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1. 发明申请

WO2005074440A2 SUPERCRITICAL HYDROCARBON CONVERSION PROCESS 审中-公开
标题翻译：超临界碳氢转化过程
公开(公告)号：WO2005074440A2
公开(公告)日：2005-08-18
申请号：PCT/US2004/037645
申请日：2004-11-10
申请人： KELLOGG BROWN & ROOT, INC. , McCALL, Thomas, F. , RAMAMURTHY, Pritham , SHAH, Kiran, V. , SILVERMAN, Michael, A. , VAN SICKELS, Martin, J.
发明人： McCALL, Thomas, F. , RAMAMURTHY, Pritham , SHAH, Kiran, V. , SILVERMAN, Michael, A. , VAN SICKELS, Martin, J.
IPC分类号： C01G11/02 , C10G9/28 , C10G9/32 , C10G69/06
CPC分类号： C10G9/28 , C10G9/32 , C10G69/06
摘要： Supercritical conversion of hydrocarbons (108,208) boiling above 538°C (1000°F) with a solvating hydrocarbon (106,206) at a weight ratio of solvating hydrocarbon to high-boiling hydrocarbons of at least 2:1 and at conditions above the critical temperature and pressure of the high-boiling hydrocarbons-solvent mixture, in the presence of hot fluidized solids (136,236). The hydrocarbons (108,208) are supplied to a reaction zone (114,214) at a temperature below that of the hot solids (136,236) supplied thereto, whereby the resulting hydrocarbons-solids suspension has a thermal equilibrium temperature corresponding to the reaction temperature. The conversion has high rates of sulfur, nitrogen and metals removal, nearly complete conversion to lower molecular weight products, high naphtha and distillate selectivity, and low coke formation. The supercritical conversion can replace crude distillation, vacuum distillation, solvent deasphalting, coking, hydrocracking, hydrotreating, and/or fluid catalytic cracking, and/or used in parallel with such unit operations for debottlenecking or increasing capacity.
摘要翻译：超临界转化沸点高于538°C（1000°F）的烃（108°C）与溶剂化烃（106,206）以溶剂化烃与高沸点烃的重量比至少为2：1和高于临界温度的条件，以及在热流化固体存在下，高沸点烃 - 溶剂混合物的压力（136,236）。在低于供给的热固体（136,236）的温度下，将烃（108,208）供应到反应区（114,214），由此得到的烃 - 固体悬浮液具有对应于反应温度的热平衡温度。转化率高，硫，氮和金属去除率高，几乎完全转化为较低分子量产物，高石脑油和馏出物选择性，低焦炭形成。超临界转化可以替代原油蒸馏，真空蒸馏，溶剂脱沥青，焦化，加氢裂化，加氢处理和/或流化催化裂化，和/或与这种单元操作并行地用于消除瓶颈或增加容量。

2. 发明申请

WO00055281A1 FCC PROCESS INCORPORATING ATOMIZATION OF FCC FEED OIL 审中-公开
标题翻译： FCC进料加氢FCC原油的原理
公开(公告)号：WO00055281A1
公开(公告)日：2000-09-21
申请号：PCT/US2000/007024
申请日：2000-03-17
IPC分类号： A62C31/12 , B01J8/24 , B01J19/26 , C10G11/18 , F23D11/00 , C10G9/28
CPC分类号： F23D11/007 , A62C31/12 , B01J8/1827 , B01J19/26 , B01J2208/00327 , B01J2208/0053 , B01J2208/00539 , C10G11/18 , Y10T137/87652
摘要： A liquid atomization process comprises forming a two-phase fluid mixture of a liquid and a gas, under pressure, dividing the fluid into two separate streams which are passed into and through an impingement mixing zone (22) in which they are impingement mixed to form a single stream of two-phase fluid. The mixed, single stream is then passed into and through a shear mixing zone (24) and then into a lower pressure expansion zone (30), in which atomization occurs to form a spray of atomized drops of the liquid. The impingement (22) and shear (24) mixing zones comprise respective upstream (16) and downstream (18) portions of a single cavity (14) in a nozzle (10). This is useful for atomizing the hot oil in a FCC process.
摘要翻译：液体雾化方法包括在压力下形成液体和气体的两相流体混合物，将流体分成两个分离的流，所述两个分离的流进入冲击混合区（22）并通过冲击混合区（22），在冲击混合区中它们被冲击混合形成单流二相流体。然后将混合的单一流进入并通过剪切混合区（24），然后进入低压膨胀区（30），其中发生雾化以形成液体的雾化液滴的喷雾。冲击（22）和剪切（24）混合区域包括在喷嘴（10）中的单个空腔（14）的相应的上游（16）和下游（18）部分。这对于在FCC工艺中雾化热油是有用的。

