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1. 发明公开

EP2937404A1 Liquid-phase catalytic cracking of heavy petroleum materials to produce petroleum products for use as motor fuel components and chemical raw materials 审中-公开
标题翻译：催化液相生产的石油产品裂化重油材料用作发动机燃料组分和化学的起始原料
公开(公告)号：EP2937404A1
公开(公告)日：2015-10-28
申请号：EP14187754.8
申请日：2014-10-06
申请人： Popova, Natalia
发明人： Fridzon, Konstantin , Platonov, Vladimir , Vorobev, Nikolay , Balashova, Galina
IPC分类号： C10G47/02 , B01J31/04
CPC分类号： C10G47/02 , B01J31/04 , C10G11/02 , C10G47/34 , C10G2300/305 , C10G2300/4081
摘要： The present application relates to a process for catalytic cracking of heavy petroleum starting materials by treating the starting material with a catalyst and optionally a hydrogen donor at a temperature of 280-400 °C and a pressure of 2-7 MPa, wherein the catalyst comprises one or more metal carboxylate salt(s).
摘要翻译：本申请涉及一种用于重质石油原料通过在280-400的℃的温度和2-7 MPa的压力的催化剂和任选氢供体处理该起始材料的材料，worin所述催化剂包含的催化裂化的方法一个或多个金属羧酸盐（S）。

2. 发明公开

EP2751230A2 USE OF SUPERCRITICAL FLUID IN HYDROPROCESSING HEAVY HYDROCARBONS 审中-公开
标题翻译：使用超临界流体海德鲁处理重质烃
公开(公告)号：EP2751230A2
公开(公告)日：2014-07-09
申请号：EP12762124.1
申请日：2012-08-30
申请人： ExxonMobil Research and Engineering Company
发明人： BROWN, Stephen, Harold , HO, Teh, C. , CHENG, Jane, Chi-ya , WOO, Hyung, Suk
IPC分类号： C10G47/34
CPC分类号： C10G47/34 , C10G45/02 , C10G47/00 , C10G2300/205 , C10G2300/206 , C10G2300/301 , C10G2300/308 , C10G2300/44
摘要： This invention is directed to a process for producing a hydroprocessed product. The invention is particularly advantageous in that substantially longer run length can be attained relative to conventional hydroprocessing methods. This benefit is achieved by using a particular solvent as a co-feed component, particular, the solvent component is comprised of at least one or more supercritical solvent compounds.

3. 发明公开

EP2119756A1 PROCESS FOR CHANGING THE VISCOSITY OF PETROLEUM 审中-公开
标题翻译： VERFAHREN ZURÄNDERUNGDERVISKOSITÄTVONERDÖL
公开(公告)号：EP2119756A1
公开(公告)日：2009-11-18
申请号：EP07702544.3
申请日：2007-02-06
申请人： Acosta Estrada, Marcelo
发明人： Acosta Estrada, Marcelo
IPC分类号： C10G47/34 , C07C211/27 , C09K3/32
CPC分类号： C09K3/32 , C10G29/02 , C10G47/34 , C10G2300/1014 , C10G2300/1033 , C10G2300/205 , C10G2300/302 , Y02P20/582 , Y02P30/20
摘要： The purpose of the invention described in this document is to disclose a novel method using mixtures to change the viscosity of both light and heavy petroleums, by decreasing or increasing said viscosity. The methods derived from this invention are useful at ambient temperature and atmospheric pressure. The active component of the invention is dopamine, a compound that combined with other substances enables a change in the fluidity properties of petroleum, an increase in the electric charge properties of the mixtures and solutions and the dissolution of insoluble compounds in water or aqueous solutions. Some of the mixtures of this invention have been applied to modifying proton mobility, whereby significant increases in particular caused by the presence of metals chosen to bring about this purpose, can be detected within these mixtures, by measuring the electric charge. The experiments which led to this invention demonstrated that the juice obtained from any part of the banana plant, whereof the chemical analysis includes dopamine and other compounds such as quinonas, carotenes and terpenes, is the cause of the effects found, in particular effects on the electric properties and on dissolving metals and metal compounds.
摘要翻译：本文中描述的本发明的目的是公开一种使用混合物通过降低或增加所述粘度来改变轻质和重质石油的粘度的新方法。衍生自本发明的方法在环境温度和大气压下是有用的。本发明的活性组分是多巴胺，与其它物质组合的化合物能够改变石油的流动性质，混合物和溶液的电荷特性的增加以及不溶性化合物在水或水溶液中的溶解。本发明的一些混合物已被应用于改变质子迁移率，由此通过测量电荷可以在这些混合物内检测特别是由于选择用于实现该目的的金属的存在引起的显着增加。导致本发明的实验表明，从香蕉植物的任何部分获得的果汁，其化学分析包括多巴胺和其他化合物如醌，胡萝卜素和萜烯，是所发现的效果的原因，特别是对电性能和溶解金属和金属化合物。

