Process for production of alkanesulfonic acid
    2.
    发明申请
    Process for production of alkanesulfonic acid 失效
    烷基磺酸的生产工艺

    公开(公告)号:US20040186316A1

    公开(公告)日:2004-09-23

    申请号:US10393403

    申请日:2003-03-20

    IPC分类号: C07C39/02

    CPC分类号: C07C303/16 C07C309/04

    摘要: The present invention relates to a process for the production of alkanesulfonic acid. More particularly, the present invention relates to a process for the production of alkanesulfonic acid from alkyl mercaptan effluents generated in chemical industries. The process of the invention comprises the oxidation of the entire alkyl mercaptan generated as an effluent in the chemical industries to serve two concomitant purposes: (1) complete removal of obnoxious odour, and (2) value addition by the production of alkanesulfonic acids selectively in quantitative yields.

    摘要翻译: 本发明涉及一种生产烷烃磺酸的方法。 更具体地说,本发明涉及由化学工业中生成的烷基硫醇废水生产烷基磺酸的方法。 本发明的方法包括在化学工业中作为流出物生成的整个烷基硫醇的氧化,用于两个伴随的目的:(1)完全除去令人讨厌的气味,和(2)通过选择性地生产烷烃磺酸的价值添加 定量收益率。

    Optically active chiral diphosphine ligands

    公开(公告)号:US20030195369A1

    公开(公告)日:2003-10-16

    申请号:US10356233

    申请日:2003-01-31

    申请人: PPG-SIPSY

    摘要: A (R) or (S) chiral diphosphine of formula (I): 1 wherein R and R1, which can be identical or different, represent an optionally saturated C1-10 alkyl group, an optionally saturated C3-9 cycloalkyl group, a C5-10 aryl group, the groups being optionally substituted by a halogen, a hydroxy, a C1-5 alkoxy, an amino such as NH2, NHR4, N(R4)2, a sulfino, a sulonfyl, with R4 representing an alkyl, an alkoxy or an alkylcarbonyl, the alkyl, cycloalkyl, aryl groups optionally comprising one or more heteroatoms, or R and R1 together represent an optionally saturated C2-6 substituted alkyl group, an optionally saturated C3-9 cycloalkyl group, a C5-10 aryl group, the cycloalkyl or aryl groups being optionally substituted by a C1-5 alkyl, a halogen, a hydroxy, a C1-5 alkoxy, an amino, a sulfino, a sulonfyl, with R4 representing an alkyl, an alkoxy or an alkylcarbonyl, the alkyl, cycloalkyl, aryl groups optionally comprising one or more heteroatoms, R2 and R3, which can be identical or different, represent an optionally saturated C3-8 cycloalkyl group, a C6-10 aryl group, the groups being optionally substituted by a halogen, a hydroxy, a C1-5 alkoxy, an amino, a sulfino, a sulonfyl, with R4 representing an alkyl, an alkoxy or an alkylcarbonyl, the cycloalkyl, aryl groups optionally comprising one or more heteroatoms, or R2 and R3 together form an optionally saturated C4-8 cyclic group, a C6-10 aryl group, the groups being optionally substituted

    Method of extractive separation of diaryl carbonates and the original
aromatic hydroxy compounds from reaction solutions
    4.
    发明授权
    Method of extractive separation of diaryl carbonates and the original aromatic hydroxy compounds from reaction solutions 失效
    从反应溶液中萃取分离碳酸二芳基酯和原始芳族羟基化合物的方法

    公开(公告)号:US5712406A

    公开(公告)日:1998-01-27

    申请号:US794435

    申请日:1997-02-05

    CPC分类号: C07C68/08 C07C68/005

    摘要: Diaryl carbonate and an aromatic hydroxy compound are simultaneously separated from a crude reaction mixture for producing diaryl carbonates by oxidative carbonylation of the aromatic hydroxy compound and containing the diaryl carbonate and excess hydroxy compound together with the catalyst system, consisting of a noble-metal catalyst, co-catalyst, quaternary salt and a base. The crude reaction mixture is mixed with a covalent aprotic extraction agent, a phase separation is carried out into a donor phase containing the catalyst system and a recipient phase containing the diaryl carbonate and the hydroxy compound in concentrated form, and the diaryl carbonate and the hydroxy compound are isolated from the recipient phase.