3. 发明申请

WO2022132368A1 PROCESSES AND SYSTEMS FOR UPGRADING A HYDROCARBON-CONTAINING FEED 审中-公开
公开(公告)号：WO2022132368A1
公开(公告)日：2022-06-23
申请号：PCT/US2021/059703
申请日：2021-11-17
申请人： EXXONMOBIL CHEMICAL PATENTS INC.
发明人： HARANDI, Mohsen, N. , KEUSENKOTHEN, Paul, F. , LIU, Ying , LATTNER, James, R.
IPC分类号： C10G9/36 , C10G9/28 , C10J3/00 , C10B55/04 , B01J38/02
摘要： Processes and for converting a hydrocarbon-containing feed by pyrolysis and gasification/combustion. The hydrocarbon-containing feed can be heated to produce a heated feed that can be separated into a vapor and a liquid. At least a portion of the vapor and/or at least a portion of the liquid and a particle stream can be fed into a pyrolysis zone and contacted therein to effect pyrolysis of the hydrocarbons and produce a pyrolysis effluent.

4. 发明申请

WO2005074440A3 SUPERCRITICAL HYDROCARBON CONVERSION PROCESS 审中-公开
标题翻译：超临界油气转化工艺
公开(公告)号：WO2005074440A3
公开(公告)日：2005-12-29
申请号：PCT/US2004037645
申请日：2004-11-10
申请人： KELLOGG BROWN & ROOT INC , MCCALL THOMAS F , RAMAMURTHY PRITHAM , SHAH KIRAN V , SILVERMAN MICHAEL A , VAN SICKELS MARTIN J
发明人： MCCALL THOMAS F , RAMAMURTHY PRITHAM , SHAH KIRAN V , SILVERMAN MICHAEL A , VAN SICKELS MARTIN J
IPC分类号： C01G11/02 , C10G9/28 , C10G9/32 , C10G69/06
CPC分类号： C10G9/28 , C10G9/32 , C10G69/06
摘要： Supercritical conversion of hydrocarbons (108,208) boiling above 538°C (1000°F) with a solvating hydrocarbon (106,206) at a weight ratio of solvating hydrocarbon to high-boiling hydrocarbons of at least 2:1 and at conditions above the critical temperature and pressure of the high-boiling hydrocarbons-solvent mixture, in the presence of hot fluidized solids (136,236). The hydrocarbons (108,208) are supplied to a reaction zone (114,214) at a temperature below that of the hot solids (136,236) supplied thereto, whereby the resulting hydrocarbons-solids suspension has a thermal equilibrium temperature corresponding to the reaction temperature. The conversion has high rates of sulfur, nitrogen and metals removal, nearly complete conversion to lower molecular weight products, high naphtha and distillate selectivity, and low coke formation. The supercritical conversion can replace crude distillation, vacuum distillation, solvent deasphalting, coking, hydrocracking, hydrotreating, and/or fluid catalytic cracking, and/or used in parallel with such unit operations for debottlenecking or increasing capacity.
摘要翻译：在溶剂化烃与高沸点烃的重量比为至少2:1的条件下和在高于临界温度的条件下，用溶剂化烃（106,206）超临界转化沸点高于538℃（1000°F）的烃（108,208）和高沸点烃 - 溶剂混合物在热流化固体（136,236）存在下的压力。在低于供给其中的热固体（136,236）的温度下将烃（108,208）供应到反应区（114,214），由此所得到的烃 - 固体悬浮液具有对应于反应温度的热平衡温度。该转化具有高硫，氮和金属去除率，几乎完全转化为较低分子量产物，高石脑油和馏分选择性以及低焦炭形成。超临界转化可以取代原油蒸馏，减压蒸馏，溶剂脱沥青，焦化，加氢裂化，加氢处理和/或流化催化裂化，和/或与用于消除瓶颈或增加容量的此类单元操作并行使用。

