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1. 发明授权

EP2473584B1 NON-FRACTIONATION PROCESS FOR PRODUCTION OF LOW-BOILING FUEL FROM CRUDE OIL OR FRACTIONS THEREOF 有权
公开(公告)号：EP2473584B1
公开(公告)日：2018-11-21
申请号：EP10812466.0
申请日：2010-07-27
申请人： Gunnerman, Rudolf W. , Gunnerman, Peter W.
发明人： GUNNERMAN, Rudolf, W. , GUNNERMAN, Peter, W.
IPC分类号： B01J23/889 , C10L1/04 , C10G29/20 , C10G49/00 , C10G49/04 , B01J23/888 , B01J23/86 , B01J23/745 , B01J23/75 , B01J23/755 , B01J35/06 , C10G11/00 , C10G11/10 , C10G15/08
CPC分类号： C10L1/04 , B01J23/8892 , B01J35/06 , C10G11/00 , C10G11/10 , C10G15/08 , C10G29/205 , C10G49/007 , C10G49/04 , C10G2300/1025 , C10G2300/104 , C10G2300/1044 , C10G2300/1051 , C10G2300/1055 , C10G2300/1059 , C10G2300/4006
摘要： A clean-burning fuel with an upgraded mixture of hydrocarbons is produced by reacting methane-containing gas with crude oil or a liquid petroleum fraction in a process wherein the gas is fed to a reaction vessel to contact both the liquid and a metallic catalyst grid that is formed from windings of a transition metal supported on an iron frame immersed in a liquid petroleum fraction, at a moderate temperature to produce a gaseous reaction product which is condensed to form the fuel. The fuel has a variety of uses, including serving as an additive to crude oil for transport purposes.

2. 发明公开

EP3318619A1 VERFAHREN ZUR HERSTELLUNG VON KRAFTSTOFFEN AUS GASKONDENSATEN 审中-公开
标题翻译：从气体冷凝生产燃料的方法
公开(公告)号：EP3318619A1
公开(公告)日：2018-05-09
申请号：EP16197027.2
申请日：2016-11-03
申请人： Wolfdieter Klein Consulting GmbH Oel- und Gastechnologie
发明人： KLEIN, Wolfdieter
IPC分类号： C10G35/095
CPC分类号： C10G35/095 , C10G2300/104 , C10G2300/1044 , C10G2300/305 , C10G2400/02
摘要： Die Erfindung betrifft ein Verfahren zur Umwandlung von Gaskondensaten mit einem Siedebereich bis etwa 180°C in Kraftstoffe, insbesondere hochoktanige Otto-Kraftstoffe, bei dem aus der Gasgewinnung stammendes Kondensat unter Verwendung mindestens eines Zeolith-Katalysators reformiert wird, bei dem der Reforming-Prozess unter einem Druck von 1 bis 5 bar bei einer Temperatur von 380°C bis 560°C durchgeführt wird.
摘要翻译：本发明涉及一种方法，用于具有沸在燃料范围高达约180℃，特别是高辛烷值汽油燃料气体冷凝物的转化，其中源自使用至少一种沸石催化剂下重整气体回收冷凝物，其中，所述重整过程在380℃至560℃的温度下进行1至5巴的压力。

3. 发明授权

EP2072604B1 A PROCESS FOR CATALYTIC CONVERTING HYDROCARBONS 有权
标题翻译：一种催化转化烃的方法
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
申请人： China Petroleum & Chemical Corporation , Research Institute Of Petroleum Processing, Sinopec
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.

