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19 条记录 (耗时 0.01 秒)

    Process for manufacturing molecular sieving carbon
    2.
    发明授权
    Process for manufacturing molecular sieving carbon 失效
    制造分子筛碳的方法

    公开(公告)号：US4458022A

    公开(公告)日：1984-07-03

    申请号：US495488

    申请日：1983-05-17

    申请人： Takushi Ohsaki ,  Susumu Abe

    发明人： Takushi Ohsaki ,  Susumu Abe

    IPC分类号： B01J20/20 ,  C01B31/08 ,  C01B37/00 ,  B01J21/20 ,  B01J21/18

    CPC分类号： C01B31/085

    摘要： A process for manufacturing molecular sieving carbon is disclosed, wherein pelletized charcoal made of coconut shell charcoal powder and coal tar is washed with dilute mineral acid solution, then a specified amount of coal tar is added, penetrated therein, followed by heat treatment under a particular range of temperature, and cooling in inert gas.

    摘要翻译： 公开了制造分子筛碳的方法，其中由椰壳炭粉和煤焦油制成的造粒炭用稀无机酸溶液洗涤，然后加入指定量的煤焦油，渗入其中，然后在特定的条件下进行热处理 温度范围和惰性气体中的冷却。

    Method of manufacturing carbonaceous granular molecular sieve
    3.
    发明授权
    Method of manufacturing carbonaceous granular molecular sieve 失效
    碳质粒状分子筛的制造方法

    公开(公告)号：US4046709A

    公开(公告)日：1977-09-06

    申请号：US561164

    申请日：1975-03-24

    申请人： Nakaji Yuki

    发明人： Nakaji Yuki

    IPC分类号： C01B31/14 ,  B01J20/20 ,  B01J29/03 ,  C01B31/08 ,  C01B37/00 ,  B01J37/00 ,  B01J21/18 ,  C01B31/00

    CPC分类号： C01B31/085

    摘要： Granular molecular sieve may be obtained, without necessitating any activng treatment, by subjecting a vinylidene chloride copolymer to a thermal carbonization treatment for removal of hydrochloric acid, pulverizing the resultant product to a grain size smaller than 100 mesh size, adding 15 to 35 parts by weight of a carbonaceous sintering agent and 8 to 15 parts by weight of an organic pelletizer capable of gas generation by heating to 100 parts by weight of the pulverized product, pelletizing the resultant mixture and carbonizing the resultant pellets at a temperature of 400 to 900.degree. C for a period of 2 to 6 hours. The pore diameter of this molecular sieve can be suitably controlled within a range of from 5 to 10 A by appropriately selecting the sintering agent and pelletizer employed and the conditions of the thermal treatment.

    摘要翻译： 可以通过使偏二氯乙烯共聚物进行热碳化处理除去盐酸，将所得产物粉碎成小于100目尺寸的粒度，加入15〜35份的方法，得到粒状分子筛，而不需要任何活化处理 碳质烧结剂的重量和8〜15重量份能够通过加热至100重量份粉碎产物而产生气体的有机造粒机，造粒所得混合物并在400-900℃的温度下碳化所得颗粒。 C 2至6小时。 通过适当选择所使用的烧结剂和造粒机以及热处理条件，可以将该分子筛的孔径适当地控制在5〜10A的范围内。

    Controlled selectivity activated carbon
    5.
    发明授权
    Controlled selectivity activated carbon 失效
    受控选择性活性炭

    公开(公告)号：US3955944A

    公开(公告)日：1976-05-11

    申请号：US521992

    申请日：1974-11-08

    申请人： Richard John Grant

    发明人： Richard John Grant

    IPC分类号： B01D53/02 ,  C01B31/08 ,  C07C51/47 ,  B01D53/04

    CPC分类号： C01B31/085 ,  B01D53/02 ,  C07C51/47

    摘要： A series of fast acting activated carbons is made having high surface areas and at the same time very small pore size. The method of manufacturing them, which specifies certain carbonaceous starting materials and pulverizing, agglomerating, crushing and oxidizing steps, determines or controls the pore sizes and surface areas. My activated carbon has highly uniform, very small pore sizes and at the same time a large surface area per unit of weight and a large macropore volume. New methods of separating mixtures of compounds, such as mixtures of hydrocarbons, are disclosed employing my new molecular sieve activated carbon. In my fast-adsorbing molecular sieve, molecules of generally lower molecular weight are adsorbed by the carbon rather than the usual case for activated carbon, which is that the carbon tends to adsorb generally larger molecules in preference to smaller ones.

