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    • 81. 发明申请
    • METHOD AND MEANS FOR FILTERING AN AIR STREAM WITH AN AQUEOUS FROTH
    • 用空气流过滤空气流的方法和手段
    • WO01024909A1
    • 2001-04-12
    • PCT/US2000/027771
    • 2000-10-04
    • B01D39/16B01D46/12B01D47/02B01D47/04B01D50/00
    • B01D50/006B01D47/021B01D47/04
    • A method and means (20) for filtering an air stream with an aqueous froth are provided. The process includes: passing a contaminated air stream through a diffusing sieve (56), into an aqueous solution in an expansion chamber (24); generating, maintaining, and containing an aqueous froth (27) between the liquid bath reservoir (72) and a saturated fiber element (42); and continually saturating a coarse fiber element (42) with liquid from the aqueous solution (72). The froth (27) is generated and maintained, and the fiber element (42) is saturated, by controlling the dynamic interface between the contaminated air stream and the liquid bath reservoir (72). The means for filtering an air stream includes: an air filter device (20) that incorporates a liquid bath filter initial stage (72); an aqueous froth filter second stage (27); a constantly saturated, coarse fiber filter (42) as a third stage and froth limiting means (42); and a moist, fine fiber filter (44) as the final stage.
    • 提供了一种用水性泡沫过滤空气流的方法和装置(20)。 该方法包括:使污染的空气流通过扩散筛(56)进入膨胀室(24)中的水溶液中; 产生,保持和容纳液体储存器(72)和饱和纤维元件(42)之间的水性泡沫(27); 并用来自水溶液(72)的液体连续地使粗纤维元件(42)饱和。 产生并保持泡沫(27),通过控制被污染的空气流和液槽储存器(72)之间的动态界面,使纤维元件(42)饱和。 用于过滤空气流的装置包括:包含液浴过滤器初始阶段(72)的空气过滤器装置(20); 水性泡沫过滤器第二级(27); 作为第三级的恒定饱和的粗纤维过滤器(42)和泡沫限制装置(42); 和作为最后阶段的潮湿的细纤维过滤器(44)。
    • 84. 发明授权
    • Method and apparatus for multi-stage air treatment system
    • 多级空气处理系统的方法和装置
    • US08128742B1
    • 2012-03-06
    • US12802435
    • 2010-06-08
    • Thomas R. McGuffin
    • Thomas R. McGuffin
    • B01D47/02
    • B01D47/021A61L9/145A61L2209/14B01D47/04B01D2247/14
    • Method and apparatus for treating air containing hydrogen sulfide gas, volatile organic compounds, heavy metals and other mercaptans in order to reduce odor and corrosion related to wet wells, dry pits, grease traps and the like. The system comprises a first and second stage air treatment system. A vacuum pump in the primary (stage 2) treatment housing vacuums the contaminated air from the source and pumps the air through a set of diffusers into a treatment fluid wherein the air is then passed through a pair of porous plates and upward through a discharge pump and then into the atmosphere. Prior to treating the air in the primary housing, it is treated in a pretreatment dry air filter wherein the air is inlet into the pretreatment (stage 1) housing and then through a microfilter prior to being passed into the primary housing for further treatment.
    • 用于处理含有硫化氢气体,挥发性有机化合物,重金属和其他硫醇的空气的方法和装置,以减少与湿井相关的气味和腐蚀,干燥凹坑,油脂捕集器等。 该系统包括第一和第二级空气处理系统。 初级(阶段2)处理壳体中的真空泵将来自源的污染空气抽真空并将空气通过一组扩散器泵送到处理流体中,其中空气然后通过一对多孔板并向上通过排出泵 然后进入大气层。 在处理主壳体中的空气之前,将其在预处理干燥空气过滤器中进行处理,其中空气入口到预处理(阶段1)外壳中,然后通过微型过滤器,然后进入主壳体进行进一步处理。
    • 90. 发明授权
    • Method for reducing the amount of coal dust in the environment
surrounding coal mining
    • 减少采煤环境中煤尘量的方法
    • US4380459A
    • 1983-04-19
    • US308222
    • 1981-10-05
    • David I. Netting
    • David I. Netting
    • B01D47/04E21F5/16E21C7/06
    • E21F5/16B01D47/04
    • Coal dust laden air is treated with an aqueous foam of controlled durability and controlled penetrability so that a very high proportion of the particles in the air, including very small particles, are captured by the foam and drained into the liquid resulting from the collapse of the foam. The foam has a propensity to collapse during a brief period, thus forming drainage liquid. The volume of drainage liquid five minutes after foam generation provides a measure of the controlled durability of the foam. The usefulness of the foam is also affected by the rate at which the liquid resulting from foam collapse is absorbed into absorbtive materials, which rate should desirably be slower than the absorption rate of water. The precursor for the foam is a very dilute aqueous solution containing a surfactant plus a synthetic gum in a concentration from about 15 percent to about 45 percent of the weight of the surfactant. An appropriate mixture of sodium salts of alkylated benzene sulfonic acids is an effective surfactant which can be combined with about 35 percent of sodium carboxymethylcellulose having a substitution range from about 0.38 to about 0.48 and a sodium content near 5 percent plus or minus 0.5 percent which type of sodium carbomethoxycellulose is marketed as 7H-4 type of cellulose gum. Such gum has a viscosity of about 3,500 centipose plus or minus 1,000 centipoise when dispersed as a 1 percent solution in water.
    • 含尘粉尘的空气用具有受控耐久性和受控的渗透性的含水泡沫处理,使得空气中包括非常小的颗粒在内的非常高比例的颗粒被泡沫捕获并排放到由于 泡沫。 泡沫在短时间内有倾倒倾向,从而形成排水液体。 泡沫发生后5分钟的排水液体积可以测量泡沫的受控耐久性。 泡沫的有效性还受到泡沫破裂所产生的液体吸收到吸收材料中的速率的影响,该速率应优选比水的吸收速度慢。 泡沫的前体是含有表面活性剂加合成胶的非常稀的水溶液,其浓度为表面活性剂重量的约15%至约45%。 烷基化苯磺酸的钠盐的适当混合物是有效的表面活性剂,其可以与约35%的羧甲基纤维素钠混合,其取代范围为约0.38至约0.48,钠含量接近5%加或减0.5% 的甲基甲氧基纤维素钠作为7H-4型纤维素胶市售。 当以1%的水溶液分散时,这种口香糖具有约3,500厘泊的粘度加上或减去1,000厘泊。