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81. 发明申请

US20100300932A1 Process for the production of a hydrocarbon fraction with a high octane number and a low sulfur content 有权
$Process for the production of a hydrocarbon fraction with a high octane number and a low sulfur content$
标题翻译：用于生产具有高辛烷值和低硫含量的烃馏分的方法
公开(公告)号：US20100300932A1
公开(公告)日：2010-12-02
申请号：US12471736
申请日：2009-05-26
申请人： Quentin Debuisschert , Jacinthe Frecon , Robert L. Huggins
发明人： Quentin Debuisschert , Jacinthe Frecon , Robert L. Huggins
IPC分类号： C10G69/04 , C10G67/04 , C10G69/06
CPC分类号： C10L1/06 , C10G9/00 , C10G9/36 , C10G11/00 , C10G35/00 , C10G45/32 , C10G67/02 , C10G2300/1096 , C10G2300/202 , C10G2300/305 , C10G2300/44 , C10G2400/02 , C10G2400/04 , C10G2400/08
摘要： Process for the production of a hydrocarbon fraction with a high octane number and a low sulfur content from a hydrocarbon feedstock, comprising at least the following stages: A hydrodesulfurization stage of the hydrocarbon feedstock, At least one stage for extracting aromatic compounds on all or part of the effluent that is obtained from the hydrodesulfurization stage, whereby said extraction leads to a paraffin-enriched raffinate and an aromatic compound-enriched extract sent to a gasoline pool to improve its octane number. A portion of the paraffinic raffinate can be used in a mixture with the aromatic extract; another portion can be used as a petrochemistry base either for producing aromatic compounds or for producing olefins.
摘要翻译：用于从烃原料生产具有高辛烷值和低硫含量的烃馏分的方法，至少包括以下阶段：烃原料的加氢脱硫阶段，用于全部或部分萃取芳族化合物的至少一个阶段从加氢脱硫阶段获得的流出物，由此所述萃取通向富含烷烃的萃余液和富含芳族化合物的提取物送至汽油池以改善其辛烷值。一部分链烷烃提余液可以与芳族提取物混合使用; 另一部分可用作石油化学基料，用于制备芳族化合物或用于生产烯烃。

82. 发明申请

US20060006098A1 Synthetic hydrocarbon products 失效
标题翻译：合成烃产品
公开(公告)号：US20060006098A1
公开(公告)日：2006-01-12
申请号：US10886861
申请日：2004-07-08
申请人： Rafael Espinoza , Keith Lawson
发明人： Rafael Espinoza , Keith Lawson
IPC分类号： C10L1/08 , C10G69/00 , C10G69/06
CPC分类号： C10G63/04 , C10G2400/04 , C10L1/08 , Y10S208/95
摘要： The invention includes a process for producing synthetic middle distillates and synthetic middle distillates produced therefrom. In one embodiment, the process comprises fractionating a hydrocarbon synthesis product to at least generate a light middle distillate, a heavy middle distillate, and a waxy fraction; thermally cracking the waxy fraction; and isomerizing the heavy middle distillate. A synthetic diesel or blending component is formed by the combination of at least a portion of the light middle distillate; at least a portion or fraction of the thermally cracked product; and at least a portion or fraction of the isomerized product. In some embodiments, the hydrocarbon synthesis product and/or the thermally cracked product may be hydrotreated. In other embodiments, a synthetic middle distillate comprises at least two fractions: a light fraction with not more than 10% branched hydrocarbons, and a heavy fraction with at least 30% branched hydrocarbons.
摘要翻译：本发明包括一种生产合成中间馏分和由其制备的合成中间馏分的方法。在一个实施方案中，该方法包括将烃合成产物分馏至少产生轻质中间馏分，重质中间馏分和蜡状馏分; 热裂解蜡质部分; 并使重质中间馏分异构化。合成柴油或共混组分通过至少部分轻质中间馏分的组合形成; 所述热裂化产品的至少一部分或部分; 和至少一部分或部分的异构化产物。在一些实施方案中，烃合成产物和/或热裂化产物可以被加氢处理。在其它实施方案中，合成中间馏分包含至少两个馏分：具有不超过10％支链烃的轻馏分和具有至少30％支链烃的重馏分。

