利索-全球专利检索

  1. 登录
  2. 注册

搜索结果

15 条记录 (耗时 0.034 秒)

    Absorbents
    1.
    发明授权
    Absorbents 失效
    吸收剂

    公开(公告)号：US5853681A

    公开(公告)日：1998-12-29

    申请号：US704639

    申请日：1996-09-04

    申请人： Patrick John Denny ,  Peter John Herbert Carnell ,  Brian Peter Williams ,  Cathy Anne Woodroffe ,  Peter Wood

    发明人： Patrick John Denny ,  Peter John Herbert Carnell ,  Brian Peter Williams ,  Cathy Anne Woodroffe ,  Peter Wood

    IPC分类号： B01D53/52 ,  B01D15/00 ,  B01D53/34 ,  B01J20/02 ,  B01J20/06 ,  C01B17/16

    CPC分类号： B01D53/34 ,  B01D15/00 ,  B01J20/0237 ,  B01J20/0277 ,  B01J20/06 ,  B01J20/08 ,  B01J20/3028

    摘要： Absorbents, suitable for absorbing sulphur compounds such as hydrogen sulphide from gases and liquids, in the form of shaped units having an average size within the range 1-10 mm and containing at least 75% by weight of an absorbent material comprising copper carbonate, basic copper carbonate, and/or copper hydroxide. The units preferably have a bulk density of at least 0.9 kg/l, especially at least 1.2 kg/l. The units are preferably agglomerates containing a small amount of a binder such as a cement and may also contain a proportion of alumina to catalyse hydrolysis of carbon-containing sulphur compounds such as carbonyl sulphide or carbon disulphide.

    摘要翻译： PCT No.PCT / GB95 / 00448 Sec。 371日期1996年9月4日 102（e）日期1996年9月4日PCT 1995年3月2日PCT公布。 公开号WO95 / 24962 日期1995年9月21日适用于从气体和液体中吸收硫化物如硫化氢的吸附剂，其形式为平均尺寸在1-10mm范围内并且含有至少75重量％的吸收材料 包括碳酸铜，碱式碳酸铜和/或氢氧化铜。 单元优选具有至少0.9kg / l，特别是至少1.2kg / l的堆积密度。 这些单元优选是含有少量粘合剂如水泥的附聚物，并且还可以含有一定比例的氧化铝以催化含碳硫化合物如硫化羰或二硫化碳的水解。

    Absorbents
    2.
    发明授权
    Absorbents 失效
    吸收剂

    公开(公告)号：US5897845A

    公开(公告)日：1999-04-27

    申请号：US693202

    申请日：1996-10-08

    申请人： Patrick John Denny ,  Peter John Herbert Carnell ,  Brian Peter Williams ,  Cathy Anne Woodroffe

    发明人： Patrick John Denny ,  Peter John Herbert Carnell ,  Brian Peter Williams ,  Cathy Anne Woodroffe

    IPC分类号： B01D53/68 ,  B01J20/04 ,  B01J20/08 ,  B01J20/00 ,  C01B7/00

    CPC分类号： B01D53/68 ,  B01J20/041 ,  B01J20/043 ,  B01J20/08 ,  B01J20/28004 ,  B01J20/28014 ,  B01J20/2803 ,  B01J20/28057 ,  B01J20/3028 ,  B01J20/3078

    摘要： Absorbent granules comprising an intimate mixture of particles of alumina trihydrate, 0.5 to 2 parts by weight of particles of a sodium component selected from the group consisting of sodium carbonate, sodium bicarbonate and mixtures thereof per part by weight of said alumina trihydrate and from 5 to 20% by weight of a binder, said alumina trihydrate, sodium component and binder being present in such proportions that, after ignition of a sample of the granules at 900.degree. C., the sample has a sodium oxide, Na.sub.2 O, content of at least 20% by weight. Processes for manufacturing such absorbent granules and for using such absorbent granules for the removal of acidic gases are also disclosed.

    摘要翻译： PCT No.PCT / GB95 / 00303 Sec。 371日期1996年10月8日第 102（e）日期1996年10月8日PCT提交1995年2月14日PCT公布。 WO95 / 22403 PCT出版物 日期1995年8月24日吸收剂颗粒包含三水合氧化铝颗粒的紧密混合物，0.5至2重量份选自碳酸钠，碳酸氢钠的钠组分的颗粒及其混合物，每重量份所述氧化铝 三水合物和5至20重量％的粘合剂，所述三水合氧化铝，钠组分和粘合剂以如下比例存在，使得在900℃下将颗粒样品点燃后，样品具有氧化钠，Na 2 O ，含量至少为20重量％。 还公开了制造这种吸收性颗粒和使用这种吸收性颗粒去除酸性气体的方法。

    Sulphided ion exchange resins
    3.
    发明授权
    Sulphided ion exchange resins 失效
    硫化离子交换树脂

    公开(公告)号：US07591944B2

    公开(公告)日：2009-09-22

    申请号：US10502236

    申请日：2003-01-17

    申请人： Peter John Herbert Carnell ,  Nicola Young ,  Peter Wood

    发明人： Peter John Herbert Carnell ,  Nicola Young ,  Peter Wood

    IPC分类号： C10G25/00 ,  C10G25/06 ,  C10G17/00 ,  B01J20/26

    CPC分类号： B01J41/14 ,  B01J41/07 ,  C10G25/02

    摘要： A method of making a sulphided ion exchange resin from an ion exchange resin containing primary or secondary amino group comprises passing a non-aqueous liquid, e.g. a hydrocarbon, feedstock containing elemental sulphur or organic, or inorganic, di-or poly-sulphides through a bed of an ion exchange resin containing primary or secondary amino groups, and so unsulphided ion exchange resins containing primary or secondary amine groups may be used to remove such elemental sulphur or sulphur compounds from liquid, e.g. hydrocarbon, feedstocks. The sulphided ion exchange resins may be used to remove elemental mercury or organic mercury compounds from liquid, e.g. hydrocarbon, streams.

