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140 条记录 (耗时 0.025 秒)

    Methanol manufacture using pressure swing reforming
    31.
    发明授权
    Methanol manufacture using pressure swing reforming 有权
    使用压力挥发重整的甲醇制造

    公开(公告)号：US07148261B2

    公开(公告)日：2006-12-12

    申请号：US11011984

    申请日：2004-12-14

    申请人： Frank Hershkowitz ,  James R. Lattner

    发明人： Frank Hershkowitz ,  James R. Lattner

    IPC分类号： C07C27/00 ,  C07C1/00

    CPC分类号： C07C29/1518 ,  Y02P30/42 ,  C07C31/04 ,  C07C31/08 ,  C07C31/10 ,  C07C31/02

    摘要： A process for producing methanol is described in which a hydrocarbon is steam reformed in a reforming zone, and during the reforming stage, of a cyclic steam reformer having a reforming stage and a regeneration stage, the steam reforming being conducted under conditions effective to produce a first effluent stream containing synthesis gas. Fuel and an oxygen-containing gas are combusted in the regeneration stage of the reformer so as to reheat the reforming zone to a temperature sufficient for the reforming stage and generate a flue gas. At least part of the first effluent stream is contacted with a methanol synthesis catalyst under conditions effective to convert synthesis gas to methanol and form a methanol-containing stream and a tail gas stream comprising unreacted carbon monoxide and hydrogen. At least part of the tail gas stream is recycled as fuel for the regeneration stage of the cyclic steam reformer.

    摘要翻译： 描述了一种生产甲醇的方法，其中烃在重整区中进行蒸汽重整，并且在重整阶段期间，在具有重整阶段和再生阶段的循环蒸汽重整器中，蒸汽重整在有效产生 含有合成气的第一流出物流。 燃料和含氧气体在重整器的再生阶段中燃烧，以便将重整区再加热到足以进行重整阶段的温度并产生烟道气。 在有效地将合成气转化成甲醇并形成含甲醇流和包含未反应的一氧化碳和氢气的尾气流的条件下，将至少部分第一流出物流与甲醇合成催化剂接触。 至少部分尾气流作为循环蒸汽重整器的再生阶段的燃料再循环。

    Oxygenate to olefin process
    32.
    发明授权
    Oxygenate to olefin process 有权
    氧化烯到烯烃工艺

    公开(公告)号：US06965057B2

    公开(公告)日：2005-11-15

    申请号：US10807818

    申请日：2004-03-24

    申请人： James H. Beech, Jr. ,  Cor F. Van Egmond ,  Teng Xu ,  James R. Lattner

    发明人： James H. Beech, Jr. ,  Cor F. Van Egmond ,  Teng Xu ,  James R. Lattner

    IPC分类号： B01J20/34 ,  B01J38/30 ,  B01J38/32 ,  C07C1/00 ,  C07C1/20 ,  C07C1/207 ,  C10G3/00

    CPC分类号： C07C1/20 ,  B01J38/30 ,  B01J38/32 ,  C10G3/49 ,  C10G3/62 ,  C10G2300/4093 ,  C10G2300/708 ,  C10G2300/802 ,  C10G2300/805 ,  C10G2400/20 ,  Y02P20/584 ,  Y02P30/42 ,  C07C11/02

    摘要： The invention relates to a process for converting an oxygenate feedstock into an olefin product stream comprising (a) contacting an oxygenate feedstock with a molecular sieve catalyst in a reactor under conditions effective to convert the feedstock into an olefin product stream and to form carbonaceous deposits on the catalyst; (b) contacting at least a portion of the catalyst having said carbonaceous deposits with an oxygen containing gas under conditions effective to obtain a regenerated catalyst having a reduced carbonaceous deposit level and having an increased molecular oxygen content; (c) removing at least 60% by volume of said molecular oxygen from the regenerated catalyst based upon the total volume of molecular oxygen; (d) returning said regenerated catalyst to said reactor; and (e) repeating steps (a)–(d).

