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    • 65. 发明申请
    • CONTINUOUS DROPLET GENERATOR DEVICES AND METHODS
    • 连续滴灌发生器装置和方法
    • US20100180765A1
    • 2010-07-22
    • US12689520
    • 2010-01-19
    • Sang Young SonJae Yong LeeJames LockeyGrace LeMasters
    • Sang Young SonJae Yong LeeJames LockeyGrace LeMasters
    • B01D47/05
    • B01D47/05B01D5/0027B01D5/006
    • Continuous droplet generators and methods are provided. In one embodiment, a continuous droplet generator includes an outer housing that defines a working liquid reservoir configured to maintain a working liquid. The continuous droplet generator also includes one or more heaters configured to change the phase of the working liquid and an evaporation-condensation tube positioned at least partially within the outer housing. The evaporation-condensation tube includes a gas inlet configured to receive a particle-containing gas flow, a gas outlet configured to export generated condensed droplets, a wall, an outer wall surface configured to be in contact with the working liquid, and an inner wall surface in contact with the particle-containing gas flow. The vapor is transported to the particle-containing gas flow through the evaporation-condensation tube by diffusion and vapor pressure difference to increase a relative humidity and grow particles within the particle-containing gas flow by nuclei heterogeneous condensation.
    • 提供连续的液滴发生器和方法。 在一个实施例中,连续液滴发生器包括外壳,其限定被构造成维持工作液体的工作液体储存器。 连续液滴发生器还包括被配置为改变工作液体的相位的一个或多个加热器和至少部分地位于外部壳体内的蒸发冷凝管。 蒸发冷凝管包括构造成接收含颗粒的气流的气体入口,被配置为输出产生的冷凝液滴的气体出口,壁,构造成与工作液体接触的外壁表面,以及内壁 表面与含颗粒的气流接触。 通过扩散和蒸汽压差将蒸气输送到通过蒸发冷凝管的含颗粒的气体流中以增加相对湿度,并通过核异质凝结生长含颗粒的气流内的颗粒。
    • 66. 发明授权
    • Closed system for volatile organic compound recycling
    • 封闭系统用于挥发性有机化合物回收利用
    • US5728185A
    • 1998-03-17
    • US718256
    • 1996-09-20
    • Le Roy H. Buchholz, Jr.Loretta P. Buchholz
    • Le Roy H. Buchholz, Jr.Loretta P. Buchholz
    • B05B15/12B01D47/05
    • B05B15/1233Y02P70/36Y10S55/46
    • In the system of the instant invention, volatile organic compounds (VOCs) liberated in the course of solvent-based painting of a workpiece, are recovered. The atmosphere within a closed spray-booth is maintained at a fixed humidity such that vaporized water, supplied in the form of steam or nebulized water vapor, acts as a carrier for VOCs liberated in the course of spray painting or heat curing of a workpiece. The VOCs may be recovered continuously, including during the spray-painting or heat curing of the workpiece. The VOC laden, humidified air is circulated through a condenser such that VOCs dissolved in the water vapor condense and are directed to a recovery means. The water and solvent are separated, recovered and purified for re-use or placed in an appropriate container for disposal, thereby eliminating the usual practice of expelling VOC laden air into the atmosphere. The system is provided with a flame-free heat source to cure the painted workpiece and to guard against the danger of explosion.