83. 发明授权

US6156190A Conversion process of hydrocarbon oils 有权
标题翻译：烃油的转化过程
公开(公告)号：US6156190A
公开(公告)日：2000-12-05
申请号：US272246
申请日：1999-03-19
申请人： Guofu Xia , Mei Zhu , Enze Min , Yahua Shi , Zhiping Tao , Guici Pang , Mingfeng Li , Guopeng Ran , Haitao Huang , Runqiang Zhang , Jian Li , Hong Nie
发明人： Guofu Xia , Mei Zhu , Enze Min , Yahua Shi , Zhiping Tao , Guici Pang , Mingfeng Li , Guopeng Ran , Haitao Huang , Runqiang Zhang , Jian Li , Hong Nie
IPC分类号： B01J23/85 , C10G45/08 , C10G69/04 , C10G69/06 , C10G45/04 , C10G45/00
CPC分类号： B01J23/85 , C10G45/08 , C10G69/04 , C10G69/06
摘要： A conversion process of hydrocarbon oils comprises at least a hydrodemercaptanization process, wherein said hydrodemercaptanization process comprises contacting a feedstock with a hydrofining catalyst containing a tungsten oxide and/or a molybdenum oxide, a nickel oxide and a cobalt oxide supported on an alumina under the conditions of hydrodemercaptanization, in which the content of said tungsten oxide and/or molybdenum oxide is from 4 wt % to less than 10 wt %, the nickel oxide content is 1-5 wt %, the cobalt oxide content is 0.01-1 wt % based on the catalyst, and the ratio of total atom number of nickel and cobalt to total atom number of nickel, cobalt, tungsten and/or molybdenum is 0.3-0.9. Said process can be carried out at a lower temperature and a lower H/oil volume ratio.
摘要翻译：烃油的转化方法包括至少一种氢化硫醇化方法，其中所述加氢硫醇化方法包括使原料与在氧化铝上负载的氧化钨和/或氧化钼，氧化镍和氧化钴的加氢精制催化剂接触，的氢化硫醇化，其中所述氧化钨和/或氧化钼的含量为4重量％至小于10重量％，氧化镍含量为1-5重量％，氧化钴含量为0.01-1重量％在催化剂上，镍和钴的总原子数与镍，钴，钨和/或钼的总原子数之比为0.3-0.9。所述方法可以在较低的温度和较低的H /油体积比下进行。

84. 发明授权

US6153086A Combination cocurrent and countercurrent staged hydroprocessing with a vapor stage 失效
标题翻译：组合并流和逆流分级加氢处理与蒸气阶段
公开(公告)号：US6153086A
公开(公告)日：2000-11-28
申请号：US73414
申请日：1998-05-06
申请人： Ramesh Gupta , Henry Jung , Edward S. Ellis , James J. Schorfheide , Larry L. Iaccino
发明人： Ramesh Gupta , Henry Jung , Edward S. Ellis , James J. Schorfheide , Larry L. Iaccino
IPC分类号： C10G65/12 , C10G45/00 , C10G47/00 , C10G65/00 , C10G65/02 , C10G69/04 , C10G69/06
CPC分类号： C10G65/12 , C10G65/00 , C10G69/04 , C10G69/06 , C10G2300/202 , C10G2300/207
摘要： A hydroprocessing process includes a cocurrent flow liquid reaction stage, a countercurrent flow liquid reaction stage and a vapor reaction stage in which feed components are catalytically hydroprocessed by reacting with hydrogen. Both liquid stages both produce a liquid and a vapor effluent, with the cocurrent stage liquid effluent the feed for the countercurrent stage and the countercurrent stage liquid effluent the hydroprocessed product liquid. Both liquid stage vapor effluents are combined and catalytically reacted with hydrogen in a vapor reaction stage, to form a hydroprocessed vapor. This vapor is cooled to condense and recover a portion of the hydroprocessed hydrocarbonaceous vapor components as additional product liquid. The uncondensed vapor is rich in hydrogen and is cleaned up if necessary, to remove contaminants, and then recycled back into the cocurrent stage as hydrogen-containing treat gas. Fresh hydrogen is introduced into the countercurrent stage and the countercurrent stage effluent contains sufficient, and preferably all of the hydrogen for the vapor stage reaction.
摘要翻译：加氢处理方法包括并流流动液体反应阶段，逆流流动反应阶段和蒸气反应阶段，其中进料组分通过与氢反应进行催化加氢处理。两个液相都产生液体和蒸汽流出物，并流阶段液体流出物是逆流阶段的进料和逆流阶段液体流出加氢产物液体。两个液相蒸气流出物在蒸气反应阶段中与氢组合并催化反应，形成加氢处理的蒸汽。将该蒸气冷却以冷凝并回收一部分加氢处理的含烃蒸汽组分作为另外的产物液体。未冷凝的蒸汽富含氢气，如果需要，将其清除，以除去污染物，然后再循环回到并流阶段作为含氢处理气体。将新鲜氢气引入逆流阶段，逆流阶段流出物含有足够的，优选全部用于蒸气阶段反应的氢气。

