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    • 81. 发明申请
    • Integrated scheme of processes for extracting and treating an extra-heavy or bituminous crude
    • 用于提取和处理超重或沥青原油的方法的综合方案
    • US20070045155A1
    • 2007-03-01
    • US11508331
    • 2006-08-23
    • Arnault SelmenThierry GauthierMathieu PinaultEric Benazzi
    • Arnault SelmenThierry GauthierMathieu PinaultEric Benazzi
    • C10G65/02
    • C10G45/02C10G1/047C10G9/005C10G9/007C10G47/02C10G65/12C10G69/06C10G2300/1033C10G2300/1096C10G2300/302C10G2300/308C10G2300/807
    • A process for preparation of synthetic crude from a deposit of heavy crude, comprises: (a) the extraction of heavy crude by technology using steam; (b) the separation of crude extract and water; (c) the separation of crude into at least one light fraction and one heavy fraction; (d) the conversion of the heavy fraction of separation into a lighter product, said converted product, and a residue; (e) optionally, the partial or total hydrotreatment of the converted product and/or the light fraction (or fractions) obtained during the separation c), (f) the combustion and/or gasification of the conversion residue; the converted product and the light fraction (or fractions) for separation, optionally having been subjected to a hydrotreatment e), constituting the synthetic crude; said combustion allowing the generation of steam and/or electricity and said gasification allowing the generation of hydrogen; the steam and/or electricity thus generated being used for the extraction a) and/or the electricity and/or hydrogen thus generated being used for the conversion d) and/or the hydrotreatment e).
    • 由重质原油沉积物制备​​合成原油的方法包括:(a)通过蒸汽技术提取重质原油; (b)粗提物与水的分离; (c)将粗分离成至少一个轻馏分和一个重馏分; (d)将重馏分转化成更轻的产物,所述转化的产物和残余物; (e)任选地,在分离期间获得的转化产物和/或轻馏分(或级分)的部分或全部加氢处理c),(f)转化残余物的燃烧和/或气化; 转化产物和用于分离的轻馏分(或级分),任选已经进行加氢处理e)构成合成粗品; 所述燃烧允许产生蒸汽和/或电,并且所述气化允许产生氢气; 由此产生的蒸汽和/或电力用于提取a)和/或由此产生的电和/或氢用于转化d)和/或加氢处理e)。
    • 83. 发明授权
    • Hydrocracking catalyst having a unique silica-alumina substrate
    • 具有独特二氧化硅 - 氧化铝底物的加氢裂化催化剂
    • US06733657B2
    • 2004-05-11
    • US10045678
    • 2002-01-15
    • Eric BenazziTivadar CseriMagalie Roy-AubergerPatrick Euzen
    • Eric BenazziTivadar CseriMagalie Roy-AubergerPatrick Euzen
    • C10G4704
    • C10G47/12B01J21/12B01J35/1019B01J35/1042B01J35/1047B01J35/1061B01J35/108B01J37/0009B01J37/20
    • A hydrocarbon conversion catalyst contains at least one silica-alumina having the following characteristics: A content by weight of silica SiO2 of between 10 and 60% by weight; an Na content less than 300 ppm by weight; a total pore volume of between 0.5 and 1.2 m/g measured by mercury porosimetry; a porosity of said silica-alumina wherein: the volume of mesopores whose diameter is between 40 Å and 150 Å, and whose mean diameter varies between 80 and 120 Å represents between 30 and 80% of the total pore volume, and (ii) the volume of macropores, whose diameter is greater than 500 Å and preferably between 1000 Å and 10,000 Å represents between 20 and 80% of the total pore volume; a specific surface area greater than 200 m2/g, and at least one hydro-dehydrogenating element selected metals of group VIB and group VIII, and optionally phosphorus, boron, silicon, or elements of group VIIA, VIIB or VB.