4. 发明授权

EP1893726B1 PROCESS FOR INCREASING PRODUCTION OF LIGHT OLEFIN HYDROCARBON FROM HYDROCARBON FEEDSTOCK 有权
标题翻译：从烃类原料中提高轻质烯烃生产工艺
公开(公告)号：EP1893726B1
公开(公告)日：2018-04-04
申请号：EP05780593.9
申请日：2005-08-17
申请人： SK Innovation Co., Ltd.
发明人： CHOI, Sun , OH, Seung Hoon, , SUNG, Kyoung Hak , LEE, Jong Hyung, , KANG, Sin Choel , KIM, Yong Seung , LIM, Byeung Soo , CHOI, Ahn Seop , CHANG, Byoung Mu
IPC分类号： C10G45/60 , C10G63/04
CPC分类号： C10G57/00 , B01J29/185 , B01J29/22 , B01J2229/20 , B01J2229/42 , C10G9/00 , C10G45/58 , C10G45/64 , C10G69/06 , C10G2300/104 , C10G2300/1044 , C10G2300/4081 , C10G2400/20 , C10G2400/28 , C10G2400/30 , Y02P20/132 , Y02P30/40
摘要： A process for increasing the production of light olefin hydrocarbons from a hydrocarbon feedstock. A process for producing an aromatic hydrocarbon mixture and liquefied petroleum gas (LPG) from a hydrocarbon mixture, and a process for producing a hydrocarbon feedstock which is capable of being used as a feedstock in the former process, that is to say, a fluidized catalytic cracking (FCC) process, a catalytic reforming process, and/or a pyrolysis process, are integrated, thereby it is possible to increase the production of C 2 -C 4 light olefin hydrocarbons.

5. 发明公开

EP3207105A1 PROCESS FOR THE PRODUCTION OF HIGH VALUE CHEMICALS FROM BIOLOGICALLY PRODUCED MATERIALS 有权
标题翻译：从生物制造材料生产高价值化学品的方法
公开(公告)号：EP3207105A1
公开(公告)日：2017-08-23
申请号：EP15778657.5
申请日：2015-10-09
申请人： Total Research & Technology Feluy
发明人： VERMEIREN, Walter , VANRYSSELBERGHE, Valérie
IPC分类号： C10G9/36 , C07C4/04 , C10G3/00
CPC分类号： C10G9/36 , C01B3/24 , C01B2203/0272 , C01B2203/065 , C07C4/04 , C10G3/46 , C10G3/50 , C10G2300/1011 , C10G2300/104 , C10G2300/1044 , C10G2300/1051 , C10G2300/1055 , C10G2300/1081 , C10G2300/202 , C10G2400/20 , C10G2400/30 , Y02P20/52 , C07C11/04 , C07C11/06 , C07C15/04 , C07C15/06 , C07C15/08 , C07C11/167
摘要： The present invention relates to a process for the production of high value chemicals, preferably including at least ethylene and propylene, by steam cracking a mixture of non-cyclic paraffin stream (A) comprising at least 90% of components having at least 12 carbon atoms, with either a mixture of hydrocarbons having from 3 to 4 carbon atoms or a mixture of hydrocarbons comprising at least 90% of components having a boiling point ranging from 15° C. to 200° C.
摘要翻译：本发明涉及一种生产高价值化学品的方法，所述高价值化学品优选至少包括乙烯和丙烯，通过蒸汽裂解包含至少90％具有至少12个碳原子的组分的非环状石蜡料流（A）的混合物与具有3至4个碳原子的烃的混合物或包含至少90％的具有15℃至200℃的沸点的组分的烃的混合物接触。

6. 发明授权

EP2202286B1 PROCESS FOR PRODUCING GASOLINE BASE AND GASOLINE 有权
标题翻译：生产汽油碱和汽油的方法
公开(公告)号：EP2202286B1
公开(公告)日：2017-07-19
申请号：EP08837277.6
申请日：2008-10-06
申请人： Nippon Oil Corporation
发明人： HATANAKA, Shigeto , SHIMADA, Koji , IKI, Hideshi
IPC分类号： C10G65/04 , C10G45/06 , C10G45/08 , C10L1/06 , C10G45/04 , C10G69/04 , C10G11/00 , C10G45/02
CPC分类号： C10G11/00 , C10G45/02 , C10G45/04 , C10G65/04 , C10G69/04 , C10G2300/104 , C10G2300/1044 , C10G2300/202 , C10G2300/301 , C10G2300/4018 , C10G2400/02 , C10L1/06

