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碱性介质多元体系中钒酸钠结晶分离 被引量:7

Separation of Sodium Vanadate in Alkaline Multi-component System
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摘要 测定了NaOH-NaNO_3-NO_3VO_4-Na_2CrO_4-H_2O五元体系各盐在碱中的相平衡浓度,根据所得数据对该体系中的Na_3VO_4进行了冷却结晶分离.通过研究NaOH浓度、NaNO_3浓度、结晶终点温度、降温速度、搅拌速度、晶种对钒酸钠结晶分离的影响,得到的最优实验条件为:结晶液中NaOH浓度200~250g/L,NaN0_3浓度200g/L左右,搅拌转速200r/min,80~40℃自然降温,添加晶种量1%(ω),该条件下Na_3VO_4结晶率为61%,晶体纯度可达95%,且晶体颗粒人(147μm),沉降分离速度快(〈10min). The phase equilibrium of sodium salts in the NaOH-NaNO_3-Na_3VO_4-Na_2CrO_4-H_2O systems was determined.Based on the solubility data,sodium vanadate can be separated by cooling from the solution.By examination of NaOH concentration,NaNO_3 concentration,crystallization end temperature,cooling rate,stirring speed,and seeds on the crystallization of sodium vanadate from multi-component alkaline solutions,the optimal experimental conditions for separation of sodium vanadate were obtained as follows:NaOH concentration 200~250 g/L,NaNO_3 concentration 200 g/L,stirring speed 200 r/min,temperature from 80℃ to 40℃ with natural cooling,and seed addition 1%(ω).Under the optimal conditions,the sodium vanadate yield of 61% was obtained,and the purity of the crystal was about 95%.The obtained crystal particles with large size(147 μm) exhibited excellent sedimentation and separation property(sedimentation speed 10 min).
出处 《过程工程学报》 CAS CSCD 北大核心 2010年第4期660-666,共7页 The Chinese Journal of Process Engineering
基金 国家重点基础研究发展规划(973)基金资助项目(编号:2007CB613500) 国家高技术研究发展计划(863)基金资助项目(编号:2009AA064003)
关键词 NAOH NaNO3 Na3VO4 结晶 钒渣 NaOH NaNO3 sodium vanadate crystallization separation vanadium slag
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