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    • 3. 发明申请
    • UV LIQUID STERILISER
    • 紫外线液体灭菌器
    • US20140328985A1
    • 2014-11-06
    • US14343692
    • 2012-08-30
    • Malcolm Robert Snowball
    • Malcolm Robert Snowball
    • A23L3/28A23L2/50
    • A23L3/28A23C3/076A23L2/50A23V2002/00C02F1/325C02F2201/3223C02F2201/3227C02F2201/328C02F2209/09C02F2209/40C02F2301/024C02F2301/08C02F2303/04C12H1/165
    • A fluid steriliser comprising a fluid duct having a UV transmissive wall providing a surface area for irradiation, wherein the cross section of the duct is between 1×10−4 m2 and 5×10−2 m2 and the thickness of the duct defines the depth of fluid flow adjacent the UV transmissive wall of no more than 50mm; a source of UV radiation arranged to irradiate fluid flowing in the duct through the UV transmissive wall such that the UV radiation incident on fluid in the duct has a UV power density; a plurality of mixing stages configured to provide turbulent flow in the fluid and spaced apart along the length of the duct wherein the segments of the duct between the mixing stages are arranged to provide flow adjacent the UV transmissive wall; a flow control means arranged to control the linear speed of fluid flow along the duct based on the length of the duct and the UV power density so that at least 300 Joules of UV energy per square metre of the surface area for irradiation is provided to the fluid during the dwell time of the fluid in the duct.
    • 一种流体灭菌器,包括具有提供用于照射的表面积的UV透射壁的流体管道,其中所述管道的横截面在1×10 -4 m 2和5×10 -2 m 2之间,并且所述管道的厚度限定深度 的流体流动邻近UV透射壁不超过50mm; UV辐射源被布置成通过UV透射壁照射在管道中流动的流体,使得入射在管道中的流体的UV辐射具有UV功率密度; 多个混合阶段被配置为在流体中提供湍流并沿着管道的长度间隔开,其中混合阶段之间的管道段被设置成提供邻近UV透射壁的流动; 流量控制装置,其布置成基于管道的长度和UV功率密度来控制沿着管道的流体流动的线速度,使得每平方米的用于照射的表面积的至少300焦耳的紫外线能量被提供给 流体在管道中的流体停留时间内的流体。
    • 4. 发明申请
    • Method And Apparatus For Treating Tailings Using Alternating Current
    • 使用交流电处理尾矿的方法和装置
    • US20140008229A1
    • 2014-01-09
    • US13765924
    • 2013-02-13
    • DPRA CANADA INCORPORATED
    • Paul GarciaBruce S. BeattieBen HarrisDoug KimzeyRobert C. ParrottJames Micak
    • C02F1/48
    • C02F1/48C02F1/04C02F1/4698C02F2101/325C02F2103/10C02F2201/46135C02F2201/4615C02F2201/46175C02F2209/09
    • There is a method described of treating tailings which are composed of at least some water and clay particles. Within the tailings, at least some water molecules are weakly bond to the clay particles to form a gel like fluid from which water does not readily separate. An alternating current is applied to the tailings to change the electro-chemical properties of the tailings to reduce the weak bonding between the water and the clay particles so that water within the treated tailings is able to separate. Water within the treated tailings is then allowed to separate without further application of electricity. In some embodiments, the treated tailings are allowed to separate through evaporation. Liquid tailings may also be treated with alternating current by applying alternating current to the liquid tailings at a voltage gradient range of 1 to 5 V/cm for a total duration of 24 to 300 hours. The application of alternating current may further comprise applying alternating current at a frequency of 1 to 30 Hz.
    • 有一种处理由至少一些水和粘土颗粒组成的尾矿的方法。 在尾矿中,至少一些水分子与粘土颗粒很弱地结合,形成凝胶,如水不容易分离出来的凝胶。 向尾矿施加交流电流以改变尾矿的电化学性质,以减少水和粘土颗粒之间的弱结合,使得经处理的尾矿中的水能够分离。 然后允许经处理的尾矿中的水分离,无需进一步施加电力。 在一些实施方案中,经处理的尾矿经蒸发分离。 液态尾矿也可以用交流电处理,通过在1至5V / cm的电压梯度范围内向液体尾矿施加交流电,总持续时间为24至300小时。 交流电的应用还可以包括以1至30Hz的频率施加交流电。
    • 5. 发明申请
    • CONTROL OF IMMERSED MEMBRANE SYSTEM CONSIDERING ENERGY COST FLUCTUATIONS
    • 考虑能源成本波动的渗透膜系统的控制
    • US20130043188A1
    • 2013-02-21
    • US13212310
    • 2011-08-18
    • Michael David THEODOULOU
    • Michael David THEODOULOU
    • B01D65/00C02F1/44B01D61/00
    • B01D61/22B01D2311/10B01D2311/16B01D2315/06B01D2321/185C02F1/008C02F3/1273C02F2209/006C02F2209/008C02F2209/02C02F2209/09C02F2209/40C02F2303/16C02F2303/20Y02W10/15
    • An immersed membrane filtration system is operated in view of an electricity pricing programs in which the price of electricity varies over time. Examples of such programs include time of use pricing, critical peak pricing and critical peak rebate programs. Alternatively, the filtration system may be operated, for example as part of a smart grid, in view of requests or demands by an electrical utility for time limited reductions in energy use. During a high energy cost period of time, one or more membrane units are shut down. Preferably, aeration of the still operating membrane units is not increased. The flux of the still operating trains may be increased towards a pre-determined maximum permitted flux, or towards a maximum flux that is calculated in view of operational parameters such as water temperature or viscosity. Optionally, during a low energy cost period of time, one or more additional membrane units may be turned on. Optionally, the transfer of water from an equalization tank may also be controlled in view of the energy pricing program.
    • 考虑到电力价格计算,电力价格随时间变化,运行浸入式膜过滤系统。 这些计划的例子包括使用时间定价,临界峰值定价和关键的高峰退税计划。 或者,考虑到电力公司对于能量使用的时间限制的减少的要求或要求,过滤系统可以被操作,例如作为智能电网的一部分。 在高能耗成本期间,关闭一个或多个膜单元。 优选地,仍然工作的膜单元的曝气不增加。 静止操作列车的通量可以朝着预先确定的最大允许通量增加,或者朝向根据操作参数例如水温或粘度计算的最大通量增加。 可选地,在低能耗成本期间,可以接通一个或多个附加的膜单元。 可选地,还可以根据能量定价程序来控制来自均衡罐的水的转移。