แก้ ไขตาม comment editor 1 The writing needs an intensive editing. There are errors (“Mass Chang” in Table 2, Fig. 6 is missing) แก้ไข Mass Chang เป็ น Mass change แก้ไขลำดับภำพใ ห้ถูกต้อง แก้ไขลำดับภำพใ ห้ถูกต้อง 2 The results must be discussed in reference to recent journal publications TG and DTG curves at the heating rate of 20 0C /min from room temperature to 500 0C are shown in Figure 5(a). The thermal decomposition process of all the samples can be divided into two distinguished stages. The first stage ranged from room temperature to approximately 300 0C is as a result of moisture evaporation and possible degradation of light organic compounds. The second stage ranged from approximately 300 to 500 0C is the main devolatilization process, during which intense decomposition of bacterial cellulose and nylon in samples is observed. The carbonization process inducing weight loss due to nylon evaporization occurred in this stage. These results can also be observed from the TGA and DTG curves in nitrogen atmosphere at the heating rate 0 0 TG and DTG curves at the heating rate of 20 C /min from room temperature to of 20 C /min Figure 5(b). In all curves two kinds of weight loss were observed during the thermal scanning runs. The first, weigh loss occured 500 0C are shown in Figure 5(a). The thermal decomposition process of all the samples can be divided into two distinguished stages. The first stage ranged at 100-300 ºC, due to dehydration or removal of physically adsorbed water from room temperature to approximately 300 0C is as a result of moisture from the surface of the particles. The majority of weight loss is according evaporation and possible degradation of light organic compounds. The second to condensation of hydroxyl groups at the particle surface in the range of stage ranged from approximately 300 to 500 0C is the main devolatilization 300-500 ºC [12,19]. process, during which intense decomposition of bacterial cellulose and nylon in samples is observed. The carbonization process inducing weight loss due to nylon evaporization occurred in this stage. These results can also be observed from the TGA and DTG curves in nitrogen atmosphere at the heating rate of 20 0 C /min Figure 5(b). 100 80 60 % Removal 40 20 TiO2 5% TiO2 2.5% TiO2 1% 0 0 50 100 150 200 250 Time (min) Toluene removal Photocatalytic system set up as described in the prior section was utilized to study the toluene removal from indoor air. TiO2 coated nanofilms with 3 different dosage of TiO2 were used in the photocatalytic reactor. Initial Toluene removal Photocatalytic system set up as described in the prior section was utilized to study the toluene removal from indoor air. TiO2 coated nanofilms with 3 different dosage of TiO2 were used in the photocatalytic reactor. Initial concentration of toluene in the system was approximately 200 ppm. Toluene photocatalytic degration was displayed in figure 6. As seen in the figure 6, percentage removal of toluene increased as the amount of TiO2 coated onto the film increased. However, when the amount of TiO2 was increased from 2.5% to 5%, the significant difference of removal could not be observed. These results were correspond and with previous work[2]. It is suggested that a low number of particle deposited on surface of nanofilm cannot provide enough TiO2 photocatalytic, while a large amount of TiO2 may lead to a drop in the removal of toluene due to concentration of toluene in the system was approximately 200 ppm. Toluene photocatalytic degration was displayed in Figure 6, as seen in the figure, 5% wt of TiO2 coated on nanofilm yielded the best toluene removal efficiency (92.71%), followed by 2.5% and 1% TiO2 coated nanofilm (90.95% and 87.98%,respectively). the nucleation of TiO2 on the support removal of toluene, which decreases the amount of TiO2 surface[3]. 