BAO Weijun, ZHAO Hongtao, LI Huiquan, et al. Equilibrium conversion analysis of pressurized carbonation with phosphogypsum[J]. CIESC Journal, 2017, (3): 1155-1162.
DOI:
BAO Weijun, ZHAO Hongtao, LI Huiquan, et al. Equilibrium conversion analysis of pressurized carbonation with phosphogypsum[J]. CIESC Journal, 2017, (3): 1155-1162.DOI: 10.11949/j.issn.0438-1157.20161290.
Equilibrium conversion analysis of pressurized carbonation with phosphogypsum
围绕磷石膏加压碳酸化转化过程,首先通过实验研究了原料种类对加压碳酸化转化过程的影响,进一步采用Aspen plus 流程模拟软件深入分析了各工艺参数对磷石膏加压碳酸化过程平衡转化率的影响规律。结果表明,在加压条件下碳酸化反应均可在5 min时达到平衡,其中分析纯无水硫酸钙更容易完全转化,而二水硫酸钙及磷石膏因含有结晶水或其他杂质,使得其难以完全转化。增大初始氨水浓度、N/S(氨和原料中SO3的摩尔比)以及适量提高反应温度与体系压力,均能有效提高磷石膏加压碳酸化反应平衡转化率。特别是在高温和加压条件下,氨与CO2反应生成的碳酸铵盐可以通过降压闪蒸操作实现其自分解,经吸收返回用于加压碳酸化转化过程,可有效提高氨的利用率,降低硫酸铵生产成本。
Abstract
Based on the process of pressurized carbonation with phosphogypsum
the effect of raw material types on carbonation conversion was experimentally studied. In addition
the influence of some operation parameters on the conversion had been analyzed by Aspen plus process simulation software. The results showed that the carbonation reaction can reach equilibrium within 5 minutes under pressured conditions
and it was much more easily for pure anhydrous calcium sulfate to convert completely. However
because of containing crystal water or other impurities
it was difficult for both pure dihydrate calcium sulfate and phosphogypsum to convert completely. Besides
it was found that increasing the initial ammonia concentration
the mole ratio of added ammonia to SO3 in the raw materials
and properly increasing the reaction temperature and system pressure can effectively improve the equilibrium carbonation conversion. Most importantly
the formed ammonium carbonate from the reaction between ammonia and CO2 under high temperature and pressure condition is unstable when pressure decreased. Thus combing the flash operation after pressured carbonation
the formed ammonium carbonate can decompose to release ammonia and CO2
which can further be absorbed and returned to the pressurized carbonation process. This could effectively improve the ammonia utilization rate and reduce the production cost of ammonium sulfate as well.