4. 发明公开

EP0984054A3 Process and apparatus for upgrading hydrocarbon feeds containing sulfur, metals, and asphaltenes 有权
标题翻译：改进的硫，金属和沥青含有的烃进料的方法和装置
公开(公告)号：EP0984054A3
公开(公告)日：2000-04-05
申请号：EP99117256.0
申请日：1999-09-02
申请人： ORMAT INDUSTRIES, LTD.
发明人： Friday, Robert J. , Rettger, Philip B. , Goldstein, Randall S.
IPC分类号： C10G69/00 , C10G47/34 , C10G67/04
CPC分类号： C10G47/34 , C10G67/049
摘要： Upgrading of a hydrocarbon feed containing sulfur, metals, and asphaltenes involves applying the feed to a distillation column for producing a substantially asphaltene-free, and metal-free distillate fraction and a non-distilled fraction containing sulfur, asphaltenes, and metals. At least some of the substantially asphaltene-free, and metal-free distillate fraction is converted to a hydrogen donor diluent. The non-distilled fraction is processed in a solvent deasphalting unit for producing a deasphalted oil stream and an asphaltene stream. After a combined stream is formed from the hydrogen donor diluent and the deasphalted oil stream, the combined stream is thermally cracked forming a thermally cracked stream that is applied to the distillation column.

5. 发明授权

EP0540793B1 Improvements for reducing coke deposition in thermal upgrading processes 失效
标题翻译：在Koksabsetzungen热加工工序的还原改进
公开(公告)号：EP0540793B1
公开(公告)日：1997-01-08
申请号：EP91310328.9
申请日：1991-11-07
申请人： ALBERTA OIL SANDS TECHNOLOGY AND RESEARCH AUTHORITY
发明人： Lott, Roger Kai , LEE, Lap Keung , Cyr, Theodore
IPC分类号： C10G47/26 , C10G47/00 , C10G47/34
CPC分类号： C10G47/00 , C10G47/26 , C10G47/34

6. 发明公开

EP0103053A1 Upgrading of heavy hydrocarbons 失效
标题翻译： Aufarbeitung von schweren Kohlenwasserstoffen。
公开(公告)号：EP0103053A1
公开(公告)日：1984-03-21
申请号：EP82304498.7
申请日：1982-08-26
申请人： Conoco Inc.
发明人： Anderson, Ardis L. , McConaghy, James R.
IPC分类号： C10G45/00 , C10G47/00 , C10G47/22
CPC分类号： C10G47/34 , C10G45/00 , C10G69/06
摘要： Heavy hydrocarbonaceous materials are converted to distillate products and pitch in a hydrogen donor diluent cracking process, and the pitch is utilized as feed to a delayed coker. Green coke is calcined in a vertical shaft kiln, and steam is injected into the bottom of the kiln to produce hydrogen by reaction of steam with coke. The hydrogen is drawn from the kiln and used to hydrogenate recycle donor solvent for the cracking step. High sulfur coke can be desulfurized in the kiln, and distillate products in addition to donor solvent can be hydrotreated using hydrogen from the kiln.
摘要翻译：重质含烃材料在氢供体稀释剂裂解过程中转化为馏出物产物和沥青，沥青用作延迟焦化器的进料。绿色焦炭在垂直立式窑中煅烧，蒸汽通过蒸汽与焦炭的反应被注入到窑底部产生氢气。氢气从窑中抽出并用于氢化循环供体溶剂进行裂解步骤。高硫焦炭可以在窑中脱硫，除了供体溶剂之外还可以使用氢气从窑加氢处理馏出物。

