包括氧化有机硫化合物在内的氧化产物用沥青相排出。

46. 发明申请

WO2011043904A1 PRESSURE CASCADED TWO-STAGE HYDROCRACKING UNIT 审中-公开
标题翻译：压力式两级加压装置
公开(公告)号：WO2011043904A1
公开(公告)日：2011-04-14
申请号：PCT/US2010/049031
申请日：2010-09-16
申请人： SAUDI ARABIAN OIL COMPANY , KOSEOGLU, Omer, Refa
发明人： KOSEOGLU, Omer, Refa
IPC分类号： C10G55/00
CPC分类号： C10G65/10 , B01J23/8885 , B01J29/076 , B01J2219/00006 , B01J2219/0004 , C10G45/08 , C10G47/16 , C10G65/12 , C10G2300/202 , C10G2300/207 , C10G2300/301 , C10G2400/02 , C10G2400/04
摘要： A method and apparatus for hydrocracking an oil feedstock to produce a light oil stream without build-up of heavy polynuclear aromatic (HPNA) hydrocarbons in the recycle stream is provided. The method includes the steps of (1) hydrocracking the oil feedstock with a hydrotreating catalyst in a first reactor to produce an effluent stream; (2) fractionating the effluent stream into first, second and third product streams, wherein the first product stream includes C 1 -C 4 , naphtha and diesel boiling in the range of 36-370 °C, the second product stream includes hydrocarbon components with an initial nominal boiling point of 370 °C and a final boiling point ranging from 420-480 °C, and the third product stream that includes HPNA hydrocarbons and other hydrocarbons boiling above about 4200C to about 4800C, depending upon the final boiling point of the second product stream; (3) cracking the second product stream in a second reactor; and (4) cracking the third product stream in a third reactor at a higher operational pressure than the second reactor.
摘要翻译：提供了一种用于加氢裂化油原料以生产轻油流而不在再循环流中堆积重多环芳烃（HPNA）烃的方法和装置。该方法包括以下步骤：（1）在第一反应器中用加氢处理催化剂加氢裂化油原料以产生流出物流; （2）将流出物流分馏成第一，第二和第三产物流，其中第一产物流包括在36-370℃范围内沸腾的C1-C4，石脑油和柴油，第二产物流包括具有初始标称沸点为370℃，最终沸点为420-480℃，第三产物流包括HPNA烃和沸点高于约4200℃至约4800℃的其它烃，这取决于第二产物的最终沸点流; （3）在第二反应器中裂化第二产物流; 和（4）在第三反应器中以比第二反应器更高的操作压力裂化第三产物流。

47. 发明申请

WO2008051498A2 ENHANCED SOLVENT DEASPHALTING PROCESS FOR HEAVY HYDROCARBON FEEDSTOCKS UTILIZING SOLID ADSORBENT 审中-公开
标题翻译：使用固体吸附剂的重油加氢催化剂的增溶溶剂去除方法
公开(公告)号：WO2008051498A2
公开(公告)日：2008-05-02
申请号：PCT/US2007/022381
申请日：2007-10-19
申请人： SAUDI ARABIAN OIL COMPANY , KOSEOGLU, Omer, Refa
发明人： KOSEOGLU, Omer, Refa
IPC分类号： C10G67/04
CPC分类号： C10G21/003 , C10G25/00 , C10G25/003 , C10G25/05
摘要： A solvent deasphalting of crude oil or petroleum heavy fractions and residues is carried out in the presence of a solid adsorbent, such as clay, silica, alumina and activated carbon, which adsorbs the contaminants and permits the solvent and oil fraction to be removed as a separate stream from which the solvent is recovered for recycling; the adsorbent with contaminants and the asphalt bottoms is mixed with aromatic and/or polar solvents to desorb the contaminants and washed as necessary, e.g.. with benzene, toluene, xylenes and terahydrofuran. to clean adsorbent which is recovered and recycled; the solvent-asphalt mixture is sent to a fractionator for recovery and recycling of the aromatic or polar solvent. The bottoms from the fractionator include the concentrated PNA and contaminants and are further processed as appropriate.
摘要翻译：原油或石油重馏分和残余物的溶剂脱沥青在固体吸附剂如粘土，二氧化硅，氧化铝和活性炭的存在下进行，其吸附污染物并允许将溶剂和油馏分作为回收溶剂的回收分离物流; 具有污染物的吸附剂和沥青底部物质与芳族和/或极性溶剂混合以解吸污染物并根据需要例如用苯，甲苯，二甲苯和四氢呋喃洗涤。清洁回收和再循环的吸附剂; 将溶剂 - 沥青混合物送至分馏器以回收和再循环芳族或极性溶剂。来自分馏器的底部物质包括浓缩的PNA和污染物，并且根据需要进一步加工。

