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    • 2. 发明授权
    • Monomodal and polymodal catalyst supports and catalysts having narrow
pore size distributions and their production
    • 单峰和多模式催化剂载体和具有窄孔径分布及其生产的催化剂
    • US5935898A
    • 1999-08-10
    • US711989
    • 1996-09-10
    • Peter TrubenbachAlfred HagemeyerGunter LauthUwe DingerdissenFranz Josef BrockerKlemens Flick
    • Peter TrubenbachAlfred HagemeyerGunter LauthUwe DingerdissenFranz Josef BrockerKlemens Flick
    • C12M1/40B01J21/00B01J27/00B01J29/00B01J35/10B01J37/00B01J23/00
    • B01J37/0018B01J35/10B01J35/1009B01J35/1014B01J35/1019B01J35/108B01J35/1085
    • Monomodal or polymodal catalyst supports or catalysts having a BET specific surface area of from 0.01 to 250 m.sup.2 /g and a monomodal or polymodal pore size distribution having a mean pore diameter of from 50 to 300,000 nm measured by the mercury pressure porosimetry method, whereina) from 10 to 95% of the pore volume is at from 0.1 to 3 times the mean pore diameter and/orb) from 10 to 80% of the pore volume is at from 0.4 to 3 times the mean pore diameter and/orc) from 50 to 95% of the pore volume is at from 0.1 to 1 times the mean pore diameter and/ord) from 50 to 80% of the pore volume is at from 0.4 to 1 times the mean pore diameter ande) the width at half height of the pore size distribution is less than 0.5 times the mean pore diameter,which are useful for preparing chlorine from hydrogen chloride in a non-steady-state Deacon process, for the reaction of ethylbenzene to give styrene in a non-steady-state oxydehydrogenation, for preparing aziridine from ethanolamine, in reductions, hydrogenations, oxidations, dehydrogenations, acid- or base-catalyzed reactions or reactions in a fluidized bed, for removing combustion residues from diesel exhaust gases and for removing NO.sub.x from waste gases, in bioreactors together with bacteria and as biocatalyst supports with immobilized enzymes or microbes, and a process for producing said monomodal or polymodal catalyst supports or catalysts.
    • 单峰或多模式催化剂载体或BET比表面积为0.01至250m 2 / g的催化剂载体和通过汞压孔隙度法测量的平均孔径为50至300,000nm的单峰或多模孔径分布,其中a )孔体积的10至95%为平均孔径的0.1至3倍和/或b)孔体积的10至80%为平均孔径的0.4至3倍和/或c )孔体积的50至95%为平均孔径的0.1至1倍,和/或d)孔体积的50至80%为平均孔径的0.4至1倍,e) 孔尺寸分布的半高宽度小于平均孔径的0.5倍,这可用于在非稳态Deacon方法中从氯化氢制备氯,用于乙苯的反应, 稳态氧化脱氢,用于从乙醇胺制备氮丙啶,还原 ns,氢化,氧化,脱氢,酸或碱催化的反应或在流化床中的反应,用于从生物反应器中连同细菌和作为生物催化剂载体与固定化酶一起从柴油机排气中除去燃烧残余物并从废气中除去NOx 或微生物,以及用于生产所述单峰或多模式催化剂载体或催化剂的方法。
    • 7. 发明授权
    • Preparation of amines and aminonitriles
    • 胺和氨基腈的制备
    • US5789621A
    • 1998-08-04
    • US693983
    • 1996-08-08
    • Werner SchnurrGuido VoitKlemens FlickRolf-Hartmuth Fischer
    • Werner SchnurrGuido VoitKlemens FlickRolf-Hartmuth Fischer
    • B01J23/78B01J23/94B01J27/187B01J27/28B01J38/10C07B43/04C07B61/00C07C20060101C07C209/48C07C209/52C07C211/12C07C211/35C07C253/30C07C255/24C07C209/02
    • C07C209/48C07C209/52
    • A process for preparing an NH.sub.2 -containing compound by hydrogenating a compound containing at least one unsaturated carbon-nitrogen bond with hydrogen in the presence of a catalyst at temperatures not below room temperature and elevated hydrogen partial pressure in the presence or absence of a solvent which process includes the following steps: a) using a catalyst comprising a cobalt- and/or iron-containing catalyst, and b) after the conversion based on the compound to be hydrogenated and/or the selectivity based on the desired product has or have dropped below a defined value or the amount of an unwanted by-product has risen beyond a defined value, interrupting the hydrogenation by stopping the feed of the compound to be hydrogenated and of the solvent, if used, c) treating the catalyst at from 150.degree. to 400.degree. C. with hydrogen using a hydrogen pressure within the range from 0.1 to 30 MPa and a treatment time within the range from 2 to 48 h, and d) subsequently continuing the hydrogenation of the compound containing at least one unsaturated carbon-nitrogen bond.
    • 在催化剂存在下,在不低于室温和升高的氢分压的情况下,在存在或不存在溶剂的情况下,通过氢化含有至少一个不饱和碳 - 氮键的化合物与氢气来制备含NH 2的化合物的方法, 方法包括以下步骤:a)使用包含含钴和/或含铁催化剂的催化剂,和b)基于待氢化的化合物转化后,和/或基于所需产物的选择性具有或已经下降 低于定义的值或不想要的副产物的量已经超过定义的值,如果使用,则通过停止待氢化化合物的进料和溶剂的中断氢化,c)在150℃下处理催化剂 在氢气压力为0.1〜30MPa,处理时间为2〜48h的范围内,使氢气变为400℃,d)随后继续进行水压 该化合物含有至少一个不饱和碳 - 氮键。