The characteristics of CuSnZr catalyst applied to NTP enhanced catalytic desulfurization process
ZHOU Zheng-hua1, JIANG Lian-shuang2, ZHANG Zhen-yu2, HUANG Rui2, NING Jing-yuan3, NING Zhi-yuan2
1. School of Materials and Energy, Yunnan University, Kunming 650000, China; 2. School of Chemical Science and Technology, Yunnan University, Kunming 650000, China; 3. Kunming Zhongkeyun Environmental Protection Co. LTD, Kunming 650000, China
Abstract:In order to efficiently process a large amount of low-concentration electrolytic aluminium flue gas at low temperature, the Sn Zr type metal oxide was prepared by the impregnation method with Cu added as a catalyst, and this desulfurization effect of CuSnZr catalyst was the first time to be tested in low temperature plasma (NTP) technology. The best desulfurization performance results when the catalyst was loaded with 20wt% Cu and when the aging temperature was 40℃. Compared with the fresh catalyst, the X-ray diffraction analysis (XRD) results showed that the discharge basically did not affect the crystal form of the catalyst; the scanning electron microscopy (SEM), nitrogen adsorption and desorption (BET) indicated that the discharge will greatly improve the adsorption capacity, the desorption capacity and the pore structure of the catalyst; X-ray photoelectron spectroscopy (XPS) also showed that the discharge will change the valence state of the elements on the catalyst surface, thereby changing its redox performance and deviating the reaction path. For the catalyst performance analysis, theoretical calculations indicate that the increase in copper content will cause changes in the energy band structure of the catalyst, which is better used for exciting gas.
Hanif M A, Ibrahim N, Jalil A A. Sulfur dioxide removal: An overview of regenerative flue gas desulfurization and factors affecting desulfurization capacity and sorbent regeneration [J]. Environmental Science and Pollution Research, 2020, 22(27): 27515–40.
[2]
余创, 彭学斌, 田林, 等. 电解铝烟气脱硫技术研究进展[J]. 云南冶金, 2019, 4(48): 40-43. Yu C, Peng X B, Tian L, et al. Research progress of electrolytic aluminum flue gas desulfurization technology [J]. Yunnan Metallurgy, 2019, 4(48): 40-43.
[3]
Wang X H, Wang A Q, Li N, et al. Catalytic reduction of SO2 with CO over supported iron catalysts [J]. Industrial & Engineering Chemistry Research, 2006, 45(13): 4582-4588.
[4]
Feng T, Zhao X, Wang T, et al. Reduction of SO2 with CO to elemental sulfur in activated carbon bed [J]. Energy & Fuels, 2016, 30(8): 6578-6584.
[5]
Han G B, Park N K, Yoon S H, et al. Synergistic catalysis effect in SO2 reduction by CO over Sn–Zr-based catalysts [J]. Applied Catalysis A General, 2008, 337(1): 29-38.
[6]
Han G B, Park N K, Lee T J. Effect of O2 on SO2 reduction with CO or H2 over SnO2-ZrO2 Catalyst [J]. Industrial & Engineering Chemistry Research, 2009, 48(23): 10307-10313.
[7]
Park N K, Park J Y, Lee T J, et al. Catalytic reduction of SO2 over Sn-Zr based catalysts for DSRP under high pressure [J]. Catalysis Today, 2011, 174(1): 46-53.
[8]
Park N K, Lee T H, Lee T J, et al. Catalytic reduction of SO2 under the regeneration of off-gas containing oxygen over Cu-Sn-Zr-based oxides for the hot coal gas desulfurization process [J]. Catalysis Today, 2016, 265: 131-137.
[9]
Happel M, Lykhach Y, Tsud N, et al. SO2 decomposition on Pt/CeO2(111) model catalysts: On the reaction mechanism and the influence of H2 and CO[J]. The Journal of Physical Chemistry C, 2012, 116(20): 10959-1096.