    摘要翻译: 碳酸二芳酯和芳族羟基化合物同时从用于通过芳族羟基化合物的氧化羰基化产生碳酸二芳基酯的粗制反应混合物中分离,并含有碳酸二芳基酯和过量的羟基化合物以及由贵金属催化剂组成的催化剂体系, 助催化剂,季盐和碱。 将粗反应混合物与共价非质子提取剂混合,将相分离进入含有催化剂体系的供体相和含有碳酸二芳酯和浓缩形式的羟基化合物的接收相,碳酸二芳基酯和羟基 化合物从受体相分离。

    Process for continuous production of cumene and/or diisopropylbenzene
    7.
    发明授权
    Process for continuous production of cumene and/or diisopropylbenzene 失效
    连续生产枯烯和/或二异丙基苯的方法

    公开(公告)号:US4347393A

    公开(公告)日:1982-08-31

    申请号:US294204

    申请日:1981-08-19

    申请人: Hisaya Miki

    发明人: Hisaya Miki

    摘要: In a process for producing cumene and/or diisopropylbenzene which comprises, in combination,(I) an alkylating step,(II) a transalkylating step,(III) a catalyst separating step,(IV) a neutralization step, and(V) fractionally distilling step;characterized in that(a) step (I) is carried out at a temperature of about 40.degree. C. to about 85.degree. C. while maintaining the activity coefficient (M) of the catalyst at about 10.times.10.sup.-4 to about 300.times.10.sup.-4 and the concentration of aluminum chloride in the system at 0.005 to 0.15 mole/liter, and(b) step (II) is carried out without removing the catalyst from the reaction product of step (I) and at a temperature of about 40.degree. C. to about 75.degree. C. in the presence of added fresh aluminum chloride in an amount of 2 to 20 parts by weight/hr per 1000 parts by weight/hr of diisopropylbenzene in the reaction system while maintaining the activity coefficient (M) of the catalyst in the system at about 30.times.10.sup.-4 to about 300.times.10.sup.-4 and the concentration of aluminum chloride in the system at 0.3 to 1 mole/liter.

    摘要翻译: 在制备异丙苯和/或二异丙基苯的方法中,组合包括(I)烷基化步骤,(II)烷基转移步骤,(III)催化剂分离步骤,(IV)中和步骤和(V) 蒸馏步骤 其特征在于(a)步骤(I)在约40℃至约85℃的温度下进行,同时将催化剂的活性系数(M)保持在约10×10 -4至约300×10 -4, 系统中氯化铝的浓度为0.005〜0.15摩尔/升,(b)步骤(II)在不从步骤(I)的反应产物和约40℃的温度下除去催化剂的情况下进行。 在加入的新鲜氯化铝的存在下,在反应体系中每1000重量份/小时的二异丙基苯为2至20重量份/小时,同时保持催化剂的活性系数(M)至约75℃ 在系统中为约30×10 -4至约300×10 -4,系统中氯化铝的浓度为0.3至1摩尔/升。

    Process for the autoxidation of an isopropylphenyl ester
    8.
    发明授权
    Process for the autoxidation of an isopropylphenyl ester 失效
    异丙基苯基酯的自氧化方法

    公开(公告)号:US4164510A

    公开(公告)日:1979-08-14

    申请号:US879788

    申请日:1978-02-21

    申请人: Sheng-Hong A. Dai

    发明人: Sheng-Hong A. Dai

    摘要: Isopropylphenyl esters are converted to di- or trihydric phenols via a novel autoxidation of the esters at high conversion rates to the corresponding hydroperoxyisopropylphenyl esters in the presence of a catalyst combination comprising at least two members selected from the group consisting of (i) a metal phthalocyanine; (ii) a di-tertiary alkyl peroxide; and (iii) a tertiary alkyl hydroperoxide.Rearrangement of the hydroperoxyisopropylphenyl esters to the corresponding hydroxyphenyl esters and the hydrolysis of the latter compounds provides the phenols in overall yields (from the starting esters) heretofore not obtainable. Novel bis(hydroperoxyisopropylphenyl)carbonates are described which are attractive intermediates for the intermediate bisphenol carbonate or the final hydroquinone hydrolysis product.

    摘要翻译: 在包含至少两种选自(i)金属酞菁的组分的催化剂组合物存在下,通过将酯以高转化率的新型自氧化转化成相应的氢过氧化异丙基苯基酯,将异丙基苯基酯转化成二元或三元酚 ; (ii)二叔烷基过氧化物; 和(iii)叔烷基氢过氧化物。

    Process for splitting alkylaromatic hydroperoxides into phenolic
compounds
    9.
    发明授权
    Process for splitting alkylaromatic hydroperoxides into phenolic compounds 失效
    将烷基羟基氢氧化物分解成苯酚化合物的方法

    公开(公告)号:US3978141A

    公开(公告)日:1976-08-31

    申请号:US501434

    申请日:1974-08-28

    申请人: Michel Jouffret

    发明人: Michel Jouffret

    CPC分类号: C07C37/08

    摘要: Process for splitting primary alkylaromatic hydroperoxides to yield phenolic products is described which consists of reacting the hydroperoxide with a catalytic amount of a compound with an acid reaction, in an organic solvent medium, the characteristic feature being that the splitting medium is a mixture consisting of:A. at least one solvent chosen from the group of aprotic polar solvents formed by polymethylene-sulphones, alkylene glycol carbonates which contain 2 to 4 carbon atoms (in the alkylene portion) and aliphatic or aromatic nitriles, andB. at least one hydroxylic solvent taken from the group formed by aliphatic alcohols containing 1 to 3 carbon atoms and alkylene glycols containing up to 4 carbon atoms.