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公开(公告)号：EP2834326B1
公开(公告)日：2018-10-03
申请号：EP13718037.8
申请日：2013-04-05
申请人： IGTL Technology Ltd
发明人： HYMAN, Richard John
CPC分类号： C10L1/04 , C10G2/332 , C10G2/343 , C10G35/04 , C10G45/58 , C10G2300/4081 , C10G2400/02 , C10G2400/04 , C10G2400/08 , C10G2400/20 , C10L1/06 , C10L1/08 , C10L2200/0438 , C10L2200/0446 , C10L2200/0492 , C10L2270/023 , C10L2270/026
摘要： The invention relates to a process for the conversion of hydrogen and one or more oxides of carbon to hydrocarbons, which process comprises: contacting hydrogen and one or more oxides of carbon with a catalyst in a reaction zone; removing from the reaction zone an outlet stream comprising unreacted hydrogen, unreacted one or more oxides of carbon and one or more hydrocarbons and feeding the outlet stream to a separation zone in which the outlet stream is divided into at least three fractions, in which; a first fraction predominantly comprises unreacted hydrogen, unreacted one or more oxides of carbon and hydrocarbons having from 1 to 4 carbon atoms; a second fraction predominantly comprises hydrocarbons having 5 to 9 carbon atoms, at least a portion of which hydrocarbons having from 5 to 9 carbon atoms are olefinic; and a third fraction predominantly comprises hydrocarbons having 10 or more carbon atoms; characterised in that at least a portion of the second fraction is recycled to the reaction zone.
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公开(公告)号：EP2737018B1
公开(公告)日：2018-09-12
申请号：EP12772829.3
申请日：2012-07-27
发明人： KOSEOGLU, Omer, Refa
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.
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公开(公告)号：EP2694621B1
公开(公告)日：2018-09-12
申请号：EP12715417.7
申请日：2012-04-04
申请人： WSE Limited
发明人： WIRTZ, Ulrich , HORNUNG, Andreas
CPC分类号： C10G3/00 , C10G3/40 , C10G9/00 , C10G9/42 , C10G55/04 , C10G2300/1011 , C10G2300/107 , C10G2300/1074 , C10G2300/1077 , C10G2300/1085 , C10G2300/42 , C10G2400/04 , C10L1/04 , Y02E50/13 , Y02P30/20
摘要： The present invention relates to a reaction method and apparatus, suitable for producing fuel by reaction of bio-oil with oil and/or melt. The present inventors have found that where bio-oil vapour is flowed into a reaction chamber and heated together with oil/melt (e.g. hydrocarbon oil/melt), a product useful as a fuel (e.g. as a diesel fuel) can be produced. This provides a particularly convenient method for cracking oil/melt. Advantageously, by providing the bio-oil as a vapour, the formation and accumulation of char in the reaction chamber can be reduced or avoided. The bio-oil vapour and the oil and/or melt may be heated together without the addition of a catalyst.
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公开(公告)号：EP2454343B1
公开(公告)日：2018-09-05
申请号：EP10739380.3
申请日：2010-07-02
CPC分类号： C10G65/00 , A61K8/31 , A61K47/06 , C10G3/46 , C10G3/50 , C10G45/02 , C10G45/58 , C10G2300/1014 , C10G2300/202 , C10G2300/207 , C10G2400/02 , C10G2400/04 , C10G2400/08 , C10L1/04 , Y02P30/20
摘要： The invention relates to a process and an apparatus for producing hydrocarbon components in the presence of a hydrodesulphurization catalyst. The components obtained by the process are suitable for use as fuel composition as such or as an additive in fuel compositions, and in cosmetics or pharmaceutical products.
