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公开(公告)号：EP1169416B1
公开(公告)日：2005-08-24
申请号：EP00908284.3
申请日：2000-01-14
CPC分类号： B01J23/002 , B01J23/85 , B01J23/88 , B01J23/883 , B01J23/8878 , B01J23/888 , B01J23/8885 , B01J37/03 , B01J37/082 , B01J2523/00 , C08F8/00 , C08F8/04 , C08F8/50 , C10G45/08 , C10G45/16 , C10G47/04 , C10G65/04 , C10G65/08 , C10G65/12 , C10G2300/1062 , C10G2300/301 , C10G2300/302 , C10G2300/4018 , C10G2300/44 , C10G2400/10 , C10G2400/14 , C08F240/00 , B01J2523/68 , B01J2523/69 , B01J2523/842 , B01J2523/67 , B01J2523/847 , B01J2523/31 , B01J2523/41
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2.发明公开HYDROFINING PROCESS USING BULK GROUP VIII/GROUP VIB CATALYSTS 有权使用组VIII / VIb的散装形式催化剂的方法HYDRORAFFINERIERUNG
公开(公告)号：EP1171549A1
公开(公告)日：2002-01-16
申请号：EP00908287.6
申请日：2000-01-14
IPC分类号： C10G17/00 , C10G71/00 , C10G47/02 , C10G47/24 , C10G47/04 , C10G45/00 , C10G45/04 , C10G45/60 , C10G29/00
CPC分类号： B01J23/002 , B01J23/85 , B01J23/88 , B01J23/883 , B01J23/8878 , B01J23/888 , B01J23/8885 , B01J37/03 , B01J37/082 , B01J2523/00 , C08F8/00 , C08F8/04 , C08F8/50 , C10G45/08 , C10G45/16 , C10G47/04 , C10G65/04 , C10G65/08 , C10G65/12 , C10G2300/1062 , C10G2300/301 , C10G2300/302 , C10G2300/4018 , C10G2300/44 , C10G2400/10 , C10G2400/14 , C08F240/00 , B01J2523/68 , B01J2523/69 , B01J2523/842 , B01J2523/67 , B01J2523/847 , B01J2523/31 , B01J2523/41
摘要： Hydrofining of petroleum and chemical feedstocks using bulk Group VIII/Group VIB catalysts. Preferred catalysts include those comprised of Ni-Mo-W.
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3.发明公开
公开(公告)号：EP1157083A1
公开(公告)日：2001-11-28
申请号：EP00909912.8
申请日：2000-01-14
发明人： SOLED, Stuart, Leon , RILEY, Kenneth, Lloyd , SCHLEICHER, Gary, P. , DEMMIN, Richard, A. , SCHUETTE, William, Lee , CODY, Ian, Alfred
CPC分类号： B01J23/002 , B01J23/85 , B01J23/88 , B01J23/883 , B01J23/8878 , B01J23/888 , B01J23/8885 , B01J37/03 , B01J37/082 , B01J2523/00 , C08F8/00 , C08F8/04 , C08F8/50 , C10G45/08 , C10G45/16 , C10G47/04 , C10G65/04 , C10G65/08 , C10G65/12 , C10G2300/1062 , C10G2300/301 , C10G2300/302 , C10G2300/4018 , C10G2300/44 , C10G2400/10 , C10G2400/14 , C08F240/00 , B01J2523/68 , B01J2523/69 , B01J2523/842 , B01J2523/67 , B01J2523/847 , B01J2523/31 , B01J2523/41
摘要： Hydrocracking process for hydrocracking petroleum and chemical feedstocks using bulk Group VIII/Group VIB catalysts. Preferred catalysts include those comprised of Ni-Mo-W.
