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    • 3. 发明授权
    • Process for the preparation of a catalyst for the polymerization of
olefins
    • 制备烯烃聚合催化剂的方法
    • US5574116A
    • 1996-11-12
    • US214691
    • 1994-03-18
    • Karel BujadouxJean-Michel BrussonFrancis PetitAndre Mortreux
    • Karel BujadouxJean-Michel BrussonFrancis PetitAndre Mortreux
    • C08F4/654C08F10/00
    • C08F10/00
    • A process is disclosed for the polymerization of olefins, using (i) a catalyst and (ii) an organometallic activator from Groups I, II or III of the Periodic Table at temperatures between 20.degree. and 250.degree. C., and pressure up to 200 bar, in solution, or in suspension in an inert liquid hydrocarbon, at temperatures between 160.degree. and 350.degree. C., under pressures of between 400 and 3000 bar, in a continuous manner in a reactor where the mean residence time of the catalyst is between 1 and 150 seconds. The catalyst comprises at least one titanium compound, at least one halogen-containing organoaluminum compound and at least one inorganic magnesium compound in suspension in at least one .alpha.,.omega.-dihaloalkane. The titanium compound is essentially a titanium (III) compound, the total content of titanium (II) and titanium (IV) being less than or equal to 15% of the total content of titanium. The catalyst is obtained by a process comprising, in a first step, the reduction of a titanium (IV) compound in an .alpha.,.omega.-dihaloalkane by means of a molar excess of at least one halogen-containing organoaluminum compound, in the absence of an ether, and, in a second step, the addition to the reaction mixture of a compound which forms a magnesium halide in situ without supplementary reduction of the titanium compound obtained in the first step. Molar ratios of the .alpha.,.omega.-dihaloalkane, the titanium compound, halogen-containing organoaluminum, and the compound which forms a magnesium halide in situ are also described.
    • 公开了一种用于烯烃聚合的方法,其使用(i)催化剂和(ii)在20℃至250℃之间的元素周期表第I,II或III族的有机金属活化剂,压力高达200 在惰性液体烃中,160-150℃的温度下,在400-3000巴的压力下,在反应器中连续地在惰性液体烃中悬浮或悬浮,其中催化剂的平均停留时间为 1到150秒之间。 催化剂包含至少一种钛化合物,至少一种含卤素的有机铝化合物和至少一种α,ω-二卤代烷烃中的悬浮液中的至少一种无机镁化合物。 钛化合物基本上是钛(III)化合物,钛(II)和钛(IV)的总含量小于或等于钛总含量的15%。 该催化剂是通过一种方法获得的,该方法包括在第一步骤中,通过摩尔过量的至少一种含卤素的有机铝化合物在α,ω-二卤代烷烃中还原钛(IV)化合物, 醚,并且在第二步中,在没有补充还原第一步中获得的钛化合物的情况下向原位形成镁卤化物的化合物的反应混合物加入。 还描述了α,ω-二卤代烷烃,钛化合物,含卤素的有机铝和原位形成卤化镁的化合物的摩尔比。
    • 4. 发明授权
    • Catalyst and process for the synthesis of saturated carboxylic esters
    • 用于饱和羧酸酯合成的催化剂和方法
    • US5194676A
    • 1993-03-16
    • US674745
    • 1991-03-26
    • Yves CastanetChristophe LegrandAndre MortreuxFrancis Petit
    • Yves CastanetChristophe LegrandAndre MortreuxFrancis Petit
    • B01J27/13B01J31/02C07B61/00C07C67/303C07C67/38C07C69/24
    • C07C69/24C07C67/38
    • Saturated carboxylic esters are produced from alkyl formate and an olefin, without the presence of substantial amounts of carbon monoxide, at a temperature of 120.degree. to 280.degree. C., under a pressure of 1 to 3,000 bars, in the presence of a catalyst based on ruthenium coordinated by ligands selected from carbon monoxide, halogen atoms and amines, and in the presence of an amide as a solvent. The catalyst is selected from catalysts consisting essentially of RuCl.sub.3.3H.sub.2 O; catalysts consisting essentially of the combination of an RuCl.sub.3.3H.sub.2 O together with at least one stabilizer selected from iodine, covalent iodides and quaternary ammonium halides; catalysts comprising Ru.sub.3 (CO).sub.12 together with at least one stabilizer such as is mentioned above; and catalysts selected from RuI.sub.3, [RuCl.sub.2 (CO).sub.3 ].sub.2, Ru(NH.sub.3).sub.6 Cl.sub.3 and [Ru(NH.sub.3).sub.5 Cl]Cl.sub.2, comprising, where appropriate, in addition, at least one stabilizer such as is mentioned above.
