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    • 1. 发明授权
    • Process or making 3-hydroxyaldehydes
    • 制备或制备3-羟基醛
    • US5344993A
    • 1994-09-06
    • US130258
    • 1993-10-01
    • Lynn H. SlaughJuan P. Arhancet
    • Lynn H. SlaughJuan P. Arhancet
    • C07C29/16C07C31/20C07C45/58C07C45/50C07C45/57
    • C07C45/58C07C29/16C07C31/20
    • This invention relates to a process for making 3-hydroxyaldehydes having 4 or more carbon atoms by intimately contacting(a) 1,2-epoxides having 3 or more carbon numbers,(b) ditertiary phosphine-modified cobalt carbonyl catalyst, said phosphine being a hydrocarbylene-bis(monophosphabicyclononane) in which each phosphorus atom is joined to hydrocarbylene and is a member of a bridge linkage without being a bridgehead atom and which hydrocarbylene-bis(monophosphabicyclononane) has 11 to 80 carbon atoms, 5 to 12 carbon atoms thereof together with a phosphorus atom being members of each of the two bicyclic skeletal structures,(c) carbon monoxide, and(d) hydrogen, the molar ratio of carbon monoxide to hydrogen being from about 4:1 to about 1:6, in liquid-phase solution in an inert reaction solvent, at a temperature of from about 30.degree. C. to about 150.degree. C. and a pressure of from about 50 psi to about 10,000 psi. Acids and promoter salts may be added to the reaction mixture to promote the hydroformylation reaction.
    • 本发明涉及一种通过紧密接触(a)具有3个或更多个碳数的1,2-环氧化物制备具有4个或更多个碳原子的3-羟基醛的方法,(b)二膦膦改性的羰基钴催化剂,所述膦是 其中每个磷原子连接到亚烃基并且不是桥头原子的桥连构件的亚烃基 - 双(单磷酰基二环壬烷),并且亚烃基 - 双(单磷杂二环壬烷)具有11至80个碳原子,5至12个碳原子在一起 其中磷原子是两个双环骨架结构中的每一个的成员,(c)一氧化碳和(d)氢,一氧化碳与氢的摩尔比为约4:1至约1:6, 在惰性反应溶剂中,在约30℃至约150℃的温度和约50psi至约10,000psi的压力下进行。 可以向反应混合物中加入酸和促进剂盐以促进加氢甲酰化反应。
    • 3. 发明授权
    • Process for preparing 1,3-propanediol
    • 1,3-丙二醇制备方法
    • US5463144A
    • 1995-10-31
    • US316671
    • 1994-09-30
    • Joseph B. PowellLynn H. SlaughThomas C. ForschnerTerry B. ThomasonThomas C. SemplePaul R. WeiderJuan P. Arhancet
    • Joseph B. PowellLynn H. SlaughThomas C. ForschnerTerry B. ThomasonThomas C. SemplePaul R. WeiderJuan P. Arhancet
    • C07C29/141C07C29/16C07C45/58C07C45/80C07C27/20C07C45/49C07C47/17
    • C07C45/58C07C29/141C07C29/16C07C45/80
    • 1,3-propanediol is prepared in a process comprising the steps of:contacting ethylene oxide with carbon monoxide and hydrogen in an essentially non-water-miscible solvent in the presence of an effective amount of a non-phosphine-ligated cobalt catalyst and an effective amount of a lipophilic quaternary ammonium salt at a temperature within the range of about 50.degree. to about 100.degree. C. and a, pressure within the range of about 500 to about 5000 psig, under reaction conditions effective to produce an intermediate product mixture comprising less than 15 wt % 3-hydroxypropanal;adding an aqueous liquid to said intermediate product mixture and extracting into said aqueous liquid at a temperature less than about 100.degree. C. a major portion of the 3-hydroxypropanal so as to provide an aqueous phase comprising 3-hydroxypropanal in greater concentration than the-concentration of 3-hydroxypropanal in said intermediate product mixture and an organic phase comprising at least a portion of the cobalt catalyst or a cobalt-containing derivative thereof and at least a portion of the lipophilic quaternary ammonium salt;contacting the aqueous phase comprising 3-hydroxypropanal with hydrogen in, the presence of a hydrogenation catalyst at a pressure of at least about 100 psig and a temperature during at least a portion of the hydrogenation step of at least 40.degree. C. to provide a hydrogenation product mixture comprising 1,3-propanediol.
