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硫对含草酸钠铝酸钠溶液蒸发排盐的影响
引用本文:魏国令,李军旗,陈朝轶,刘龙,杨夏琼. 硫对含草酸钠铝酸钠溶液蒸发排盐的影响[J]. 有色金属(冶炼部分), 2016, 0(7): 26-29
作者姓名:魏国令  李军旗  陈朝轶  刘龙  杨夏琼
作者单位:贵州大学材料与冶金学院 贵州,贵州省冶金工程与过程节能重点实验室S贵州;贵州大学材料与冶金学院 贵州,贵州省冶金工程与过程节能重点实验室S贵州;贵州大学材料与冶金学院 贵州,贵州省冶金工程与过程节能重点实验室S贵州;贵州大学材料与冶金学院 贵州,贵州省冶金工程与过程节能重点实验室S贵州;贵州大学材料与冶金学院 贵州
基金项目:国家自然科学基金资助项目(51264006,51474079);贵州省教育厅项目(黔教合重大专项字[2012]0002);贵州省校合作项目(LH[2014]7609)
摘    要:通过添加不同量的硫酸钠和硫化钠,研究硫对含一定浓度草酸钠(Ns)的铝酸钠溶液蒸发排盐的影响。结果表明,当Ns=6g/L时,硫酸钠对铝酸钠溶液中Na_2CO_3、硫盐、Na_2C_2O_4和NaAlO_2的结晶析出均有影响,随着添加量的增加,盐析出率均增大,排盐率也增大,当Ns=6g/L时,排盐率达到92.02%,排盐渣中存在Na_2CO_3、Na_2C_2 O4、NaAlO_2·1.25H_2O、Na_2SO_4以及Na_6CO_3(SO_4)_2、Na_4(SO_4)1.39(CO_3)0.61等结晶复盐;添加硫化钠也可以增加盐析出率与排盐率,但是效果不明显,在当Ns=6g/L时,排盐率仅为71.71%,结晶物相有Na_2CO_3、Na_2C_2O_4、NaAlO_2·1.25H_2O以及Na_2S,Na_2S2O_3,Na_2SO_3等,并不存在结晶复盐;随着硫化钠添加量的增加,抽滤时间增长,增加了排盐的难度,硫化钠滞留在溶液中,继续对生产产生危害,需要引入氧化剂将硫化钠充分氧化为硫酸钠,才能达到良好的强化排盐效果。

关 键 词:草酸钠  硫酸钠  硫化钠  排盐
收稿时间:2016-02-18
修稿时间:2016-02-24

Effect of Sulfur on Salt Elimination from NaAlO2 Solution Bearing Na2C2O4
weiguoling,lijunqi,chenchaoyi,liulong and yangxiaqiong. Effect of Sulfur on Salt Elimination from NaAlO2 Solution Bearing Na2C2O4[J]. Nonferrous Metals(Extractive Metallurgy), 2016, 0(7): 26-29
Authors:weiguoling  lijunqi  chenchaoyi  liulong  yangxiaqiong
Affiliation:Guizhou University,,,,
Abstract:The effect of sulfur on evaporation salt discharge from sodium aluminate solution bearing Na2C2O4 was studied by adding different amount of Na2SO4 and Na2S respectively. The results show that when concentration of sodium oxalate is NS=6 g/L, sodium sulfate exerts effect on crystallization of Na2CO3, sulfur salt, Na2C2O4 and NaAlO2 in sodium aluminate solution. Salting-out rate and brine rate rises with increase of adding amount. With Ns=6 g/L, brine rate is 92.02%, and there are Na2CO3, Na2C2O4, NaAlO2?1.25H2O, Na2SO4, Na6CO3(SO4)2, and Na4(SO4)1.39(CO3)0.61 in evaporation residue. Adding sodium sulfide can also improve salting-out rate and brine rate with limited effect. With Ns=6 g/L, brine rate is as only as 71.71%, and crystal phase are Na2CO3, Na2C2O4, NaAlO2?1.25H2O, Na2S, Na2S2O3, and Na2SO3, etc, with no double salt crystallization. With increase of adding amount of sodium sulfide, suction filter time is growing, difficulty of row of salt enhances, and sodium sulphide remains in solution with continuing harm to production. It is necessary to apply oxidant to oxidize sodium sulphide to sodium sulfate to discharge more salts.
Keywords:sodium oxalate   sodium sulfate   sodium sulfide   salt elimination
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