广东工业大学环境工程专业毕业设计1 M. Petalaa, V. Tsiridisa, P. Samarasb*, A. Zouboulisc, G.P. SakellaropoulosaaChemical Process Engineering Laboratory, Department of Chemical Engineering, Aristotle University of Thessalonikiand Chemical Process Engineering Research Institute, 57001Thermi-Thessaloniki, Greece bDepartment of Pollution Control Technologies, Technological Educational Institute of Western Macedonia,50100 Kozani, Greece Tel. +30 (24610) 40161; Fax +30 (24610) 39682; email: psamaras@kozani.teikoz.gr cDivision of Chemical Technology, Department of Chemistry, Aristotle University of Thessaloniki,54124 Thessaloniki, Greece Received 4 May 2005; accepted 17 October 2005 参数未经消毒的二级出水砂滤，吸附和 7.1mgO 3/L臭氧氧化后出水砂滤，吸附和26.7mgO 3/L 臭氧氧化后出水93000 240 <2 43000 21 <2 2400 460 <2 参数参数去除率，％去除率，％广东工业大学环境工程专业毕业设计2 [1] A.N. Aggelakis and L. Bontoux, Water Policy, 3 (2001)47–59. [2] G. Shelef and Y. Asov, Wat. Sci. Technol., 33 (1996)115–125. 臭氧剂量， mg/L 效果，％广东工业大学环境工程专业毕业设计3 [3] A.N. Aggelakis, M.H.F. Marecos de Monte, L. Bontouxand T. Asano, Wat. Res., 33 (1999) 2201–2217. [4] K. Perakis, K. Kyrimis and A. Kungolos, FreseniusEnvir. Bull., 9 (2000) 659–666. [5] M. Abdel Jawad, S. Ebrahim, M. Al-Tabtabei and S.Al-Shammari, Desalination, 124 (1999) 251–261. [6] H. Bouwer, Wat. Sci. Technol., 33(10–11) (1996) 381–390. [7] T. Asano and A.D. Levine, Wat. Sci. Technol., 3(10–11) (1996) 1–14. [8] M.F. Hamoda, I. Al-Ghusain and N.Z. Al-Mutairi,Desalination, 164 (2004) 203 –211. [9] B. Jimenez, A.M. Chavez, A. Leyva and G. Tchobanoglous,Wat. Res., 34(2) (2000) 473–480. [10] D. Abdessemed and G. Nezzal, Desalination, 152(2002) 367–373. [11] P. Xu, M.-L. Janex, P. Savoye, A...