    摘要翻译： 本发明涉及一种将含氧化合物原料转化成烯烃产物流的方法，该方法包括（a）在有效将原料转化成烯烃产物流并形成碳质沉积物的条件下，使反应器中的含氧化合物原料与分子筛催化剂接触 催化剂; （b）在有效获得具有降低的碳沉积物水平并且具有增加的分子氧含量的再生催化剂的条件下使至少一部分具有所述碳质沉积物的催化剂与含氧气体接触; （c）基于分子氧的总体积从再生催化剂中除去至少60体积％的所述分子氧; （d）将所述再生催化剂返回到所述反应器; 和（e）重复步骤（a） - （d）。

    Use of catalytic distillation to produce cyclopentane or cyclopentene
    34.
    发明授权
    Use of catalytic distillation to produce cyclopentane or cyclopentene 失效
    使用催化蒸馏生产环戊烷或环戊烯

    公开(公告)号：US6100435A

    公开(公告)日：2000-08-08

    申请号：US191488

    申请日：1998-11-13

    申请人： Steven E. Silverberg ,  Leonel E. Sanchez ,  James R. Lattner

    发明人： Steven E. Silverberg ,  Leonel E. Sanchez ,  James R. Lattner

    IPC分类号： C07C13/10 ,  C07C13/12 ,  C07C1/00 ,  C07C4/22 ,  C07C13/15 ,  C07C5/33

    CPC分类号： C07C13/12 ,  C07C13/10 ,  C07C2101/08 ,  C07C2101/10 ,  C07C2523/42 ,  C07C2523/44 ,  C07C2523/72 ,  C07C2523/755 ,  C07C2523/86 ,  C07C2523/882 ,  C07C2523/883 ,  Y02P20/127 ,  Y10S203/06

    摘要： A process is disclosed for converting dicyclopentadiene to cyclopentane and/or cyclopentene, wherein dicyclopentadiene is fed to a catalytic distillation column, the dicyclopentadiene is cracked to cyclopentadiene in the catalytic distillation column, the cyclopentadiene is hydrogenated to cyclopentane in the catalytic distillation column, and the cyclopentane is recovered from the catalytic distillation column. The dicyclopentadiene is fed into and cracked to cyclopentadiene at the bottom of the catalytic distillation column. Hydrogen is then fed to the catalytic distillation column below the catalytic zone, where cyclopentadiene is hydrogenated as it is produced, thus suppressing polymerization of the cyclopentadiene. The resulting cyclopentane and/or cyclopentene vapor phase stream is condensed, thereby producing a liquid stream of cyclopentane and/or cyclopentene and a vapor stream of hydrogen and other off-gas by-products.

    摘要翻译： 公开了将二环戊二烯转化为环戊烷和/或环戊烯的方法，其中将二环戊二烯加入到催化蒸馏塔中，二环戊二烯在催化蒸馏塔中裂解成环戊二烯，环戊二烯在催化蒸馏塔中氢化成环戊烷， 从催化蒸馏塔回收环戊烷。 将二环戊二烯在催化蒸馏塔的底部加入并裂化成环戊二烯。 然后将氢气送入催化区下方的催化蒸馏塔，其中环戊二烯在其生产时被氢化，从而抑制环戊二烯的聚合。 所得到的环戊烷和/或环戊烷气相物流被冷凝，从而产生环戊烷和/或环戊烯的液体流以及氢气和其它废气副产物的蒸汽流。

    Process for forming cyclopentane from dicyclopentadiene
    35.
    发明授权
    Process for forming cyclopentane from dicyclopentadiene 失效
    从二环戊二烯形成环戊烷的方法

    公开(公告)号：US5998683A

    公开(公告)日：1999-12-07

    申请号：US899544

    申请日：1997-07-24

    申请人： James R. Lattner ,  C. Harry McMullen ,  Leonel E. Sanchez ,  Steven E. Silverberg ,  Tronze-I Dennis Wu

    发明人： James R. Lattner ,  C. Harry McMullen ,  Leonel E. Sanchez ,  Steven E. Silverberg ,  Tronze-I Dennis Wu

