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用于磷酸生产的磷酸盐浆液增强磷石膏分解中二氧化硫的吸收。

Enhanced absorption of SO from phosphogypsum decomposition by phosphate slurry for phosphoric acid production.

作者信息

Qian Wenmin, Yang Yanyu, Liu Zewei, Zhang Jin, Song Xin, Shi Nan, Xie Ming, Li Bin, Ning Ping

机构信息

Faculty of Environmental Science and Engineering, Kunming University of Science and Technology, Kunming 650500, China; Yunnan Appraisal Center for Ecological and Environmental Engineering, Kunming 650228, China.

Faculty of Environmental Science and Engineering, Kunming University of Science and Technology, Kunming 650500, China.

出版信息

J Hazard Mater. 2024 Mar 5;465:133431. doi: 10.1016/j.jhazmat.2024.133431. Epub 2024 Jan 4.

Abstract

Phosphogypsum (PG) is a major industrial by-product of wet process phosphoric acid production, and untreated PG stockpiled on land will cause severe environmental pollution. Thermal treatment of PG is currently the mainstream treatment method PG can be thermally decomposed to produce CaO, and the decomposition process produces large amounts of SO. In this paper, phosphate slurry was used to absorb SO generated during the PG decomposition to produce phosphoric acid. The effects of operating conditions such as pressure, inlet SO concentration, and additive content on the desulfurization efficiency, as well as phosphoric acid yield, were investigated. Under the optimal experimental parameters, the desulfurization efficiency was 100% in the first 3 h, and decreased to 67.42% after 5 h, the maximum phosphate concentration in the solution was 1445.92 mg/L. The Density functional theory (DFT) calculations showed that SO and O adsorbed on the surface of PO underwent to generate SO, which can react with HO to produce HSO. Moreover, it was found that Fe could enhance the catalytic oxidation process of SO and O by decreasing the reaction energy barrier. This study should be helpful for the recycling of phosphorus resources.

摘要

磷石膏(PG)是湿法磷酸生产的主要工业副产品,未经处理的磷石膏堆存会造成严重的环境污染。目前,磷石膏的热处理是主流处理方法,磷石膏可通过热分解产生CaO,分解过程会产生大量SO。本文采用磷酸盐浆液吸收磷石膏分解过程中产生的SO以制备磷酸。研究了压力、入口SO浓度和添加剂含量等操作条件对脱硫效率以及磷酸产率的影响。在最佳实验参数下,前3小时脱硫效率为100%,5小时后降至67.42%,溶液中最大磷酸盐浓度为1445.92mg/L。密度泛函理论(DFT)计算表明,SO和O吸附在PO表面生成SO,SO可与HO反应生成HSO。此外,研究发现Fe可通过降低反应能垒来增强SO和O的催化氧化过程。该研究有助于磷资源的回收利用。

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