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    Distributed injection catalytic partial oxidation process and apparatus for producing synthesis gas
    2.
    发明授权
    Distributed injection catalytic partial oxidation process and apparatus for producing synthesis gas 失效
    分布式注入催化部分氧化工艺和生产合成气的设备

    公开(公告)号：US06267912B1

    公开(公告)日：2001-07-31

    申请号：US08845700

    申请日：1997-04-25

    申请人： Frank Hershkowitz ,  Harry W. Deckman ,  Robert P. Reynolds ,  Constantine P. Gonatas ,  John W. Fulton ,  Leonard Schoenman ,  Jack I. Ito ,  Leroy R. Clavenna

    发明人： Frank Hershkowitz ,  Harry W. Deckman ,  Robert P. Reynolds ,  Constantine P. Gonatas ,  John W. Fulton ,  Leonard Schoenman ,  Jack I. Ito ,  Leroy R. Clavenna

    IPC分类号： C07C102

    CPC分类号： C01B3/386 ,  B01F3/02 ,  B01F5/0682 ,  B01J8/0278 ,  C01B2203/0261 ,  C01B2203/062 ,  C01B2203/065 ,  C01B2203/085 ,  C01B2203/1023 ,  C01B2203/1052 ,  C01B2203/1064 ,  C01B2203/1241 ,  C01B2203/1276

    摘要： A novel injector/reactor apparatus and an efficient process for the partial oxidation of light hydrocarbon gases, such as methane, to convert such gases to useful synthesis gas for recovery and/or subsequent hydrocarbon synthesis. Sources of a light hydrocarbon gas, such as methane, and oxygen or an oxygen-containing gas are preheated and pressurized and injected through an injector means at high velocity into admixture with each other in the desired relative proportions, at a plurality of mixing nozzles which are open to the catalytic partial oxidation reaction zone and are uniformly-spaced over the face of the injector means, to form a reactant gaseous premix having a pressure drop equal to at least about 3% of the lowest upstream pressure of either of said gases. The gaseous premix is injected in a time period which is less than its autoignition time, preferably less than 9 milliseconds, at a velocity between about 25 to 1000 feet/second, into a catalytic partial oxidation zone so that the gaseous premix reacts in the presence of the fixed catalyst to reduce the amounts of CO2, H2O and heat produced by the partial oxidation reaction, to form a useful syngas which is cooled and recovered.

    摘要翻译： 一种新颖的注射器/反应器装置以及用于部分氧化轻质烃气体（例如甲烷）的有效方法，以将这种气体转化成有用的合成气以用于回收和/或随后的烃合成。 来自诸如甲烷和氧气或含氧气体的轻质烃气体在多个混合喷嘴处被预热和加压并通过喷射器装置以高速度以所需的相对比例彼此混合， 对催化部分氧化反应区开放，并且在喷射器装置的表面上均匀间隔开，形成具有等于任一气体的最低上压压力的至少约3％的压降的反应物气态预混物。 将气体预混物在小于其自燃时间（优选小于9毫秒）的时间内以约25至1000英尺/秒的速度注入到催化部分氧化区中，使得气态预混物在存在下反应 的固定催化剂以减少CO 2，H 2 O的量和由部分氧化反应产生的热量，以形成冷却和回收的有用的合成气。

    Direct hydroformylation of a multi-component synthesis gas containing carbon monoxide, hydrogen, ethylene, and acetylene
    10.
    发明授权
    Direct hydroformylation of a multi-component synthesis gas containing carbon monoxide, hydrogen, ethylene, and acetylene 失效
    含有一氧化碳，氢气，乙烯和乙炔的多组分合成气的直接加氢甲酰化

    公开(公告)号：US5675041A

    公开(公告)日：1997-10-07

    申请号：US573052

    申请日：1995-12-15

    申请人： Gabor Kiss ,  Frank Hershkowitz ,  Harry W. Deckman ,  Michael Gerard Matturro ,  Istvan T. Horvath ,  Anthony M. Dean ,  Raymond A. Cook

    发明人： Gabor Kiss ,  Frank Hershkowitz ,  Harry W. Deckman ,  Michael Gerard Matturro ,  Istvan T. Horvath ,  Anthony M. Dean ,  Raymond A. Cook

    IPC分类号： C07C45/50

    CPC分类号： C07C45/50 ,  Y02P20/582

    摘要： The invention is a process for production of C.sub.3 to C.sub.6 aldehydes by hydroformylating a mixture containing: (a) C.sub.2 to C.sub.5 olefins and mixtures thereof, and (b) (i) C.sub.2 to C.sub.5 alkynes and mixtures thereof or (ii) C.sub.3 to C.sub.5 cumulated dienes and mixtures thereof or (iii) mixtures of (i) and (ii), with CO, H.sub.2 and a solution of a rhodium complex catalyst produced by complexing Rh and an organophosphorus compound at a concentration of Rh in solution from 1 to 1000 ppm by weight. Alternatively, the solution of rhodium complex catalyst can have a P/Rh atom ratio of at least 30. Alternatively, the solution of rhodium complex catalyst can have a P/Rh atom ratio greater than the value R.sub.L defined by the formula: ##EQU1## in which R.sub.B is the P/Rh ratio sufficient for a catalytically active Rh complex, pKa.sub.TPP is the pKa value for triphenylphosphine, pKa.sub.L is the pKa value for the triorganophosphorus compound, R is the gas constant, and .DELTA.S.sub.B is 35(N-1) cal/mole/.degree.K., N is the number of P-Rh attachments per ligand molecule. The process has utility for the hydroformylation of streams that contain olefins and alkynes.

    摘要翻译： 本发明是通过加氢甲酰化含有：（a）C 2〜C 5烯烃及其混合物的混合物，和（b）（ⅰ）C2〜C5炔烃及其混合物或（ⅱ）C3〜C5 累积的二烯及其混合物，或（iii）（ⅰ）和（ⅱ）的混合物与CO，H 2和铑络合物催化剂的溶液形成，所述铑配合物催化剂是通过使Rh和溶液中Rh浓度为1〜1000的有机磷化合物 重量ppm。 或者，铑络合物催化剂的溶液的P / Rh原子比可以至少为30.另外，铑络合物催化剂的溶液可以具有大于由下式定义的值RL的P / Rh原子比： 其中RB是催化活性Rh配合物的P / Rh比，pKaTPP是三苯基膦的pKa值，pKaL是三有机磷化合物的pKa值，R是气体常数，DELTA SB是35（N-1 ）cal / mole / DEGK，N是每个配体分子的P-Rh附着物的数目。 该方法可用于含有烯烃和炔烃的物流的加氢甲酰化。