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    • 73. 发明公开
    • PROCESS TO MAKE OLEFINS FROM ETHANOL
    • 用于由乙醇制备烯烃
    • EP2238096A1
    • 2010-10-13
    • EP09709326.4
    • 2009-02-05
    • Total Petrochemicals Research Feluy
    • MINOUX, DelphineNESTERENKO, NikolaiVERMEIREN, WalterVAN DONK, SanderGRASSO, Giacomo
    • C07C11/06C07C11/04C07C1/24C07C4/06
    • C07C11/04C07C1/24C07C4/06C07C11/06
    • The present invention relates to a process for the conversion of ethanol to make essentially ethylene and propylene, comprising : a) introducing in a reactor (A) (also called the first low temperature reaction zone) a stream comprising ethanol, optionally water, optionally an inert component, b) contacting said stream with a catalyst (A1) in said reactor (A) at conditions effective to dehydrate at least a portion of the ethanol to essentially ethylene, c) recovering from said reactor an effluent comprising : essentially ethylene, minor amounts of various hydrocarbons, water, optionally unconverted ethanol and the optional inert component of step a), d) fractionating said effluent of step c) to remove water, unconverted ethanol, optionally the inert component, and optionally the whole or a part of the various hydrocarbons to get a stream (D) comprising essentially ethylene and optionally the inert component, e) introducing at least a part of said stream (D) mixed with a stream (D1 ) comprising olefins having 4 carbon atoms or more (C4+ olefins) in a OCP reactor (also called the second high temperature reaction zone) under the condition that the mixture (D)+(D1) comprises at least 10wt% of C4+ olefins, f) contacting said stream comprising at least a part of (D) and the stream (D1 ) in said OCP reactor with a catalyst which is selective towards light olefins in the effluent, to produce an effluent with an olefin content of lower molecular weight than that of the feedstock, g) fractionating said effluent of step f) to produce at least an ethylene stream, a propylene stream and a fraction consisting essentially of hydrocarbons having 4 carbon atoms or more, optionally recycling ethylene in whole or in part at the inlet of the OCP reactor of step f), or at the inlet of the reactor (A) or in part at the inlet of the OCP reactor of step f) and in part at the inlet of the reactor (A), optionally recycling the fraction consisting essentially of hydrocarbons having 4 carbon at
    • 74. 发明公开
    • DEHYDRATION OF ALCOHOLS IN THE PRESENCE OF AN INERT COMPONENT
    • 酒精脱水惰性成分的存在
    • EP2238093A1
    • 2010-10-13
    • EP09708640.9
    • 2009-02-05
    • Total Petrochemicals Research Feluy
    • MINOUX, DelphineNESTERENKO, NikolaiVERMEIREN, WalterVAN DONK, Sander
    • C07C1/24C07C11/02C07C11/04
    • C07C11/02C07C1/24C07C11/04
    • The present invention (first embodiment) relates to a process for the dehydration of at least an alcohol to make at least an olefin, comprising : a) introducing in a reactor a stream (A) comprising at least an alcohol optionally in aqueous solution and an inert component, b) contacting said stream with a catalyst in said reactor at conditions effective to dehydrate at least a portion of the alcohol to make an olefin, c) recovering from said reactor a stream (B) comprising : the inert component and at least an olefin, water and optionally unconverted alcohol, d) optionally fractionating the stream (B) to recover the unconverted alcohol and recycling said unconverted alcohol to the reactor of step a), e) optionally fractionating the stream (B) to recover the inert component and the olefin and recycling said inert component to the reactor of step a), Wherein, the inert component is selected among ethane, the hydrocarbons having from 3 to 10 carbon atoms, naphtenes and CO2, the proportion of the inert component is such as the reactor operates essentially adiabatically. The present invention also relates to a similar process as above but the catalyst is : • a crystalline silicate having a ratio Si/AI of at least 100, or • a dealuminated crystalline silicate, or • a phosphorus modified zeolite, the WHSV of the alcohol is at least 2 h-1 when the catalyst is a crystalline silicate having a ratio Si/AI of at least 100 or a dealuminated crystalline silicate. Advantageously the pressure of the dehydration reactor is high enough to help the recovery of the inert component and recycling thereof in the reactor of step a) without a gas compressor but only a pump.
    • 77. 发明公开
    • MIXTURES OF MOLECULAR SIEVES COMPRISING MEAPO, THEIR USE IN CONVERSION OF ORGANICS TO OLEFINS.
