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    • 5. 发明申请
    • Aerosol or gaseous decontaminant generator and application thereof
    • 气溶胶或气体净化发生器及其应用
    • US20090321534A1
    • 2009-12-31
    • US11292720
    • 2005-12-02
    • Virgil FlaniganShubhender Kapila
    • Virgil FlaniganShubhender Kapila
    • B05B1/24
    • A61L9/03
    • Disclosed is a generator for the production of an oil based aerosol or a gaseous vapor, which can be used for decontamination of an area, by heating petroleum fuels, plant oils, animal fat derived oils, or light mineral oils in the temperature range of from 250° C. to 800° C., ±5° C. The generator is capable of producing oil particles of a diameter of about 0.04 microns to 3 microns, the most preferred diameter being of about 0.15 microns to 1.5 microns. A condensing trap distal to a concentric tubular oven, which is used to heat the oil, removes non vaporized oil particles from the smoke to produce a gaseous vapor having the advantage of leaving no residue in the area following the decontamination process. An additional filter apparatus controls the size of the oil particles released into the environment.
    • 公开了一种用于生产油基气溶胶或气体蒸汽的发生器,其可以用于对区域进行去污,通过加热石油燃料,植物油,动物脂肪衍生的油或轻质矿物油,其温度范围为 250℃至800℃,±5℃。发生器能够生产直径为约0.04微米至3微米的油颗粒,最优选的直径为约0.15微米至1.5微米。 远离用于加热油的同心管状炉的冷凝阱从烟中除去未汽化的油颗粒,产生气体蒸汽,其具有在除污处理之后的区域中不留下残留物的优点。 附加的过滤装置控制释放到环境中的油颗粒的尺寸。
    • 7. 发明授权
    • Process for the decontamination and treatment with oxidative counterflow
of a liquid, gaseous or solid matrix
    • 用于液体,气态或固体基质的氧化反流的去污和处理方法
    • US6100440A
    • 2000-08-08
    • US29129
    • 1998-06-08
    • Wander TumiattiShubhender Kapila
    • Wander TumiattiShubhender Kapila
    • A62D3/176A62D3/38A62D101/20A62D101/22A62D101/28A62D3/00
    • A62D3/38A62D3/176A62D2101/20A62D2101/22A62D2101/28A62D2203/02
    • The process includes the steps of filling a first reactor (10) with a particulate support (22) comprising a solid matrix to be decontaminated and treated, or a matrix impregnated by a liquid or gaseous matrix to be decontaminated and treated; and introducing at one end (23) of the reactor (10) an oxidative flow triggering a thermoxidation reaction at the opposite end (24) in such a manner that a mobile flame front (26) is generated in the direction opposite (28) to the oxidative flow. The flame front has a temperature of at least 1200.degree. C. so as to substantially decompose or destroy contaminants, undesired substances and compounds initially present in the matrix. Preferably, prior to triggering the thermoxidation reaction, the particulate support (22) is mixed and/or treated with a decontaminating reagent.
    • PCT No.PCT / EP96 / 03682 Sec。 371日期1998年6月8日第 102(e)日期1998年6月8日PCT 1996年8月21日PCT公布。 公开号WO97 / 07858 日期1997年3月6日该方法包括以下步骤:向第一反应器(10)填充包含待净化和处理的固体基质的颗粒载体(22),或由待去污和处理的液体或气体基质浸渍的基质 ; 以及在反应器(10)的一端(23)处引入在相对端(24)处引发热氧化反应的氧化流,使得在相反(28)到(...)的方向上产生可移动火焰前沿(26) 氧化流。 火焰前端具有至少1200℃的温度,以便基本上分解或破坏最初存在于基质中的污染物,不需要的物质和化合物。 优选地,在触发热氧化反应之前,颗粒状载体(22)与去污试剂混合和/或处理。