公开(公告)号：US20110042234A1

公开(公告)日：2011-02-24

申请号：US12989810

申请日：2009-04-26

Applicant: Filip Magalnik

Inventor： Filip Magalnik

IPC: C02F1/461

CPC classification number: C02F1/4676 ,  C02F1/4674 ,  C02F2001/46133 ,  C02F2001/46157 ,  C02F2101/18 ,  C02F2103/10 ,  C02F2103/16 ,  C02F2103/28 ,  C02F2103/365 ,  C02F2201/46145 ,  C02F2209/003 ,  C02F2209/006 ,  C02F2209/04 ,  C02F2209/44

Abstract: Integrated electrolytic and chemical method for producing clean treated water having cyanide species concentration less than 1 mg/liter. (a) Electrolytically treating cyanide-containing water having initial cyanide species concentration less than about 500 mg/liter, via synchronized operation of units: input, electrolytic reactor, recycle, output, and, power supply and process control, forming recycled electrolytically treated cyanide-containing water. (b) Stopping electrolytic treatment when cyanide species concentration decreases to first concentration value of about 10 percent initial concentration, forming recycled electrolytically treated cyanide-containing water of first concentration value inside recycle tank of recycle unit. (c) Chemically treating recycled electrolytically treated cyanide-containing water with in-situ real time freshly generated hypochlorite ion solution electrolytically produced by an in-situ hypochlorite ion solution generating electrolytic reactor assembly in-line with recycle tank. (d) Stopping chemical treatment when cyanide species concentration decreases to second concentration value less than 1 mg/liter, forming clean treated water, (e) output to output unit.

Abstract translation: 用于生产氰化物浓度小于1mg /升的清洁处理水的综合电解和化学方法。 （a）通过单元的同步操作，电化学处理具有初始氰化物浓度小于约500mg /升的含氰化物的水：输入，电解反应器，再循环，输出以及电源和过程控制，形成再循环的电解氰化物 含水。 （b）当氰化物浓度降低至初始浓度约10％的初始浓度值时，停止电解处理，在再循环单元的回收罐内形成第一浓度值的再循环电解处理含氰化物水。 （c）通过原位次氯酸根离子溶液电解生产的原位实时新生产的次氯酸根离子溶液化学处理再循环电解处理的含氰化物的水，产生电解反应器组件与回收罐一致。 （d）当氰化物浓度降至第二浓度值小于1毫克/升时停止化学处理，形成干净的处理水，（e）输出到输出单元。