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    • 51. 发明授权
    • Water treatment process for membranes
    • 膜的水处理工艺
    • US06416668B1
    • 2002-07-09
    • US09653691
    • 2000-09-01
    • Riad A. Al-Samadi
    • Riad A. Al-Samadi
    • B01D6508
    • B01D61/16B01D61/025B01D61/027B01D61/04B01D61/145B01D61/147B01D2311/04C02F1/441C02F1/444C02F1/56B01D2311/12B01D2311/18B01D2311/2642
    • This invention discloses a cost-effective process for separating contaminants and a wide-range of fouling material from surface water, ground water and from industrial effluents. Having undergone effective pre-treatment, the water can be purified further by using high-surface area spirally wound micro-filtration (MF), ultra-filtration (UF), nano-filtration (NF) or reverse osmosis (RO) membranes. High-quality potable water free from pathogen and other contaminants is thus produced at low-cost from the pre-treated surface water and ground-water. Conversely, pre-treated industrial effluents are further purified at a relatively low-cost using NF or RO membranes, thus producing water suitable for recycle or surface discharge. The process of this invention uses cationic inorganic and/or polymeric flocculants to coagulate and flocculate the water-borne colloidal matter (e.g. clays, iron hydroxides, naturally occurring matter (NOM's), etc.), followed by filtration using a multi-media filter, charge neutralization and reversal and final filtration using a 5-micron cartridge filter. These pre-treatment steps provides a good quality water having a low Silt Density Index and a significant negative zeta potential, thereby ensuring against irreversible chemical fouling of the spirally-wound membranes.
    • 本发明公开了一种从地表水,地下水和工业废水中分离污染物和大范围污染物质的成本有效的方法。 经过有效的预处理后,可以通过使用高表面积螺旋缠绕的微滤(MF),超滤(UF),纳滤(NF)或反渗透(RO)膜进一步净化水。 因此,从预处理的地表水和地下水中以低成本生产不含病原体和其他污染物的高品质饮用水。 相反,使用NF或RO膜,预处理的工业废水以相对低成本进一步纯化,从而产生适于再循环或表面排放的水。 本发明的方法使用阳离子无机和/或聚合物絮凝剂来凝结和絮凝水性胶体物质(例如粘土,氢氧化铁,天然存在物质(NOM)等),然后使用多介质过滤器 ,电荷中和,反转和最终过滤使用5微米滤芯。 这些预处理步骤提供了具有低沉降密度指数和显着的负ζ电位的优质水,从而确保了螺旋缠绕膜的不可逆化学结垢。
    • 52. 发明授权
    • Silica precipitate
    • 二氧化硅沉淀
    • US06312601B1
    • 2001-11-06
    • US09651807
    • 2000-08-30
    • Stephen D. AllenJosh H. Golden
    • Stephen D. AllenJosh H. Golden
    • C02F144
    • B01D65/02B01D61/147B01D61/16B01D2311/04B01D2321/04B01D2321/162B01D2321/164B01D2321/168B01D2321/28C02F1/444C02F1/5236C02F1/56C02F1/583C02F2101/20C02F2103/346B01D2311/18B01D2311/2642
    • A process and system for removing heavy metals, fluoride, silica and other contaminants from large volumes of wastewater is disclosed. In the process, a wastewater stream containing the contaminant is treated with a chemical coagulant to create a particle having a diameter greater than 5 microns. Treated wastewater is passed through a microfiltration membrane which physically separates the metal contaminant particle from the wastewater. Commercially available microfiltration membranes having a pore size from 0.5 micron to 5 microns may be used. The treated wastewater flow rate through the microfiltration membranes can range from 700 gallons per square foot of membrane per day (“GFD”) to 1500 GFD. Solids are removed from the membrane surface by periodically backflushing the micro-filtration membranes and draining the filtration vessel within which the membranes are located. The dislodged solid material within the filtration vessel is flushed into a holding tank for further processing of the solids.
    • 公开了一种用于从大量废水中去除重金属,氟化物,二氧化硅和其它污染物的方法和系统。 在此过程中,用化学凝结剂处理含有污染物的废水流,产生直径大于5微米的颗粒。 经处理的废水通过微生物膜,其将金属污染物颗粒与废水物理分离。 可以使用孔径为0.5微米至5微米的市售微滤膜。 通过微滤膜处理的废水流量可以从每天平均每平方米700加仑(“GFD”)到1500 GFD的范围。 通过周期性地反冲微滤膜并排出膜所在的过滤容器,从膜表面除去固体。 将过滤容器内的移出的固体材料冲入储存罐中以进一步处理固体。