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    • 112. 发明授权
    • 교반건조기
    • 混合干燥机
    • KR101274011B1
    • 2013-06-12
    • KR1020120157272
    • 2012-12-28
    • 디엠엔텍 주식회사최기억
    • 최기억
    • C02F11/12C02F3/20B01D1/18B01D11/02
    • C02F11/12B01D1/18B01D11/0257C02F3/206C02F2201/002
    • PURPOSE: A mixing dryer is provided to simultaneously implement operations by integrating and interlinking units for mixing, drying, and sucking. CONSTITUTION: A mixing dryer(100) includes a mixing unit(110), a drying unit(130), and a suction unit(150). The suction unit discharges gas generated from the mixing unit and the drying unit to outside. The mixing unit includes a mixing housing, a mixer(1130), and a pulverizer(1150). The mixer is mounted in the mixing housing, and the pulverizer is mounted in the mixing housing. The mixing housing includes a mixing chamber and a pulverizing chamber. A dryer is arranged at the lower part of the mixer to integrate both inner parts of the mixer and the dryer. The inner part of the suction unit is integrated with the inner parts of the mixer and the dryer.
    • 目的:提供混合干燥器,通过整合和互连单元进行混合,干燥和吸吮,同时实现操作。 构成:混合干燥机(100)包括混合单元(110),干燥单元(130)和抽吸单元(150)。 抽吸单元将从混合单元和干燥单元产生的气体排出到外部。 混合单元包括混合壳体,混合器(1130)和粉碎机(1150)。 混合器安装在混合壳体中,粉碎机安装在混合壳体中。 混合壳体包括混合室和粉碎室。 在搅拌器的下部布置有干燥器,以将混合器的内部部分与烘干机相结合。 抽吸单元的内部与混合器和干燥器的内部部件集成。
    • 113. 发明授权
    • 수중 폭기장치
    • 水下航空装置
    • KR101165660B1
    • 2012-07-16
    • KR1020107008285
    • 2008-09-02
    • 가부시기가이샤 쓰루미세이사쿠쇼
    • 다나카히로유키마츠모토사토시
    • C02F3/20B01D3/04F04D7/02C02F7/00
    • B01F3/04617B01F7/00733B01F7/1635C02F3/206F04D7/02F04D13/086F04D29/2288Y02W10/15
    • [Object] To provide a submersible aerator which can improve its aeration action, reduce load at the time of startup, prevent clogging by foreign objects, reduce maintenance work, and lower production and running costs. [Means for solution] An impeller 4 including blades 4 having partition walls which separate liquid passages 4w and air passages 4a is accommodated within a guide casing 6 for rotation between a lower surface 5d of an intermediate plate having an air suction opening 5s and an upper surface 7u of a suction cover having a liquid suction opening 7s. The liquid passages 4w and the air passages 4a meet through communication portions 4h at radially outer ends of rear-side blade partition walls 4r. Intermediate blades 4m are provided at radially outer ends of the liquid passages 4w. A conical space is defined between the blade lower end surfaces 4d and the suction cover upper surface 7u such that the space, which is wide at a portion adjacent to the liquid suction opening 7s, becomes narrower toward a radially outward region including guide vane tongues. A plurality of support legs 8 and a plurality of straining projections 9 are integrally formed on the lower surface of a peripheral portion of a bottom wall 6d of the guide casing. Sloping surfaces are provided on the top wall upper surface 6o between air-liquid discharge passages such that the sloping surfaces are inclined downward and increase in width in the radially outward direction.
    • 114. 发明授权
    • Oxygen control system and method for wastewater treatment
    • 氧气控制系统及废水处理方法
    • US08980091B2
    • 2015-03-17
    • US13888580
    • 2013-05-07
    • Malcolm E. Fabiyi
    • Malcolm E. Fabiyi
    • C02F3/00
    • C02F3/006C02F3/1268C02F3/1273C02F3/16C02F3/206C02F2209/006C02F2209/08C02F2209/10C02F2209/22C02F2303/06C02F2303/20Y02W10/15
    • A method and system for controlling dissolved oxygen levels in a secondary treatment system of a wastewater treatment facility that can employ a membrane bioreactor in which oxygen introduction into mixed liquor is controlled to prevent bulking and minimize generation of extra cellular polymeric substances. The control is exercised by insuring that dissolved oxygen levels within the mixed liquor do not fall below a minimum system level at which microorganism stress would occur. This is done by setting a minimum dissolved oxygen level control point equal to a sum of the minimum system level and an adjustment factor determined on the basis of oxygen uptake rate and time delays inherent in sensing oxygen levels and changes thereof within the mixed liquor. The minimum system dissolved oxygen level can be continually calculated on the basis of an inferred food to mass ratio that would vary with sensed mixed liquor suspended solids.