    • 以包括以下步骤的方法制备1,3-丙二醇:在有效量的非磷化氢连接的钴催化剂存在下,将环氧乙烷与一氧化碳和氢气在基本上不与水相混溶的溶剂中接触, 在有效量的亲油性季铵盐的温度范围为约50至约100℃,和a,压力范围为约500至约5000psig,在有效产生中间产物混合物的反应条件下,包括 小于15重量%的3-羟基丙醛; 向所述中间产物混合物中加入水性液体,并在低于约100℃的温度下将3-羟基丙醛的主要部分萃取到所述含水液体中,以提供包含比所述中间产物混合物更高浓度的3-羟基丙醛的水相, 所述中间产物混合物中的3-羟基丙醛的浓度和包含至少一部分钴催化剂或其含钴衍生物和至少一部分亲脂性季铵盐的有机相; 在氢化催化剂存在下,在至少约100psig的压力和在至少40℃的至少一部分氢化步骤期间的温度下使包含3-羟基丙醛的水相与氢接触以提供氢化 产物混合物包含1,3-丙二醇。
    • 4. 发明授权
    • Process for making 3-hydroxypropanal and 1,3-propanediol
    • 制备3-羟基丙醛和1,3-丙二醇的方法
    • US5304686A
    • 1994-04-19
    • US91107
    • 1993-07-13
    • Lynn H. SlaughJuan P. Arhancet
    • Lynn H. SlaughJuan P. Arhancet
    • C07C29/16C07C31/20C07C45/58C07C47/19
    • C07C31/20C07C29/141C07C45/58
    • This invention relates to a process for making 3-hydroxypropanal by intimately contacting(a) ethylene oxide,(b) ditertiary phosphine-modified cobalt carbonyl catalyst, said phosphine being a hydrocarbylene-bis(monophosphabicyclononane) in which each phosphorus atom is joined to hydrocarbylene and is a member of a bridge linkage without being a bridgehead atom and which hydrocarbylene-bis(monophosphabicyclononane) has 18 to 50 carbon atoms, 8 carbon atoms thereof together with a phosphorus atom being members of each of the two bicyclic skeletal structures,(c) a catalyst promoter comprising an acid and a metal salt promoter selected from a salt of a metal of Group IIA, Group IIB, Group IIIB and the Rare Earth Series of the Periodic Table of the Elements (CAS version),(d) carbon monoxide, and(e) hydrogen, the molar ratio of carbon monoxide to hydrogen being from about 4:1 to about 1:6,in liquid-phase solution in an inert reaction solvent, at a temperature of from about 30.degree. C. to about 150.degree. C. and a pressure of from about 50 psi to about 10,000 psi. The use of the acid/metal salt promoter enhances the activity of the catalyst.
    • 本发明涉及一种通过使(a)环氧乙烷紧密接触来制备3-羟基丙醛的方法,(b)二膦膦改性的羰基钴催化剂,所述膦是其中每个磷原子连接到亚烃基的亚烃基 - 二(单磷酰基二环壬烷) 并且是桥联原子的成员,而不是桥头原子,并且亚烃基 - 双(单磷杂二环壬烷)具有18至50个碳原子,其8个碳原子和作为两个双环骨架结构中的每一个的成员的磷原子(c )催化剂促进剂,其包含酸和选自IIA族,IIB族,IIIB族的金属和元素周期表的稀土系列(CAS版)的金属盐助催化剂,(d)一氧化碳 ,和(e)氢气,一氧化碳与氢的摩尔比约为4:1至约1:6,在惰性反应溶剂中的液相溶液中,温度为约30℃。 至约150℃和约50psi至约10,000psi的压力。 酸/金属盐助催化剂的使用增强了催化剂的活性。
    • 7. 发明授权
    • Hydrogenation catalyst and hydrogenation process wherein said catalyst
is used
    • 氢化催化剂和氢化方法,其中使用所述催化剂
    • US5057582A
    • 1991-10-15
    • US289158
    • 1988-12-23
    • Ronald J. HoxmeierLynn H. Slaugh
    • Ronald J. HoxmeierLynn H. Slaugh
    • B01J31/04B01J31/14C08C19/02C08F8/04
    • C08F8/04B01J31/0225B01J31/04B01J31/143B01J31/2234C08C19/02B01J2231/645B01J2531/845B01J2531/847
    • A hydrogenation catalyst prepared by combining a Group VIIIA metal compound and an alkylalumoxane and a hydrogenation process wherein said catalyst is used to hydrogenate compounds or materials containing ethylenic and/or aromatic unsaturation. The Group VIIIA metal compound is selected from the group of compounds consisting of carboxylates, chelates, alkoxides, salts of acids containing sulfur, salts of partial half esters of acids containing sulfur and salts of aliphatic and aromatic sulfonic acids. Nickel and cobalt compounds are preferred for use in preparing the hydrogenation catalyst. Hydrogenation catalysts prepared with methylalumoxane initially exhibit less hydrogenation activity than catalysts known heretofore in the prior art and prepared with a metal alkyl of a metal selected from Groups I, II and III. These catalysts, then, permit or enable greater control over the extent of hydrogenation, particularly when partial hydrogenation is a desired end result. Ultimately, however, the catalyst permits substantially complete hydrogenation of both ethylenic and aromatic unsaturation. Hydrogenation catalysts prepared with higher alkyl (C.sub.2 -C.sub.8) alumoxanes on the other hand are generally more active at all hydrogenation times at least those greater than about 30 minutes.
    • 通过组合ⅦA族金属化合物和烷基铝氧烷制备的氢化催化剂和氢化方法,其中所述催化剂用于氢化含有烯属和/或芳族不饱和度的化合物或材料。 VIIIA族金属化合物选自羧酸盐,螯合物,醇盐,含硫酸盐,含硫酸的部分半酯盐和脂族和芳族磺酸盐组成的化合物。 镍和钴化合物优选用于制备氢化催化剂。 用甲基铝氧烷制备的氢化催化剂最初显示出比现有技术中已知的催化剂更少的氢化活性,并用选自I,II和III族的金属的金属烷基制备。 然后,这些催化剂允许或可以更好地控制氢化的程度,特别是当部分氢化是期望的最终结果时。 然而,最终催化剂允许乙烯和芳族不饱和基团完全氢化。 另一方面,由高级烷基(C 2 -C 8)铝氧烷制备的氢化催化剂在所有氢化时间通常在大于约30分钟的时间内更具活性。