5. 发明申请

WO2004056942A1 VERFAHREN ZUR HOCHTEMPERATUR-KURZZEIT-DESTILLATION VON RÜCKSTANDSÖL 审中-公开
标题翻译： PROCESS渣油蒸馏的高温短时间
公开(公告)号：WO2004056942A1
公开(公告)日：2004-07-08
申请号：PCT/EP2003/007377
申请日：2003-07-09
申请人： LURGI AG , WEISS, Hans-Jürgen , ZENTNER, Udo , HEURICH, Helmut
发明人： WEISS, Hans-Jürgen , ZENTNER, Udo , HEURICH, Helmut
IPC分类号： C10G9/28
CPC分类号： C10G9/28 , C10G70/043 , C10G2300/107 , C10G2300/1077 , C10G2300/301 , C10G2400/02 , C10G2400/06
摘要： Ein Verfahren zur Hochtemperatur-Kurzzeit-Destillation von Rückstandsölen wird dahingehend verbessert, dass von dem Gas/Öldampf-Gemisch aus dem Mischwerk (1) eine kleine Rückstandsfraktion auf technisch einfache Weise gewonnen wird, in der die unerwünschten Katalysator-Schadstoffe (CCR, Ni, V, Asphaltene) weitgehend aufkonzentriert sind. Hierzu wird das in einem Mischreaktor (1) erzeugte Gas/Öldampf-Gemisch in einer Kolonne (17) soweit mit Gas oder Wasserdampf verdünnt, dass bei unter 450°C eine schwer siedende schadstoffhaltige Fraktion mit einem Siedebeginn über 450°C kondensiert und abgezogen wird in der die Schadstoffe weitgehend aufkonzentriert sind. Nach einer weiteren Verbesserung wird das nicht kondensierte Produktöl aus Kolonne (17) einer Fraktionier-Kolonne (19) zugeführt, in der es in eine schadstoffarme Vakuum Gasöl sowie in eine Benzin/Gasöl-Fraktion zerlegt wird.
摘要翻译：一种用于剩余油的高温短期蒸馏方法进行了改进，即从混合器中的气/油蒸气混合物的（1）在技术上简单的方式获得小的残余馏分，其中所述不希望的催化剂污染物（CCR，镍， V，沥青质）在很大程度上浓缩。为了这个目的，在（1）中产生的柱（17）稀释气体/油蒸气混合物，只要气体或水蒸汽的混合反应器，是在低于450℃的高沸点污染馏分的初始沸点冷凝以上450℃，汽提在其中污染物在很大程度上浓缩。根据本发明的分馏塔的进一步改进，从塔（17）的不凝结油产物（19）供入，其被分解成低污染物的真空瓦斯油并进入燃料/瓦斯油馏分。

6. 发明申请

WO2018200650A1 ENHANCED LIGHT OLEFIN YIELD VIA STEAM CATALYTIC DOWNER PYROLYSIS OF HYDROCARBON FEEDSTOCK 审中-公开
公开(公告)号：WO2018200650A1
公开(公告)日：2018-11-01
申请号：PCT/US2018/029325
申请日：2018-04-25
申请人： SAUDI ARABIAN OIL COMPANY , ARAMCO SERVICES COMPANY
发明人： AL-GHRAMI, Musaed, Salem , XU, Wei , AKAH, Aaron, Chi
IPC分类号： C10G9/28 , C10G11/16 , C10G11/20
摘要： Systems and methods for steam and catalytic cracking of a hydrocarbon inlet stream comprising hydrocarbons. Systems and methods can include a catalyst feed stream, where the catalyst feed stream comprises a fluid and a heterogeneous catalyst, the heterogeneous catalyst operable to catalyze cracking of the hydrocarbons on surfaces of the heterogeneous catalyst a steam feed stream, where the steam feed stream is operable to effect steam cracking of the hydrocarbons, and where the steam feed stream decreases coking of the heterogeneous catalyst; and a downflow reactor, where the downflow reactor is operable to accept and mix the hydrocarbon inlet stream, the catalyst feed stream, and the steam feed stream, where the downflow reactor is operable to produce light olefins by steam cracking and catalytic cracking, and where the downflow reactor is operable to allow the heterogeneous catalyst to flow downwardly by gravity.