    • 含的MeAPO分子筛的混合物,它们在有机物中烯烃的转化
    • EP2175990A1
    • 2010-04-21
    • EP08786525.9
    • 2008-07-28
    • Total Petrochemicals Research Feluy
    • VERMEIREN, WalterNESTERENKO, Nikolai
    • B01J29/00C07C1/20
    • C07C1/20B01J29/005B01J29/035B01J29/84B01J29/85C07C1/322Y02P30/42C07C11/02
    • The present invention is a mixture comprising by weight 0.01 to 28% of at least one medium or large pore crystalline silicoaluminate, silicoaluminophosphate materials or silicoaluminate mesoporous molecular sieves (co-catalyst) (A) for respectively 99.99 to 72% of at least a MeAPO molecular sieve. Preferably the proportion of (A) is 1 to 15% for respectively 99 to 85% of MeAPO molecular sieves. MeAPO molecular sieves having CHA (SAPO-34) or AEI (SAPO-18) structure or mixture thereof are the most preferable. Si is the most desirable metal in MeAPO. The present invention also relates to catalysts consisting of the above mixture or comprising the above mixture. The present invention also relates to a process (hereunder referred as 'XTO process') for making an olefin product from an oxygen-containing, halogenide-containing or sulphur-containing organic feedstock wherein said oxygen-containing, halogenide-containing or sulphur-containing organic feedstock is contacted with the above catalyst (in the XTO reactor) under conditions effective to convert the oxygen- containing, halogenide-containing or sulphur-containing organic feedstock to olefin products (the XTO reactor effluent). The present invention also relates to a process (hereunder referred as 'combined XTO and OCP process') to make light olefins from an oxygen-containing, halogenide-containing or sulphur-containing organic feedstock comprising : contacting said oxygen-containing, halogenide-containing or sulphur-containing organic feedstock in the XTO reactor with the above catalyst at conditions effective to convert at least a portion of the feedstock to form an XTO reactor effluent comprising light olefins and a heavy hydrocarbon fraction; separating said light olefins from said heavy hydrocarbon fraction; contacting said heavy hydrocarbon fraction in the OCP reactor at conditions effective to convert at least a portion of said heavy hydrocarbon fraction to light olefins.
    • 79. 发明公开
    • MTO PROCESS BASED ON MEAPO MOLECULAR SIEVES COMBINED WITH AN OCP PROCESS TO MAKE OLEFINS
    • 在组合的MeAPO分子SEVEN基于MTO处理与OCP PROCESS FOR生产烯烃
    • EP2121543A1
    • 2009-11-25
    • EP08717563.4
    • 2008-03-10
    • Total Petrochemicals Research Feluy
    • VERMEIREN, WalterNESTERENKO, Nikolai
    • C07C1/20C07C4/06C07C11/04C07C11/06C08F10/02C08F10/06
    • C07C11/04C01B3/44C07C1/20C07C1/26C07C4/06C07C11/06C07C17/10C07C2529/035C07C2529/40C07C2529/85C10G3/45C10G3/49C10G2300/202C10G2300/4081C10G2300/802C10G2400/20Y02P20/52Y02P30/42C07C9/00C07C19/075
    • The present invention relates to a process to make light olefins from an oxygen-containing, halogenide-containing or sulphur-containing organic feedstock comprising: contacting said oxygen-containing, halogenide-containing or sulphur-containing organic feedstock in a primary reactor with a catalyst made of a metalloaluminophosphate (MeAPO) molecular sieve with lamellar crystal morphology at conditions effective to convert at least a portion of the feedstock to form a first reactor effluent comprising light olefins and a heavy hydrocarbon fraction; separating said light olefins from said heavy hydrocarbon fraction; contacting said heavy hydrocarbon fraction in a second reactor at conditions effective to convert at least a portion of said heavy hydrocarbon fraction to light olefins; wherein said MeAPO has an empirical chemical composition on an anhydrous basis, after synthesis and calcination, expressed by the formula HxMeyAlzPkO2 in which, y+z+k=1 x = 10 and advantageously ranges from 10 to 100.
    • 本发明涉及一种从在含氧使轻质烯烃,或含卤化物有机原料包括含硫:使所述含氧,含卤化物或含硫的有机原料在主反应器中与催化剂 制成的金属铝磷酸盐(MeAPO的)分子筛具有层状晶体形态在有效地使至少原料的一部分转化,以形成第一反应器流出物包括轻质烯烃和重质烃级分的条件; 所述分离从所述重质烃馏分的轻烯烃; 在有效条件下,使所述重质烃馏分在第二反应器,以便将所述重质烃馏分以轻质烯烃中的至少一部分上; worin说的MeAPO或者具有到无水基的经验化学组成,在合成和煅烧后,由式过表达高x我ý系Al Z pk信息O 2,其中,Y + Z + K = 1×<= YY具有 值范围从0.0008〜0.4且有利地为0005至12时18 z具有0:25〜0.67且有利地12时38分至12点55 k具有的值范围从0.2至0.67且有利地12时36分至12点54所述主要具有片状晶体分子筛的值 的形态,其中宽度(W)和厚度(T)是如:W / T是> = 10且有利地为10至100,或worin说的MeAPO已编制一种方法,包括:a)形成反应 混合物含有织构影响剂(TIA),有机模板剂(TEMP),至少一个反应性无机的MeO 2的不溶性的在TIA源,的Al 2反应性来源O 3和P 2 O 5,b)使上述 反应混合物由此形成直到金属铝磷酸盐的晶体是FO Rmed指,c)回收固体反应产物,D)洗涤它与水以除去所述TIA和e)对其煅烧以除去所述有机模板。