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    • 8. 发明授权
    • Recovering sulfur from ammonia acid gas stream
    • 从氨酸气流中回收硫
    • US5292492A
    • 1994-03-08
    • US877936
    • 1992-05-04
    • J. Scott BuchananJagannathan N. Iyengar
    • J. Scott BuchananJagannathan N. Iyengar
    • B01D53/50B01D53/52C01B17/04C01B17/16
    • C01B17/0491B01D53/508B01D53/523C01B17/0408C01B17/0456C01B17/0478
    • Method and system for recovering sulfur from an ammonia acid gas stream containing hydrogen sulfide comprising the steps of combusting the ammonia acid gas stream with air or oxygen to convert the ammonia and the hydrogen sulfide therein to N.sub.2 and SO.sub.x, respectively, and thus form a nitrogen and sulfur oxide enriched gas stream. The nitrogen and sulfur oxide enriched gas stream is contacted with a solid absorbent bed to extract the sulfur oxides and retain them as sulfur compounds, thus forming a nitrogen bearing stream. The absorbent bed is then contacted with a hydrogen and/or hydrocarbon bearing stream to reduce the retained sulfur compounds to hydrogen sulfide and/or sulfur dioxide and thereby form a hydrogen sulfide and/or sulfur dioxide bearing stream. Sulfur is recovered from the hydrogen sulfide and/or sulfur dioxide bearing stream. The nitrogen bearing stream is sent to an incinerator or vented through a stack.
    • 从含有硫化氢的氨酸气流中回收硫的方法和系统,包括以下步骤:将氨酸气流与空气或氧气一起燃烧以将氨和硫化氢分别转化为N 2和SO x,从而形成氮 和富含硫氧化物的气流。 富含氮氧化物和氧化硫的气流与固体吸收剂床接触以提取硫氧化物并将其保留为硫化合物,从而形成含氮气流。 然后将吸收剂床与氢气和/或含烃流体接触以将保留的硫化合物还原成硫化氢和/或二氧化硫,从而形成含硫化氢和/或二氧化硫的物流。 从硫化氢和/或二氧化硫气流中回收硫。 氮气流被送到焚烧炉或通过堆垛排放。
    • 9. 发明授权
    • Process for converting cyclic urea to corresponding diamine in a gas
treating system
    • 在气体处理系统中将环脲转化为相应的二胺的方法
    • US4282194A
    • 1981-08-04
    • US122589
    • 1980-02-19
    • Geoffrey R. SayJames R. Hays, Sr.Jagannathan N. IyengarBarbara A. Hacker
    • Geoffrey R. SayJames R. Hays, Sr.Jagannathan N. IyengarBarbara A. Hacker
    • B01D53/14B01D53/52B01D53/34
    • B01D53/1425B01D53/1456B01D53/1493B01D53/526Y02C10/06
    • Acidic gases such as carbon dioxide are removed from a normally gaseous mixture including the acidic component by contacting the gaseous mixture in an absorption zone with an acid absorbing scrubbing solution comprising a basic alkali metal compound and an activator for the compound, during which process at least a portion of the activator is converted to a cyclic urea. The solution is then transferred to the desorption zone to remove at least a portion of the absorbed acidic component. At least a portion of the partially desorbed scrubbing solution containing the cyclic urea is transferred from the desorption zone to a thermal conversion zone maintained at an elevated temperature wherein at least a portion of the cyclic urea is converted back to the activator. A portion of the scrubbing solution from the thermal conversion zone, relatively rich in the acidic component is vaporized and returned to the desorption zone, and another portion, relatively lean in the acidic component, is returned from the thermal conversion zone to the absorption zone.
    • 通过使吸收区中的气体混合物与包含碱性碱金属化合物和化合物的活化剂的吸酸洗涤溶液接触,将酸性气体如二氧化碳从包括酸性组分的常规气态混合物中除去,在该过程中至少 活化剂的一部分转化为环状脲。 然后将溶液转移到解吸区以除去至少一部分吸收的酸性组分。 含有环状尿素的部分解吸附的洗涤溶液的至少一部分从解吸区转移到保持在高温下的热转化区,其中至少一部分环脲转化回活化剂。 相对富含酸性组分的来自热转化区的洗涤溶液的一部分被蒸发并返回到解吸区,并且酸性组分中相对贫的另一部分从热转化区返回到吸收区。