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METHOD OF ION EXCHANGE CLEANING OF SODIUM IODIDE SOLUTION FROM MICROADMIXTURES OF HEAVY METALS AND POTASSIUM

机译:重金属和钾的微混合态离子交换法净化碘化钠的方法

摘要

the invention u043eu0442u043du043eu0441u0438u0442u0441u00a0 chemical technology, in particular to a method of regeneration of inorganic u0438u043eu043du043eu043eu0431u043cu0435u043du043du0438u043au043eu0432 type tin phosphate or titanium phosphate, u043fu0440u0438u043cu0435u043du00a0u0435 u043cu044bu0445 in obtaining highly pure substances, and can be used in the deep treatment of u043au0430u043bu0438u00a0 u043du0430u0442u0440u0438u00a0 salts and other metal impurities.the invention u043fu043eu0437u0432u043eu043bu00a0u0435u0442 at 25 - 30% increase the cleaning solution from u0438u043eu0434u0438u0434u0430 u043du0430u0442u0440u0438u00a0 as traces u0442u00a0u0436u0435u043bu044bu0445 metals. u043fu0440u043eu0432u043eu0434u00a0u0442 u043cu043du043eu0433u043eu0446u0438u043au043bu0438u0447u043du044bu0439 cleaning process u0438u043eu0434u0438u0434u0430 u043du0430u0442u0440u0438u00a0 from impurities u0442u00a0u0436u0435u043bu044bu0445 metals and u043au0430u043bu0438u00a0 including their u0441u043eu0440u0431u0446u0438u044e on u0444u043eu0441u0444u0430u0442u0435 titanium. then u043fu0440u043eu0432u043eu0434u00a0u0442 u0434u0435u0441u043eu0440u0431u0446u0438u044e impurities from the sorbent by coherent processing of first in the 3 to 6 h.nitric acid, and then a neutral solution u0442u0438u043eu0441u0443u043bu044cu0444u0430u0442u0430 u043du0430u0442u0440u0438u00a0 concentration of 2%. 2, table 2).
机译:本发明的化学技术,特别是涉及一种无机的再生方法,该方法是将无机物再生为无机金属的。 u043d u0438 u043a u043e u0432类型的磷酸锡或磷酸钛, u043f u0440 u0438 u043c u0435 u043d u00a0 u0435 u043c u044b u0445可用于获得高纯度的物质,并可用于 u043a u0430 u043b u0438 u00a0 u043d u0430 u0442 u0440 u0438 u00a0盐和其他金属杂质的深层处理。发明 u043f u043e u0437 u0432 u0432 u043e u043e u043b u00a0 u0435 u0442以25-30%的比例将清洁溶液从 u0438 u043e u0434 u0438 u0434 u0430 u043d u04d u0430 u0442 u0440 u0438 u00a0作为痕迹 u0442 u00a0 u0436 u0435 u043b u044b u0445金属。 u043f u0440 u043e u0432 u043e u0434 u00a0 u0442 u043c u043d u043e u0433 u043e u0446 u0438 u043a u043b u0438 u0447 u043d u043d u043b u043b u0439e u0434 u0438 u0434 u0430 u043d u0430 u0442 u0440 u0438 u00a0来自杂质 u0442 u00a0 u0436 u0435 u043b u044b u0445金属和 u043a u0430 u043b u0438 u00a0 u0441 u043e u0440 u0431 u0446 u0438 u044e在 u0444 u043e u0441 u0444 u0430 u0442 u0435钛上。然后通过在3至6 h内首先进行相干处理,从吸附剂中提取杂质,从而从吸附剂中提取出杂质,从而将其从吸附剂中分离出来,然后通过吸附剂将杂质吸附到吸附剂中,并从吸附剂中分离出杂质。 u043f u0440 u043e u0432 u043e u0434 u043e u0432 u0434 u0435硝酸,然后中性溶液浓度为2%时浓度为2%.u0442 u0438 u043e u0441 u0443 u043b u044c u044c u0444 u0430 u0442 u0430 u0430 u043d u0430 u0442 u0440 u0440 u0438 u00a0 2,表2)。

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