    • 烃转化催化剂含有至少一种具有以下特征的二氧化硅 - 氧化铝:二氧化硅SiO 2的重量含量为10至60重量%; Na含量小于300重量ppm; 通过水银孔率法测量的总孔体积为0.5-1.2m 2 / g; 所述二氧化硅 - 氧化铝的孔隙率,其中直径为介于40和150之间,其平均直径在80和120之间变化的介孔的体积占总孔体积的30至80%,和(ii) 其直径大于500埃,优选在1000埃至10,000埃之间的大孔体积占总孔体积的20至80%; 比表面积大于200m 2 / g,以及至少一种加氢脱氢元素选择VIB族和VIII族的金属,以及任选的磷,硼,硅或VIIA,VIIB或VB族的元素。
    • 87. 发明授权
    • Process for preparing a zeolite with structure type MTT using specific template precursors
    • 使用特定模板前体制备具有MTT结构类型的沸石的方法
    • US06548040B1
    • 2003-04-15
    • US09672053
    • 2000-09-29
    • Loïc RouleauFrédéric KolendaEric Benazzi
    • Loïc RouleauFrédéric KolendaEric Benazzi
    • C01B3948
    • B01J20/18B01J29/04C01B39/48C10G45/64Y10S423/36
    • The present invention concerns a process for synthesising a zeolite with structure type MTT comprising at least one element X selected from silicon and germanium and at least one element T selected from aluminium, iron gallium, boron, titanium, vanadium, zirconium, molybdenum, arsenic, antimony, chromium and manganese, comprising reacting an aqueous mixture comprising at least one source of at least one element X, at least one source of at least one element T, and at least one precursor of an organic compound comprising at least one alkylated polymethylene &agr;-&ohgr; diammonium derivative, characterized in that at least one precursor is selected from monoamines. The present invention also concerns the use of the zeolite obtained as a catalyst in a process for converting hydrocarbon-containing feeds, as an adsorbent to control pollution and as a molecular sieve for separation.
    • 本发明涉及合成具有结构类型MTT的沸石的方法,该方法包括至少一种选自硅和锗的元素X和至少一种选自铝,铁镓,硼,钛,钒,锆,钼,砷, 锑,铬和锰,包括使包含至少一种元素X的至少一种源,至少一种元素T的至少一种源的至少一种含有至少一种烷基化聚亚甲基α - 大豆二铵衍生物,其特征在于至少一种前体选自单胺。 本发明还涉及在用于转化含烃原料作为吸附剂以控制污染和分离分子筛的方法中作为催化剂获得的沸石的用途。
    • 89. 发明授权
    • Process for improving the pour point, and a catalyst based on at least one MTT, Ton or Fer zeolite
    • 改善倾点的方法,以及基于至少一种MTT,Ton或Fer沸石的催化剂
    • US06235960B1
    • 2001-05-22
    • US09310181
    • 1999-05-12
    • Eric BenazziSlavik KasztelanNathalie George-Marchal
    • Eric BenazziSlavik KasztelanNathalie George-Marchal
    • C07C513
    • C10G45/64B01J29/67B01J29/7284B01J29/7292B01J29/7484B01J29/7492B01J29/7884B01J29/7892B01J35/1061B01J35/1085B01J2229/26B01J2229/42
    • A process for improving the pour point of a feed comprising paraffins containing more than 10 carbon atoms, in which the feed to be treated is brought into contact with a catalyst comprising at least one zeolite with structure type MTT, TON or FER or any possible combination of these three, at least one hydro-dehydrogenating element selected from elements from group VIB and group VIII of the periodic table, at least one deposited promoter element (boron, silicon, phosphorous), optionally at least one group VIIA element, optionally at least one group VIIB element, at a temperature in the range 170° C. to 500° C., a pressure in the range 1 to 250 bars and at an hourly space velocity in the range 0.05 to 100 h−1, in the presence of hydrogen in an amount of 50 to 2000 l/l of feed. The oils obtained have good pour points and high viscosity indices (VI). The process is also applicable to gas oils, and other feeds requiring a reduction in pour point. The invention also relates to a catalyst containing silicon and to its use for converting hydrocarbon-containing feeds.
    • 一种用于改进含有多于10个碳原子的链烷烃的进料的倾点的方法,其中待处理的进料与包含至少一种结构类型为MTT,TON或FER的沸石或任何可能的组合的催化剂接触 这些三种中的至少一种选自元素周期表第VIB族和第VIII族元素的至少一种加氢脱氢元素,至少一种沉积的促进元素(硼,硅,磷),任选至少一种VIIA族元素,任选至少 一组VIIB元素,在170℃至500℃的温度范围内,压力范围为1至250巴,时间空间速度为0.05至100小时-1,在存在 量为50至2000升/升的进料的氢。 所得油具有良好的倾点和高粘度指数(VI)。 该方法也适用于需要降低倾点的瓦斯油和其它进料。本发明还涉及含硅的催化剂及其用于转化含烃物料的用途。