Titanium-containing solution, catalyst for polyester preparation, process for preparation of polyester resin, and blow molded product comprising polyester
    2.
    发明申请
    Titanium-containing solution, catalyst for polyester preparation, process for preparation of polyester resin, and blow molded product comprising polyester 审中-公开
    含钛溶液,聚酯制备用催化剂,聚酯树脂的制造方法以及包含聚酯的吹塑成型体

    公开(公告)号:US20070100124A1

    公开(公告)日:2007-05-03

    申请号:US10560923

    申请日:2004-06-16

    IPC分类号: C08G63/00

    摘要: The present invention provides a titanium-containing solution having excellent storage stability and containing the titanium component at a high concentration; a catalyst for polyester preparation exhibiting excellent supply uniformity and high catalyst performance, which does not have adverse effect on the quality of the aliphatic diols to be recovered and recycled; and a catalyst for polyester preparation having high catalyst activity and high molding stability. The invention also provides a process for preparation of a polyester resin using the catalyst, and a blow molded product comprising the polyester resin. A first embodiment of the invention is a titanium-containing solution which contains titanium, an aliphatic diol and a polyhydric alcohol having a valency of 3 or greater. A second embodiment of the invention is a titanium-containing solution which has the titanium particle size in the solution within a specific range.

    摘要翻译: 本发明提供了具有优异的储存稳定性并且含有高浓度的钛成分的含钛溶液; 用于聚酯制备的催化剂,其表现出优异的供应均匀性和高催化剂性能,对待回收和再循环的脂族二醇的质量没有不利影响; 和具有高催化剂活性和高成型稳定性的聚酯制备用催化剂。 本发明还提供了使用该催化剂制备聚酯树脂的方法和包含聚酯树脂的吹塑制品。 本发明的第一个实施方案是含有钛,脂肪族二醇和三价以上的多元醇的含钛溶液。 本发明的第二个实施方案是一种含钛溶液,其溶液中的钛颗粒尺寸在特定范围内。

    Method for preparing acrolein or methacrolein
    3.
    发明授权
    Method for preparing acrolein or methacrolein 失效
    制备丙烯酸或甲基纤维素的方法

    公开(公告)号:US5144090A

    公开(公告)日:1992-09-01

    申请号:US711032

    申请日:1991-06-06

    摘要: A method for preparing acrolein or methacrolein comprises subjecting propylene, secondary propanol, isobutylene or tertiary butanol to gas phase catalytic oxidation with molecular oxygen in the presence of a catalyst represented by the following general formula (I):Mo.sub.a Bi.sub.b Fe.sub.c X.sub.d Y.sub.O Z.sub.f O.sub.g (I)wherein X represents at least one element selected from the group consisting of Ni and Co; Y represents at least one element selected from the group consisting of K, Rb, Cs and Tl; and Z represents at least one element selected from the group consisting of Be, Mg, Ca, Sr, Ba, Ce, Ti, Zr, Nb, Cr, W, Mn, Cu, Ag, Zn, Cd, B, Al, Si, Ge, Sn, Pb, P, As, Sb, S, Se and Te; a, b, c, d, e, f and g each represents an atomic ratio of the corresponding element and when a is assumed to be 12, b=0.1.about.10, c=0.1.about.20, d=2.about.20, e=0.01.about.2, f=0.about.4 and g represents the number of oxygen atoms required for satisfying the valency requirement of the constituent elements, wherein the catalyst used is prepared by separately preparing solutions each of which contains the starting compound for the foregoing catalyst components, mixing these solutions within a short period of time, spray-drying the resulting mixture immediately after the mixing and then calcining the dried powder. A catalyst which further comprises 5 to 15% by weight of silica in addition to the foregoing composition is also used in the method. End products can be obtained in high conversion and selectivity through the use of the foregoing catalyst. Moreover, the catalyst is excellent in stability and has good reproducibility.