7. 发明申请

WO2009131623A1 SYSTEMS AND METHODS FOR UPGRADING HYDROCARBONS 审中-公开
标题翻译：升级油气的系统和方法
公开(公告)号：WO2009131623A1
公开(公告)日：2009-10-29
申请号：PCT/US2009/002138
申请日：2009-04-06
申请人： KELLOGG BROWN & ROOT LLC , IQBAL, Rashid , AGRAWAL, Ravindra, K.
发明人： IQBAL, Rashid , AGRAWAL, Ravindra, K.
IPC分类号： C10G9/28
CPC分类号： C10G9/36 , C01B3/24 , C01B3/50 , C01B2203/0266 , C01B2203/0283 , C01B2203/0415 , C01B2203/042 , C01B2203/0425 , C01B2203/043 , C01B2203/045 , C01B2203/0475 , C01B2203/0485 , C01B2203/061 , C01B2203/062 , C01B2203/068 , C01B2203/0811 , C01B2203/1041 , C01B2203/1052 , C01B2203/169 , C10G9/38 , C10J3/56 , C10J2300/0956 , C10J2300/0959 , C10J2300/0976 , C10J2300/0989 , C10J2300/0993 , C10J2300/165 , C10J2300/1659 , C10J2300/1665 , C10J2300/1668 , C10J2300/1675 , C10K1/004 , C10K1/024 , C10K3/04
摘要： Systems and methods for upgrading hydrocarbons are provided. A portion of a hydrocarbon can be vaporized in the presence of gasified hydrocarbons, combustion gas, and solids to provide a vaporized gas. A portion of the hydrocarbon can be cracked in the presence of the gasified hydrocarbons, the combustion gas, and the solids to provide a cracked gas. A portion of the hydrocarbon can be deposited onto the solids to provide hydrocarbon containing solids. At least a portion of the hydrocarbon containing solids can be selectively separated to provide separated hydrocarbon containing solids and a hot gas product. The hot gas product can be at a temperature of from about 400°C to about 1,650°C. A portion of the hydrocarbon containing solids can be combusted in the presence of an oxidant to provide the combustion gas. A portion of the hydrocarbon containing solids can be gasified to provide the gasified hydrocarbon.
摘要翻译：提供了用于升级碳氢化合物的系统和方法。在气化的烃，燃烧气体和固体的存在下，一部分烃可以蒸发以提供蒸发的气体。在气化的烃，燃烧气体和固体的存在下，一部分烃可以裂化，以提供裂化气体。可以将一部分烃沉积在固体上以提供含烃固体。可以选择性地分离至少一部分含烃固体以提供分离的含烃固体和热气产物。热气体产物可以在约400℃至约1650℃的温度下。一部分含烃固体可以在氧化剂存在下燃烧以提供燃烧气体。可将一部分含烃固体气化以提供气化烃。

8. 发明申请

WO00063320A1 IMPROVED PROCESS FOR DEASPHALTING RESIDUA BY REACTIVE RECYCLE OF HIGH BOILING MATERIAL 审中-公开
标题翻译：通过高沸点材料的反应性回收去除残留物的改进方法
公开(公告)号：WO00063320A1
公开(公告)日：2000-10-26
申请号：PCT/US2000/009607
申请日：2000-04-11
IPC分类号： B01J19/00 , C10C1/04 , C10C3/04 , C10G9/28 , C10G9/32 , C10G9/36 , C10G31/06 , C10C3/00
CPC分类号： C10G9/32 , C10G31/06
摘要： The vaporized fraction is passed via line (11) to soaker drum (2) which is maintained at effective conditions so that the highest boiling materials are condensed out. Typically these conditions will include controlled quenching of vapor fraction just below the dewpoint. A quench stream can also be passed into soaker drum via line (21).
摘要翻译：蒸发的馏分通过管线（11）通入到保持在有效条件下的浸泡桶（2），使得最高沸点的物质冷凝出来。通常这些条件将包括正好低于露点的蒸气分数的受控淬火。淬火流还可以通过管线（21）进入到烘缸中。