7. 发明公开

EP3060627A4 PYROLYSIS GASOLINE TREATMENT PROCESS 审中-公开
标题翻译： PYROLYSEBENZIN-BEHANDLUNGSVERFAHREN
公开(公告)号：EP3060627A4
公开(公告)日：2017-05-31
申请号：EP14856399
申请日：2014-10-08
申请人： UOP LLC
发明人： SCHMIDT ROBERT J , LUEBKE CHARLES P , JANULIS ROSE M
IPC分类号： C10G9/00
CPC分类号： C07C5/05 , C10G7/00 , C10G45/02 , C10G45/22 , C10G45/38 , C10G45/40 , C10G65/06 , C10G2300/104 , C10G2300/1044 , C10G2400/02 , C10G2400/22 , C10G2400/30
摘要： A process for treating pyrolysis gasoline that includes providing a first stage di-olefin reactor that includes a first bed and a second bed and introducing a pyrolysis gasoline stream to the first bed of the first stage di-olefin reactor. The process also preferably includes providing interstage cooling to the pyrolysis gasoline stream between the first and second beds of the first stage di-olefin reactor and routing the cooled pyrolysis gasoline stream through the second bed of the first stage di-olefin reactor. Finally, embodiments of the process also preferably involve routing at least a portion of an effluent stream from the second bed of the first stage di-olefin reactor to a location upstream of the first bed of the first stage di-olefin reactor, such that the effluent stream is configured to be combined with the pyrolysis gasoline stream.
摘要翻译：一种处理裂解汽油的方法，其包括提供包含第一床和第二床的第一阶段二烯烃反应器，并将裂解汽油物流引入第一阶段二烯烃反应器的第一床。该方法还优选包括对第一级二烯烃反应器的第一和第二床之间的裂解汽油流提供级间冷却，并将冷却的裂解汽油流引导通过第一级二烯烃反应器的第二床。最后，该方法的实施方式还优选涉及将来自第一阶段二烯烃反应器的第二床的流出物流的至少一部分引导至第一阶段二烯烃反应器的第一床的上游位置，使得流出物流被配置为与裂解汽油流结合。

8. 发明公开

EP3167027A1 PROCESS FOR PRODUCING BTX AND LPG 有权转让
标题翻译：生产BTX和LPG的工艺
公开(公告)号：EP3167027A1
公开(公告)日：2017-05-17
申请号：EP15732744.6
申请日：2015-07-06
申请人： SABIC Global Technologies B.V.
发明人： HOUSMANS, Thomas Hubertus Maria , TURNER, M Steve
IPC分类号： C10G47/18 , C10G70/06 , C10L3/12
CPC分类号： C10G47/18 , C10G47/00 , C10G70/06 , C10G2300/104 , C10G2300/1044 , C10G2300/4081 , C10G2400/28 , C10G2400/30 , C10L3/12
摘要： The invention is directed to a process for producing BTX and LPG, comprising: a) contacting a feed stream comprising C5-C12 hydrocarbons in the presence of hydrogen with a hydrocracking catalyst in a hydrocracking reactor to produce a hydrocracking product stream comprising hydrogen, methane, LPG and BTX, b) separating the hydrocracking product stream into a first gas stream and a first liquid stream, c) separating the first gas stream to obtain a second gas stream comprising hydrogen and methane and a second liquid stream comprising LPG and BTX, wherein the separation is performed such that the second liquid stream is substantially free of hydrogen and methane, d) separating the second liquid stream into a third gas stream comprising LPG and a third liquid stream comprising BTX, wherein step (c) involves adding a part of the third liquid stream to the first gas stream to absorb the LPG in the first gas stream to obtain the second liquid stream or adding a part of the third liquid stream to a gas stream sep crated from the first gas stream to absorb the LPG in said gas stream separated from the first gas stream to obtain the second liquid stream.
摘要翻译：本发明涉及一种生产BTX和LPG的方法，包括：a）在氢存在下，将包含C5-C12烃的进料流与加氢裂化催化剂在加氢裂化反应器中接触以产生加氢裂化产物流，所述加氢裂化产物流包含氢气， LPG和BTX，b）将加氢裂化产物流分离成第一气流和第一液流，c）分离第一气流得到包含氢和甲烷的第二气流和包含LPG和BTX的第二液流，其中进行分离使得第二液体流基本上不含氢和甲烷，d）将第二液体流分离成包含LPG的第三气体流和包含BTX的第三液体流，其中步骤（c）涉及添加一部分将第三液体流引导至第一气体流以吸收第一气体流中的LPG以获得第二液体流或添加第三液体流的一部分从第一气流中分离出的气流吸收与第一气流分离的气流中的LPG以获得第二液流。

