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  • Küçük Resim
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    Co-combustion thermal conversion characteristics of textile dyeing sludge and pomelo peel using TGA and artificial neural networks
    (Elsevier Sci Ltd, 2018) Xie, Candie; Liu, Jingyong; Zhang, Xiaochun; Xie, Wuming; Sun, Jian; Chang, Kenlin; Kuo, Jiahong; Büyükada, Musa; Evrendilek, Fatih
    Co-combustion characteristics of textile dyeing sludge (TDS) and pomelo peel (PP) under O-2/N-2 and O-2/CO2 atmospheres were investigated using a thermogravimetric analysis (TGA) and artificial neural networks. 30% O-2/70% CO2 and air atmospheres led to a similar co-combustion performance. Increases in O-2 concentration and PP significantly improved the oxy-fuel co-combustion performance of TDS. Principal component analysis was applied to reduce the dimensionality of differential TGA curves and to identify the principal reactions. The interaction between TDS and PP occurred mainly at 490-600 degrees C, thus improving the process of residue co combustion. Radial basis function was found to have more reliable and robust predictions of TGA under different O-2/CO2 atmospheres than did Bayesian regularized network. Regardless of Flynn-Wall-Ozawa (FWO) and Kissinger-Akahira-Sunose (KAS) methods used, the lowest mean value of apparent activation energy (155.4 kJ.mol(-1) by FWO and 153.2 kJ.mol(-1) by KAS) was obtained under the 30% O-2/70% CO2 atmosphere.
  • Küçük Resim
    Öğe
    Influence of catalysts on co-combustion of sewage sludge and water hyacinth blends as determined by TG-MS analysis
    (Elsevier Sci Ltd, 2018) Huang, Limao; Xie, Candie; Liu, Jingyong; Zhang, Xiaochun; Chang, KenLin; Kuo, Jiahong; Sun, Jian; Büyükada, Musa; Evrendilek, Fatih
    Effects of the three metal carbonates (K2CO3, Na2CO3, and MgCO3) were quantified on catalytic co-combustion of the sewage sludge and water hyacinth (SW) blend using a thermogravimetric-mass spectrometric (TG-MS) analysis and kinetics modeling. The main dominating steps of the catalysts were the organic volatile matter release and combustion stage. Weighted mean values of activation energy (E-m) were estimated at 181.18 KJ . mol(-1), 199.76 KJ . mol(-1), 138.76 KJ . mol(-1), and 177.88 KJ . mol(-1) for SW, SW + 5% K2CO3, SW + 5% Na2CO3, and SW+ 5% MgCO3, respectively. The lowest E-m occurred with SW+ 5% Na(2)CO3. Overall, catalyst effect on co-combustion appeared to be negligible as indicated by Gibbs free energy (Delta G). The normalized intensities of SW+ MgCO3 were strongest. The addition of Na2CO3 and MgCO3 to SW increased flue gases emissions (CO2, NO2, SO2, HCN, and NH3) of SW, whereas the addition of K2CO3 to SW reduced flue gases emissions from the entire combustion process.