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    • 53. 发明公开
    • DEHYDRATION OF ALCOHOLS ON CRYSTALLINE SILICATES
    • 晶体硅酸盐上醇的脱水
    • EP2238094A1
    • 2010-10-13
    • EP09709286.0
    • 2009-02-05
    • Total Petrochemicals Research Feluy
    • MINOUX, DelphineNESTERENKO, NikolaiVERMEIREN, WalterVAN DONK, SanderDATH, Jean-Pierre
    • C07C1/24C07C11/04
    • C07C1/24B01J29/40B01J2229/16B01J2229/36B01J2229/37B01J2229/42C07C2529/40Y02P20/52C07C11/04
    • The present invention relates to a process for the dehydration of at least an alcohol to make at least an olefin, comprising: introducing in a reactor a stream (A) comprising at least an alcohol, optionally water, optionally an inert component, 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, recovering from said reactor an olefin containing stream (B), Wherein the catalyst is : • a crystalline silicate having a ratio Si/AI of at least about 100, or • a dealuminated crystalline silicate, or • a phosphorus modified zeolite, the WHSV of the alcohols is at least 2 h-1, the temperature ranges from 280°C to 500°C. It relates also to the same process as above but wherein the catalyst is a phosphorus modified zeolite and at any WHSV. The partial pressure of the alcohol in the dehydration reactor advantageously ranges from 1.2 to 4 bars absolute (0.12 MPa to 0.4 MPa), the temperature of the dehydration reactor ranges advantageously from 300°C to 400°C and the alcohol is selected among ethanol, propanol, butanol and phenylethanol.
    • 本发明涉及使至少一种醇脱水以制备至少一种烯烃的方法,该方法包括:在反应器中引入包含至少一种醇,任选的水,任选的惰性组分的物流(A),将所述物流 在有效使至少一部分醇脱水以制备烯烃的条件下,在所述反应器中用催化剂从所述反应器中回收含烯烃物流(B),其中所述催化剂是:·结晶硅酸盐,其比例为Si / Al 至少约100,或·脱铝酸盐结晶硅酸盐或·磷改性沸石,醇的WHSV至少为2h-1,温度范围为280℃-500℃。 它也涉及与上述相同的方法,但其中催化剂是磷改性沸石和任何WHSV。 脱水反应器中醇的分压有利地为1.2至4巴绝对压力(0.12MPa至0.4MPa),脱水反应器的温度有利地为300℃至400℃,并且醇选自乙醇, 丙醇,丁醇和苯乙醇。
    • 55. 发明公开
    • PROCESS FOR OBTAINING MODIFIED MOLECULAR SIEVES
    • VERFAHREN ZUR GEWINNUNG MODIFIZIERTER MOLEKULARER SIEBE
    • EP2234718A2
    • 2010-10-06
    • EP09703599.2
    • 2009-01-23
    • Total Petrochemicals Research Feluy
    • NESTERENKO, NikolaiVERMEIREN, WalterVAN DONK, SanderMINOUX, Delphine
    • B01J27/16B01J29/06B01J29/40C07C1/20C07C4/06
    • C07C1/20B01J27/16B01J29/06B01J29/061B01J29/40B01J29/405B01J37/0201B01J37/0207B01J37/024B01J37/28B01J2229/16B01J2229/186B01J2229/36B01J2229/37C07C4/06C07C2523/02C07C2527/14C07C2529/06C07C2529/40C07C2529/82C07C2529/85C08F110/02C10G2400/20Y02P30/42C07C11/02
    • The invention covers a process for obtaining an alkaline earth or rare earth metal-P-modified molecular sieve (M-P-modified molecular sieve) comprising the following steps: a). selecting a molecular sieve selected from one of: - a P-modified molecular sieve which contains at least 0.3 wt% of P - a molecular sieve which is modified with P prior to or during step b) thereby introducing at least 0.3 wt % of P b). contacting said molecular sieve with an alkaline earth or rare earth metal-containing compound (M-containing compound) to introduce at least 0.05 wt% of the alkaline earth or rare earth metal to the molecular sieve. The invention also covers a catalyst composite comprising: a). at least 10 wt % of a M-P-modified molecular sieve comprising at least 0.05 % by weight of an alkaline earth or rare earth metal (M) and at least 0.3 wt% of P, b). optionally metal phosphate, c). optionally matrix material, and d). optionally binder. The catalyst of the invention can also be used in a 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 in the XTO reactor with the catalyst composite according to the invention under conditions effective to convert the oxygen-containing, halogenide-containing or sulphur-containing organic feedstock to olefin products (the XTO reactor effluent). The catalyst composite of the invention can also be used in addition or alternatively in an OCP process.
    • 本发明涉及一种获得碱土金属或稀土金属-P改性分子筛(M-P-改性分子筛)的方法,包括以下步骤:a)。 选择选自以下之一的分子筛:P-改性分子筛,其含有至少0.3重量%的P - 在步骤b)之前或期间用P改性的分子筛,由此引入至少0.3重量%的P b)。 使所述分子筛与含碱土或含稀土金属的化合物(含M化合物)接触,以将至少0.05重量%的碱土金属或稀土金属引入到分子筛中。 本发明还涵盖了一种催化剂复合材料,其包括:a)。 至少10重量%的包含至少0.05重量%的碱土金属或稀土金属(M)和至少0.3重量%的P,b)的M-P改性分子筛。 任选的金属磷酸盐,c)。 任选的基质材料,和d)。 可选粘合剂。 本发明的催化剂也可用于从含氧,含卤素或含硫有机原料制备烯烃产物的方法,其中所述含氧卤化物或含硫有机原料接触 在具有将含氧,含卤素或含硫有机原料转化为烯烃产物(XTO反应器流出物)的条件下,具有根据本发明的催化剂复合材料的XTO反应器。 本发明的催化剂复合物也可以在OCP方法中加入或替代地使用。