9. 发明申请

WO00054844A1 PROCESS AND APPARATUS FOR ATOMIZING FCC FEED OIL 审中-公开
标题翻译：用于进口FCC进料油的方法和装置
公开(公告)号：WO00054844A1
公开(公告)日：2000-09-21
申请号：PCT/US2000/005033
申请日：2000-02-25
IPC分类号： A62C31/12 , B01J8/24 , B01J19/26 , C10G11/18 , F23D11/00 , A62C5/02 , C10G9/28 , F23D14/68
CPC分类号： F23D11/007 , A62C31/12 , B01J8/1827 , B01J19/26 , B01J2208/00327 , B01J2208/0053 , B01J2208/00539 , C10G11/18 , Y10T137/87652
摘要： A liquid atomization process comprises forming a two-phase fluid mixture of a liquid and a gas, under pressure, dividing the fluid into two separate streams which are passed into and through an impingement mixing zone (22) in which they are impingement mixed to form a single stream of two-phase fluid. The mixed, single stream is then passed into and through a shear mixing zone (24) and then into a lower pressure expansion zone (30), in which atomization occurs to form a spray of atomized drops of the liquid. The impingement (22) and shear (24) mixing zones comprise respective upstream (16) and downstream (18) portions of a single cavity (14) in a nozzle (10). This is useful for atomizing the hot feed oil in an FCC process.
摘要翻译：液体雾化方法包括在压力下形成液体和气体的两相流体混合物，将流体分成两个分离的流，所述两个分离的流进入冲击混合区（22）并通过冲击混合区（22），在冲击混合区中它们被冲击混合形成单流二相流体。然后将混合的单一流进入并通过剪切混合区（24），然后进入低压膨胀区（30），其中发生雾化以形成液体的雾化液滴的喷雾。冲击（22）和剪切（24）混合区域包括在喷嘴（10）中的单个空腔（14）的相应的上游（16）和下游（18）部分。这对于在FCC工艺中雾化热进料油是有用的。

10. 发明申请

WO2020212403A1 PLASTIC-TO-OIL PLANT, ACCORDING CRACKING REACTOR, AND RELATED METHODS FOR CONVERTING PLASTIC WASTE INTO PETROCHEMICAL PRODUCTS 审中-公开
公开(公告)号：WO2020212403A1
公开(公告)日：2020-10-22
申请号：PCT/EP2020/060558
申请日：2020-04-15
申请人： PRUVIA GMBH
发明人： MASTELLONE, Maria Laura
IPC分类号： C10G1/10 , C10G9/28
摘要： A plastic-to-oil plant for converting plastics into petrochemical products shall be easy to build, to operate, and to maintain. Operation shall be energy- and resource-efficient. To reach this aim, the inventions suggests a plastic-to-oil plant, comprising a cracking reactor (V.1) for a pyrolysis reaction, wherein plastics, in particular polyolefins, are converted into at least gasified pyrolysis products and char, and further comprising a separate combustor (V.2), the cracking reactor (V.1) comprising a plastics inlet port, in particular a plastic melt flow inlet port (5), a particles inlet port (23), a pyrolysis products outlet port (6), and a char and particles outlet port (24), the combustor (V.2) comprising a char and particles inlet port (26), a combustion air inlet port (28), and a combustion products and particles outlet port (29), the char and particles outlet port (24) of the cracking reactor (V.1 ) being connected to the char and particles inlet port (26) of the combustor (V.2), and the combustion products and particles outlet port (29) of the combustor (V.2) being connected to the particles inlet port (23) of the cracking reactor (V.1), the cracking reactor (V.1) and the combustor (V.2) therefore being part of a parti- cles loop (94) which contains a multitude of solid particles, such that during opera- tion the particles are cycled from the cracking reactor (V.1) to the combustor (V.2) and back, wherein the cracking reactor (V.1) is designed such that mixing in the cracking reactor (V.1) is mainly promoted by a flow of said particles fed at the top of the cracking reactor (V.1) essentially in counter-current with a flow of the pyrolysis products, without need of mechanical mixing devices.

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