Application of ozone treatment in cooling water systems for energy and chemical conservation

A. Ataei, M. G. Mirsaeed, Jun-Ki Choi, R. Lashkarboluki
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引用次数: 4

Abstract

In this study, a complete set of recirculating cooling water system and the required instruments were built in a semi-industrial-scale and a 50 g/h ozone generation plant and a chlorine system were designed for cooling water treatment. Both chlorination and ozonation treatment methods were studied and the results were analyzed during two 45-days periods. The concentrations of ozone and chlorine in recirculating water were constant at 0.1 mg/lit and 0.6 mg/lit, respectively. In ozone treatment, by increasing the concentration cycle to 33%, the total water consumption decreased by 26% while 11.5% higher energy efficiency achieved thanks to a better elimination of bio-films. In case of Carbon Steel, the corrosion rate reached to 0.012 mm/yr and 0.025 mm/yr for the ozonation and chlorination processes, respectively. Furthermore, consumptions of the anti-corrosion and anti-sedimentation materials in the ozone cooling water treatment were reduced about 60% without using any oxidant and non-oxidant biocides. No significant changes in sediment load were seen in ozonation compared to chlorination. The Chemical Oxygen Demand of the blow-down in ozonation method decreased to one-sixth of that in the chlorination method. Moreover, the soluble iron and water turbidity in the ozonation method were reduced by 97.5% and 70%, respectively. Although no anaerobic bacteria were seen in the cooling water at the proper concentration range of ozone and chlorine, the aerobic bacteria in chlorine and ozone treatment methods were 900 and 200 CFU/ml, respectively. The results showed that the payback time for the ozone treatment is about 2.6 years.
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臭氧处理在冷却水系统中的应用,以节能和节约化学品
本研究在半工业规模下搭建了一套完整的循环冷却水系统和所需仪器,设计了50 g/h臭氧生成装置和氯系统进行冷却水处理。研究了氯化和臭氧氧化两种处理方法,并分析了两个45天的处理结果。循环水中臭氧和氯的浓度分别为0.1 mg/lit和0.6 mg/lit。在臭氧处理中,通过将浓度循环增加到33%,总用水量减少了26%,同时由于更好地消除了生物膜,能源效率提高了11.5%。对于碳钢,臭氧氧化和氯化工艺的腐蚀速率分别为0.012 mm/yr和0.025 mm/yr。此外,在不使用任何氧化剂和非氧化剂杀菌剂的情况下,臭氧冷却水处理中防腐和抗沉降材料的消耗减少了约60%。与氯化相比,臭氧化中沉积物负荷没有明显变化。臭氧化法排污的化学需氧量降至氯化法的六分之一。此外,臭氧化法的可溶性铁和水浊度分别降低了97.5%和70%。在适宜的臭氧和氯浓度范围内,冷却水中未见厌氧菌,而氯处理和臭氧处理的好氧菌分别为900和200 CFU/ml。结果表明,臭氧处理的投资回收期约为2.6年。
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