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Ultrafiltration of stone cutting mine wastewater with ceramic membranes―a case study

机译:陶瓷膜超滤石cutting矿山废水的案例研究

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摘要

Wastewater from an open stone cutting mine was ultrafiltered with a silica-modified alumina membrane (pore size 100 nm) and a γ-alumina membrane (pore size 10 nm), in order to remove very fine suspended solids. For the 100 nm membrane the backflushing was used in all experiments to reduce cake layer formation during the filtration. For the 10 nm membrane the effect of backflushing was tested in one experiment. The permeate flux achieved with the 100 nm membrane decreased and continued to decline even after 24 h of filtration. This along with the high reductions of the pure water fluxes indicated the continuous fouling of the membrane. The rinsing of the membrane with the ion exchanged water and soaking of the membrane in diluted nitric acid between the filtration tests was not efficient enough to restore the pure water flux of the membrane. The permeate flux achieved with the 10 nm membrane was almost stable [55 l/(m~2h)j and the fouling of the membrane was much smaller. Backflushing was not beneficial and a higher permeate flux was achieved without backflushing. The permeate quality achieved was similar to the water quality in the receiving lake.
机译:用二氧化硅改性的氧化铝膜(孔径为100 nm)和γ-氧化铝膜(孔径为10 nm)对来自露天石材开采矿山的废水进行超滤,以除去非常细的悬浮固体。对于100 nm膜,在所有实验中均使用反吹以减少过滤过程中形成的滤饼层。对于10 nm膜,在一个实验中测试了反吹的效果。即使在过滤24小时后,使用100 nm膜获得的渗透通量仍会下降并继续下降。这与纯水通量的极大降低一起表明了膜的连续结垢。在过滤测试之间,用离子交换水冲洗膜并将膜浸入稀硝酸中的效率不足以恢复膜的纯净水通量。用10 nm膜获得的渗透通量几乎稳定[55 l /(m〜2h)j,并且膜的结垢小得多。反吹无益,无需反吹即可获得更高的渗透通量。所达到的渗透水质与接收湖的水质相似。

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