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    • 4. 发明授权
    • Process for biologically removing phosphorus and nitrogen from
wastewater by controlling carbohydrate content therein
    • 通过控制碳水化合物含量从废水中生物去除磷和氮的方法
    • US5833856A
    • 1998-11-10
    • US896662
    • 1997-07-18
    • Yanhua LiuZaoyan Yang
    • Yanhua LiuZaoyan Yang
    • C02F3/30
    • C02F3/308
    • The present invention relates to a process and a treatment system for biologically removing phosphorus and nitrogen from wastewater. In the anaerobic contact and settlement zone 1, wastewater 7 is first mixed with the returned activated sludge 8 to form a mixed liquor which is then allowed to settle in zone 1, and organic matters present in influent are mostly taken up by the sludge. The supernatant from zone 1 is passed through an aerobic reaction zone 2, furnished with packings, for complete nitrification; the settled sludge from zone 1 is hold in an anaerobic zone 3 for a sufficient period of time for controlling the sludge carbohydrate content to low levels in order to enlarge the sludge capacity for phosphorus removal because the extended anaerobic sludge degradation in zone 3 is very effective in controlling the sludge carbohydrate content to low levels. The sludge from zone 3 is then allowed to be remixed with the nitrified supernatant from zone 2 in zone 4, where the products of the extended anaerobic reaction allowed very high denitrification rates and efficiencies. The aerobic zone 5 is supplemented to complete phosphorus uptake by the activated sludge, in which the dissolved oxygen (DO) level is controlled at relatively low levels in order to limit the aerobic synthesis of sludge carbohydrate. The aerated mixed liquor is then transferred into a final clarifier where settled sludge is separated from purified supernatant. At least a portion of the settled sludge is recycled back to zone 1 to be mixed with raw wastewater, while a portion of the settled sludge is wasted.
    • 本发明涉及从废水中生物去除磷和氮的方法和处理系统。 在厌氧接触和沉降区1中,首先将废水7与返回的活性污泥8混合,形成混合液,然后使其在区域1中沉降,并且存在于流入物中的有机物主要被污泥吸收。 来自区域1的上清液通过需氧反应区2,配有填料,用于完全硝化; 来自区域1的沉降污泥在厌氧区3中保持足够的时间,以便将污泥碳水化合物含量控制在低水平,以便扩大污泥的除磷能力,因为区域3中延长的厌氧污泥降解非常有效 将污泥碳水化合物含量控制在较低水平。 然后将来自区域3的污泥与区域4中的区域2的硝化上清液重新混合,其中延长厌氧反应的产物允许非常高的脱氮率和效率。 补充好氧区5以通过活性污泥完成磷吸收,其中将溶解氧(DO)水平控制在相对低的水平,以限制污泥碳水化合物的需氧合成。 然后将充气混合液转移到最终的澄清器中,其中沉淀的污泥与纯化的上清液分离。 至少一部分沉淀的污泥被循环回到区域1以与原始废水混合,而一部分沉降的污泥被浪费。