    摘要翻译： 一系列快速活化的碳​​被制成具有高的表面积，同时非常小的孔径。 制造它们的方法，其规定了某些含碳原料和粉碎，附聚，粉碎和氧化步骤，确定或控制孔径和表面积。 我的活性炭具有高度均匀，非常小的孔径，同时每单位重量的大表面积和大的大孔体积。 使用我的新分子筛活性炭公开了分离化合物混合物的新方法，例如烃的混合物。 在我的快速吸附分子筛中，通常较低分子量的分子被碳吸附，而不是通常用于活性炭的情况，这是因为碳倾向于较小的吸附通常较大的分子。

    Purification of sterols with activated carbon as adsorbent and chlorobenzene as desorbent
    7.
    发明授权
    Purification of sterols with activated carbon as adsorbent and chlorobenzene as desorbent 失效
    用活性炭作为吸附剂和氯苯作为解吸剂纯化甾醇

    公开(公告)号：US4882065A

    公开(公告)日：1989-11-21

    申请号：US131611

    申请日：1987-12-11

    申请人： Timothy J. Barder

    发明人： Timothy J. Barder

    IPC分类号： B01D15/00

    CPC分类号： B01D15/00 ,  C01B31/085 ,  C07J9/00 ,  C11B3/10

    摘要： An adsorptive separation process for separating sterols from a tall oil feed mixture, which process comprises contacting the feed mixture with an adsorbent comprising an activated-type carbon sieve having a pore diameter of 15-20 .ANG. and a surface area of 300-1500 m.sup.2 /g, selectively adsorbing substantially all of the sterols to be separated on the adsorbent and thereafter recovering high purity sterols. A desorption step is used to desorb the adsorbed sterols with an aromatic liquid, e.g., chlorobenzene.

    摘要翻译： 一种用于从妥尔油进料混合物中分离固醇的吸附分离方法，该方法包括使进料混合物与包含孔径为15-20AgTm，表面积为300-1500m2 / g的活性炭筛的吸附剂接触， g，在吸附剂上选择性吸附待分离的所有固醇，然后回收高纯度甾醇。 解吸步骤用于用芳族液体如氯苯解吸吸附的甾醇。

    Method for the adsorptive removal of hydrogen sulfide from gas mixtures
    8.
    发明授权
    Method for the adsorptive removal of hydrogen sulfide from gas mixtures 失效
    从气体混合物吸附去除硫化氢的方法

    公开(公告)号：US4440551A

    公开(公告)日：1984-04-03

    申请号：US289515

    申请日：1981-08-03

    申请人： Klaus-Dirk Henning ,  Jurgen Klein ,  Burkhard Harder

    发明人： Klaus-Dirk Henning ,  Jurgen Klein ,  Burkhard Harder

    IPC分类号： B01D53/52 ,  B01D53/02 ,  C01B3/56 ,  C01B21/04 ,  C01B31/08 ,  B01D53/04

    CPC分类号： C01B21/045 ,  B01D53/02 ,  C01B3/56 ,  C01B31/085 ,  C01B2203/043 ,  C01B2203/0485 ,  C01B2210/0064

    摘要： A method is disclosed for the adsorptive removal of H.sub.2 S from gas mixtures in C-containing adsorption agents with 1-80 bar pressures and regeneration, employing pressure lowering and/or temperature change and simultaneous rinsing with an at most negligibly absorbable component of the gas mixture. A carbon molecular sieve of fossil and/or bituminous fuel is used, with for pore diameter less than 10 nm a pore volume of 15-25 cm.sup.3 /100 g, and micropore volume in pore diameter range 0.35-10 nm less than 10 cm.sup.3 /100 g. The inner surface of the molecular screen can be freed of surface groups capable of reacting with the H.sub.2 S by aftertreatment with reducing gas.

    摘要翻译： 公开了一种用于在具有1-80巴压力的含C吸附剂中的气体混合物中吸附除去H 2 S的方法，并且使用降压和/或温度变化并同时用气体混合物中最可忽略的可吸收组分进行冲洗 。 使用化石和/或沥青燃料的碳分子筛，孔径小于10nm，孔体积为15-25cm 3 / 100g，孔径范围为0.35-10nm的微孔体积小于10cm 3 / 100克。 分子筛的内表面可以通过用还原气体进行后处理而脱离能够与H 2 S反应的表面基团。