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    • 5. 发明授权
    • Process for producing methyl lactate
    • 生产乳酸甲酯的方法
    • US4500727A
    • 1985-02-19
    • US359414
    • 1982-03-18
    • Takanori KitamuraMitsuo MatsumotoMasuhiko Tamura
    • Takanori KitamuraMitsuo MatsumotoMasuhiko Tamura
    • C07C67/03C07C69/14C07C69/24C07C69/68
    • C07C67/293C07C67/03C07C67/29C07C67/30Y02P20/584
    • A process for producing methyl lactate by (I) hydroformylating vinyl acetate or vinyl propionate with a gaseous mixture of hydrogen and carbon monoxide in an organic solvent in the presence of a substantially water-insoluble rhodium complex and a tri-substituted phosphine to form .alpha.-acetoxy- or propionyloxy-propionaldehyde, (II) subjecting at least part of the reaction mixture obtained in step (I) to extraction with an aqueous medium to obtain an aqueous layer containing .alpha.-acetoxy- or propionyloxy-propionaldehyde and an extraction residue containing the catalyst components, and recycling the extraction residue to the hydroformylation step (I), (III) separating .alpha.-acetoxy- or propionyloxy-propionaldehyde from the aqueous layer containing the same as obtained in step (II), (IV) oxidizing .alpha.-acetoxy- or propionyloxy-propionaldehyde obtained in step (III) in the liquid phase with oxygen gas or an oxygen-containing gas in the presence of an oxidation catalyst to form .alpha.-acetoxy- or propionyloxy-propionic acid, and (V) reacting .alpha.-acetoxy- or propionyloxy-propionic acid obtained in step (IV) with methanol in the presence of an acid catalyst, and recovering the resultant methyl lactate by distillation.
    • (I)在有机溶剂中,在基本上不溶于水的铑络合物和三取代的膦存在下,通过(I)在氢气和一氧化碳的气体混合物中将乙酸乙烯酯或丙酸乙烯酯加氢甲酰化以生产甲酸乳酸的方法, 乙酰氧基 - 或丙酰氧基 - 丙醛,(II)使步骤(I)中获得的反应混合物的至少一部分用水性介质萃取,得到含有α-乙酰氧基或丙酰氧基丙醛的水层和含有 催化剂组分,并将提取残余物循环到加氢甲酰化步骤(I)中,(III)从含有与步骤(II)中获得的相同的水层分离α-乙酰氧基或丙酰氧基丙醛,(IV)氧化α-乙酰氧基 - 或步骤(III)中获得的丙酰氧基 - 丙醛在氧气或含氧气体的液相中,在氧化催化剂存在下形成α - 乙酰氧基 - 或丙酰氧基 - 丙酸,和(V)使在步骤(IV)中获得的α-乙酰氧基 - 或丙酰氧基 - 丙酸与甲醇在酸催化剂存在下反应,并通过蒸馏回收得到的乳酸甲酯。
    • 8. 发明授权
    • Hydroformylation of olefinic compounds
    • 烯烃化合物的加氢甲酰化
    • US4238419A
    • 1980-12-09
    • US45301
    • 1979-06-04
    • Mitsuo MatsumotoMasuhiko Tamura
    • Mitsuo MatsumotoMasuhiko Tamura
    • C07C45/49C07C45/50C07D309/10
    • C07D309/10C07C45/49C07C45/50Y02P20/584
    • Rhodium catalyzed hydroformylation of olefinic compounds is essentially effected in the presence of a secondary phosphine oxide of the general formula (I) in an amount of at least one mole per gram atom of rhodium, which supresses the thermal degradation of the rhodium catalyst in the hydroformylation stage as well as in the distillation of the reaction products: ##STR1## wherein, in the formula (I), R.sup.1 and R.sup.2 are the same or different, substituted or unsubstituted hydrocarbon residues containing not more than 20 carbon atoms.The phosphine oxide of the general formula (I) maintains the catalytic activity over a prolonged period of time and prevents essentially metallic rhodium from sticking to the vessel during distillation of the reaction products from the reaction mixture, and consequently makes recycle of the catalyst easier and enables lowering the hydroformylation pressure.
    • 烯属化合物的铑催化加氢甲酰化基本上是在通式(I)的次膦氧化物存在下,以每克原子铑至少1摩尔的量存在,这抑制了加氢甲酰基化中铑催化剂的热降解 阶段以及反应产物的蒸馏:其中在式(I)中,R 1和R 2是相同或不同的含有不超过20个碳原子的取代或未取代的烃基。 通式(I)的氧化膦在延长的时间内维持催化活性,并且在从反应混合物中蒸馏反应产物期间防止基本上金属铑粘附到容器上,因此使催化剂的再循环更容易, 可以降低加氢甲酰化压力。