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公开(公告)号：EP2640808B1
公开(公告)日：2018-07-18
申请号：EP11802489.2
申请日：2011-11-21
发明人： MAYEUR, Vincent , PREAU, Alexandre
CPC分类号： C10G3/50 , B01J8/0453 , B01J8/0457 , B01J8/0496 , B01J2208/00061 , B01J2208/00548 , B01J2208/025 , C10G1/02 , C10G3/42 , C10G3/45 , C10G3/46 , C10G3/47 , C10G3/48 , C10G3/49 , C10G3/60 , C10G45/72 , C10G2300/1014 , C10G2300/4006 , C10G2300/4081 , C10G2300/42 , C10G2400/02 , C10G2400/04 , C10G2400/08 , C10L1/00 , Y02P30/20
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公开(公告)号：EP3341575A1
公开(公告)日：2018-07-04
申请号：EP16770107.7
申请日：2016-08-23
CPC分类号： F01K13/02 , C07C5/2732 , C07C7/00 , C10G53/04 , C10G55/00 , C10G57/00 , C10G59/00 , C10G61/00 , C10G61/10 , C10G63/00 , C10G69/00 , C10G2300/4006 , C10G2400/04 , C10G2400/30 , F01D17/145 , F01K3/00 , F01K3/185 , F01K27/00 , H02K7/1823 , C07C15/08
摘要： Optimizing power generation from waste heat in large industrial facilities such as petroleum refineries by utilizing a subset of all available hot source streams selected based, in part, on considerations for example, capital cost, ease of operation, economics of scale power generation, a number of organic Rankine cycle (ORC) machines to be operated, operating conditions of each ORC machine, combinations of them, or other considerations are described. Subsets of hot sources that are optimized to provide waste heat to one or more ORC machines for power generation are also described. Further, recognizing that the utilization of waste heat from all available hot sources in a mega-site such as a petroleum refinery and aromatics complex is not necessarily or not always the best option, hot source units in petroleum refineries from which waste heat can be consolidated to power the one or more ORC machines are identified.
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公开(公告)号：EP3341455A1
公开(公告)日：2018-07-04
申请号：EP16758058.8
申请日：2016-08-22
CPC分类号： F28D7/0083 , B01D3/007 , B01D3/32 , B01D51/10 , B01D53/047 , B01D53/1462 , B01D53/185 , B01D53/343 , B01D53/48 , B01D53/8603 , B01D53/96 , B01D2252/204 , C01B3/24 , C01B2203/0233 , C02F1/586 , C02F2101/10 , C02F2101/101 , C02F2101/16 , C02F2103/18 , C02F2103/36 , C07C7/08 , C10G33/06 , C10G35/04 , C10G45/00 , C10G45/02 , C10G45/44 , C10G47/00 , C10G65/00 , C10G65/12 , C10G69/00 , C10G2300/202 , C10G2300/207 , C10G2300/4006 , C10G2300/4056 , C10G2400/04 , C10G2400/30 , C10K3/04 , C10L3/101 , C10L3/103 , C10L3/104 , C10L2290/06 , C10L2290/541 , F01D17/145 , F01K3/185 , F01K13/00 , F01K13/02 , F01K23/06 , F01K23/064 , F01K25/06 , F01K25/08 , F01K27/00 , F01K27/02 , F28F9/26 , H02K7/1823 , Y02P20/129 , Y02P30/10
摘要： Configurations and related processing schemes of specific inter-plants and hybrid, intra- and inter-plants waste heat recovery schemes for thermal energy consumption reduction in integrated refining-petrochemical facilities synthesized for grassroots medium grade crude oil semi-conversion refineries to increase energy efficiency from specific portions of low grade waste heat sources are described. Configurations and related processing schemes of specific inter-plants and hybrid, intra- and inter-plants waste heat recovery schemes for thermal energy consumption reduction in integrated refining-petrochemical facilities synthesized for integrated medium grade crude oil semi-conversion refineries and aromatics complex for increasing energy efficiency from specific portions of low grade waste sources are also described.
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公开(公告)号：EP3135749B1
公开(公告)日：2018-06-06
申请号：EP16182920.5
申请日：2016-08-05
发明人： KUMAR, Pravesh , NARESH, Pappu , CHAUDHARY, Vinay Kumar , DAVE, Darshankumar Manubhai , KUMAR, Kamal , BALASUNDARAM, Murugan , RAMESH, Karumanchi , BUTLEY, Ganesh Vitthalrao , NANDWANI, Om Prakash , SAU, Madhusudan , KUMAR, Brijesh , DAS, Biswapriya
IPC分类号： C10G67/00 , C10G47/00 , C10G7/06 , B01J35/12 , B01J31/02 , C10G47/26 , C10G65/12 , C10G45/62
CPC分类号： C10G67/00 , B01J31/02 , B01J35/023 , B01J35/12 , B01J37/20 , B01J38/72 , C10G7/06 , C10G45/62 , C10G47/00 , C10G47/26 , C10G65/12 , C10G2300/1037 , C10G2400/00 , C10G2400/04
摘要： This invention relates to a process for hydro cracking of heavy oils. More particularly, this invention relates to a catalytic process for converting heavy oils, such as vacuum gas oil (VGO) and VGO containing a high proportion of vacuum resid (VR) to middle distillate products.