10. 发明公开

EP3100784A1 CATALYST AND METHOD FOR AROMATIZATION OF C3-C4 GASES, LIGHT HYDROCARBON FRACTIONS AND ALIPHATIC ALCOHOLS, AS WELL AS MIXTURES THEREOF 审中-公开
标题翻译： CATALYST AND METHOD FOR调味C3-C4气体，较轻的烃馏分与脂族醇以及它们的混合物
公开(公告)号：EP3100784A1
公开(公告)日：2016-12-07
申请号：EP14881043.5
申请日：2014-12-17
申请人： NGT Global AG
发明人： LISHCHINER, Iosif Izrailevich , MALOVA, Olga Vasilyevna , TARASOV, Andrey Leonidovich
IPC分类号： B01J29/40 , B01J29/80 , B01J23/10 , B01J21/10 , B01J21/06 , C10G35/095
CPC分类号： C07C2/864 , B01J21/04 , B01J21/08 , B01J29/061 , B01J29/40 , B01J29/405 , B01J29/80 , B01J35/0006 , B01J37/04 , B01J37/30 , B01J2029/062 , B01J2229/183 , B01J2229/38 , C07C2521/04 , C07C2521/08 , C07C2529/40 , C07C2529/80 , C10G35/065 , C10G2300/104 , C10G2300/1044 , C10G2400/30
摘要： The invention relates to hydrocarbon feedstock processing technology, in particular, to catalysts and technology for aromatization of C 3 -C 4 hydrocarbon gases, light low-octane hydrocarbon fractions and oxygen-containing compounds (C 1 -C 3 aliphatic alcohols), as well as mixtures thereof resulting in producing an aromatic hydrocarbon concentrate (AHCC). The catalyst comprises a mechanical mixture of 2 zeolites, one of which is characterized by the silica/alumina ratio SiO 2 /Al 2 O 3 =20, pre-treated with an aqueous alkali solution and modified with oxides of rare-earth elements used in the amount from 0.5 to 2.0 wt% based on the weight of the first zeolite. The second zeolite is characterized by the silica/alumina ratio SiO 2 /Al 2 O 3 =82, comprises sodium oxide residual amounts of 0.04 wt% based on the weight of the second zeolite, and is modified with magnesium oxide in the amount from 0.5 to 5.0 wt% based on the weight of the second zeolite. Furthermore, the zeolites are used in the weight ratio from 1.7:1 to 2.8:1, wherein a binder comprises at least silicon oxide and is used in the amount from 20 to 25 wt% based on the weight of the catalyst. The process is carried out using the proposed catalyst in an isothermal reactor without recirculation of gases from a separation stage, by contacting a fixed catalyst bed with a gaseous feedstock, which was evaporated and heated in a preheater. The technical result consists in achieving a higher aromatic hydrocarbon yield while ensuring almost complete conversion of the HC feedstock and oxygenates, an increased selectivity with respect to forming xylols as part of an AHCC, while simultaneously simplifying the technological setup of the process by virtue of using a reduced (inter alia, atmospheric) pressure.
摘要翻译：本发明涉及烃原料的加工技术，特别是，为了催化剂和技术对于C的芳构化3 -C 4个烃类气体，光低辛烷值的烃馏分和含氧化合物（C1-C3脂族醇），以及它们的混合物如在芳香烃浓缩物（AHCC）制备得到的。该催化剂包含两种沸石，它是由二氧化硅/氧化铝比的SiO为特征的所有的一个的机械混合物2 /的Al 2 O 3 = 20，用在wässrige碱溶液进行预处理，并用中使用的稀土类元素的氧化物改性从0.5至2.0重量％，基于所述第一沸石的重量的量。第二沸石的二氧化硅/氧化铝比的SiO 2 /的Al 2 O 3 = 82，包括基于所述第二沸石的重量的12时04重量％氧化钠的残留量为特征，并且从0.5改性氧化镁的量到5.0重量％，基于所述第二沸石的重量。进一步，所述的沸石在重量比使用从1.7：1至2.8：1，worin粘合剂包含至少氧化硅和基于所述催化剂的重量的量被用于从20至25重量％。该过程是使用在等温反应器的建议的催化剂，而不脱离分离阶段的气体的再循环，通过接触固定催化剂床与气态原料，将其在预热器蒸发并加热。技术结果besteht在实现更高的芳香族烃的收率，并在增加的选择性相对于确保HC原料和含氧化合物的几乎完全转化为形成二甲苯作为AHCC的一部分，而同时由于使用的简化过程的工艺设置降低（尤其是，大气）压力。

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