3 Quality of Fig 5, 7, 8 must be improved. Lines are too thin and words are not comprehensible. ขยำยจุดให้ใหญ่ข้ ึน และขยำยภำพ ปรับตัวอักษรเป็ น Time new roman ในกรำฟ และเพิ่มเติมเนื้อหำตำม หัวข้อ 2 ด้ำนบน 4 The reference format must be consistent. Journal names must be abbreviated according to standard use. [1] K Suwannahong, S Sinvithayapakorn, P Noophan and W Sanongraj. Improvement of Ti02/LDPE Composite Films for Photocatalytic Oxidation of Acetone. Advanced Materials Research. 2014; 931, 235240. [2] K Suwannahong, W Sanongra, J Kruenate, S Phibanchon, S Jawjit and W Khamwichit. Photo Catalytic Oxidtion Degradation of Volatile Organic Compound with Nano-TiO2/LDPE Composite Film. International Journal of Chemical, Molecular, Nuclear, Materials and Metallurgical Engineering. 2013; 7, 1. [3] K Suwannahong, W Liengcharernsit, W Sanongraj and J Kruenate. Application of Nano-TiO2 /LDPE composite film on photocatalytic oxidation degradation of dichloromethane, Journal of Environmental Biology. 2012; 33, 955-959. [4] M.L Bechec, N Kinadjianb, O.R Backov and S Lacombea. Comparison of kinetics of acetone, heptane and toluene photocatalytic mineralization over TiO2 microfibers and Quartzel mats. Applied Catalysis B: Environmental. 2015; 179, 78-87. [5] W William, A.J Daniel, M.B John, A.F James, E.B Leann, M.V Marya and C.G Suzanne. Heterogeneous photocatalysis for control of volatile organic compounds in indoor air. Air & Waste Management Association. 1996; 46, 891-898. [6] S Khami, W Khamwichit, K Suwannahong and W Sanongraj. Characteristics of bacterial cellulose production from agricultural wastes. Advanced Materials Research. 2014; 931-932, 693-697. [7] M Mehrab, A William, M Murray and M Park. Non-linear parameter estimation for a dynamic model in photocatalytic reaction. Chemical Engineering Science. 2000;55, 4885-4891. [8] C Mendozaa, A Vallea, M Castellote, A Bahamondea and M Faraldos. TiO2 and TiO2–SiO2 coated cement: Comparison of mechanic and photocatalytic properties. Applied Catalysis B: Environmental. 2015; 178, 155–164. [9] M Aihong, C Shen, Z Hui, L Yanqiu, Z Yanguo and L Qinghai. Pyrolysis and simulation of typical components in wastes with macro-TG. Fuel. 2015; 157, 1–8. [10] S Ok Han, J.H Youk, K.D Min, Y.O Kang and W.H Park. Electrospinning of cellulose acetate nanofibers using a mixed solvent of acetic acid/water:Effects of solvent composition on the fiber diameter. Journal of materials letters. 2008; 62, 759–762. [11] K.C Seavey and W.G Glasser. Continuous cellulose fiberreinforced cellulose ester composites. II. Fiber surface modification and [1] [2] [3] [4] [5] [6] [7] [8] [9] [10] [11] [12] [13] [14] K Suwannahong, S Sinvithayapakorn, P Noophan and W Sanongraj. Improvement of Ti02/LDPE Composite Films for Photocatalytic Oxidation of Acetone. Adv. Mater. Res. 2014; 931, 235-240. K Suwannahong, W Sanongra, J Kruenate, S Phibanchon, S Jawjit and W Khamwichit. Photo Catalytic Oxidtion Degradation of Volatile Organic Compound with Nano-TiO2/LDPE Composite Film. Int. J. of Chem. Mole., Nec. Mate. and Meta. Engineering. 2013; 7, 1. K Suwannahong, W Liengcharernsit, W Sanongraj and J Kruenate. Application of Nano-TiO2 /LDPE composite film on photocatalytic oxidation degradation of dichloromethane, J. Env. Bio. 2012; 33, 955-959. M.L Bechec, N Kinadjianb, O.R Backov and S Lacombea. Comparison of kinetics of acetone, heptane and toluene photocatalytic mineralization over TiO 2 microfibers and Quartzel mats. A. Catal. B: Env. 2015; 179, 78-87. W William, A.J Daniel, M.B John, A.F James, E.B Leann, M.V Marya and C.G Suzanne. Heterogeneous photocatalysis for control of volatile organic compounds in indoor air. Air & Waste Manag. Ass. 1996; 46, 891-898. S Khami, W Khamwichit, K Suwannahong and W Sanongraj. Characteristics of bacterial cellulose production from agricultural wastes. Adv. Mater. Res. 2014; 931932, 693-697. M Mehrab, A William, M Murray and M Park. Non-linear parameter estimation for a dynamic model in photocatalytic reaction. Chem. Eng. Sci. 2000; 55, 48854891. C Mendozaa, A Vallea, M Castellote, A Bahamondea and M Faraldos. TiO2 and TiO2-SiO2 coated cement:Comparison of mechanic and photocatalytic properties. A.Catal.B:Env. 2015; 178, 155-164. M Aihong, C Shen, Z Hui, L Yanqiu, Z Yanguo and L Qinghai. Pyrolysis and simulation of typical components in wastes with macro-TG. Fuel. 2015; 157, 1–8. S Ok Han, J.H Youk, K.D Min, Y.O Kang and W.H Park. Electrospinning of cellulose acetate nanofibers using a mixed solvent of acetic acid/water:Effects of solvent composition on the fiber diameter. J. Mater. lett. 2008; 62, 759–762. K.C Seavey and W.G Glasser. Continuous cellulose fiberreinforced cellulose ester composites. II. Fiber surface modification and consolidation conditions. J. Cellulose. 