会员体验
专利管家(专利管理)
工作空间(专利管理)
风险监控(情报监控)
数据分析(专利分析)
侵权分析(诉讼无效)
联系我们
交流群
官方交流:
QQ群: 891211   
微信请扫码    >>>
现在联系顾问~
热词
    • 2. 发明授权
    • Gaseous reagent generator
    • 气态试剂发生器
    • US4357309A
    • 1982-11-02
    • US240158
    • 1981-03-03
    • Sara J. ArnoldKenneth D. Foster
    • Sara J. ArnoldKenneth D. Foster
    • B01J7/02C01B7/13H01S3/095C01B7/18
    • H01S3/095B01J7/02C01B7/135
    • An apparatus and method for generating on demand a gaseous product from a liquid phase reaction of one reactant in the solid phase at ambient room conditions and another reactant in the liquid phase at ambient room conditions. The reactants preferably are iodine crystals, and liquid tetrahydronaphthalene (THN), with the gaseous product being hydrogen iodide. The liquid phase reaction, in the preferred embodiment, is 2I.sub.2 +C.sub.10 H.sub.12 .fwdarw.4HI+C.sub.10 H.sub.8, known per se. Preferably, THN is pumped from a reservoir to be sprinkled over the iodine crystals in another reservoir. Some iodine dissolves into the liquid THN, with the resulting solution then percolating through a reaction zone containing a heated, porous packing material. Heat is transferred to the solution, thereby promoting, i.e., driving the above reaction. The gaseous hydrogen iodide is then removed from the reaction zone; typically for direct use, for example, in a chemical laser. The gaseous HI is generated at sufficiently high flow rates and/or partial pressures to be used in chemical lasers, eg., based on HF, HCl or HBr which operate at about 2700 nm, 3800 nm, and 4100 nm, respectively.
    • 一种用于在环境室条件下根据需要从固相中的一种反应物的液相反应产生气态产物的装置和方法,以及在环境室条件下在液相中的另一种反应物。 反应物优选为碘晶体和液体四氢化萘(THN),气态产物为碘化氢。 在优选实施方案中,液相反应是本身已知的2I2 + C10H12→4HI + C10H8。 优选地,THN从储存器泵送以在另一储存器中的碘晶体上喷洒。 一些碘溶解到液体THN中,所得溶液然后渗透通过含有加热多孔填料的反应区。 将热量转移到溶液中,从而促进,即驱动上述反应。 然后从反应区中除去气态碘化氢; 通常用于直接使用,例如在化学激光中。 气体HI以足够高的流速和/或分压产生,用于化学激光器,例如分别基于在约2700nm,3800nm和4100nm处工作的HF,HCl或HBr。
    • 3. 发明授权
    • Multistage incineration of halogenated hydrocarbon containing waste
streams
    • US4198384A
    • 1980-04-15
    • US850641
    • 1977-11-11
    • Sam P. Robinson
    • Sam P. Robinson
    • B01D53/70C01B7/01F23G5/16F23G7/00C01B7/18C01B7/00C01B7/22
    • B01D53/70C01B7/01F23G5/16F23G7/00Y02P20/129
    • A method and apparatus for disposing of waste material by means of a multi-stage reaction favoring desired reaction products. The rate at which different reactions reach equilibrium at different temperatures and the effects of reaction stoichiometry are controlled by the process to promote desired reactions and discriminate against undesired ones. In the preferred embodiment, the present invention is a method of incinerating chlorinated hydrocarbons comprisingreacting the chlorinated hydrocarbon at high temperature with less than a stoichiometric amount of oxygen for a period of time minimizing generation of nitrogen oxides;quenching the reacting chlorinated hydrocarbon-air mixture with water, whereby phosgene generated in the first part of the reaction is hydrolized, free chlorine is minimized and the temperature of the reacting chlorinated hydrocarbon-air mixture is reduced to a lower temperature to minimize generation of nitrogen oxides;further reacting the chlorinated hydrocarbon-air-steam reaction mixture at said lower temperature for a period of time not long enough to allow the formation of a significant amount of nitrogen oxides;adding additional air to the reacting chlorinated hydrocarbon-air-steam mixture to further reduce the temperature of said reacting mixture and to provide a stoichiometric excess of oxygen and lower the reaction temperature;further reacting said chlorinated hydrocarbon-air-water mixture with said stoichiometric excess of oxygen at said still lower temperature for a period of time long enough to fully react said chlorinated hydrocarbon to HCl, CO.sub.2 and H.sub.2 O, but still sufficiently short to prevent formation of a significant amount of nitrogen oxides;heating water and generating steam from indirect heat exchange with the effluent gas stream; andscrubbing hydrogen chloride gas out of said effluent gas stream.Apparatus is provided to permit this stage-wise reaction and to control the addition of quench water and air, as well as the addition of any additional hydrocarbon fuel, as needed, to insure minimum generation of nascent oxygen and chlorine and nitrogen oxides while insuring substantially all the chlorine in the combustion gas stream is converted into hydrogen chloride.
    • 7. 发明授权
    • Process and device for manufacturing synthetic anhydrous calcium
sulphate and pure hydrofluoric acid
    • 制造合成无水硫酸钙和纯氢氟酸的方法和装置
    • US4460551A
    • 1984-07-17
    • US456090
    • 1982-12-28
    • Dieter BoeseRene Etter
    • Dieter BoeseRene Etter
    • C01B7/19C01F11/46C01B7/08C01B7/18
    • C01B7/195C01B7/192C01F11/46
    • In the process for the production of synthetic anhydrite and pure hydrofluoric acid, a reaction is initiated using fluorspar with a mixture containing sulphuric acid, oleum and the reflux of the acidic scrubbing. The aim is to produce synthetic anhydrite which contains only the desired small proportion of CaF.sub.2, while the free H.sub.2 SO.sub.4 is completely neutralized, but other desirable accelerators are still retained. The reaction is so arranged that fluorosulphonic acid does not enter the reactor at all or only in minute quantity and the new formation of fluorosulphonic acid is effectively repressed. For this end, the components of CaF.sub.2 and acid mixture are fed into the reactor at an elevated temperature and the reactor intake is so heated, whereby the reaction is initiated at 100.degree. C. and thus new formation of fluorosulphonic acid is arrested. The exhaust gases from the reactor are hot-dried in a first stage and the dust is expelled, before the material is cooled in the subsequent stages.
    • PCT No.PCT / CH81 / 00146 Sec。 371日期1982年12月28日 102(e)日期1982年12月28日PCT提交1981年12月28日PCT公布。 公开号WO82 / 03848 日期为1982年11月11日。在生产合成无水石膏和纯氢氟酸的方法中,使用氟石与含硫酸,发烟硫酸和酸性洗涤剂的回流的混合物开始反应。 目的是生产合成的无水石膏,其仅含有所需的小比例的CaF 2,而游离H 2 SO 4完全中和,但仍然保留其它所需的促进剂。 反应如此布置,使得氟磺酸全部或仅以微量的量进入反应器,并且氟代磺酸的新形成被有效地抑制。 为此,将CaF 2和酸混合物的组分在升高的温度下进料到反应器中,并将反应器进料如此加热,由此在100℃开始反应,从而阻止新的氟磺酸形成。 来自反应器的废气在第一阶段被热干燥,并且在随后的阶段中冷却材料之前将粉尘排出。