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    • 4. 发明授权
    • Dehydration of alcohols on crystalline silicates
    • 醇在结晶硅酸盐上的脱水
    • US09061954B2
    • 2015-06-23
    • US12864966
    • 2009-02-05
    • Delphine MinouxNikolai NesterenkoWalter VermeirenSander Van DonkJean-Pierre Dath
    • Delphine MinouxNikolai NesterenkoWalter VermeirenSander Van DonkJean-Pierre Dath
    • C07C1/20C07C1/24B01J29/40
    • 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/Al 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.
    • 本发明涉及一种使至少一种醇脱水以制备至少一种烯烃的方法,其包括:在反应器中引入至少包含醇,任选的水,任选的惰性组分的物流(A) 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的催化剂,从所述反应器回收含烯烃的料流(B),其中所述催化剂是:具有Si / Al比率的结晶硅酸盐 至少约100个,或脱铝的结晶硅酸盐或磷改性沸石,醇的WHSV为至少2h -1,温度范围为280℃至500℃。它还涉及相同的方法 如上所述,但是其中催化剂是磷改性沸石并且在任何WHSV。 脱水反应器中的醇的分压有利地为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℃,醇选自 乙醇,丙醇,丁醇和苯乙醇。
    • 5. 发明申请
    • DEHYDRATION OF ALCOHOLS ON ACIDIC CATALYSTS
    • 酒精在酸性催化剂上的脱水
    • US20130217943A1
    • 2013-08-22
    • US13701774
    • 2011-06-20
    • Delphine MinouxCindy AdamNikolai NesterenkoJean-Pierre DathWalter VermeirenSander Van Donk
    • Delphine MinouxCindy AdamNikolai NesterenkoJean-Pierre DathWalter VermeirenSander Van Donk
    • C07C1/24
    • C07C1/24C07C2521/04C07C2521/06C07C2521/12C07C2529/40C07C2529/65C07C2529/82C07C2529/83C07C2529/85Y02P20/52C07C11/04
    • The present invention is a process for the dehydration of an alcohol having at least 2 carbon atoms to make the corresponding olefin, comprising: a) introducing in a reactor a stream (A) comprising at least an alcohol, optionally water, optionally an inert component, b) contacting said stream with an acidic 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, water and the olefin and optionally recycling said inert component and optionally a part of the water to the reactor of step a), wherein, f) an effective amount of a component capable to neutralize a part of the catalyst active site is introduced in stream (A) or directly in the dehydration reactor and g) optionally the temperature of the dehydration reactor is adjusted to increase the alcohol conversion or the olefin yield or both. In another embodiment at step f) an effective amount of a component capable to increase the selectivity for the desired corresponding olefin is introduced in stream (A) or directly in the dehydration reactor.The component introduced at step f) can be chosen from the group consisting of ammonia, organic ammonium salts, hydrazine, nitriles, amines (including pyridines, pyrrols, pyrrolydones and pyrrolidines), amides, imines, di-imines, imides, cyanates, isocyanates, nitrites and nitroso compounds, aldehydes, ketones, carboxylic esters, and their corresponding thio-compounds (thiols, sulphides, disulfides).