7. 发明公开

EP0078796A1 STEAM REFORMING OF CARBO-METALLIC OILS 失效
标题翻译：方法蒸汽重整的碳前体和金属含油。
公开(公告)号：EP0078796A1
公开(公告)日：1983-05-18
申请号：EP81901650.0
申请日：1981-05-13
申请人： ASHLAND OIL, INC.
发明人： HETTINGER, William P., Jr. , KOVACH, Stephen M. , MYERS, George D. , ZANDONA, Oliver J.
IPC分类号： C10G11 , C10G47
CPC分类号： C10G47/30 , C10G11/18 , C10G47/34
摘要： Procede permettant de convertir economiquement des huiles carbo-metalliques en combustibles liquides, qui consiste a mettre en contact-un produit d'alimentation d'un convertisseur contenant un materiau de point d'ebullition 650 F + caracterise par un residu de pyrolyse carbonee d'environ 1 et contenant au moins 4 ppm d'equivalents nickel de metaux lourds, y compris le nickel, avec un catalyseur de craquage sous forme particulaire dans un reacteur du type a circulation continue (2) possedant une zone de conversion allongee. La suspension de catalyseur et le produit d'alimentation du reacteur ont une duree de maintien dans la vapeur d'environ 0,5 a 10 secondes, une temperature d'environ 900 a 1400 F et une pression absolue d'environ 10 a 50 livres par pouce carre pour provoquer un taux de conversion d'environ 50 a 90% lors du depot du nickel et du coke sur le catalyseur en quantites se situant dans la gamme de 0,3 a 3% en poids. Le catalyseur charge de coke est separe du courant d'hydrocarbures resultant et regenere par combustion du coke avec de l'oxygene, le catalyseur regenere etant caracterise par du nickel depose dans au moins un etat partiellement oxyde et un niveau de carbone sur le catalyseur d'environ 0,25% en poids ou moins. Le catalyseur regenere est mis en contact avec un gaz reducteur dans des conditions reductrices suffisantes pour reduire au moins une partie des depots de nickel reduit est recycle vers une zone de conversion pour etre mis en contact avec du produit d'alimentation non traite. On introduit egalement de l'eau dans la zone de conversion du reacteur et les quantites d'eau et de nickel reduit sur le catalyseur recycle sont suffisantes pour assurer une reaction de reformage a la vapeur telle que les composants deficients en hydrogene soient convertis en produits possedant des rapports hydrogene/carbone plus eleves, et que la quantite de produit converti en coke soit reduite. La quantite de nickel deposee sur le catalyseur est de preference dans la gamme d'environ 2.000 a 20.000 ppm et le

8. 发明公开

EP0078689A2 Thermal cracking with hydrogen donor diluent 失效
标题翻译：用wasserstoffgebendem稀释剂热裂解。
公开(公告)号：EP0078689A2
公开(公告)日：1983-05-11
申请号：EP82305782.3
申请日：1982-11-01
申请人： MOBIL OIL CORPORATION
发明人： Derbyshire, Francis John , Varghese, Philip , Whitehurst, Darrell Duayne
IPC分类号： C10G47/34 , B01J23/34
CPC分类号： C10G45/46 , C10G47/34
摘要： An improved hydrogen donor for hydrogen donor diluent cracking is provided by extraction with naphtha from the cracked product and hydrogenation by hydrogen transfer from a lower boiling hydrogen donor such as tetralin.