    • 一种用于控制废水处理设备的二次处理系统中的溶解氧水平的方法和系统,其可以使用膜生物反应器,其中控制引入混合液体的氧气以防止膨胀并最小化细胞外多聚物质的产生。 通过确保混合液中的溶解氧水平不低于微生物应力发生的最低系统水平来进行控制。 这是通过将最小溶解氧水平控制点设置为等于最小系统水平和基于氧吸收速率和感测氧含量所固有的时间延迟确定的调整因子和其在混合液体中的变化的总和来完成的。 可以根据推测的食物与质量比不断地计算最小系统溶解氧水平,这将随感测到的混合悬浮固体而变化。
    • 115. 发明申请
    • SEPTIC SYSTEM AND METHOD OF TREATING SEWAGE AND GREASE
    • 污水处理系统及其处理方法
    • US20140367332A1
    • 2014-12-18
    • US13916355
    • 2013-06-12
    • Hadi Hillo
    • Hadi Hillo
    • C02F3/28
    • C02F3/006C02F3/1242C02F3/1284C02F3/206C02F3/342C02F2203/006C02F2209/001C02F2209/02C02F2209/03C02F2209/36C02F2209/38Y02E50/343Y02W10/15Y02W10/37
    • A septic system is provided which receives both sewage and fat, oil, and grease (FOG) at an inlet. The inlet provides fluids to a first chamber. A treatment unit is adjacent the inlet. The treatment unit includes a unit for breaking down solids and mixing them with surrounding liquid. Hydro-jetting water and oxygen into the mixture at high or low pressures achieves oxygenation. Jets injecting an enzyme solution provide for maximum contact with the waste. Injection pressure may be selected to achieve rapid oxygenation at a high level. Optionally, the water may be heated. In another form, hot or cold water is injected at selected times. Temperature may be controlled to keep enzymes working properly. Enzymes may be directly injected and carried by liquid that is hydro-jetted into the fluids being treated.
    • 提供一种在入口处接收污水和脂肪,油和油脂(FOG)的化粪池系统。 入口将流体提供给第一室。 处理单元靠近入口。 处理单元包括用于分解固体并将其与周围液体混合的单元。 在高压或低压下将水和水喷射到混合物中实现氧合。 注射酶溶液的喷射器最大限度地与废物接触。 可以选择注射压力以实现高水平的快速氧合。 任选地,水可以被加热。 在另一种形式中,在选定的时间注入热水或冷水。 可以控制温度以保持酶的正常工作。 酶可以被直接注射并由被喷射到待处理的流体中的液体携带。
    • 120. 发明申请
    • Floating Oxygenation Circulator Platform (OCP) with Sub-Vortex Induction Means
    • 具有子涡流感应装置的浮动氧化循环器平台(OCP)
    • US20100093074A1
    • 2010-04-15
    • US12251372
    • 2008-10-14
    • William Frederick Tooley
    • William Frederick Tooley
    • C12M1/06B01F3/04C12M1/09C12R1/00
    • B01F3/04773B01F13/0049C02F3/206C12N13/00Y02W10/15Y02W10/37
    • A floating oxygenation circulator platform (OCP) is disclosed employing sub-vortex induction means to initiate numerous, gentle yet complex, tumbling, swirling, rolling, roiling or rotating sub-vortices spreading outward on the liquid surface. The circulator platform itself sets in motion a non-turbulent, high efficiency, bottom to top, primary toroidal vortex flow. Varied sub-vortex induction means, mounted on, made part of, attached to, extending out from or placed around the body of the circulator platform, induce sub-vortices to increase the surface exposure of the liquid and its contents, including microbes, nutrients and large molecules, to atmospheric oxygen and UV sunlight. The OCP and its sub-vortex induction means taken together act in the manner of a Rotating Inverse Biological Contactor (RIBC), labeled “inverse” because the liquid itself rotates and tumbles its contents into direct contact with the atmosphere and sunlight, in contrast to RBC devices where solid disks rotate in and out of a liquid.
    • 公开了一种浮动氧化循环器平台(OCP),其使用副涡流感应装置来启动在液体表面上向外扩展的许多柔和但复杂的翻滚,旋转,滚动,滚动或旋转副涡流。 循环器平台本身将非湍流,高效率的底部到顶部的主环形涡流流动。 安装在附件,从循环器平台的身体上延伸出或放置在循环器平台的周围的各种副涡流感应装置引起副涡旋,以增加液体及其内容物的表面暴露,包括微生物,营养物质 大分子,大气氧和紫外线。 由于液体本身旋转并使其内容物与大气和阳光直接接触,OCP及其副涡流感应装置以旋转反向生物接触器(RIBC)的方式起作用,标记为“反向”,与 RBC设备,其中固体盘旋转进出液体。