    • 在本发明的系统中,回收在工件的溶剂型涂布过程中释放的挥发性有机化合物(VOC)。 封闭的喷雾室内的气氛保持在固定的湿度,使得以蒸汽或雾化水蒸气的形式供应的汽化水作为在喷涂或加热固化工件的过程中释放的VOC的载体。 VOC可以连续地回收,包括在喷涂或加热固化工件期间。 VOC负载的加湿空气通过冷凝器循环,使得溶解在水蒸气中的VOC凝结并被引导到回收装置。 水和溶剂分离,回收和纯化再次使用或放置在适当的容器中进行处理,从而消除将含有VOC的空气排入大气中的通常做法。 该系统配有无焰热源,用于固化涂漆的工件并防止爆炸的危险。
    • 67. 发明授权
    • Apparatus for cleaning solids-laden gas
    • 用于清洁固体载气的装置
    • US4695298A
    • 1987-09-22
    • US547690
    • 1983-11-01
    • Hubertus W. A. A. Dries
    • Hubertus W. A. A. Dries
    • B01D45/12B01D47/05B01D47/06B01D47/10B04C3/00B01D47/12
    • B01D47/06B01D47/10
    • A solids-laden gas is cleaned by introducing a condensing fluid in the gas to saturate the gas and allowing liquid to condense on the solids to form enlarged particles. Liquid separated from the gas with enlarged particles is then atomized in the gas to form agglomerates of liquid and enlarged particles, whereafter the formed agglomerates are separated from the gas. An apparatus for carrying out this process is also described, the apparatus being characterized by a first stage in which means are provided for enlarging solids in a solids-laden gas flow by contact with a condensing fluid, separation of liquid from the gas flow, and a second stage in which means are provided for introducing the separated liquid into the gas flow in a venturi-shaped gas passage member.
    • 通过在气体中引入冷凝流体来使气体饱和并使液体在固体上冷凝以形成扩大的颗粒来清洁固体含量的气体。 然后将气体与扩大的颗粒分离的液体在气体中被雾化以形成液体和增大的颗粒的附聚物,之后形成的附聚物与气体分离。 还描述了用于执行该方法的装置,该装置的特征在于第一阶段,其中提供装置,用于通过与冷凝流体接触,从气体流中分离液体,在固体载气流中扩大固体,以及 提供了用于将分离的液体引入文丘里形气体通道构件中的气流中的装置的第二阶段。
    • 68. 发明授权
    • Sub-micron particle sampler apparatus
    • 亚微米粒子采样器
    • US4677863A
    • 1987-07-07
    • US715319
    • 1985-03-25
    • Don D. GayWilliam G. McMillan
    • Don D. GayWilliam G. McMillan
    • B01D46/54B01D51/10G01N1/22B01D50/00B01D47/05
    • G01N1/2205B01D51/10G01N2001/2223Y10T436/25375
    • Apparatus and method steps for collecting sub-micron sized particles include a collection chamber and cryogenic cooling. The cooling is accomplished by coil tubing carrying nitrogen in liquid form, with the liquid nitrogen changing to the gas phase before exiting from the collection chamber in the tubing. Standard filters are used to filter out particles of diameter greater than or equal to 0.3 microns; however the present invention is used to trap particles of less than 0.3 micron in diameter. A blower draws air to said collection chamber through a filter which filters particles with diameters greater than or equal to 0.3 micron. The air is then cryogenically cooled so that moisture and sub-micron sized particles in the air condense into ice on the coil. The coil is then heated so that the ice melts, and the liquid is then drawn off and passed through a Buchner funnel where the liquid is passed through a Nuclepore membrane. A vacuum draws the liquid through the Nuclepore membrane, with the Nuclepore membrane trapping sub-micron sized particles therein. The Nuclepore membrane is then covered on its top and bottom surfaces with sheets of Mylar.RTM. and the assembly is then crushed into a pellet. This effectively traps the sub-micron sized particles for later analysis.
