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基于双循环多级水幕塔的无机盐强化烟气脱硫研究 被引量:5

Flue gas desulfurization enhanced by inorganic salts using double circulation and multi-stage water film tower
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摘要 在传统双循环脱硫塔基础上对双循环多级水幕塔进行改进;上下段采用不同pH控制,以多级水幕代替复杂的多层喷淋,增强气液传质效果。研究结果表明:浓度均为0.2 mol/L MgSO4和Na2SO4促进石灰石溶解的效果明显,SO42-可促进石灰石溶解,而Cl-对石灰石溶解起抑制作用;MgSO4和Na2SO4对石灰石转化率的影响与空白实验相比最高分别增加15%和10%,反应时间缩短2 h,而NaCl对石灰石转化率的影响与空白实验结果相比低约3%;MgSO4和Na2SO4的加入明显延长pH缓冲时间,MgSO4加入时pH从7.9降至3.6需要2 h;MgSO4和Na2SO4能明显提高脱硫效率,0.2 mol/L MgSO4和Na2SO4对应的脱硫效率分别比非强化时提高7%和4%;MgSO4和Na2SO4强化后石灰石利用率与非强化时相比分别提高11%和5%。 Double circulation and multi-stage water film tower were retrofitted based on the traditional double cycle desulfurization tower.Different pH and multi-stage water film towers were used to substitute the traditional complicated multilayer sprayers to increase mass transfer impetus.The results show that the limestone has the best solubility when the concentration of MgSO4 or Na2SO4 is 0.2 mol/L.The sulfate radical can promote the limestone's solubility,but chloridion may restrain it.The limestone's transformations influenced by MgSO4 and Na2SO4 increase by 15% and 10% respectively compared with those without additive's enhancement and its reaction time can be shortened by 2 h,but its transformation influenced by NaCl decreases by 3% compared with that without additive's enhancement.It can delay buffer time of pH when inorganic salt is added,and needs 2 h when pH decreases from 7.9 to 3.6 and MgSO4 is added.Desulfurization efficiency can increase 7% and 4% when the concentration of MgSO4 or Na2SO4 is 0.2 mol/L.The limestone's utilities improve 11% and 5% respectively when MgSO4 or Na2SO4 is added compared with those without additives' enhancement.
出处 《中南大学学报(自然科学版)》 EI CAS CSCD 北大核心 2011年第2期555-560,共6页 Journal of Central South University:Science and Technology
基金 江苏省环境科技基金资助项目(BK2004031) 中国矿业大学青年科研基金资助项目(0P061020)
关键词 无机盐 添加剂 双循环 多级水幕塔 烟气脱硫 inorganic salts additives double circulation multi-stage water film tower flue gas desulfurization(FGD)
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  • 1吴忠标,谭天恩.石灰/石灰石湿法脱硫中添加剂的研究[J].中国环境科学,1995,15(6):438-442. 被引量:27
  • 2顾夏生 等.水处理工程[M].清华大学出版社,1985..
  • 3Weisnicht W L,Overman J,Wang C C,et al. Calcium sulfite oxidation in a slurry reactor. Chem. Eng. Sci. , 1980,35: 463~468.
  • 4Huss A,Schlitt W, Joseph P,et al. Oxidation of aqueous sulfur dioxide. 1. Homogeneous managanese(Ⅱ) and iron(Ⅱ) catalysis at low pH. J. Phys. Chem. , 1982,86:4224~4228..
  • 5BROGREN C, HANNA T K. The impact of the electrical potential gradient on limestone dissolution under wet FGD conditions[J]. Chemical Engineering Science, 1997,52(3): 3101-3106.
  • 6WALLIS M, BERGER I. A model for absorption of sulphur dioxide into limestone slurry [ J ]. Chemical Engineering Journal, 1993, 51(2) :2099-2108.
  • 7Naohiko Ukawa,Toru Takashina.Effect of salts on limestone dissolution rate in wet limestone flue gas desulfurization[J].Environ Progr,1993,12(4):294-299.
  • 8Naohiko Ukawa,Toru Takashina.Effect of particle size distribution on limestone dissolution in wet FGD process applications[ J].Environ Progr,1993,12(3):238-242.
  • 9Frandsen Jan B W,Kiil Soren.Optimisation of a wet FGD pilot plant using fine limestone and organic acids[ J ].Chemical Engineering Science,2001,56(10):3275-3287.
  • 10Henzel D S,Laseke B A.Handbook for flue gas desulfurization scrubbing with limestone[ M ].Park Ridge,New Jersey:Noyes Data Corporation,1982.

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