The Effect of Cone Area Variations on the Continuous Discharges Flow (CDF) Method Sedimentation Unit as a New Method for Raw Water Turbidity Removal

Ridwan Ridwan, Reri Afrianita, Aulia Massyaf Putri, Reski Anggika
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Abstract

The Sedimentation Unit Continuous Discharges Flow (CDF) method is a modification by adding a continuous and controlled discharge flow as a net force acting on the particles to increase the efficiency of turbidity removal by applying the principle of a leaky tank at the bottom of the settling zone. The production capacity of the sedimentation unit using the CDF method is reduced due to the CDF flow of 6% of the flow rate so it needs to be recirculated. This study aims to maintain the production flow rate of the system and increase the efficiency of turbidity removal by recirculating the CDF flow. The research reactor consisted of a coagulation unit, flocculation unit, and sedimentation method using 6% CDF with a flow rate of 240 L/hour and 360 L/hour, and variations in the recirculation flow of 6% CDF to the flocculation unit were 0%, 25%, 50%, 75%, and 100 %. The sedimentation detention time at a flow rate of 240 L/hour and 360 L/hour was 90 minutes and 60 minutes, respectively. Research on a laboratory scale with raw water turbidity of 25,536 NTU. The results showed that the greater the CDF flow recirculation value, the higher the turbidity removal efficiency. Rank Spearman analysis, the correlation value of the CDF flow recirculation value to the efficiency of removal of turbidity is 0.980 and the significance value is 0.00 which means strong and significant. The highest turbidity removal efficiency was achieved at the 100% CDF flow recirculation value, ie at 240 L/hour flow rate was 87.21% with final turbidity 3.267 NTU, while at 360 L/hour flow rate was 82.50% with final turbidity 4,528 NTU. Uprating the flow rate in the experiment was able to produce a final turbidity value that met the drinking water quality standard, which was 5 NTU
锥面积变化对CDF法沉降装置作为原水除浊新方法的影响
沉淀池连续排放流(CDF)方法是一种改进方法,通过在沉降区底部应用漏槽的原理,增加连续和受控的排放流作为作用于颗粒的净力,以提高除浊效率。采用CDF法的沉降装置,由于CDF流量为流量的6%,生产能力降低,需要再循环。本研究旨在维持系统的生产流量,并通过循环CDF流来提高除浊效率。研究反应器由混凝装置、絮凝装置和沉淀法组成,采用6% CDF,流速分别为240 L/h和360 L/h, 6% CDF到絮凝装置的再循环流量变化分别为0%、25%、50%、75%和100%。在240 L/h和360 L/h的流速下,沉淀滞留时间分别为90 min和60 min。原水浊度25,536 NTU的实验室规模研究。结果表明,CDF流量再循环值越大,除浊效率越高。通过Spearman分析,CDF流量再循环值与除浊效率的相关值为0.980,显著性值为0.00,表示较强且显著。在100% CDF流量再循环值下,浊度去除率最高,即240 L/h流量下,浊度去除率为87.21%,最终浊度为3.267 NTU; 360 L/h流量下,浊度去除率为82.50%,最终浊度为4528 NTU。在实验中提高流量,最终浊度值为5 NTU,达到饮用水水质标准
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