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公开(公告)号：EP2072604B1
公开(公告)日：2018-04-25
申请号：EP06791147.9
申请日：2006-09-28
发明人： XIE, Chaogang , ZHU, Genquan , YANG, Yihua , LUO, Yibin , LONG, Jun , SHU, Xingtian , ZHANG, Jiushun
IPC分类号： C10G11/05 , B01J29/80 , B01J29/072 , B01J29/076 , B01J29/40
CPC分类号： B01J29/80 , B01J29/084 , B01J29/18 , B01J29/40 , B01J29/60 , B01J29/7057 , B01J29/7615 , B01J29/7815 , B01J37/0045 , B01J2229/18 , B01J2229/42 , C10G11/02 , C10G11/05 , C10G11/14 , C10G11/16 , C10G11/18 , C10G2300/1033 , C10G2300/104 , C10G2300/1044 , C10G2300/1055 , C10G2300/107 , C10G2300/1074 , C10G2300/1077 , C10G2300/4018 , C10G2300/4093 , C10G2300/807 , C10G2400/02 , C10G2400/04 , C10G2400/20
摘要： A process for the catalytic conversion of hydrocarbons, said process comprising the following steps: a feedstock of hydrocarbons is contacted with a hydrocarbon-converting catalyst to conduct a catalytic cracking reaction in a reactor, then the reaction products are taken from said reactor and fractionated to give light olefins, gasoline, diesel, heavy oil and other saturated hydrocarbons with low molecular weight, wherein said hydrocarbon-converting catalyst comprises, based on the total weight of the catalyst, 1-60 wt% of a zeolite mixture, 5-99 wt% of a thermotolerant inorganic oxide and 0-70 wt% of clay, wherein said zeolite mixture comprises, based on the total weight of said zeolite mixture, 1-75 wt% of a zeolite beta modified with phosphorus and a transition metal M, 25-99 wt% of a zeolite having a MFI structure and 0-74 wt% of a large pore zeolite, wherein the anhydrous chemical formula of the zeolite beta modified with phosphorus and the transition metal M is represented in the mass percent of the oxides as (0-0.3)Na 2 O·(0.5-10)Al 2 O 3 ·(1.3-10)P 2 O 5 ·(0.7-15)M x O y ·(64-97)SiO 2 , in which the transition metal M is one or more selected from the group consisting of Fe, Co, Ni, Cu, Mn, Zn and Sn; x represents the atom number of the transition metal M, and y represents a number needed for satisfying the oxidation state of the transition metal M. The process of the present invention has a higher ability to convert petroleum hydrocarbon in a higher yield for light olefins, particularly for propylene.
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公开(公告)号：EP3132006A4
公开(公告)日：2017-12-06
申请号：EP15768372
申请日：2015-03-26
申请人： NESTE OYJ
发明人： MYLLYOJA JUKKA PEKKA , PIILOLA RAMI
IPC分类号： C10G50/00 , B01J21/04 , B01J21/06 , B01J21/08 , B01J23/00 , B01J23/04 , B01J23/10 , B01J23/30 , B01J23/883 , B01J35/00 , B01J35/10 , C07C51/353 , C07C51/367 , C07C59/347 , C07D307/33 , C10G3/00 , C10L1/04 , C10L1/06 , C10L1/08
CPC分类号： C07C51/353 , B01J21/04 , B01J21/063 , B01J21/08 , B01J23/002 , B01J23/04 , B01J23/10 , B01J23/30 , B01J23/883 , B01J35/002 , B01J35/10 , B01J35/1014 , B01J35/1019 , C07C51/367 , C07C59/347 , C07D307/33 , C10G3/46 , C10G3/47 , C10G3/48 , C10G3/50 , C10G50/00 , C10G2300/202 , C10G2300/301 , C10G2300/302 , C10G2300/304 , C10G2400/02 , C10G2400/04 , C10G2400/08 , C10L1/04 , C10L1/06 , C10L1/08 , C10L2200/0469 , C10L2270/04 , Y02P30/20
摘要： The present invention relates to catalytic conversion of ketoacids, including methods for increasing the molecular weight of ketoacids, the method comprising the steps of providing in a reactor a feedstock comprising at least one ketoacid. The feedstock is then subjected to one or more C-C-coupling reaction(s) in the presence of a catalyst system comprising a first metal oxide and a second metal oxide.
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