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    • 2. 发明授权
    • Process for adiabatic production of mononitrotoluene
    • 绝热生产单硝基甲苯的方法
    • US08907144B2
    • 2014-12-09
    • US13427688
    • 2012-03-22
    • Michael Gattrell
    • Michael Gattrell
    • C07C205/00C07B41/00C07C27/26
    • C07C201/08C07C205/06
    • A process for continuous adiabatic nitration of toluene to mononitrotoluene (MNT). The process yields a product quality of MNT that is comparable to that obtained by isothermal production. The process uses excess toluene, with the reaction rate being controlled to maintain a residual of 0.003-0.102 wt % nitric acid in the spent acid and an orange to red color of the spent acid. Further process conditions include re-concentrated sulfuric acid at 83 to 99 degrees C. with a concentration of sulfuric acid from 66 to 70.5 wt %. This is mixed with nitric acid to generate a mixed acid with 1.0 to 3.8 wt % nitric acid and toluene is added at a rate of 1.1 to 1.71 moles toluene/mole nitric acid. The reactants are mixed in a reactor with an overall average mixing intensity of 5.8 to 19 W/kg of contained solution.
    • 将甲苯连续绝热硝化成单硝基甲苯(MNT)的方法。 该方法产生与通过等温生产获得的MNT相当的MNT的产品质量。 该方法使用过量的甲苯,其反应速率被控制以维持废酸中的0.003-0.102重量%的硝酸残留量和废酸的橙色至红色。 进一步的工艺条件包括在83至99℃下的浓硫酸,浓度为66至70.5重量%的硫酸。 将其与硝酸混合以产生具有1.0至3.8重量%硝酸的混合酸,并以1.1至1.71摩尔甲苯/摩尔硝酸的速率加入甲苯。 反应物在反应器中混合,总体平均混合强度为5.8至19W / kg的所含溶液。
    • 3. 发明授权
    • High volumetric efficiency electrochemical cell design for treatment of low concentrations of contaminants in low conductivity water
    • 高体积效率电化学电池设计,用于处理低电导率水中的低浓度污染物
    • US07232507B2
    • 2007-06-19
    • US10653132
    • 2003-09-03
    • Michael GattrellThierry GuenaBarry MacDougall
    • Michael GattrellThierry GuenaBarry MacDougall
    • C25B9/20C25C7/04C02F1/461
    • C02F1/46109C02F1/4672C02F2001/46142C02F2001/46152C02F2101/18C02F2101/345C02F2103/04
    • An electrochemical cell design is disclosed for the particular application of the electrochemical treatment of contaminants in water. The cell is designed to allow the treatment of low concentrations of contaminants in low conductivity water efficiently, and to be simple to fabricate. The design incorporates tapered inlet and outlet fluid flow manifolds so that the cell pressure drop will be almost entirely due to fluid contacting the electrodes, thus maximising the effective use of the system pump power. A short anode to cathode distance and thin working electrodes are used to minimise resistive electrical power losses. The parallel slacked arrangement of the electrodes and the smooth inlet and outlet designs leads to relatively even distributions of current density and mass transfer resulting in maximal utilisation of the entire active electrode surface area. The electrodes are connected internally in parallel in monopolar stack modules, and the modules are then connected externally in series, with insulating baffles to minimise current by-pass problems. This provides a simple cell construction (a minimum number of simple insulating baffles) while still simplifying the cell wiring and reducing the cell current demand (allowing lighter wiring to be used).
    • 公开了一种用于电化学处理污染物在水中的电化学电池设计。 该电池被设计成能够有效地处理低电导率水中的低浓度污染物,并且制造简单。 该设计包括锥形入口和出口流体流量歧管,使得单元压降几乎完全是由于流体接触电极,从而最大限度地提高系统泵浦功率的有效使用。 使用短的阳极至阴极距离和薄的工作电极来最小化电阻电功率损耗。 电极的平行松弛布置和平滑的入口和出口设计导致电流密度和质量传递的相对均匀的分布,导致整个有源电极表面积的最大利用。 电极在单极堆叠模块内部并联连接,然后将模块串联连接到绝缘挡板上,以最大限度地减少电流旁路问题。 这提供了简单的电池结构(最少数量的简单绝缘挡板),同时还简化了电池布线并降低了电池电流需求(允许使用更轻的布线)。
    • 5. 发明申请
    • PROCESS FOR ADIABATIC PRODUCTION OF MONONITROTOLUENE
    • 用于生产单硝基苯的方法
    • US20130253233A1
    • 2013-09-26
    • US13427688
    • 2012-03-22
    • Michael Gattrell
    • Michael Gattrell
    • C07C201/08
    • C07C201/08C07C205/06
    • A process for continuous adiabatic nitration of toluene to mononitrotoluene (MNT). The process yields a product quality of MNT that is comparable to that obtained by isothermal production. The process uses excess toluene, with the reaction rate being controlled to maintain a residual of 0.003-0.102 wt % nitric acid in the spent acid and an orange to red color of the spent acid. Further process conditions include re-concentrated sulfuric acid at 83 to 99 degrees C. with a concentration of sulfuric acid from 66 to 70.5 wt %. This is mixed with nitric acid to generate a mixed acid with 1.0 to 3.8 wt % nitric acid and toluene is added at a rate of 1.1 to 1.71 moles toluene/mole nitric acid. The reactants are mixed in a reactor with an overall average mixing intensity of 5.8 to 19 W/kg of contained solution.
    • 将甲苯连续绝热硝化成单硝基甲苯(MNT)的方法。 该方法产生与通过等温生产获得的MNT相当的MNT的产品质量。 该方法使用过量的甲苯,控制反应速率以维持废酸中的0.003-0.102重量%的硝酸残留量和废酸的橙色至红色。 进一步的工艺条件包括在83至99℃下的浓硫酸,浓度为66至70.5重量%的硫酸。 将其与硝酸混合以产生具有1.0至3.8重量%硝酸的混合酸,并以1.1至1.71摩尔甲苯/摩尔硝酸的速率加入甲苯。 反应物在反应器中混合,总体平均混合强度为5.8至19W / kg的所含溶液。