CN104548471A - 一种氰化钾无毒处理的方法 - Google Patents
一种氰化钾无毒处理的方法 Download PDFInfo
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- A62D3/00—Processes for making harmful chemical substances harmless or less harmful, by effecting a chemical change in the substances
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- A—HUMAN NECESSITIES
- A62—LIFE-SAVING; FIRE-FIGHTING
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Abstract
本发明公开了一种氰化钾无毒处理的方法,其方法是先将含氰化钾的溶液加入氢氧化钠溶液,调pH值,使PH>12;接着在上述溶液中加入适量的硫酸亚铁;充分搅拌,生成无毒的亚铁氰化钾。本方法利用络合反应,将主要起毒副作用的游离态氰基(CN-),络合成(Fe(CN)64-)4+一个基团,使其失去活性,以无游离态的氰基存在,从而实现了无毒化。
Description
技术领域
本发明涉及到剧毒物氰化钾的无毒处理的方法,具体的说,是涉及到将剧毒物氰化钾转化成无毒的铁氰化钾的一种处理方法。
背景技术
氰化钾为白色或灰色粉末状结晶,有微弱的氰化氢(苦杏仁)气味的无机剧毒品,主要用于提炼金、银等贵重金属和淬火,并用于塑料、农药、医药、染料等有机合成业。
氰化钾剧毒物品,人口服致死量约为1∽2mg/kg。它的毒性作用是在体内释放氰基(CN-),与氧化型细胞色素氧化酶的Fe3+结合,使细胞色素失去传递电子能力,使呼吸链中断。出现细胞内窒息引起组织缺氧而事毒。
根据国家二类排放标准(GB8978-1996)规定,总氰化物排放一级标准为浓度为不大于0.5mg/L。公司化验室氰化钾废液浓度已超出了工业废水允许排放浓度,因此必须进行处理后方可排放。
发明内容
本发明要解决的技术问题是:提供一种用化学方法处理
氰化钾无毒的方法。
为解决该技术问题,本发明采用的技术方案是:
一种氰化钾无毒处理的方法,其步骤是:
(1)将含氰化钾的溶液加入氢氧化钠溶液,调pH值,使pH>12;
(2)接着在上述溶液中加入适量的硫酸亚铁;
(3)充分搅拌,生成无毒的亚铁氰化钾。
所述步骤1中的pH=13。
所述氰化钾溶液浓度为0.2g/l-1.0g/l。
所述硫酸亚铁的浓度为2%。
所述氢氧化钠溶液的浓度为2%。
本发明的有益效果是:
本发明采用化学处理法处理氰化钾,采用络合法,使CN-失去活性。
反应原理:氰化钾的剧毒主要是游离的氰基。本方法利用络合反应,将主要起毒副作用的游离态氰基(CN-),络合成(Fe(CN)64-)4+一个基团,使其失去活性,以无游离态的氰基存在,从而实现了无毒化。
化学反应式:FeSO4+6KCN=K4[Fe(CN)6]+K2SO4。
具体实施方式
实施例1
取0.2g/l氰化钾溶液100ml,加入2%的氢氧化钠溶液10ml,调pH值至12.8,充分搅拌;加入2%的硫酸亚铁39ml,充分搅拌,生成无毒的亚铁氰化钾。溶液成墨绿色。用0.01∽0.1%CN-根浓度测试纸测不出CN-根的存在。
实施例2
取0.5g/l氰化钾溶液100ml,加入2%的氢氧化钠溶液10ml,调pH值至13,充分搅拌;加入2%的硫酸亚铁97ml,充分搅拌,生成无毒的亚铁氰化钾,溶液成墨绿色。用0.01∽0.1%CN-根浓度测试纸测不出CN-根的存在。
实施例3
取1.0g/l氰化钾溶液100ml,加入2%的氢氧化钠溶液10ml,调pH值至13.2,充分搅拌;加入2%的硫酸亚铁195ml,充分搅拌,生成无毒的亚铁氰化钾,溶液成墨绿色。用0.01∽0.1%CN-根浓度测试纸测不出CN-根的存在。
实验数据
Claims (5)
1.一种氰化钾无毒处理的方法,其步骤是:
(1)将含氰化钾的溶液加入氢氧化钠溶液,调pH值,使pH>12;
(2)接着在上述溶液中加入适量的硫酸亚铁;
(3)充分搅拌,生成无毒的亚铁氰化钾。
2.根据权利要求1所述的一种氰化钾无毒处理的方法,其特征是:所述步骤1中的pH=13。
3.根据权利要求2所述的一种氰化钾无毒处理的方法,其特征是:氰化钾溶液浓度为0.2g/l-1.0g/l。
4.根据权利要求3所述的一种氰化钾无毒处理的方法,其特征是:所述硫酸亚铁的浓度为2%。
5.根据权利要求4所述的一种氰化钾无毒处理的方法,其特征是:所述氢氧化钠溶液的浓度为2%。
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Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB144398A (en) * | 1919-03-14 | 1920-06-14 | John James Hood | Improvements in the recovery of cyanogen from coal gas |
GB250824A (en) * | 1925-09-18 | 1926-04-22 | Jean Denis | Improved process of treating waste liquors containing cyanogen compounds |
US3864453A (en) * | 1972-03-27 | 1975-02-04 | Degussa | Process for the production of alkali ferrocyanide |
CN1562751A (zh) * | 2004-04-05 | 2005-01-12 | 张中富 | 一种以氰化钠为原料生产亚铁氰化钠的工艺控制技术 |
CN101811806A (zh) * | 2010-04-29 | 2010-08-25 | 华南理工大学 | 一种电镀工业混合废水的处理方法 |
-
2013
- 2013-10-15 CN CN201310480655.9A patent/CN104548471A/zh active Pending
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB144398A (en) * | 1919-03-14 | 1920-06-14 | John James Hood | Improvements in the recovery of cyanogen from coal gas |
GB250824A (en) * | 1925-09-18 | 1926-04-22 | Jean Denis | Improved process of treating waste liquors containing cyanogen compounds |
US3864453A (en) * | 1972-03-27 | 1975-02-04 | Degussa | Process for the production of alkali ferrocyanide |
CN1562751A (zh) * | 2004-04-05 | 2005-01-12 | 张中富 | 一种以氰化钠为原料生产亚铁氰化钠的工艺控制技术 |
CN101811806A (zh) * | 2010-04-29 | 2010-08-25 | 华南理工大学 | 一种电镀工业混合废水的处理方法 |
Non-Patent Citations (2)
Title |
---|
M.D.阿当斯: "使用硫酸亚铁除去水溶液中的氰化物", 《国外金属矿选矿》 * |
熊正为: "硫酸亚铁法处理电镀含氰废水的试验研究", 《湖南科技学院学报》 * |
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