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257 条记录 (耗时 0.027 秒)

    VSA adsorption process with continuous operation
    31.
    发明授权
    VSA adsorption process with continuous operation 失效
    VSA吸附过程连续运行

    公开(公告)号：US5429666A

    公开(公告)日：1995-07-04

    申请号：US191401

    申请日：1994-02-03

    申请人： Rakesh Agrawal ,  Ravi Kumar ,  Tarik Naheiri ,  Charles F. Watson

    发明人： Rakesh Agrawal ,  Ravi Kumar ,  Tarik Naheiri ,  Charles F. Watson

    IPC分类号： B01D53/04 ,  B01D53/047 ,  C01B21/04 ,  B01D53/053

    CPC分类号： B01D53/0476 ,  B01D2256/12 ,  B01D2257/102 ,  B01D2259/402 ,  B01D53/0446

    摘要： A process for separating a feed gas mixture into a more strongly adsorbable component and a less strongly adsorbable component in a plurality of adsorbent beds containing an adsorbent selective for the more strongly adsorbable component using pressurization by product end to product end pressure equalization between beds simultaneous with cocurrent ambient and elevated pressure feed pressurization, coproduction of product and purge gas, and cocurrent depressurization for pressure equalization gas simultaneous with countercurrent evacuation. Oxygen product can be recovered from air at high recovery using the process.

    摘要翻译： 一种将进料气体混合物分离成多个吸附床中的较强吸附组分和较不强吸附组分的方法，所述多个吸附剂床含有选择性较强吸附组分的吸附剂，其通过产物端部至产物端部之间的压力平衡，同时与床 并发环境和高压进料加压，产品和吹扫气体的共同生产，以及与逆流排空同时进行均压气体的并流减压。 使用该方法可以以高回收率从空气中回收氧气产物。

    Process for the cryogenic distillation of an air feed to produce an ultra-high purity oxygen product
    32.
    发明授权
    Process for the cryogenic distillation of an air feed to produce an ultra-high purity oxygen product 失效
    用于空气进料的低温蒸馏以产生超高纯度氧产物的方法

    公开(公告)号：US5425241A

    公开(公告)日：1995-06-20

    申请号：US241247

    申请日：1994-05-10

    申请人： Rakesh Agrawal ,  Donald W. Woodward

    发明人： Rakesh Agrawal ,  Donald W. Woodward

    IPC分类号： F25J3/04

    CPC分类号： F25J3/04715 ,  F25J2200/06 ,  F25J2200/32 ,  F25J2200/34 ,  F25J2200/90 ,  F25J2215/56 ,  Y10S62/924

    摘要： A process is set forth for the cryogenic distillation of an air feed to produce an ultra-high purity oxygen product. A first oxygen-containing but heavy contaminants-lean (free) stream is removed from the main distillation column system and subsequently stripped in an auxiliary distillation column. A second oxygen-containing but light contaminants-lean (free) gaseous stream is also removed from the main distillation column system and subsequently fed to the bottom section of the auxiliary distillation column in order to provide heat duty/reboil to the bottom of the auxiliary distillation column. The ultra-high purity oxygen product (ie total contaminant concentration less than 10.0 vppm, preferably less than 1.0 vppm) is withdrawn from an intermediate section of the auxiliary distillation column.

    摘要翻译： 阐述了用于空气进料的低温蒸馏以产生超高纯度氧产物的方法。 从主蒸馏塔系统中除去第一含氧但重的污染物（游离）物流，随后在辅助蒸馏塔中汽提。 还有从主蒸馏塔系统中除去第二个含氧但轻质污染物（自由）的气流，随后将其送入辅助蒸馏塔的底部，以便向辅助蒸馏塔的底部提供热负荷/再沸腾 蒸馏塔。 从辅助蒸馏塔的中间部分排出超高纯度氧产物（即总污染物浓度小于10.0vppm，优选小于1.0vppm）。

    Cryogenic process for the separation of air to produce ultra high purity nitrogen
    37.
    发明授权
    Cryogenic process for the separation of air to produce ultra high purity nitrogen 失效
    用于分离空气以产生超高纯氮的低温工艺

    公开(公告)号：US5123947A

    公开(公告)日：1992-06-23

    申请号：US638853

    申请日：1991-01-03

    申请人： Rakesh Agrawal

    发明人： Rakesh Agrawal

    IPC分类号： F25J3/04

    CPC分类号： F25J3/04872 ,  F25J3/044 ,  F25J3/0443 ,  F25J3/04448 ,  F25J3/04454 ,  F25J2200/30 ,  F25J2200/32 ,  F25J2200/50 ,  F25J2200/54 ,  F25J2200/74 ,  F25J2200/94 ,  F25J2205/02 ,  F25J2215/44 ,  F25J2220/42 ,  F25J2220/44 ,  F25J2250/20

    摘要： This invention relates to a cryogenic process for the separation of air utilizing an integrated multi-column distillation system wherein an ultra high purity nitrogen product is generated. In the cryogenic distillation separation of air, air is initially compressed, pretreated and cooled for separation into its components. Ultra high purity, e.g., nitrogen typically having less than 0.1 ppm impurities is generated in a multi-column distillation system comprising a first column and an ultra high purity nitrogen column with enhanced nitrogen product recovery by withdrawing a gaseous nitrogen fraction from a first column and charging the fraction as a feed to the ultra high purity nitrogen column, withdrawing a nitrogen stream which is rich in volatile contaminants from the top of the ultra high purity nitrogen column and recovering a nitrogen product at a point below the removal point of the nitrogen rich stream containing volatile components. Removal of volatile components in the distillation process is effected by partially condensing a nitrogen vapor stream from either the first column or the ultra high purity column and removing at least one of the uncondensed portions of the nitrogen rich stream containing volatile components as a purge stream.