    • 本发明是使具有至少2个碳原子的醇脱水以制备相应的烯烃的方法,其包括:a)在反应器中引入至少包含醇,任选的水,任选的惰性组分的流(A) b)使所述物流与所述反应器中的酸性催化剂接触,在有效使所述醇的至少一部分脱水以制备烯烃的条件下,c)从所述反应器回收流(B),其包含:所述惰性组分和至少一种 烯烃,水和任选的未转化的醇,d)任选地将料流(B)分馏以回收未转化的醇,并将所述未转化的醇再循环到步骤a)的反应器中,e)任选地将料流(B)分馏以回收惰性组分, 水和烯烃,并任选地将所述惰性组分和任选的一部分水再循环到步骤a)的反应器中,其中f)有效量的能够中和一部分Ca 天然气活性位点以流(A)或直接在脱水反应器中引入,并且g)任选地调节脱水反应器的温度以增加醇转化率或烯烃产率或两者。 在步骤f)的另一个实施方案中,有效量的能够增加所需相应烯烃的选择性的组分被引入到流(A)中,或直接在脱水反应器中引入。 在步骤f)引入的组分可以选自氨,有机铵盐,肼,腈,胺(包括吡啶,吡咯,吡咯烷酮和吡咯烷),酰胺,亚胺,二亚胺,酰亚胺,氰酸酯,异氰酸酯 ,亚硝酸盐和亚硝基化合物,醛,酮,羧酸酯及其相应的硫代化合物(硫醇,硫化物,二硫化物)。
    • 6. 发明申请
    • Dehydration of Alcohols on Crystalline Silicates
    • 醇在结晶硅酸盐上的脱水
    • US20110124939A1
    • 2011-05-26
    • US12864966
    • 2009-02-05
    • Delphine MinouxNikolai NesterenkoWalter VermeirenSander Van DonkJean-Pierre Dath
    • Delphine MinouxNikolai NesterenkoWalter VermeirenSander Van DonkJean-Pierre Dath
    • C07C1/24
    • 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/Al 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.
    • 本发明涉及一种使至少一种醇脱水以制备至少一种烯烃的方法,其包括:在反应器中引入至少包含醇,任选的水,任选的惰性组分的物流(A) 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的催化剂,从所述反应器回收含烯烃的料流(B),其中所述催化剂是:具有Si / Al比率的结晶硅酸盐 至少约100个,或脱铝的结晶硅酸盐或磷改性沸石,醇的WHSV为至少2h -1,温度范围为280℃至500℃。它还涉及相同的方法 如上所述,但是其中催化剂是磷改性沸石并且在任何WHSV。 脱水反应器中的醇的分压有利地为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℃,醇选自 乙醇,丙醇,丁醇和苯乙醇。
    • 7. 发明申请
    • Process to Make Olefins from Ethanol
    • US20110105815A1
    • 2011-05-05
    • US12864995
    • 2009-02-05
    • Delphine MinouxNikolai NesterenkoWalter VermeirenSander Van DonkGiacomo Grasso
    • Delphine MinouxNikolai NesterenkoWalter VermeirenSander Van DonkGiacomo Grasso
    • C07C1/24
    • 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 10 wt % 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 atoms or more at the inlet of the OCP reactor.
    • 10. 发明授权
    • Process for obtaining modified molecular sieves
    • 获得改性分子筛的方法
    • US09180439B2
    • 2015-11-10
    • US12811219
    • 2009-01-23
    • Nikolai NesterenkoWalter VermeirenSander Van DonkDelphine Minoux
    • Nikolai NesterenkoWalter VermeirenSander Van DonkDelphine Minoux
    • B01J29/06B01J27/16B01J29/40B01J37/28C07C1/20B01J37/02
    • 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 at least one molecular sieve selected from one of: a P-modified molecular sieve which contains at least 0.3 wt % of P obtained by dealuminating a molecular sieve in a steaming step, followed by a leaching step using an acid solution containing a source of P a molecular sieve which is modified with P during step b) by dealuminating the molecular sieve in a steaming step, followed by a leaching step using an acid solution containing a source of P 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)。 选择至少一种分子筛,其选自以下之一中的一种分子筛:P-改性分子筛,其含有至少0.3重量%的通过在蒸汽步骤中脱模分子筛获得的P,然后使用含有源的 P是在步骤b)期间用P改性的分子筛,通过在蒸汽步骤中脱分解分子筛,然后使用含有P源的酸溶液进行浸出步骤,从而引入至少0.3重量%的P b)。 使所述分子筛与含碱土金属或稀土金属的化合物(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分子筛中。 本发明还涉及一种催化剂复合材料,其包含:a)。 至少10重量%的M-P改性分子筛包含至少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)。 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以用于从含氧,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材料也可以在OCP方法中加入或替代地使用。