85. 发明授权

US6149800A Process for increased olefin yields from heavy feedstocks 失效
标题翻译：从重质原料中提高烯烃产率的方法
公开(公告)号：US6149800A
公开(公告)日：2000-11-21
申请号：US257168
申请日：1999-02-24
申请人： Larry Lee Iaccino , Nicolas P. Coute
发明人： Larry Lee Iaccino , Nicolas P. Coute
IPC分类号： C10G65/00 , C10G65/12 , C10G69/04 , C10G69/06
CPC分类号： C10G65/00 , C10G65/12 , C10G69/04 , C10G69/06
摘要： A process for upgrading petroleum feedstocks boiling in the distillate plus range, which feedstocks, when cracked, result in unexpected high yields of olefins. The feedstock is hydroprocessed in at least one reaction zone countercurrent to the flow of a hydrogen-containing treat gas. The hydroprocessed feedstock is then subjected to thermal cracking in a steam cracker or to catalytic cracking in a fluid catalytic cracking process. The resulting product slate will contain an increase in olefins compared with the same feedstock, but processed in by a conventional co-current hydroprocessing process.
摘要翻译：用于升级在馏出物加范围沸腾的石油原料的方法，该原料当裂化时导致意想不到的高产率的烯烃。原料在与含氢处理气体的流动逆流的至少一个反应区中进行加氢处理。然后将加氢处理的原料在蒸汽裂化器中进行热裂解或在流化催化裂化过程中进行催化裂化。与相同的原料相比，所得到的产品板岩将含有增加的烯烃，但是通过常规的并流加氢处理方法进行加工。

86. 发明授权

US6143940A Method for making a heavy wax composition 有权
标题翻译：制造重蜡组合物的方法
公开(公告)号：US6143940A
公开(公告)日：2000-11-07
申请号：US223227
申请日：1998-12-30
申请人： Stephen J. Miller , Gerald P. Huffman , Naresh Shah
发明人： Stephen J. Miller , Gerald P. Huffman , Naresh Shah
IPC分类号： C10G69/06 , C10G55/04 , C10G51/04
CPC分类号： C10G69/06
摘要： The invention includes a process of making a wax composition including: a process for making a heavy wax composition including the steps of (1) contacting a waste plastics feed containing primarily polyethylene in a pyrolysis zone at sub-atmospheric pressure, whereby at least a portion of the waste plastics feed is cracked, thereby forming a pyrolysis zone effluent including 1-olefins and n-paraffins; and (2) passing the pyrolysis zone effluent to a hydrotreating zone, for contacting with a hydrotreating catalyst at catalytic conditions.
摘要翻译：本发明包括一种制备蜡组合物的方法，包括：一种制备重蜡组合物的方法，包括以下步骤：（1）在低于大气压的热解区中使主要包含聚乙烯的废塑料进料接触，由此至少部分的废塑料进料裂化，从而形成包含1-烯烃和正链烷烃的热解区流出物; 和（2）将热解区流出物通入加氢处理区，以在催化条件下与加氢处理催化剂接触。