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公开(公告)号：EP0131912B1
公开(公告)日：1988-10-05
申请号：EP84108167.2
申请日：1984-07-12
发明人： Okimoto, Kazuaki , Muto, Hideru
CPC分类号： C10G49/16
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5.发明公开PROCEDE DE CONVERSION DE CHARGES COMPRENANT UNE ETAPE D'HYDROCRAQUAGE, UNE ETAPE DE PRECIPITATION ET UNE ETAPE DE SEPARATION DES SEDIMENTS POUR LA PRODUCTION DE FIOULS 审中-公开药包包括以下步骤加氢裂化，沉淀的步骤和燃料的生产分离沉积物的步骤转换过程
公开(公告)号：EP3303522A1
公开(公告)日：2018-04-11
申请号：EP16719813.4
申请日：2016-04-20
CPC分类号： C10G67/02 , C10G31/06 , C10G31/09 , C10G47/24 , C10G67/12 , C10G2300/1059 , C10G2300/1077 , C10G2300/202 , C10G2300/205 , C10G2300/206 , C10G2300/301
摘要： The invention relates to a method for converting a hydrocarbon feedstock, said method comprising the following steps: a) a step of hydrocracking the feedstock in the presence of hydrogen, b) a step of separating the effluent obtained from step a), c) a step of precipitating sediments in which the heavy fraction resulting from the separation step b) is brought into contact with a distillate cut, at least 20% by weight of which has a boiling point greater than or equal to 100 °C, for a period less than 500 minutes, at a temperature between 25 and 350 °C and a pressure less than 20 MPa, d) a step of physically separating sediments of the heavy fraction resulting from step c), e) a step of recovering a heavy fraction having a sediment content, measured according to the method of ISO 10307-2, less than or equal to 0.1% by weight.
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6.发明公开
公开(公告)号：EP2961720A1
公开(公告)日：2016-01-06
申请号：EP13876228.1
申请日：2013-02-26
申请人： G4 Insights Inc.
CPC分类号： C10G3/50 , B01J23/755 , C01B3/38 , C01B3/50 , C01B2203/0233 , C01B2203/0283 , C01B2203/0415 , C01B2203/042 , C01B2203/043 , C01B2203/0811 , C01B2203/1241 , C10G2/32 , C10G2/332 , C10J3/60 , C10K3/023 , C10K3/04 , C10L3/08 , C10L2290/04 , C10L2290/06 , C10L2290/10 , C10L2290/54 , Y02E50/14 , Y02P20/145 , Y02P20/52 , Y02P30/20
摘要： Embodiments of a thermochemical method to convert lignocellulosic biomass to a useful fuel is disclosed in a process sequence resulting in low levels of depositable tars in the output gas stream. One disclosed embodiment comprises performing a sequence of steps at elevated pressure and elevated hydrogen partial pressure, including fast (or flash) hydropyrolysis of a lignocellulosic biomass feed followed sequentially with catalytically enhanced reactions for the formation of methane operating at moderate temperatures of from about 400°C to about 650°C and under moderately elevated pressure (about 5 atm to about 50 atm). A temperature rise in the catalyst above pyrolysis temperature is achieved without the addition of air or oxygen. Gas residence time at elevated temperature downstream of methane formation zones is extended well beyond the time required for methane formation. This sequence results in low depositable tars in the output gas stream. The catalyst promotes both the cracking of pyrolysis gases and reactions with hydrogen to preferentially form methane and non-deposit forming hydrocarbons, and also preferentially promotes coke re-gasification.
摘要翻译： 将木质纤维素生物质转化成有用燃料的热化学方法的实施方案公开于导致输出气流中低水平可沉积焦油的工艺顺序中。 一个公开的实施方案包括在升高的压力和升高的氢分压下进行一系列步骤，包括木质纤维素生物质进料的快速（或快速）加氢热解，随后依次进行催化增强的反应以形成在约400° 约650℃并在适度升高的压力（约5atm至约50atm）下进行。 在没有添加空气或氧气的情况下，达到热解温度以上的催化剂的温度升高。 甲烷形成区下游高温下的气体停留时间远远超过甲烷形成所需的时间。 该顺序导致输出气流中可沉积的焦油很少。 该催化剂促进裂解气体的裂化和与氢反应以优先形成甲烷和不形成沉积物的烃，并且还优选促进焦炭再气化。
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公开(公告)号：EP2951270A2
公开(公告)日：2015-12-09
申请号：EP14716980.9
申请日：2014-01-24
申请人： Patron, Luigi
发明人： Patron, Luigi
CPC分类号： C10G67/14 , B01D3/009 , B01D3/10 , B01D19/00 , B01D19/0042 , C10G47/24 , C10G2300/1077 , C10G2300/4081 , C10G2400/06 , C10G2400/08 , C10G2400/10 , C10G2400/16
摘要： Process for the complete conversion of heavy oils into distillates, such as the vacuum residues of heavy crude oils, characterized by the simultaneous use of two separate modes of extraction of the conversion products. Alongside the current mode of recovery of the conversion products, based on the treatment of the effluent of the top zone of the reaction, a second mode is added, based on the direct extraction of liquid from the reaction zone, degassing such liquid at the same pressure as the reactor and subjecting it to vacuum extraction. The vacuum residue is recycled in the reaction. The double mode of extraction allows greatly increasing the capacity of the reactor.
