首页> 外文会议>International Congress on Membranes and Membrane Processes (ICOM 2002) Vol.4 (Desalination Vol.147) Jul 7-12, 2002 Toulouse, France >Performance of flexible membrane using kaolin dynamic membrane in treating domestic wastewater
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Performance of flexible membrane using kaolin dynamic membrane in treating domestic wastewater

机译:高岭土动力膜柔性膜处理生活污水的性能

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A study using a laboratory experimental rig with a tubular configuration microfiltration fabric membrane in treating secondary effluent from domestic waster treatment plant was carried out. Several inert materials; kaolin (both heavy and light), diatomite and Fuller's earth, were studied to identify an appropriate dynamic membrane material. Heavy kaolin was found to be effective and relatively easily to clean. A rapid decline in flux was observed when filtering the secondary effluent with a turbidity of about 5 NTU without using a dynamic membrane. The development of a heavy kaolin dynamic membrane was found to be a function of the kaolin concentration and crossflow velocity. However varying crossflow velocities within a limited range, such as 1.6 and 2.5 m/s produced a similar steady state flux. Permeate turbidity, which is an indication of the formation status of a dynamic membrane, improved with higher kaolin concentration and reduced with increasing crossflow velocity, within the range considered. The time taken to produce low permeate turbidity (of less than 1 NTU) was shorter with a higher heavy kaolin concentration. A similar steady state permeate turbidity is reached after prolonged filter run despite using a low heavy kaolin concentration. It was also found that a 10-min membraning time at heavy kaolin concentration of 333 mg/l was enough to lay the dynamic membrane before proceeding with filtering the secondary effluent. Permeate turbidity as low as 0.2 NTU could be attained. Secondary effluent was found unsuitable to be applied as a membraning liquid. The purity of membraning or carrier liquid was crucial in the production of an effective dynamic membrane. Feed concentrates turbidity was noticed to increase with the semi-continuous feeding. However, it does not have a significant impact on the permeate turbidity unlike when introducing a new batch of feed regardless of its concentration level.
机译:使用带有管状微滤织物膜的实验室实验装置进行了研究,以处理来自家用废水处理厂的二次废水。几种惰性材料;研究了高岭土(重的和轻的),硅藻土和富勒的土,以确定合适的动态膜材料。发现重的高岭土是有效的并且相对容易清洁。在不使用动态膜的情况下,以约5 NTU的浊度过滤次级污水时,通量会迅速下降。发现高岭土动态膜的发展是高岭土浓度和错流速度的函数。但是,在有限范围内(例如1.6和2.5 m / s)变化的错流速度会产生类似的稳态通量。在所考虑的范围内,渗透性浊度是动态膜形成状态的指示,随着高岭土浓度的增加而改善,而随着错流速度的增加而降低。随着高浓重高岭土浓度的增加,产生低透过率浊度(小于1 NTU)所需的时间更短。尽管使用了低浓度的高岭土,但长时间的过滤运行后仍达到了类似的稳态渗透物浊度。还发现,在高岭土浓度为333 mg / l的情况下,经过10分钟的膜化时间足以在继续过滤次级流出物之前铺好动态膜。渗透浑浊度可低至0.2 NTU。发现次要污水不适合用作膜液体。膜或载液的纯度对于生产有效的动态膜至关重要。饲料浓缩物的浊度随着半连续饲喂而增加。但是,与引入新批次的饲料(无论其浓度水平如何)不同,它对渗透物浊度没有显着影响。

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