    • 用于收集亚微米级颗粒的装置和方法步骤包括收集室和低温冷却。 冷却是通过以液体形式携带氮气的盘管来实现的,液体氮在从管道中的收集室离开之前变成气相。 标准过滤器用于过滤直径大于或等于0.3微米的颗粒; 然而,本发明用于捕获直径小于0.3微米的颗粒。 吹风机通过过滤器将空气吸入所述收集室,所述过滤器过滤直径大于或等于0.3微米的颗粒。 然后空气被低温冷却,使得空气中的水分和亚微米尺寸的颗粒在线圈中冷凝成冰。 然后加热线圈使冰融化,然后将液体抽出并通过布氏漏斗,液体通过Nuclepore膜。 真空通过Nuclepore膜吸引液体,Nucleopore膜在其中捕获亚微米级的颗粒。 然后在其顶部和底部表面上用“Mylar TM”片覆盖Nuclepore膜,然后将该组件压碎成颗粒。 这有效地捕获亚微米级的颗粒以供以后分析。
    • 69. 发明授权
    • Energy transfer device for desulfurizing installation
    • 用于脱硫装置的能量转移装置
    • US4619671A
    • 1986-10-28
    • US738735
    • 1985-05-29
    • Klemens RuffLudwig SuhrPaul Paikert
    • Klemens RuffLudwig SuhrPaul Paikert
    • B01D53/50F23J15/08B01D47/05B01D53/14
    • F23J15/08B01D53/504
    • In order to obtain the requisite chimney temperature of cleaned gas discharged from a desulfurizing installation, and in order to avoid problems resulting at temperatures below the dew point of sulfuric acid in heat exchangers made of steel, the invention provides the following measures: the heat exchange between the crude gas stream and the cleaned gas stream is made in a first stage including conventional heat exchangers made of steel. An additional stage of heat exchangers between the crude and cleaned gas streams is constructed of corrosion-resistant and adhesion inhibiting plastic material and operating in a lower temperature range. Transfer conduits of corrosion-resistant material connect the lower temperature heat exchangers to forcibly transfer a heat carrying fluid.
    • 为了获得从脱硫装置排出的净化气体所需的烟囱温度,为了避免由钢制热交换器中的硫酸露点以下的温度导致的问题,本发明提供以下措施:热交换 在粗气流和净化气流之间的第一阶段包括由钢制成的常规热交换器。 在粗气和净化气流之间的另外一段热交换器由耐腐蚀和粘附抑制塑料制成,并在较低的温度范围内运行。 耐腐蚀材料的输送管连接低温热交换器,强制传送载热流体。
    • 70. 发明授权
    • Process for the removal of impurities from a gas stream containing
solvent vapors
    • 从含有溶剂蒸气的气流中除去杂质的方法
    • US4494967A
    • 1985-01-22
    • US502018
    • 1983-04-14
    • Peter Barth
    • Peter Barth
    • B01D53/44B01D5/00B01D53/14B01D53/74B01D53/81B05B15/12B01D53/04B01D47/05
    • B05B15/1233B01D53/14Y02P70/36
    • Solid and liquid, especially high-boiling, impurities are removed from a gas stream containing solvent vapors in such a manner that the gas stream is washed with the condensate of one or more solvent vapors contained in the gas stream, preferably with the fraction which has the greatest affinity for the impurities to be removed. After a distillatory separation of the impurities, as befits the goals of the process, the solvent or solvent mixture used for the washing process is returned again into the process, preferably after it has been removed from the gas stream by condensation and/or adsorption. The gas stream can be returned into a vaporization chamber where it is again charged with solvent vapors.
    • PCT No.PCT / EP82 / 00171 Sec。 371日期1983年4月14日 102(e)日期1983年4月14日PCT提交1982年8月13日PCT公布。 公开号WO83 / 00641 日期1983年3月3日固体和液体,特别是高沸点的杂质从含有溶剂蒸汽的气流中以这样的方式被除去:气流用气流中所含的一种或多种溶剂蒸气的冷凝物洗涤 优选与对杂质去除的亲和力最高的部分。 在杂质的蒸馏分离之后,根据该方法的目的,用于洗涤过程的溶剂或溶剂混合物再次返回到该方法中,优选在通过冷凝和/或吸附从气流中除去之后。 气流可以返回到蒸发室中,在那里再次用溶剂蒸汽充电。