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首页> 外文期刊>Journal of Chemical Technology & Biotechnology >Removal of suspended solids and residual oil from palm oil mill effluent
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Removal of suspended solids and residual oil from palm oil mill effluent

机译:去除棕榈油厂废水中的悬浮固体和残油

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Palm oil mill effluent (POME) was pretreated to remove suspended solids and residual oil. The processes used were flocculation, solvent extraction, adsorption and membrane separation. Flocculation was used to remove suspended solids, and solvent extraction and adsorption processes were used to remove residual oil. Membrane separation was subsequently applied to remove any residual suspended solids and oil remaining after the pretreatments. The solvent extraction and adsorption processes were operated on a batch basis whereas membrane separation was performed in continuous mode. The treatment efficiency of the processes was measured as percentage removal of suspended solids and oil respectively. The optimum values of the process parameters obtained in the flocculation process were an alum dosage of 4000 mg dm(-3), mixing speed of 150 rpm for 1 h and sedimentation time of 270 min, resulting in 93% suspended solids removal. In the solvent extraction process, a 95% reduction in residual oil was obtained using n-hexane as a solvent with 20 min of mixing at 200 rpm. The ratio of solvent to POME was 6: 10 and carried out at pH 9. In the batch adsorption process, an 88% reduction in residual oil was obtained at a mixing speed of 100 rpm for 1 h, pH 9 and an adsorbent dosage of 300 g dm(-3). In membrane separation processes, GH and CE(GH) membranes gave 63% and 49% reductions in suspended solids and residual oil respectively at pH 9 and pressure of 1000 kPa. (C) 2003 Society of Chemical Industry.
机译:对棕榈油厂的废液(POME)进行了预处理,以除去悬浮的固体和残余油。使用的过程是絮凝,溶剂萃取,吸附和膜分离。絮凝用于去除悬浮的固体,溶剂萃取和吸附过程用于去除残留的油。随后进行膜分离以除去预处理后残留的任何残留的悬浮固体和油。溶剂萃取和吸附过程分批进行,而膜分离以连续模式进行。该方法的处理效率分别以悬浮固体和油的去除百分比来测量。在絮凝过程中获得的工艺参数的最佳值为明矾剂量为4000 mg dm(-3),混合速度为150 rpm,持续1 h,沉降时间为270 min,从而去除了93%的悬浮固体。在溶剂萃取过程中,使用正己烷作为溶剂,在200 rpm下混合20分钟,可以减少95%的残留油。溶剂与POME的比例为6:10,pH值为9。在间歇吸附过程中,在100 rpm的混合速度,pH 9和1的吸附剂量下,残留油减少了88%。 300克dm(-3)。在膜分离过程中,GH和CE(GH)膜在pH 9和1000 kPa压力下的悬浮固体和残油分别减少了63%和49%。 (C)2003年化学工业协会。

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