Method for inhibiting polymerization during the recovery and purification of unsaturated mononitriles
    1.
    发明授权
    Method for inhibiting polymerization during the recovery and purification of unsaturated mononitriles 失效
    在不饱和单腈回收和纯化期间抑制聚合的方法

    公开(公告)号:US06984749B2

    公开(公告)日:2006-01-10

    申请号:US10309962

    申请日:2002-12-04

    IPC分类号: C07C255/03

    摘要: Economical processes are disclosed for recovery and refining of valuable nitrogen-containing organic compounds formed by catalytic oxidation of least one feed compound selected from the group consisting of propane, propylene, isobutane and isobutylene in the presence of ammonia to produce a gaseous. Processes of the invention include quenching the gaseous reactor effluent with an aqueous quench liquid; forming an aqueous solution comprising the corresponding unsaturated mononitrile, hydrogen cyanide and other organic co-products; and using an integrated sequence of distillations and phase separations to recover for recycle of a useful aqueous liquid, and obtain the desired nitrogen-containing products. According to the invention aqueous solutions are fractionated in an integrated system of multi-stage columns while an effective polymerization inhibiting amount of at least one member of a preselected class of p-phenylenediamine compounds is maintained therein.

    摘要翻译: 公开了经济方法用于在氨的存在下通过催化氧化选自丙烷,丙烯,异丁烷和异丁烯的至少一种进料化合物形成的有价值的含氮有机化合物来回收和精炼以产生气体。 本发明的方法包括用水淬火液淬火气态反应器流出物; 形成包含相应的不饱和单腈,氰化氢和其它有机副产物的水溶液; 并使用一体化的蒸馏和相分离序列来回收有用的含水液体的再循环,并获得所需的含氮产物。 根据本发明,水溶液在多级柱的一体化系统中分级,同时保持有效聚合抑制量的至少一种预选类对苯二胺化合物。

    Preparation of ceramics
    3.
    发明授权
    Preparation of ceramics 失效
    陶瓷的制备

    公开(公告)号:US4608215A

    公开(公告)日:1986-08-26

    申请号:US565077

    申请日:1983-12-23

    IPC分类号: C01B33/22 C04B35/20 C04B35/14

    CPC分类号: C04B35/20 C01B33/22

    摘要: Ceramic materials comprising steatite or forsterite which are highly dense in nature may be prepared by admixing a hydrolyzed alcoholic solution of a silicon alkoxide with a solution prepared by adding an organomagnesium compound to an alcohol at gelation conditions. Following the formation of the gel, it is then dried at an elevated temperature of from about 300.degree. to about 500.degree. C. to remove volatile compounds as well as to decompose any remaining organic compounds and thereafter the powder is pressed into a desired shape. The formed shape is then sintered at a temperature in the range of from about 850.degree. to about 950.degree. C. to form a densified ceramic.

    摘要翻译: 包含高密度性质的滑石或镁橄榄石的陶瓷材料可以通过将硅醇盐的水解醇溶液与通过在凝胶化条件下向醇中加入有机镁化合物而制备的溶液混合来制备。 在形成凝胶之后,然后在约300℃至约500℃的高温下干燥以除去挥发性化合物以及分解任何剩余的有机化合物,然后将粉末压制成所需形状。 然后将形成的形状在约850℃至约950℃的温度下烧结以形成致密的陶瓷。

    Selective reduction of edible fats and oils
    4.
    发明授权
    Selective reduction of edible fats and oils 失效
    选择性还原食用油脂

    公开(公告)号:US4424163A

    公开(公告)日:1984-01-03

    申请号:US338736

    申请日:1982-01-11

    申请人: Bruce I. Rosen

    发明人: Bruce I. Rosen

    IPC分类号: C11C3/12

    CPC分类号: C11C3/123

    摘要: Selective reductions of fatty materials occur using a catalyst consisting of essentially of zerovalent nickel dispersed on a support which shows strong metal, support interaction. A particularly desirable catalyst is one where the nickel is dispersed on titania which is subsequently activated in hydrogen at a temperature above about 325.degree. C. The catalyst is sufficiently selective so as to permit continuous reduction of fatty material using a fixed bed of catalyst.

    摘要翻译: 脂肪物质的选择性还原使用分散在显示强金属,载体相互作用的载体上的基本上由零价镍组成的催化剂发生。 特别理想的催化剂是其中镍分散在二氧化钛上的催化剂,其随后在氢气中在约325℃以上的温度下活化。催化剂是充分选择性的,以便允许使用固定床催化剂连续还原脂肪材料。

    Method for inhibiting polymerization during the recovery and purification of unsaturated mononitriles
    5.
    发明授权
    Method for inhibiting polymerization during the recovery and purification of unsaturated mononitriles 失效
    在不饱和单腈回收和纯化期间抑制聚合的方法

    公开(公告)号:US07282600B2

    公开(公告)日:2007-10-16

    申请号:US10852277

    申请日:2004-05-24

    IPC分类号: C07C255/08

    摘要: Economical processes are disclosed for recovery and refining of valuable nitrogen-containing organic compounds formed by catalytic oxidation of least one feed compound selected from the group consisting of propane, propylene, isobutane and isobutylene in the presence of ammonia to produce a gaseous. Processes of the invention include quenching the gaseous reactor effluent with an aqueous quench liquid; forming an aqueous solution comprising the corresponding unsaturated mononitrile, hydrogen cyanide and other organic co-products; and using an integrated sequence of distillations and phase separations to recover for recycle of a useful aqueous liquid, and obtain the desired nitrogen-containing products. According to the invention aqueous solutions are fractionated in an integrated system of multi-stage columns while an effective polymerization inhibiting amount of at least one member of a preselected class of p-phenylenediamine compounds is maintained therein.