48. 发明申请

WO2022010714A1 HEAVY FUEL OIL BLENDING COMPOSITION CONTAINING DISSOLVED POLYSTYRENE WASTE 审中-公开
公开(公告)号：WO2022010714A1
公开(公告)日：2022-01-13
申请号：PCT/US2021/039926
申请日：2021-06-30
申请人： SAUDI ARABIAN OIL COMPANY , KOSEOGLU, Omer, Refa , HODGKINS, Robert, Peter
发明人： KOSEOGLU, Omer, Refa , HODGKINS, Robert, Peter
IPC分类号： C10L1/16 , C08J11/08 , C10L1/04 , C10L5/48
摘要： A low value aromatic fuel blending composition containing dissolved waste polystyrene materials having a calorie value comparable to the heavy aromatic compounds in which it is dissolved is disclosed, along with a process for its production from a mixture of heavy aromatic hydrocarbons recovered as the bottoms/reject streams from a variety of refinery aromatics recovery units.

49. 发明申请

WO2021118855A1 SELECTIVE REFORMING PROCESS TO PRODUCE GASOLINE BLENDING COMPONENTS AND AROMATICS 审中-公开
公开(公告)号：WO2021118855A1
公开(公告)日：2021-06-17
申请号：PCT/US2020/063021
申请日：2020-12-03
申请人： SAUDI ARABIAN OIL COMPANY , KOSEOGLU, Omer, Refa , AL-SHAREEF, Ali, H.
发明人： KOSEOGLU, Omer, Refa , AL-SHAREEF, Ali, H.
IPC分类号： C10G35/085 , C10G61/04 , C10G21/06 , C10G21/28 , C10G25/00 , C10G61/06
摘要： Improved catalytic reforming processes and systems employ reforming reactors in a more efficient manner and can avoid problems associated with yield loss. Aromatics and isoparaffins are separated prior to passing to a reforming unit. An integrated process for producing gasoline blending components includes: separating a naphtha feedstream into an aromatic-rich stream and an aromatic-lean stream; separating the aromatic-lean stream into an isoparaffin-rich stream and an isoparaffin-lean stream; and catalytically reforming the isoparaffin-lean stream to produce a reformate stream.

50. 发明申请

WO2020214241A1 METHOD TO IMPROVE THE EFFICIENCY OF PIPELINE TRANSPORTATION OF HEAVY OILS 审中-公开
公开(公告)号：WO2020214241A1
公开(公告)日：2020-10-22
申请号：PCT/US2020/019183
申请日：2020-02-21
申请人： SAUDI ARABIAN OIL COMPANY , HODGKINS, Robert, Peter , KOSEOGLU, Omer, Refa
发明人： HODGKINS, Robert, Peter , KOSEOGLU, Omer, Refa
IPC分类号： C10G27/04 , C10L1/24 , F17D1/17
摘要： Disulfide oil (DSO) compounds recovered as a by-product of the mercaptan oxidation of a hydrocarbon refinery feedstock and their oxidized derivatives, oxidized disulfide oils (ODSO) are effective as a diluent to lower the viscosity and thereby improve the pipeline transportation properties of heavy oils, and particularly of wellhead crude oil. The use of the DSO and/or ODSO compounds as diluents converts an otherwise extremely low value or waste oil product into a valuable commodity that has utility in improving the transportation properties of heavy oils, particularly in oil field pipeline applications.

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