87. 发明授权

US6111156A Integrated high temperature high conversion olefin/polyolefin process 有权
标题翻译：集成高温高转化烯烃/聚烯烃工艺
公开(公告)号：US6111156A
公开(公告)日：2000-08-29
申请号：US189855
申请日：1998-11-10
申请人： Michael C. Oballa , David Purvis , Andrzej Z. Krzywicki , Leslie W. Benum
发明人： Michael C. Oballa , David Purvis , Andrzej Z. Krzywicki , Leslie W. Benum
IPC分类号： C07C2/30 , C07C4/04 , C07C5/333 , C10G69/06 , C10G69/12 , C07C2/06
CPC分类号： C10G69/126 , C07C2/30 , C07C4/04 , C07C5/333 , C10G69/06 , C07C2531/14 , C07C2531/16 , Y02P20/125 , Y02P20/52
摘要： A combined chain of a high temperature, high conversion steam cracker in combination with a polymerization or oligomerization unit provides capital and operating cost reduction.
摘要翻译：高温高转化蒸汽裂化器与聚合或低聚单元组合的组合链提供了资本和运营成本的降低。

88. 发明授权

US5906728A Process for increased olefin yields from heavy feedstocks 失效
公开(公告)号：US5906728A
公开(公告)日：1999-05-25
申请号：US701927
申请日：1996-08-23
申请人： Larry Lee Iaccino , Nicolas P. Coute
发明人： Larry Lee Iaccino , Nicolas P. Coute
IPC分类号： C10G65/00 , C10G65/12 , C10G69/04 , C10G69/06
CPC分类号： C10G65/00 , C10G65/12 , C10G69/04 , C10G69/06
摘要： A process for upgrading petroleum feedstocks boiling in the distillate plus range, which feedstocks, when cracked, result in unexpected high yields of olefins. The feedstock is hydroprocessed in at least one reaction zone countercurrent to the flow of a hydrogen-containing treat gas. The hydroprocessed feedstock is then subjected to thermal cracking in a steam cracker or to catalytic cracking in a fluid catalytic cracking process. The resulting product slate will contain an increase in olefins compared with the same feedstock, but processed in by a conventional co-current hydroprocessing process.

89. 发明授权

US5888469A Method of making a carbon foam material and resultant product 失效
公开(公告)号：US5888469A
公开(公告)日：1999-03-30
申请号：US887556
申请日：1997-07-03
申请人： Alfred H. Stiller , Peter G. Stansberry , John W. Zondlo
发明人： Alfred H. Stiller , Peter G. Stansberry , John W. Zondlo
IPC分类号： C01B31/04 , C04B35/52 , C04B38/00 , C10G1/00 , C10G69/06 , C01B31/00
CPC分类号： C04B35/522 , C01B31/00 , C01B31/02 , C01B31/04 , C04B35/521 , C04B38/0022 , C10G1/006 , C10G69/06 , Y10T428/249967
摘要： A method of making anisotropic carbon foam material includes de-ashing and hydrogenating bituminous coal, separating asphaltenes from oils contained in the coke precursor, coking the material to create a carbon foam. In one embodiment of the invention, the carbon foam is subsequently graphitized. The pores within the foam material are preferably generally of equal size. The pore size and carbon foam material density may be controlled by (a) altering the percentage volatiles contained within the asphaltenes to be coked, (b) mixing the asphaltenes with different coking precursors which are isotropic in nature, or (c) modifying the pressure under which coking is effected. In another embodiment of the invention, solvent separation is employed on raw bituminous coal and an isotropic carbon foam is provided. A related carbon foam product is disclosed. The carbon foam materials of the present invention are characterized by having high compressive strength as compared with prior known carbon foam materials.

90. 发明授权

US5523502A Flexible light olefins production 失效
标题翻译：柔性轻烯烃生产
公开(公告)号：US5523502A
公开(公告)日：1996-06-04
申请号：US151342
申请日：1993-11-10
申请人： Jacob N. Rubin
发明人： Jacob N. Rubin
IPC分类号： C07C11/04 , C07C11/06 , C07C11/08 , C07C41/06 , C10G51/04 , C10G69/06 , C07C4/06
CPC分类号： C07C11/08 , C07C11/04 , C07C11/06 , C07C41/06 , C10G51/04 , C10G69/06
摘要： A novel process having improved flexibility in olefins production is provided which integrates a deep catalytic cracking process with a steam cracking process, and optionally, also including steps of disproportionation and C.sub.4 hydrocarbon processing including methyl tertiary butyl ether synthesis.
摘要翻译：提供了一种在烯烃生产中具有改进的柔性的新方法，其将深催化裂化方法与蒸汽裂解方法结合，并且任选地还包括歧化和C4烃加工步骤，包括甲基叔丁基醚合成。

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