    IPC分类号： C07B61/00 ,  C07C5/03 ,  C07C13/10 ,  C07C4/02 ,  C07C4/22

    CPC分类号： C07C13/10 ,  C07C5/03 ,  C07C2101/08 ,  C07C2521/04 ,  C07C2523/44 ,  C07C2523/755 ,  C07C2523/882 ,  C07C2523/883 ,  C08G2101/0025 ,  C08G2101/005

    摘要： A method for producing a cyclopentane product which comprises the following steps: (a) cracking dicyclopentadiene to form a cyclopentadiene-rich stream and a higher boiling liquids stream; (b) separating the cyclopentadiene-rich stream from the higher boiling liquids stream; (c) diluting the cyclopentadiene-rich stream with recycled saturates such that the cyclopentadiene content is limited to between about 5-50%; (d) conducting a first hydrogenation of the cyclopentadiene-rich stream in the presence of hydrogen and a first catalyst, and at a temperature (i.e., preferably between about 26 to 94.degree. C., more preferably in the range between about 37 to 66.degree. C.) which is capable of avoiding the repolymerization of cyclopentadiene to dicyclopentadiene, thereby forming a cyclopentadiene-depleted stream; (e) conducting a second hydrogenation of the cyclopentadiene-depleted stream in the presence of a second catalyst wherein any residual olefins and/or cyclopentadiene contained within the cyclopentadiene-depleted stream are saturated, thereby forming a crude cyclopentane product; and (f) flash stripping the crude cyclopentane product to form the cyclopentane product comprising about 95% pure cyclopentane.

    摘要翻译： 一种生产环戊烷产物的方法，包括以下步骤：（a）裂解二环戊二烯以形成富含环戊二烯的料流和较高沸点的液体料流; （b）从较高沸点的液体物流中分离富含环戊二烯的物流; （c）用循环的饱和物稀释富含环戊二烯的流，使得环戊二烯含量限制在约5-50％之间; （d）在氢和第一催化剂的存在下，在一个温度（即，优选在约26至94℃之间，更优选约37至66℃的范围内）对富环戊二烯物流进行第一次氢化 DEG），其能够避免环戊二烯重新聚合成二环戊二烯，由此形成环戊二烯贫化的流; （e）在第二催化剂存在下进行环戊二烯贫化物流的第二次氢化，其中包含在环戊二烯贫化物流内的任何残留烯烃和/或环戊二烯都是饱和的，从而形成粗环戊烷产物; 和（f）快速汽提粗环戊烷产物以形成包含约95％纯环戊烷的环戊烷产物。

    Process for producing cyclohexylbenzene
    39.
    发明授权
    Process for producing cyclohexylbenzene 有权
    生产环己基苯的方法

    公开(公告)号：US08921604B2

    公开(公告)日：2014-12-30

    申请号：US13983785

    申请日：2011-11-21

    申请人： Christopher L. Becker ,  James R. Lattner ,  Charles Morris Smith ,  Kun Wang

    发明人： Christopher L. Becker ,  James R. Lattner ,  Charles Morris Smith ,  Kun Wang

    IPC分类号： C07C45/53 ,  C07C37/08 ,  C07C2/74

    CPC分类号： C07C2/74 ,  C07C2/66 ,  C07C6/126 ,  C07C2601/16 ,  C07C13/28

    摘要： In a process for producing cyclohexylbenzene, benzene is reacted with cyclohexene in a first reaction zone under conditions effective to produce a reaction product comprising cyclohexylbenzene and at least one polycyclohexylbenzene. At least a portion of the reaction product and a stripping agent comprising at least one C1 to C11 hydrocarbon or hydrogen are then separately supplied to a separation device and separated into at least a first fraction rich in cyclohexylbenzene and a second fraction rich in the at least one polycyclohexylbenzene.

    摘要翻译： 在生产环己基苯的方法中，苯在有效产生包含环己基苯和至少一种聚环己基苯的反应产物的条件下，在第一反应区中与环己烯反应。 然后将至少一部分反应产物和包含至少一个C1至C11烃或氢的汽提剂分别供应至分离装置，并分离成至少第一馏分富含环己基苯，第二馏分至少富含至少 一种聚环己基苯。