Chen Fang, Yang Chun-ping, Gan Hai-ming, Wu Ting, Chen Hai-lin, Chen Hong, Xu Ke-hui, Xie Geng-xin
College of Environmental Science and Engineering, Hunan University, Changsha 410082, China.
Huan Jing Ke Xue. 2010 Apr;31(4):897-902.
An innovative flue gas desulfurization (FGD) coupling process was proposed in this study to overcome the problems in wet-type limestone/lime processes which include fouling, clogging, and difficulty of selling the by-products and the problems in traditional process for vanadium extraction from navajoite ore such as excessive consumption of sulfuric acid and emissions of pollutants. The performance of a jet bubbling reactor (JBR) at pilot-scale was evaluated using navajoite ore produced in the process of extracting vanadium pentoxide as desulfurization absorbent. Results showed that navajoite ore slurry achieved better desulfurization performance than limestone slurry. When the inlet flue gas pressure drop was 3.0 kPa, the gas flow was about 2350 m3 x h(-1) and the pH of the navajoite ore slurry was higher than 4.5, the desulfurization efficiency was stable about 90%. The SO2 removal efficiency appeared to increase along with the increasing of absorbent cycle-index. The efficiency of the second circulation was improved 3.5% compared to the first circulation. After an operating duration of 40 minutes, the leaching rate of vanadium pentoxide was about 20%, and reached 60% when the by-products were leached with 5% dilute sulfuric acid for 10 hours. The by-product from this process not only could be used to produce vanadium pentoxide which is a valuable industrial product, but also could significantly overcome the pollution problem existing in the traditional refining process of vanadium pentoxide when navajoite ore is used as the feed material. This FGD process using roasted navajoite slurry as absorbent is environmental sound and cost-effective, and shows the potential for application in the field of flue gas desulfurization as well as hydrometallurgy.
本研究提出了一种创新的烟气脱硫(FGD)耦合工艺,以克服湿式石灰石/石灰工艺中存在的问题,如结垢、堵塞、副产品销售困难,以及从钠钒矿中提取钒的传统工艺中存在的问题,如硫酸消耗过多和污染物排放。使用五氧化二钒提取过程中产生的钠钒矿作为脱硫吸收剂,对中试规模的喷射鼓泡反应器(JBR)性能进行了评估。结果表明,钠钒矿矿浆的脱硫性能优于石灰石矿浆。当入口烟气压降为3.0 kPa、气体流量约为2350 m³·h⁻¹且钠钒矿矿浆pH值高于4.5时,脱硫效率稳定在90%左右。SO₂去除效率似乎随着吸收剂循环指数的增加而提高。第二次循环的效率比第一次循环提高了3.5%。运行40分钟后,五氧化二钒的浸出率约为20%,当副产品用5%稀硫酸浸出10小时后,浸出率达到60%。该工艺的副产品不仅可用于生产有价值的工业产品五氧化二钒,而且当以钠钒矿为原料时,还可显著克服传统五氧化二钒精炼工艺中存在的污染问题。这种以焙烧钠钒矿矿浆为吸收剂的FGD工艺环保且具有成本效益,在烟气脱硫以及湿法冶金领域显示出应用潜力。