    摘要翻译： 从含有伯或仲氨基的离子交换树脂制备硫化离子交换树脂的方法包括使非水性液体例如 通过含有伯或仲氨基的离子交换树脂的床，含有元素硫或有机或无机，二 - 或多硫化物的烃类原料，因此可以使用含有伯胺或仲胺基团的未硫化离子交换树脂 从液体中除去这些元素硫或硫化合物，例如 碳氢化合物，原料。 硫化离子交换树脂可用于从液体中除去元素汞或有机汞化合物，例如， 碳氢化合物，溪流。

    Removal of sulphur together with other contaminants from fluids
    7.
    发明授权
    Removal of sulphur together with other contaminants from fluids 失效
    与流体中的其他污染物一起去除硫

    公开(公告)号：US6007706A

    公开(公告)日：1999-12-28

    申请号：US145165

    申请日：1998-09-02

    申请人： Peter John Herbert Carnell ,  Edwin Stephen Willis

    发明人： Peter John Herbert Carnell ,  Edwin Stephen Willis

    IPC分类号： C10G25/00 ,  C10L3/10

    CPC分类号： C10L3/10 ,  C10G25/00

    摘要： A process for the purification of a fluid stream containing a sulphur contaminant, such as hydrogen sulphide, and mercury, phosphine, stibine, and/or arsenic compounds as a second contaminant wherein said fluid stream is passed through a bed of a particulate absorbent containing a sulphide of a variable valency metal, especially copper, that is more electropositive than mercury, to remove said second contaminant and then the sulphur contaminant is removed from at least part of the effluent from that bed by passing that part of the effluent through a bed of a particulate sulphur absorbent comprising a compound selected from oxides, hydroxides, carbonates and basic carbonates of said variable valency metal is disclosed. The removal of the sulphur contaminant converts said variable valency metal compound to the corresponding sulphide. The resulting bed of variable valency metal sulphide is subsequently used for the removal of the second contaminant.

    摘要翻译： 一种用于净化含硫硫化物的流体物流（例如硫化氢）和作为第二污染物的汞，磷化氢，锑和/或砷化合物的流程，其中所述流体流通过含有 通过将该部分流出物通过床的一部分，将来自该床的流出物的至少一部分从至少部分来自该床的流出物中除去所述第二污染物，然后除去硫污染物，其中比汞更具有正电性的可变价金属，特别是铜的硫化物， 公开了一种包含选自所述可变价金属的氧化物，氢氧化物，碳酸盐和碱性碳酸盐的化合物的颗粒状硫吸收剂。 去除硫污染物将所述可变价金属化合物转化为相应的硫化物。 所得到的可变价金属硫化物床随后用于除去第二污染物。

    Gas absorption
    10.
    发明授权
    Gas absorption 失效
    气体吸收

    公开(公告)号：US6139605A

    公开(公告)日：2000-10-31

    申请号：US371292

    申请日：1999-08-10

    申请人： Peter John Herbert Carnell ,  Hiren Krishnakant Shethna ,  Gavin Paul Towler ,  Edwin Stephen Willis

    发明人： Peter John Herbert Carnell ,  Hiren Krishnakant Shethna ,  Gavin Paul Towler ,  Edwin Stephen Willis

    IPC分类号： B01D53/14

    CPC分类号： B01D53/1425 ,  B01D53/1456

    摘要： A double-loop process for the removal of specified gas or gases from a process gas by absorption with a liquid absorbent for said specified gas or gases wherein the process gas is contacted counter-currently in a first absorption stage with semi-lean absorbent liquid and then in a second absorption stage with lean absorbent liquid to give a sweet process gas and the absorbed gases are stripped from the laden absorbent liquid in a first stage giving a semi-lean absorbent liquid. Part of the semi-lean absorbent is recycled to the first absorption stage while the remainder is subjected to further stripping by counter-current contact with an auxiliary gas that has a concentration of the specified gas or gases that is lower than the concentration of the specified gas or gases in the process gas to give the lean absorbent liquid which is recycled to the second absorption stage. The auxiliary gas, which is especially a part stream of the sweet process gas, may be recycled, after use for stripping, to the process gas upstream of the first absorption stage. The process may be integrated with a glycol drying stage with regeneration of the wet glycol by stripping with the part stream of the sweet process gas before the latter is used for stripping the semi-lean absorbent liquid.

    摘要翻译： 一种用于通过用用于所述特定气体或气体的液体吸收剂吸收从工艺气体中除去特定气体或气体的双循环方法，其中工艺气体在第一吸收阶段与半贫吸收液体反向接触， 然后在具有贫吸收液体的第二吸收阶段中产生甜味工艺气体，并且在第一阶段中从吸收液体中吸收吸收的气体，得到半贫吸收液体。 半贫吸收剂的一部分被再循环到第一吸收阶段，而其余部分通过与特定气体或气体的浓度低于规定浓度的辅助气体的逆流接触进行进一步的汽提 气体或气体，以产生再循环到第二吸收级的贫吸收液体。 特别是甜加工气体的一部分流的辅助气体可以在用于汽提之后再循环到第一吸收级上游的工艺气体。 该方法可以与二醇干燥阶段整合，通过用甜味工艺气体的一部分流汽提湿二醇，然后将其用于汽提半贫吸收液体。