哥伦比亚Cundinamarca地区碳酸氢盐和含铁温泉的氯需求

Yuly Sánchez, M. Mehrvar, L. McCarthy, Edgar Quiñones Bolaños, L. Cheu, Alexander Reuβ, Jairo Romero
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摘要

根据阿尔伯塔省和不列颠哥伦比亚省政府公共游泳池条例和德国DIN 19643标准,加拿大和德国对温泉的微生物和物理化学要求与游泳池相同,他们要求在水中添加氯。哥伦比亚的温泉不加氯消毒,只是不断更换水,这并不能保证温泉的微生物质量。关于哥伦比亚温泉对氯的需求的研究很少,因为由于要求使用天然水源,其水质没有得到管制。在我们的研究中,对哥伦比亚Cundinamarca地区的碳酸氢盐和含铁温泉进行了实验室测试,以确定氯的需求。试验按照标准方法2350进行,每次试验重复3次,接触时间为10分钟,氯浓度为100.47 mg/L Cl 2。对碳酸氢盐温泉进行了氯用量为0.5 ~ 10.0 mg/L Cl 2、间隔为1.0 mg/L Cl 2的试验,得到了典型的氯需要量曲线,氯需要量为5 mg/L Cl 2。在含铁温泉的情况下,剂量间隔是不同的,并且在浓度超过12毫克/升氯化钠的情况下进行了额外的试验,其中没有获得氯化断点以确定氯的需求量。只有在水与有机物质和金属发生反应且不进行消毒的情况下才能得到化合氯。在德国,不希望有机物氧化形成消毒副产物(DBPs)。为了实现这一目标,主要的努力归功于在添加氯之前对有机物进行过滤,从而在很大程度上避免了dbp的形成。因此,在今后的工作中,重要的是研究如何在这类含铁温泉中进行化学产品消毒,以确定足够的氯剂量,以满足对氯的需求,并保持残氯以消除足够的致病微生物。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Chlorine Demand In Bicarbonated And Ferruginous Hot Springs In The Cundinamarca Region, Colombia
Canada and Germany apply the same microbial and physical-chemical requirements to hot springs as for swimming pools in accordance with the Alberta and British Columbia Government Public Swimming Pool Regulations and the German DIN 19643 Standard, where they require the addition of chlorine to their waters. Chlorine is not added to hot springs in Colombia for the disinfection of their waters, only a constant replacement of the water is carried out, which does not guarantee the microbiological quality of hot springs. There has been little research on the demand for chlorine in hot springs in Colombia because by requiring water of natural origin, the quality of their waters is not regulated. In our study, laboratory tests were carried out with bicarbonated and ferruginous hot springs in the Cundinamarca region of Colombia, to determine the chlorine demand. The tests were carried out as established by Standard Methods 2350 with three replicates of each test for a contact time of 10 minutes and a chlorine concentration of 100.47 mg/L Cl 2 . For the bicarbonated hot spring, tests were carried out with chlorine doses of 0.5 to 10.0 mg/L Cl 2 with intervals of 1.0 mg/L Cl 2 , where the typical chlorine demand curve was obtained, with a chlorine demand of 5 mg/L Cl 2 . In the case of the ferruginous hot spring, the dose intervals were varied and additional tests were obtained with concentrations above 12 mg/L Cl 2 where the breakpoint chlorination was not obtained to determine the chlorine demand. Only combined chlorine was obtained where water reacts with organic materials and metals and disinfection does not occur. In Germany, the oxidation of organic matter, forming disinfection-by-products (DBPs), is not desired. In order to achieve this, the main effort is attributed to the filtration of the organic matter before addition of chlorine, thus largely avoiding the formation of DBPs. For this reason, it is important in future work to investigate how disinfection with chemical products could be carried out in this type of ferruginous hot springs to determine the dose of chlorine sufficient to satisfy the demand for chlorine and maintain a residual chlorine to eliminate enough pathogenic microorganisms.
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