    摘要翻译： 本发明涉及一种使用集成的多塔蒸馏系统分离空气的低温方法，其中产生超高纯氮产物。 在空气的低温蒸馏分离中，空气最初被压缩，预处理并冷却以分离成其组分。 在包括第一塔和超高纯度氮塔的多塔蒸馏系统中产生超高纯度，例如通常具有小于0.1ppm杂质的氮，通过从第一塔中取出气态氮馏分而提高氮产物回收率， 将该馏分作为进料加入到超高纯氮塔中，从超高纯度氮塔的顶部排出富含挥发性污染物的氮气流，并在低于富氮的去除点的一个点回收氮产物 流含有挥发性成分。 通过将来自第一塔或超高纯度塔的氮蒸汽流部分冷凝并除去含有挥发性组分的富氮流的至少一个未冷凝部分作为吹扫流来实现蒸馏过程中挥发性组分的去除。

    Cryogenic process for the separation of air to produce moderate pressure nitrogen
    38.
    发明授权
    Cryogenic process for the separation of air to produce moderate pressure nitrogen 失效
    用于分离空气以生产中等压力氮的低温方法

    公开(公告)号：US5077978A

    公开(公告)日：1992-01-07

    申请号：US537181

    申请日：1990-06-12

    申请人： Rakesh Agrawal ,  Donald W. Woodward

    发明人： Rakesh Agrawal ,  Donald W. Woodward

    IPC分类号： F25J3/04

    CPC分类号： F25J3/042 ,  F25J3/04212 ,  F25J3/04309 ,  F25J3/04315 ,  F25J3/04412 ,  F25J3/04678 ,  F25J2200/20 ,  F25J2240/44 ,  F25J2245/50 ,  F25J2250/50 ,  Y10S62/924

    摘要： This invention relates to a cryogenic process for the separation of air utilizing an integrated multi-column distillation system wherein a nitrogen rich, oxygen rich and argon rich product are generated. In the cryogenic distillation separation of air, air is initially compressed, pretreated and cooled for separation into its components. Moderate pressure, e.g., 25-80 psia nitrogen is generated with enhanced nitrogen product purity and greater recovery of both nitrogen and argon by effecting a high boil-up rate in the bottom of the lower pressure column, thereby creating a reduced liquid flow/vapor flow ratio (L/V) and utilizing a higher than customary nitrogen reflux to the top of the lower pressure column, where the concentration of oxygen in nitrogen is less than about 10 ppm by volume or the nitrogen purity is at least about 99.5% by volume. Refrigeration to drive the system is obtained by recovering the energy from the waste nitrogen stream and oxygen vapor from the lower pressure column. A second method for obtaining refrigeration is to withdraw oxygen as a bottoms liquid from the lower pressure column, expanding that liquid to a lower pressure and using it to condense the nitrogen vapor generated in a higher pressure column which has been expanded in a turbo-expander to provide the refrigeration.

    Alkylation of aromatic amines over thermally pretreated zeolites
    39.
    发明授权
    Alkylation of aromatic amines over thermally pretreated zeolites 失效
    芳族胺在热预处理沸石上烷基化

    公开(公告)号：US5026912A

    公开(公告)日：1991-06-25

    申请号：US499925

    申请日：1990-03-27

    申请人： Rakesh Agrawal ,  Steven R. Auvil

    发明人： Rakesh Agrawal ,  Steven R. Auvil

    IPC分类号： C07C209/68

    CPC分类号： C07C209/68

    摘要： A process for selectively producing ortho-alkylated aromatic amines in high selectivity relative to N-alkylated aromatic amines. The process comprises reacting an aromatic amine, having at least one hydrogen atom in a position ortho to the amine functionality, and an olefin under conditions sufficient to effect an alkylation reaction, in the presence of a zeolite catalyst which has been thermally pretreated by heating the catalyst to a temperature greater than about 500.degree. C. for a period ranging from 0.5 to about 10 hours while sweeping an inert gas over the heated catalyst to remove water and ammonia formed during the thermal treatment, and subsequently recovering the alkylated aromatic amine.

    摘要翻译： 相对于N-烷基化芳族胺，以高选择性选择性地生产邻烷基化芳族胺的方法。 该方法包括在已经通过加热热预处理的沸石催化剂的存在下使具有至少一个氢原子的胺在官能团的位置与烯烃的反应条件下进行反应，所述烯烃在足以进行烷基化反应的条件下进行 催化剂在大约500℃的温度下进行约0.5至约10小时的时间，同时在加热的催化剂上吹扫惰性气体以除去在热处理期间形成的水和氨，随后回收烷基化芳族胺。