首页> 外文期刊>Transactions of the Institutions of Mining and Metallurgy, Section B. Applied Earth Science >Gradual cyanide treatment using AYR and ozone/UV systems with various catalysts in silver mill effluents
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Gradual cyanide treatment using AYR and ozone/UV systems with various catalysts in silver mill effluents

机译:在银厂废水中使用AYR和臭氧/紫外线系统以及各种催化剂对氰化物进行逐步处理

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摘要

Wastewater of a silver processing plant at the Eti Gumus plant located at Kutahya, Turkey was treated with an acidification, volatilisation and reneutralisation (A VR) process for cyanide recovery as a preliminary treatment, and with ozone and ozone/UV light plus catalysts as a secondary treatment. Average NaCN concentrations of slurry with AYR were reduced from 900 + - 50 ppm to 50 + - 10 ppm. Then, oxidation of cyanide in the presence of titanium dioxide, zinc sulphate and copper sulphate as catalysts was investigated and variations in CN~- and CNO~- ion concentrations were measured with a cyanide electrode and ion chromatography, respectively. The reaction time reduced to 12 min with the addition of catalysts when ozone consumption was 0-100 min~(-1) after 25 min with ozone alone and 0-071 g min~(-1) after 20 min for the ozone/UV system. As a result, the most effective method to achieve appropriate discharge values for cyanide with respect to environmental protection laws was the ozone/UV/TiO_2 system with AYR recovery for the effluents of silver ore leaching.
机译:位于土耳其库塔赫亚的Eti Gumus工厂的银加工厂的废水经过酸化,挥发和中和(A VR)工艺进行氰化物回收作为初步处理,并采用臭氧和臭氧/ UV灯加催化剂作为处理材料。二级治疗。带有AYR的浆料的平均NaCN浓度从900 +-50 ppm降低到50 +-10 ppm。然后,研究了在二氧化钛,硫酸锌和硫酸铜作为催化剂存在下氰化物的氧化作用,并分别用氰化物电极和离子色谱法测量了CN_和CNO_离子浓度的变化。当单独使用臭氧25分钟后臭氧消耗为0-100分钟〜(-1),对于20分钟后臭氧/ UV消耗为0-071 g分钟〜(-1)时,添加催化剂将反应时间减少至12分钟。系统。结果,就环境保护法而言,实现氰化物适当排放值的最有效方法是采用臭氧/ UV / TiO_2系统,并用AYR回收银矿石的废水。

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