9. 发明公开

EP0035864A2 Process for upgrading heavy hydrocarbonaceous oils 失效
标题翻译： Verfahren zum Verbessern schwererKohlenwasserstofföle。
公开(公告)号：EP0035864A2
公开(公告)日：1981-09-16
申请号：EP81300887.7
申请日：1981-03-03
申请人： GULF CANADA LIMITED
发明人： Fisher, Ian Patrick , Woods, Hanbury John , Southrada, Frank
IPC分类号： C10G47/34
CPC分类号： C10G47/34 , C10G2400/06
摘要： The invention relates to a process for the upgrading of heavy, viscous hydrocarbonaceous oils, comprising fractionally distilling said hydrocarbonaceous oil to produce at least one distilled fraction and a residuum without substantially cracking said hydrocarbonaceous oil, contacting said residuum with a liquid hydrogen donor material stream to produce a hydrocracked stream and separating said hydrocracked stream into a gaseous stream and a liquid hydrocracked stream, characterized in that:

(a) said liquid hydrocracked stream is fractionally distilled to separate from higher and lower boiling fractions a hydrogen donor precursor stream boiling above a temperature from substantially 180°C to substantially 200°C and below a temperature from substantially 330°C to substantially 350°C,
(b) at least part of said hydrogenated hydrogen donor material is recycled as the material which constitutes the entire liquid hydrogen donor material stream to contact said residuum.
摘要翻译：本发明涉及一种改质重质粘性含油油的方法，包括分馏蒸馏所述烃油以产生至少一种蒸馏馏分和渣油，而基本上不裂化所述烃油，将所述残渣与液体氢供体物料流接触，产生加氢裂化的物流并将所述加氢裂化物流分离为气态物流和液体加氢裂化物流，其特征在于：（a）将所述液体加氢裂化物流分馏，从高沸点馏分和低沸点馏分中分离出沸点超过温度的氢供体前体物流从基本上180℃至基本上200℃并且低于大约330℃至大约350℃的温度，（b）至少部分所述氢氢供体材料作为构成整个液体氢供体材料的材料再循环流接触所述残渣。

10. 发明公开

EP2948529A1 SYSTEM AND PROCESS FOR HYDROCRACKING AND HYDROGENATION 审中-公开
标题翻译：系统和方法加氢裂化和加氢
公开(公告)号：EP2948529A1
公开(公告)日：2015-12-02
申请号：EP13872350.7
申请日：2013-03-08
申请人： H R D Corporation
发明人： HASSAN, Abbas , HASSAN, Aziz , ANTHONY, Rayford G. , BORSINGER, Gregory
IPC分类号： C10G45/02 , C10G45/04
CPC分类号： C10G45/00 , B01F7/00766 , B01F13/1016 , B01J8/222 , B01J10/002 , B01J19/0066 , B01J19/1806 , B01J2219/0004 , B01J2219/00189 , C10G1/065 , C10G45/02 , C10G45/16 , C10G45/22 , C10G47/00 , C10G47/26 , C10G47/34 , C10G49/007 , Y10T137/0318
摘要： Herein disclosed is a method for hydrogenation comprising: supersaturating a hydrocarbonaceous liquid or slurry stream in a high shear device with a gas stream comprising hydrogen and optionally one or more C1-C6 hydrocarbons to form a supersaturated dispersion; and introducing the supersaturated dispersion into a reactor in the presence of a hydrogenation catalyst to generate a product stream. In some embodiments, the catalyst is present as a slurry or a fluidized or fixed bed of catalyst. In some embodiments, the hydrogenation catalyst is mixed with the hydrocarbonaceous liquid or slurry stream and the gas stream in the high shear device. In some embodiments, the method further comprises recycling at least a portion of an off gas from the reactor, recycling at least a portion of the product stream from the reactor, or both. Also disclosed herein is a system for hydrogenation.

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