首页|钾长石酸浸工艺中氟循环利用可行性研究

钾长石酸浸工艺中氟循环利用可行性研究

扫码查看
以钾长石酸浸工艺为研究对象,研究氟化物回收的可行性,分析了负压介入钾长石酸浸工艺对氟回收的影响及氟循环利用对浸出钾的影响.结果表明,恒低压和组合工艺介入钾长石酸浸过程时,氟回收具备可行性.将定容后的釜底液滤液在系统压强为-0.06 MPa(低压)、温度为85 ℃的环境中蒸馏0.5 h,用50 mL去离子水吸收,可得恒低压工艺和组合工艺的氟回收率分别达到14.14%和8.39%.组合工艺的钾浸出率最高,能有效将钾元素转化为离子态.
Feasibility Study on Fluoride Recycling in Potassium Feldspar Acid Leaching Process
Taking the potassium feldspar acid leaching process as the research object,the feasibility of fluoride recovery was studied,and the influence of negative pressure intervention in the potassium feldspar acid leaching process on fluoride recovery and the impact of fluoride recycling on leached potassium were analyzed.The results indicate that fluorine recovery is feasible when constant low pressure and combined processes are involved in the potassium feldspar acid leaching process.Distillation of the bottom liquid filtrate after constant volume in an environment with a system pressure of-0.06 MPa(low pressure)and a temperature of 85 ℃ for 0.5 h,and absorption with 50 mL of deionized water,resulted in fluorine recovery rates of 14.14%and 8.39%for the constant low pressure process and the combined process,respectively.The combination process has the highest potassium leaching rate and can effectively convert potassium elements into ionic states.

potassium feldsparacid leachingfluorine recoveryrecycling utilization

彭聃、佘健、胡璟、王婉玉

展开 >

中南安全环境技术研究院股份有限公司,武汉 430000

钾长石 酸浸 氟回收 循环利用

2024

中国资源综合利用
徐州北矿金属循环利用研究所 中国物资再生协会

中国资源综合利用

CHSSCD
影响因子:0.358
ISSN:1008-9500
年,卷(期):2024.42(8)