Advanced Search+
Huijuan WANG (王慧娟), Guangshun ZHOU (周广顺), He GUO (郭贺), Cong GENG (耿聪). Kinetic analysis of soil contained pyrene oxidation by a pulsed discharge plasma process[J]. Plasma Science and Technology, 2017, 19(1): 15504-015504. DOI: 10.1088/1009-0630/19/1/015504
Citation: Huijuan WANG (王慧娟), Guangshun ZHOU (周广顺), He GUO (郭贺), Cong GENG (耿聪). Kinetic analysis of soil contained pyrene oxidation by a pulsed discharge plasma process[J]. Plasma Science and Technology, 2017, 19(1): 15504-015504. DOI: 10.1088/1009-0630/19/1/015504

Kinetic analysis of soil contained pyrene oxidation by a pulsed discharge plasma process

Funds: Supported by National Natural Science Foundation of China (No. 21207052).
More Information
  • Received Date: March 03, 2016
  • A pulsed discharge plasma (PDP) reactor with net anode and net cathode was established for investigating the pyrene degradation in soil under different pulse peak voltage, air flow rate, pyrene content in soil, initial pH value and initial water content of the soil. Pyrene oxidation within the 60 min discharge time was fitting according to the pseudo-first order equation and the corresponding reaction kinetics constants (k values) were calculated. The obtained results show that pyrene oxidation under all the different reaction conditions obeyed the pseudo-first order equation well. Higher pulsed peak voltage and appropriate air flow rate were in favor of the increase of reaction rate of pyrene oxidation. A higher k value could be achieved in the lower initial pyrene content (the value was 100 mg kg−1). The k value of pyrene oxidation in the case of pH=4 was 11.2 times higher than the value obtained under the condition of pH=9, while the initial water content of the soil also has a large effect on the oxidation rate of pyrene due to the effect of PDP.
  • [1]
    Dixit S et al 2015 J. Cleaner Prod. 87 39
    [2]
    Ribeiro A R et al 2015 Environ. Int. 75 33
    [3]
    Cheng M et al 2016 Chem. Eng. J. 284 582
    [4]
    Qi S et al 2016 Chemosphere 144 2436
    [5]
    Hanela S, Durán J and Jacobo S 2015 J. Environ. Chem. Eng. 3 1794
    [6]
    Angaji M T and Ghiaee R 2015 Ultrason. Sonochem. 23 257
    [7]
    Lee S Y and Park S J 2013 J. Ind. Eng. Chem. 19 1761
    [8]
    Gr?i? I, Papi? S and Koprivanac N 2013 Ultrason. Sonochem. 20 1037
    [9]
    Fu D et al 2015 Chin. J. Catalysis 36 952
    [10]
    Wang X, Zhou M and Jin X 2012 Electrochim. Acta 83 501
    [11]
    Rosas J M et al 2014 Appl. Catalysis B: Environ. 144 252
    [12]
    Venny G S and Ng H K 2012 Chem. Eng. J. 180 1
    [13]
    Yap C L, Gan S and Ng H K 2011 Chemosphere 83 1414
    [14]
    Higarashi M M and Jardim W F 2002 Catalysis Today 76 201
    [15]
    O’Mahony M M et al 2006 Chemosphere 63 307
    [16]
    Li J et al 2007 Desalination 212 123
    [17]
    Wang H et al 2008 Appl. Catalysis B: Environ. 83 72
    [18]
    Mizuno A 2013 Catalysis Today 211 2
    [19]
    Zhang Y et al 2013 J. Colloid Interface Sci. 409 104
    [20]
    Wang H et al 2015 Plasma Sci. Technol. 17 881
    [21]
    Wang H et al 2016 Vacuum 128 99
    [22]
    Wang H, Li J and Quan X 2006 J. Electrost. 64 416
    [23]
    Jin Y et al 2014 J. Taiwan Inst. Chem. Eng. 45 589
    [24]
    Jiang B et al 2014 Chem. Eng. J. 236 348
    [25]
    Wang T et al 2010 Environ. Sci. Technol. 44 3105
    [26]
    Wang T et al 2011 Environ. Sci. Technol. 45 9301
    [27]
    Wang T et al 2015 Water Res. 84 18
    [28]
    Wang H et al 2016 J. Electrost. 80 69
    [29]
    Geng C et al 2015 J. Electrost. 73 38
    [30]
    Luster-Teasley S, Ubaka-Blackmoore N and Masten S J 2009 J. Hazardous Mater. 167 701

Catalog

    Article views (248) PDF downloads (546) Cited by()

    /

    DownLoad:  Full-Size Img  PowerPoint
    Return
    Return