[1] 中国电力企业联合会.中国电力行业度发展报告2015 [R].北京:中国电力出版社,2015. [2] 刘定平,陈博强.一种新型液包气雾化喷嘴流场特性的研究[J].动力工程学报,2013(6):466-471. [3] 庞旭,薛勇,袁翀. 控制氧化对湿法烟气脱硫过程的影响研究[J].环境科学与技术,2008,31(5):87-90. [4] 闫军. 湿法脱硫石膏浆液品质及控制施[A].全国发电机组技术协作会.全国火电200MW级机组技术协作会第24届年会论文集[C].全国发电机组技术协作会:2006.. [5] WARYCH J,SZYMANOWSKI M.Model of the wet limestone flue gas desulfurization process for cost optimization[J].Industrial & Engineering Chemistry Research,2001,40(12):2597-2605. [6] 杨剑.湿法烟气脱硫氧化过程动力学研究[D].重庆:重庆大学,2008. [7] 李守信,胡玉亭,纪立国.湿式石灰石-石膏法烟气脱硫中石膏质量的工艺控制因素[J].电力环境保护,2002(3):5-7. [8] 汪黎东.烟气脱硫添加剂对正盐生成促进的实验研究[D].保定:华北电力大学(保定),2005. [9] CHEN T I,BARRON C H. Some aspects of the homogeneous kinetics of sulfite oxidation [J]. Industrial & Engineering Chemistry Research,1972,11:466-470. [10] MISHRA G C,SRIVASTAVA R D.Homogeneous kinetics of potassium sulfite oxidation[J].Chemistry Engineering Science,1976,31:969-971. [11] LANCIA A,MUSMARRA D,PEPE F.Uncatalyzed heterogeneous oxidation of calcium bisulfite [J].Chemical Engineering Science,1996,51(16):3889-3896. [12] KARATZA D,PRISCIANDARO M. Reaction rate of sulfite oxidation catalyzed by cuprous ions [J].Chemical Engineering Journal,2008,7:285-289. [13] ZHAO B,LI Y,TONG H,ZHOU Y. Study on the reaction rate of sulfite oxidation with cobalt ion catalyst [J]. Chemical Engineering Science,2005,60:863-868. [14] BRONIKOWSKA W,ZIAJKA J. Oxygen absorption into aqueous sulphur dioxide solutions [J]. Chemical Engineering Science,1985,40:1567-1572. [15] BENGTSSON S,BJERLE I. Catalytic oxdiation of sulphite in diluted aqueous solutions [J]. Chemical Engineering Science,1975,30:1429-1435. [16] GREENHALGH S H,MCMANAMEY W J,PORTER K E. An absorption peak in the oxidation of sodium sulphite solutions [J]. Chemical Engineering Science,1975,30:155-157. [17] FREIBERG J. The mechanism of iron catalyzed oxidation of iron catalyzed oxidation of SO2 in oxygenated solutions[J]. Atmospheric Environment,1975,9:661-672. [18] HUSS A,LIM P K,ECKERT C A.The "uncatalyzed" oxidation of sulfur(Ⅳ)in aqueous solutions [J].Journal of the American Chemical Society,2002,100(19):6252-6253. [19] KRAFT J,ELDIK R V.Kinetics and mechanism of the iron(Ⅲ)-catalyzed autoxidation of sulfur (Ⅳ) oxides in aqueous solution [J].Inorganic Chemistry,1989,28:2297-2312. [20] WANG L D, WANG J, XU P Y,et al.Selectivity of transition metal catalysts in promoting the oxidation of solid sulfites in flue gas desulfurization [J].Applied Catalysis A,2015,10:52-60. [21] 徐耀鹏,吕宏俊.强制氧化风量对湿法脱硫系统的影响分析[J]. 电站系统工程,2011(3):35-36+42. [22] 吕宏俊.石灰石-石膏实发脱硫系统中强制氧化风量的分析[C]//中原经济区环境保护暨大气环境与气候学术会议,2012:539- 542. [23] 马双忱,韩刚. 湿法烟气脱硫过程中石灰石离解模型及应用[J]. 电力科技与环保,2013(2):7-9. [24] HONJO S,SUGITA S,NAKAYAMA Y,et al.MHI wet-FGD waste water treatment technologies[C]//Air and Waste Management Association-8th Power Plant Air Pollutant Control,Mega Symposium 2010:1395-1429. [25] BROWN S. Causes & Impacts of WFGD ORP on Effluent Composition[EB/OL].Worldwide Pollution Control Association,2013,05.http://wpca.info/pdf/Presentations/Charlotte2013/4-Causes%20and%20Impact%20of%20WFGD%20ORP%20on%20Effluent%20Composition%20by%20Shannon%20Brown,%20BandW.pdf. [26] 贾西部,金万元,李兴华,等.石灰石-石膏湿法烟气脱硫系统浆液起泡原因分析[J].中国电力,2015(9):157-160. [27] 金萍,林开.湿法脱硫浆液中亚硫酸盐测量值偏小的原因分析[J]. 浙江电力,2009(2):68-71. [28] PISU M,CINCOTTI A,CAO G,et al. Prediction of uncatalysed calcium bisulphite oxidation under operating conditions relevant to wet flue gas desulphurization plants [J]. Chemical Engineering Research and Design,2004,82(A7):927-932. [29] 薛恒友,李小敏. 提高脱硫石膏生产品质的措施[J]. 粉煤灰,2010,22(3):32-40. [30] 徐宏建,李浩然,孙肆鹃,等.有机酸添加剂强化电石渣脱硫的试验研究[J].动力工程学报,2015(8):659-665. [31] 林蔚,江燕明. 浅谈电厂烟气脱硫浆液系统在线pH计测量系统的优化[J].中国科技信息,2009(11):159-160. |