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公开(公告)号：EP2906665A1
公开(公告)日：2015-08-19
申请号：EP13847245.1
申请日：2013-09-12
申请人： UOP LLC
IPC分类号： C10G47/02 , C10G47/24 , B01J23/78 , B01J27/043 , B01J21/04
摘要： One exemplary embodiment can be a slurry hydrocracking process. The process can include providing one or more hydrocarbon compounds having an initial boiling point temperature of at least 340°C, and a slurry catalyst to a slurry hydrocracking zone. The slurry catalyst may have 32 to 50%, by weight, iron; 3 to 14%, by weight, aluminum; no more than 10%, by weight, sodium; and 2 to 10%, by weight, calcium. Typically, all catalytic component percentages are as metal and based on the weight of the dried slurry catalyst.
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9.发明公开
公开(公告)号：EP2513260A2
公开(公告)日：2012-10-24
申请号：EP10842468.0
申请日：2010-12-10
申请人： UOP LLC
CPC分类号： C10G47/28 , B01J8/085 , B01J8/125 , B01J8/22 , B01J2208/00548 , B01J2219/0004 , C10G65/10 , C10G2300/107 , C10G2300/1074 , C10G2300/1077 , C10G2300/301 , C10G2400/02 , C10G2400/04 , C10G2400/06
摘要： Systems and processes for the hydroprocessing of a hydrocarbonaceous feed are provided that utilize a plurality of moving bed reactors. The reactors may be moving bed radial flow reactors. A hydrogen injection point can be provided prior to each reactor by providing a mixer that mixes hydrogen with a hydrocarbonaceous feed, or with the effluent stream from an upstream reactor, to produce a reactor feed stream. Catalyst can be provided from the reaction zone of one reactor to the reaction zone of a downstream reactor through catalyst transfer pipes, and can be regenerated after passing through the reaction zones of the reactors. The moving bed reactors can be stacked in one or more reactor stacks.
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公开(公告)号：EP1169416A4
公开(公告)日：2003-03-26
申请号：EP00908284
申请日：2000-01-14
IPC分类号： C01G53/00 , B01J23/00 , B01J23/85 , B01J23/86 , B01J23/88 , B01J23/883 , B01J23/888 , B01J27/049 , B01J27/051 , B01J27/24 , B01J37/03 , B01J37/08 , B01J37/20 , C07B61/00 , C07C29/16 , C07C31/125 , C08F8/00 , C08F8/04 , C08F8/50 , C10C1/18 , C10C3/00 , C10C3/04 , C10C3/08 , C10G11/00 , C10G11/02 , C10G11/04 , C10G21/16 , C10G21/20 , C10G45/08 , C10G45/16 , C10G45/38 , C10G45/50 , C10G45/60 , C10G45/64 , C10G47/02 , C10G47/04 , C10G47/12 , C10G47/24 , C10G49/04 , C10G65/02 , C10G65/04 , C10G65/08 , C10G65/12 , C10G65/16 , C10G67/02 , C10G67/04 , C10G67/14 , C10G69/02 , C10M101/02 , C10M177/00 , C10N20/00 , C10N20/02 , C10N70/00
CPC分类号： B01J23/002 , B01J23/85 , B01J23/88 , B01J23/883 , B01J23/8878 , B01J23/888 , B01J23/8885 , B01J37/03 , B01J37/082 , B01J2523/00 , C08F8/00 , C08F8/04 , C08F8/50 , C10G45/08 , C10G45/16 , C10G47/04 , C10G65/04 , C10G65/08 , C10G65/12 , C10G2300/1062 , C10G2300/301 , C10G2300/302 , C10G2300/4018 , C10G2300/44 , C10G2400/10 , C10G2400/14 , C08F240/00 , B01J2523/68 , B01J2523/69 , B01J2523/842 , B01J2523/67 , B01J2523/847 , B01J2523/31 , B01J2523/41
摘要： Hydroprocessing of petroleum and chemical feedstocks using bulk Group VIII/Group VIB catalysts. Preferred catalysts include those comprised of Ni-Mo-W.
摘要翻译： 使用批量VIII族/ VIB族催化剂石油化工原料的加氢处理。 优选的催化剂包括那些含有镍 - 钼 - W的。
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