[10]
Zhao H, Luo X, He J, et al. Recovery of elemental sulphur via selective catalytic reduction of SO2 over sulphided CoMo/γ-Al2O3 catalysts [J]. Fuel, 2015, 147(may 1): 67-75.
[11]
Gao G P, Wei S H, Guan X M, et al. Influence of charge state on catalytic properties of PtAu(CO)n in reduction of SO2 by CO [J]. Chemical Physics Letters, 2015, 625: 128-131.
[12]
Zhang L, Qin Y H, Chen B Z, et al. Catalytic reduction of SO2 by CO over CeO2–TiO2 mixed oxides [J]. Transactions of Nonferrous Metals Society of China, 2016, 26(11): 2960-2965.
[13]
Ban, Z, Zhang, J, Wang, S, et al. Direct reduction of SO2 to elemental sulfur by the coupling of cold plasma and catalyst (Ⅰ) [J]. Industrial & Engineering Chemistry Research, 2004, 17(43): 5000-5005.
[14]
Mizuno A, Clements J S, Davis R H. A method for the removal of sulfur dioxide from exhaust gas utilizing pulsed streamer corona for electron energization [J]. IEEE Transactions on Industry Applications, 2008, 22(3): 516-522.
[15]
Onda K, Kasuga Y, Kato K. Electric discharge removal of SO2 and NOx from combustion flue gas by pulsed corona discharge [J]. Energy Conversion & Management, 1997, 38(10): 1377-1387.
[16]
Feng F, Ye L, Liu J, et al. Non-thermal plasma generation by using back corona discharge on catalyst [J]. Journal of Electrostatics, 2013, 71(3): 179-184.
[17]
Feng F, Zheng Y, Shen X, et al. Characteristics of back corona discharge in a honeycomb catalyst and its application for treatment of volatile organic compounds [J]. Environmental ence & Technology, 2015, 49(11): 6831-6837.
[18]
Moon J D, Jung J S, Effective corona discharge and ozone generation from a wire-plate discharge system with a slit dielectric barrier [J]. Journal of Electrostatics, 2007, 65(10/11): 660-666.
[19]
Mista W, Kacprzyk R. Decomposition of toluene using non-thermal plasma reactor at room temperature [J]. Catalysis Today, 2008, 137(2-4): 345-349.
[20]
Moscosa-Santillan M, Vincent A, Santirso E, et al. Design of a DBD wire-cylinder reactor for NOx emission control: experimental and modelling approach [J]. Journal of Cleaner Production, 2008, 16(2): 198-207.
[21]
Schiorlin M, Marotta E, Rea M, et al. Comparison of toluene removal in air at atmospheric conditions by different corona discharges [J]. Environmental science & Technology, 2009, 43(24): 9386-9392.
[22]
Ban L, Liu P, Ma C, et al. Deep desulfurization of diesel fuels with plasma/air as oxidizing medium, diperiodatocuprate (Ⅲ) as catalyzer and ionic liquid as extraction solvent [J]. Plasma science and Technology, 2013, 15(12): 1226-1231.
[23]
Ban L L, Liu P, Ma C H, et al. Deep oxidative/adsorptive desulfurization of model diesel oil by DBD/FeCl3–SiO2 [J]. Catalysis Today, 2013, 211: 78-83.
[24]
Zhang H, Wang W, Li X, et al. Plasma activation of methane for hydrogen production in a N2 rotating gliding arc warm plasma: A chemical kinetics study [J]. Chemical Engineering Journal, 2018, 345: 67–78.
[25]
Pianaro S A, Bueno P R, Longo E, et al. Microstructure and electric properties of a SnO2 based varistor [J]. Ceramics International, 1999, 25(1): 1-6.
[26]
Maki-Jaskari M A, Rantala T T. Density functional study of Pd adsorbates at SnO2 (110) surfaces [J]. Surface Science, 2003, 537(1-3): 168-178.