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Dynamic modelling of a forward osmosis-nanofiltration integrated process for treating hazardous wastewater

机译:正渗透-纳滤一体化工艺处理有害废水的动态建模

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Dynamic modelling and simulation of a nanofiltration-forward osmosis integrated complete system was done along with economic evaluation to pave the way for scale up of such a system for treating hazardous pharmaceutical wastes. The system operated in a closed loop not only protects surface water from the onslaught of hazardous industrial wastewater but also saves on cost of fresh water by turning wastewater recyclable at affordable price. The success of dynamic modelling in capturing the relevant transport phenomena is well reflected in high overall correlation coefficient value (R (2) > 0.98), low relative error (< 0.1) and Willmott d-index (< 0.95). The system could remove more than 97.5 % chemical oxygen demand (COD) from real pharmaceutical wastewater having initial COD value as high as 3500 mg/L while ensuring operation of the forward osmosis loop at a reasonably high flux of 56-58 l per square meter per hour.
机译:进行了纳滤-正向渗透综合完整系统的动态建模和仿真,并进行了经济评估,从而为此类处理危险药物废物的系统的规模化铺平了道路。该系统以闭环运行,不仅可以保护地表水免受有害工业废水的冲击,还可以通过以可承受的价格回收可循环利用的废水来节省淡水成本。动态建模在捕获相关运输现象方面的成功表现在较高的整体相关系数值(R(2)> 0.98),较低的相对误差(<0.1)和Willmott d-指数(<0.95)中。该系统可从实际初始COD值高达3500 mg / L的制药废水中去除97.5%以上的化学需氧量(COD),同时确保以每平方米56-58 l的合理高通量运行正向渗透回路每小时。

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