2001; 8, 161–169. S Zhang, Q Dong, L Zhang and Y. Xiong. Effects of water washing and torrefaction on the pyrolysis behavior and kinetics of rice husk through TGA and Py-GC/MS. Biores. Technol. 2016; 199, 352-361. M Ou, F Dong, W Zhang and Z Wu. Efficient visible light photocatalytic oxidation of NO in air with band-gap tailored (BiO)2CO3–BiOI solid solutions. Chem. Eng. J. 2014; 255, 650-658. S.W Yao and H.P Kuo. Photocatalytic degradation of toluene on SiO2/TiO2 consolidation conditions. Journal Cellulose. 2001; 8, 161–169. [12] S Zhang, Q Dong, L Zhang and Y. Xiong. Effects of water washing and torrefaction on the pyrolysis behavior and kinetics of rice husk through TGA and Py-GC/MS. Bioresource Technology. 2016; 199, 352-361. [13] M Ou, F Dong, W Zhang and Z Wu. Efficient visible light photocatalytic oxidation of NO in air with band-gap tailored (BiO)2CO3–BiOI solid solutions. Chemical Engineering Journal. 2014; 255, 650-658. [14] S.W Yao and H.P Kuo. Photocatalytic degradation of toluene on SiO2/TiO2 photocatalyst in a fluidized bed reactor. Procedia Engineering. 2015; 102, 1254-1260. [15] C Guillard, D Debayle, A Gagnaire, H Jaffrezic and J.M Herrmann. Physical properties and photocatalytic efficiencies of TiO2 films prepared by PECVD and sol–gel methods. Materials Research Bulleti. 2004; 39(10), 1445-1458. [16] J Kasanen, J Salstela, M Suvanto, and T.T Pakkanen. Photocatalytic degradation of methylene blue in water solution by multilayer TiO 2 coating on HDPE. Journal of Applied Surface Science. 2011; 258(5), 1738-1743. [17] D.F Ollis. Photocatalytic purification and remediation of contaminated air and water. Journal of Chemstry. 2000; 3, 405–411. [18] S Singh, H Mahalingam and P.K Singh. Polymer-supported titanium dioxide photocatalysts for environmental remediation: A review. Journal of applied catalysis a general. 2013; 462–463(0), 178-195. photocatalyst in a fluidized bed reactor. Proc. Eng. 2015; 102, 1254-1260. [15] C Guillard, D Debayle, A Gagnaire, H Jaffrezic and J.M Herrmann. Physical properties and photocatalytic efficiencies of TiO2 films prepared by PECVD and sol–gel methods. Mat. Res. Bullet. 2004; 39(10), 1445-1458. [16] J Kasanen, J Salstela, M Suvanto, and T.T Pakkanen. Photocatalytic degradation of methylene blue in water solution by multilayer TiO2 coating on HDPE. Appl. Surf. Sci. 2011; 258(5), 1738-1743. [17] D.F Ollis. Photocatalytic purification and remediation of contaminated air and water. J. Chem. 2000; 3, 405–411. [18] S Singh, H Mahalingam and P.K Singh. Polymer-supported titanium dioxide photocatalysts for environmental remediation: A review. Appl. Catal. A Gen. 2013; 462–463(0), 178-195. [19] A Zheng, Z Zhao, S Chang, Z Huang, F He, and H Li. Effect of torrefaction temperature on product distribution from two-staged pyrolysis of biomass. Energy Fuels. 2012; 26(5), 2968–2974. [20] J.J Pei, and J.S.S Zhang. Critical review of catalytic oxidization and chemisorption methods for indoor formaldehyde removal. Hvac&r. Res. 2011; 17, 476–503. [21] X Liang, Q Feihong, P Liu, G Wei, S Xiaoli, M Lingya, H Hongping, X Lin, Y Xi, J Zhu, and R Zhu. Performance of Ti-pillared montmorillonite supported Fe catalysts for toluene oxidation: The effect of Fe on catalytic activity. Appl. Clay Sci. 2016; 132-133, 96–104. แก้แหล่ง journal ให้เป็ นตัวอย่ำง เช่น Journal of applied catalysis a general. ให้ เป็ น Appl. Catal. A Gen. และ เพิ่มตัวหนำหลังปี ที่ตีพิมพ์ เช่น 2013; 462–463(0), 178-195. ให้เป็ น 2013; 462–463(0), 178-195.
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