Production of isoprene dimers
    83.
    发明授权
    Production of isoprene dimers 失效
    异丙二烯的生产

    公开(公告)号:US3696108A

    公开(公告)日:1972-10-03

    申请号:US3696108D

    申请日:1970-11-23

    发明人: MORIKAWA HIROYUKI

    摘要: Isoprene is dimerized by being caused to contact a catalyst which is a combination of: (I) a titanium compound (e.g., titanium tetrachloride); (II) a phosphorus or antimony compound constituting an electron-donor compound (e.g., triphenyl phosphite); and (III) an aluminum compound (e.g., diethylaluminum chloride). Titanium compound (I) is representable by the general formula TiXnY4 n or TiOX2, where each of X and Y is a halogen, an OR'''' group, an acetyl-acetonato group, or a chlorosulfonyl group, and n is an integer of 1 to 4, both inclusive. Phosphorous or antimony compound (II) is representable by the general formuls P(OR)3, PO(OR)3, or Sb(OR)3. Aluminum compound (III) is representable by the general formulas AIR''2Cl or Al2R''3Cl3. Each of R, R'', and R'''' is an alkyl, cycloalkyl, alkenyl, or aryl group.

    摘要翻译: 异戊二烯通过与以下组合的催化剂接触而被二聚化:(I)钛化合物(例如四氯化钛); (II)构成电子给体化合物的磷或锑化合物(例如亚磷酸三苯酯); 和(III)铝化合物(例如二乙基氯化铝)。 钛化合物(I)可以由通式TiXnY4-n或TiOX2表示,其中X和Y各自为卤素,OR“基团,乙酰基 - 丙酮酸基或氯磺酰基,n为 1到4,包括在内。 磷或锑化合物(II)可以由一般的结构式P(OR)3,PO(OR)3或Sb(OR)3表示)。 铝化合物(III)可以由通式AIR'2Cl或Al2R'3Cl3表示。 R,R'和R“中的每一个是烷基,环烷基,烯基或芳基。

    PROCESS FOR PRODUCING ALDEHYDES
    88.
    发明申请

    公开(公告)号:US20180305285A1

    公开(公告)日:2018-10-25

    申请号:US15768397

    申请日:2016-10-27

    摘要: The present invention relates generally to processes for producing aldehydes wherein an olefinic compound, carbon monoxide, and hydrogen are reacted in the presence of a solubilized rhodium-phosphorous complex. In one embodiment, the process comprises (a) receiving a vaporized aldehyde product stream downstream from a hydroformylation reactor, the vaporized aldehyde product stream comprising aldehydes, phosphorous ligand, and aldehyde condensation by-products; (b) contacting the vaporized aldehyde product stream with a partial condenser so as to condense the phosphorous ligand and the by-products, wherein up to 10 weight percent of the vaporized stream is condensed; (c) removing the condensed phosphorous ligand and the condensed by-products from the liquid condensation stream using a refining column; and (d) further processing the vaporized aldehydes from the separate refining column.