首页> 外文期刊>Desalination: The International Journal on the Science and Technology of Desalting and Water Purification >The filtration characteristics of anaerobic digester effluents employing cross flow ceramic membrane microfiltration for nutrient recovery
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The filtration characteristics of anaerobic digester effluents employing cross flow ceramic membrane microfiltration for nutrient recovery

机译:错流陶瓷膜微滤厌氧消化池废水的过滤特性。

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In the present study, a monolithic alumina coated microfiltration ceramic membrane was used for solid particulate removal and nutrient recovery from anaerobic digester complex effluent streams. The aim was to test the effect of the cake layer developed by the solids, on the surface of the membrane channels, to the filterability of these materials. The solid content ranged between 2.6 g/L to 15.1 g/L During practical application, two processing techniques targeting the enhanced recovery of the materials of interest including ammonia, phosphate, calcium bicarbonate and volatile fatty acids, namely dewatering and diafiltration, were used. These had an immediate effect on the solid content (PDS 13 μm to 3.97 μm) enhancing the filterability of the effluents. Their processability was evaluated in terms of flux, cross flow velocity, membrane resistance and cake resistance. An important finding of this study is the nonalignment of the flux rates to the cake resistance, explained by the formation of a compressible, permeable cake layer that allowed the continuous operation of the system, under constant low pressure conditions (TMP15 psi). Permeate flux remained constant to 120 L/m~2 h when applying diafiltration, while when dewatering process is used the permeate flux remained constant at 115.4 L/m~2 h.
机译:在本研究中,整体式氧化铝涂覆的微滤陶瓷膜用于从厌氧消化池复杂废水中去除固体颗粒并回收营养。目的是测试由固体形成的滤饼层在膜通道表面上对这些材料的可过滤性的影响。固体含量在2.6 g / L到15.1 g / L之间。在实际应用中,使用了两种旨在提高目标材料的回收率的处理技术,包括氨,磷酸盐,碳酸氢钙和挥发性脂肪酸,即脱水和渗滤。这些对固体成分(PDS 13μm至3.97μm)有直接影响,可增强废水的过滤性。根据通量,错流速度,膜阻力和滤饼阻力评估了它们的可加工性。这项研究的一个重要发现是通量率与滤饼阻力之间的不一致性,可以通过形成可压缩的,可渗透的滤饼层来解释,该滤饼层允许系统在恒定的低压条件下(TMP15 psi)连续运行。进行渗滤时,渗透通量保持恒定在120 L / m〜2 h,而采用脱水工艺时,渗透通量保持恒定在115.4 L / m〜2 h。

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