    • 在120至280℃的温度下,在1至3,000巴的压力下,在催化剂基的存在下,将饱和羧酸酯由甲酸烷基酯和烯烃生产,而不存在大量的一氧化碳 在由选自一氧化碳,卤素原子和胺的配体和在作为溶剂的酰胺存在下配位的钌上。 催化剂选自基本上由RuCl 3·3H 2 O组成的催化剂; 基本上由RuCl 3·3H 2 O与至少一种选自碘,共价碘化物和季铵卤化物的稳定剂的组合组成的催化剂; 包含Ru 3(CO)12的催化剂以及如上所述的至少一种稳定剂; 以及选自RuI 3,[RuCl 2(CO)3] 2,Ru(NH 3)6 Cl 3和[Ru(NH 3)5 Cl] Cl 2的催化剂,在适当的情况下还包括至少一种如上所述的稳定剂。
    • 9. 发明授权
    • Catalyst system, process for its preparation and its application to the
manufacture of aldehydes
    • 催化剂体系,其制备方法及其在制醛中的应用
    • US5024983A
    • 1991-06-18
    • US323718
    • 1989-03-15
    • Eric PaumardSylvain MutezAndre MortreuxFrancis Petit
    • Eric PaumardSylvain MutezAndre MortreuxFrancis Petit
    • B01J31/18B01J31/24C07C45/00C07C45/50C07C47/02C07C67/00
    • B01J31/188B01J31/2409C07C45/50B01J2231/321B01J2531/828
    • The catalyst system is characterized in that it comprises:at least one platinum complex of formula LPtX.sub.2 in which L is an organic compound containing at least two phosphorus atoms capable of coordinating platinum and X is a halogen atom, andat least one combination formed between iron and an alkene carbonate, the alkene group preferably containing from 2 to 6 carbon atoms.The process for its preparation is characterized in that at least one combination formed between iron adn the alkene carbonate is reacted with at least one platinum complex of formula LPtX.sub.2 in at least one solvent for the said complex, at a temperature of between 10.degree. C. and the boiling point of the said solvent. The combination of iron and of an alkene carbonate may be formed by electrochemical reduction.Application of the catalyst system to the manufacture of aldehydes by hydroformylation of an organic compound containing ethylenic unsaturation, consisting in reacting the said organic compound with a mixture of carbon monoxide and hydrogen in the presence of an effective quantity of the said catalyst system, at a temperature of between 10.degree. and 300.degree. C. and at a pressure of between 10 and 350 bars.
    • 该催化剂体系的特征在于它包括:至少一种式LPtX2的铂络合物,其中L是含有能配位铂的至少两个磷原子的有机化合物,X是卤素原子,并且在铁 和烯烃碳酸酯,烯烃基团优选含有2至6个碳原子。 其制备方法的特征在于,在碳酸甲酯之间形成的至少一种组合与至少一种式LPtX2的铂络合物在所述络合物的至少一种溶剂中在10℃的温度下反应。 和所述溶剂的沸点。 铁和碳酸烯烃的组合可以通过电化学还原形成。 在有效量的所述催化剂体系的存在下,将所述有机化合物与一氧化碳和氢气的混合物反应,所述有机化合物含有烯属不饱和基团的加成甲酰化将所述催化剂体系应用于醛的制备中, 温度在10℃至300℃之间,压力在10至350巴之间。
    • 10. 发明授权
    • Catalysts and process for the preparation of catalysts which may be used
for the polymerization of ethylene
    • 用于制备可用于乙烯聚合的催化剂的催化剂和方法
    • US5492983A
    • 1996-02-20
    • US244679
    • 1994-06-07
    • Xavier OlondeKarel BujadouxAndre MortreuxFrancis Petit, deceased
    • Xavier OlondeKarel BujadouxAndre MortreuxFrancis Petit, deceased
    • C08F4/42C08F4/54C08F4/62C08F10/00C08F10/02C08F4/14
    • C08F10/02Y02P20/544
    • This catalyst consists of the reaction product, with at least one organomagnesium compound and/or organolithium compound R.sup.1 Li (R.sup.1 =alkyl) or ArLi (Ar=phenyl or benzyl), of the reaction product of (Cp).sub.2 MX.sub.2 Li(OR.sub.2).sub.2 (M=lanthanide, Sc, Y; (Cp)=optionally substituted cyclopentadienyl; and R=alkyl), with at least one bidentate ligand, such as .beta.-diketone or .beta.-keto imine CZ.sub.3 COCHZCDCZ.sub.3, Z selected from halogen, alkyl and H, D=O, NH or NR.sup.3 (R.sup.3 =alkyl or aryl); and phosphorus ylid R.sup.2.sub.3 P.dbd.CA--CO--R.sup.2, R.sup.2 chosen from alkyl and aryl; A=alkyl or H. It advantageously takes the form of a solution at least partially containing an aromatic hydrocarbon. The process for the polymerization of ethylene may be carried out at 20.degree.-250.degree. C. at a pressure which may range up to approximately 200 bars, in solution or in suspension in an at least C.sub.6 inert hydrocarbon or may be carried out continuously, in at least one autoclave or tubular reactor, at 150.degree.-300.degree. C., at 400-2000 bars, the reaction medium being in the supercritical state.
    • PCT No.PCT / FR93 / 00996 Sec。 371日期:1994年6月7日 102(e)日期1994年6月7日PCT提交1993年10月8日PCT公布。 第WO94 / 09044号公报 该催化剂由(Cp)的反应产物与至少一种有机镁化合物和/或有机锂化合物R1Li(R1 =烷基)或ArLi(Ar =苯基或苄基)组成, 具有至少一个二齿配位体,例如β-二酮或β-酮亚胺CZ 3 COCHZCDCZ 3,Z选自:(2)M 2镧(OR 2)2(M =镧系元素,Sc,Y;(Cp)=任选取代的环戊二烯基; R = 卤素,烷基和H,D = O,NH或NR 3(R 3 =烷基或芳基); 和磷叶立德R23P = CA-CO-R2,R2选自烷基和芳基; A =烷基或H.它有利地是至少部分含有芳族烃的溶液的形式。 乙烯聚合的方法可以在20-250℃下进行,压力范围可达200​​巴,溶液中或在至少C6惰性烃中的悬浮液中,或连续进行, 在至少一个高压釜或管式反应器中,在150-300℃,400-2000巴条件下,反应介质处于超临界状态。