首页|气化渣酸浸液去除铁铬及聚合氯化铝制备

气化渣酸浸液去除铁铬及聚合氯化铝制备

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气化渣是煤气化工艺产生的固体废弃物,其大量排放严重威胁生态环境,制约煤化工行业发展.本文针对气化渣高钙、高铁、低铝、含铬的物相组成的特点,通过混酸逆流浸出过程实现液相中铝的富集和钙离子的去除,并有效降低了浸出液中的余酸量,然后针对浸出液中的铁、铬进行除杂,得到可制备合格聚合氯化铝(PAC)的净化液,并以该富铝净化液为原料,进一步考察氯化铝和氢氧化铝添加量对聚合氯化铝产品性能的影响.结果表明:混酸逆流浸出阶段的最佳条件为盐酸浓度2.125 mol/L、硫酸浓度0.69 mol/L、液固比4∶1、温度85℃、时间4 h.在此条件下,铝浸出率达85.39%.黄钠铁矾法除杂最佳条件为反应温度97℃、反应时间1.5 h、终点pH=2.0,在此条件下,除铁率和除铬率分别达到69.46%和51.36%.在制备PAC阶段,采用净化液为原料,加入150 g/L氯化铝和100 g/L氢氧化铝,经60℃水解1 h、85℃聚合1.5 h后,制得符合国家标准GB/T 22627—2022的液体PAC产品,其去浊率达94.33%.
Removal of iron and chromium from acid leaching solution of gasification slag and preparation of polyaluminum chloride
Gasification slag is a solid waste produced by coal gasification process,and its large amount of emission seriously threatens the ecological environment and restricts the development of coal chemical industry. This study focuses on the characteristics of gasification slag with high calcium,high iron,low aluminum,and chromium content in its phase composition. Through a counter-current mixed acid leaching process,aluminum enrichment and calcium ion removal were achieved in the liquid phase while effectively reducing the residual acid content. Subsequently,iron and chromium impurities were removed from the leaching solution to obtain a purified solution suitable for preparing qualified polyaluminum chloride (PAC). Using this aluminum-rich purified solution as raw material,the effects of aluminum chloride and aluminum hydroxide addition on PAC product performance were further investigated. The results show that the optimal conditions for the mixed acid countercurrent leaching stage are hydrochloric acid concentration of 2.125 mol/L,sulfuric acid concentration of 0.69 mol/L,liquid-solid ratio of 4∶1,temperature of 85 ℃,and reaction time of 4 h,under which the aluminum leaching efficiency reaches 85.39%. The optimal conditions for the removal of impurities by the iron vitriol dreg of yellow sodium method are reaction temperature of 97 ℃,reaction time of 1.5 h,and a endpoint pH of 2.0,under which the iron removal rate and chromium removal rate are 69.46% and 51.36%,respectively. In the PAC preparation stage,using the purified solution as a raw material,aluminum chloride of 150 g/L and aluminum hydroxide of 100 g/L are added,followed by the hydrolysis process at 60 ℃ for 1 h and polymerization at 85 ℃ for 1.5 h. The liquid PAC products are produced,which is compliant with the national standard GB/T 22627—2022,achieving a turbidity removal efficiency of 94.33%.

gasification slagcounter-current leachingiron vitriol dreg of yellow sodium methodpolymeric aluminum chloride

周季龙、王亚茹、魏怡菲、孙建平、孙伟、岳彤

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中南大学资源加工与生物工程学院,长沙 410083

陕西煤业化工技术研究院有限责任公司,西安 710065

气化渣 逆流浸出 黄钠铁矾法 聚合氯化铝

2024

中国有色金属学报
中国有色金属学会

中国有色金属学报

CSTPCD北大核心
影响因子:1.108
ISSN:1004-0609
年,卷(期):2024.34(12)