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首页> 外文期刊>Desalination: The International Journal on the Science and Technology of Desalting and Water Purification >Cross-flow microfiltration using ceramic membranes applied to the cuttlefish effluents treatment:effect of operating parameters and the addition of pre or post-treatment
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Cross-flow microfiltration using ceramic membranes applied to the cuttlefish effluents treatment:effect of operating parameters and the addition of pre or post-treatment

机译:使用陶瓷膜对乌贼废水进行错流微滤:操作参数的影响以及添加前处理或后处理

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Cross-flow microfiltration alone or associated with ultrafiltration or coagulation was conducted to investigate the efficiency of this process in the reducing of chemical oxygen demand (COD) and proteins (Npr) in the waste waters produced from cuttlefish conditioning and freezing process.The study of the effect of operating parameters on the fouling of a ceramic microfiltfation membrane (velocities and pressures) using real effluent showed that the maximum permeate flux was obtained at 5.6 m/s and 2 bar;it was about 120 1/h.m~2.For the same initial COD,the last value increased by 28% and 40% respectively when the conductivity decreased from 50 to 0.6 mS/cm and the pH decreased from 7 to 4.However,the turbidity of the permeate and the retention rates of COD and nitrogen proteins were not affected by the variation of these parameters (0.8 NTU,55% and 60% respectively).The flux enhancement was also studied by using a combination of microfiltration-ultrafiltration and aluminium salt and MgO coagulation-microfiltation.The same performances were obtained in the case of the use of combined SA-MgO-MF and MF-UF.The total resistance of fouling was less important in the latter cases.However,the irreversible resistance remained the main component in all cases.Maximum steady state flux was then 140 1/h.m~2 obtained at the previously determined optimum conditions.The corresponding rejection of COD was better for SA-MgO-MF treatment (75% against 65%).However,the retention rate of nitrogen proteins was better for MF-UF treatment (78% against 57%).
机译:单独进行错流微滤或与超滤或混凝结合进行,以研究该工艺在降低墨鱼调节和冷冻过程产生的废水中减少化学需氧量(COD)和蛋白质(Npr)方面的效率。操作参数对实际流出物对陶瓷微滤膜结垢(速度和压力)的影响表明,最大渗透通量在5.6 m / s和2 bar下获得;约为120 1 / hm〜2。相同的初始COD,当电导率从50降低至0.6 mS / cm,pH值从7降低至4时,最后一个值分别增加28%和40%。但是,渗透液的浊度以及COD和氮的保留率蛋白质不受这些参数变化的影响(分别为0.8 NTU,分别为55%和60%)。还通过微滤-超滤和铝盐和Mg的组合研究了通量增强O混凝-微滤。在结合使用SA-MgO-MF和MF-UF的情况下获得相同的性能。在后一种情况下,结垢的总抵抗力不太重要,但是不可逆阻力仍然是主要成分在所有情况下,在先前确定的最佳条件下获得的最大稳态通量为140 1 / hm〜2.SA-MgO-MF处理的相应COD排斥效果更好(75%对65%)。 MF-UF处理的氮蛋白利用率更高(78%对57%)。

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