    摘要翻译: 公开了经济方法用于在氨的存在下通过催化氧化选自丙烷,丙烯,异丁烷和异丁烯的至少一种进料化合物形成的有价值的含氮有机化合物来回收和精炼以产生气体。 本发明的方法包括用水淬火液淬火气态反应器流出物; 形成包含相应的不饱和单腈,氰化氢和其它有机副产物的水溶液; 并使用一体化的蒸馏和相分离序列来回收有用的含水液体的再循环,并获得所需的含氮产物。 根据本发明,水溶液在多级柱的一体化系统中分级,同时保持有效聚合抑制量的至少一种预选类对苯二胺化合物。

    Process for recovery of aromatic acid and dihydric alcohol from waste
polyester resins
    8.
    发明授权
    Process for recovery of aromatic acid and dihydric alcohol from waste polyester resins 失效
    从废聚酯树脂中回收芳香酸和二元醇的方法

    公开(公告)号:US5473102A

    公开(公告)日:1995-12-05

    申请号:US318228

    申请日:1994-10-05

    IPC分类号: C07C51/09 C07C67/60

    CPC分类号: C07C51/09

    摘要: Processes are disclosed for recovery and purification of dibasic aromatic acids from waste polyester film, fiber, bottles, manufacturing residues, and other manufactured articles. The processes comprises: depolymerization of polyester resin in a molten polyester resin containing solvent with superheated stem, and vaporization of the aromatic carboxylic acid and other volatile products of hydrolysis to obtain a vaporized mixture containing aromatic acid, dihydric alcohol, other volatile products of hydrolysis, and water. This vapor mixture is, advantageously, substantially free of less volatile and non-volatile impurities including metals, and many colored and color causing compounds, which are, typically, found in post-consumer polyester resins.Crude acid is, optionally, purified by hydrogenated in an aqueous solution at elevated temperatures and pressures in the presence of hydrogen and an insoluble metal-containing catalyst, which is thereupon separated from the aqueous solution, and purified dibasic aromatic acid recovered by crystallization and mechanical separation from the aqueous solution. Purified terephthalic acid has, typically, a L*-value in a rage of from about 95 to about 100, an a*-value in a rage of from about -1 to about +1, and a b*-value in a range of from about 0.5 to about 2.

    摘要翻译: 公开了用于从废聚酯膜,纤维,瓶,制造残余物和其它制品中回收和纯化二元芳香酸的方法。 该方法包括:将聚酯树脂在含有过热干燥的溶剂的熔融聚酯树脂中解聚,并将芳族羧酸和其它挥发性水解产物汽化,得到含有芳族酸,二元醇,水解的其它挥发性产物的蒸发混合物, 和水。 这种蒸气混合物有利地基本上不含挥发性和非挥发性的杂质,包括金属,以及通常在消费后聚酯树脂中发现的许多着色和着色的化合物。 任选地,在氢气和不溶性金属的催化剂存在下,在高温和高压下,在水溶液中氢化,然后与水溶液分离,纯化纯酸,通过结晶和机械回收的纯化的二元芳香酸 与水溶液分离。 纯化的对苯二甲酸通常具有约95至约100的浓度的L *值,在约-1至约+1的范围内的a *值和在一定范围内的ab * 约0.5至约2。

    Process for recovery of aromatic acid from waste polyester resin
    9.
    发明授权
    Process for recovery of aromatic acid from waste polyester resin 失效
    从废聚酯树脂中回收芳香酸的方法

    公开(公告)号:US5414113A

    公开(公告)日:1995-05-09

    申请号:US138917

    申请日:1993-10-18

    IPC分类号: C07C51/09 C07C51/16

    CPC分类号: C07C51/09

    摘要: Processes are disclosed for recovery and purification of dibasic aromatic acids from waste polyester film, fiber, bottles, manufacturing residues, and other manufactured articles. The processes comprises: depolymerizing polyester resin in a solvent under conditions suitable for hydrolysis of ester bonds to obtain a mixture containing a solution of aromatic acid and impurities consisting of alcohol and/or other components of the resin; burning impurities in a liquid-phase oxidation with an oxygen-containing gas in the presence of an oxidation catalyst at elevated pressures and temperatures, to obtain an oxidation product containing the desired aromatic acid; and crystallizing and separating from the oxidation system a resulting crude dibasic aromatic acid. Crude acid is, optionally, hydrogenated in an aqueous solution at elevated temperatures and pressures in the presence of hydrogen and an insoluble metal-containing catalyst, which is thereupon separated from the aqueous solution, and purified dibasic aromatic acid recovered by crystallization and mechanical separation from the aqueous solution. Purified terephthalic acid has, typically, a L*-value in a range of from about 95 to about 100, an a*-value in a range of from about -1 to about +1, and a b*-value in a range of from about 0.5 to about 2.

    摘要翻译: 公开了用于从废聚酯膜,纤维,瓶,制造残余物和其它制品中回收和纯化二元芳香酸的方法。 该方法包括:在适于水解酯键的条件下,在溶剂中解聚聚酯树脂,得到含有芳族酸溶液和由醇和/或树脂的其它组分组成的杂质的混合物; 在氧化催化剂存在下,在升高的压力和温度下,用含氧气体进行液相氧化中的杂质,得到含有所需芳香酸的氧化产物; 并从氧化体系中结晶并分离得到的粗二元芳香酸。 任选地,在氢气和不溶性金属的催化剂存在下,在高温和高压下,在水溶液中氢化粗酸,随后将其与水溶液分离,通过结晶和机械分离回收的纯化的二元芳香酸 水溶液。 纯化的对苯二甲酸通常具有在约95至约100的范围内的L *值,在约-1至约+1的范围内的a *值和在 约0.5至约2。