|
|
Two-stage system of non-thermal plasma and adsorption for
decomposition of hydrogen sulfide |
YANG Jian-tao, PAN Hua, CHEN Jie, SU Qing-fa, WANG Da-hui, SHI Yao |
Department of Environmental Engineering, Zhejiang University, Hangzhou 310027,China |
|
|
Abstract In order to overcome the high energy consumption and discharge of byproducts for decomposition of hydrogen sulfide with nonthermal plasma (NTP) alone, a twostage system of NTP and activated carbon fibers (ACF) was presented for decomposition of H2S. The effects of twostage system and single NTP system on H2S removal efficiency and byproducts were investigated at different input voltage. The synergistic mechanisms of NTP and ACF for H2S decomposition were also analyzed. The twostage system could remarkably improve the H2S removal efficiency, decrease the energy consumption and remove byproducts, while prolong the breakthrough time of ACF and increase the decomposition and adsorption capacity for H2S. The results showed that the two-stage system improved 15% of the H2S removal efficiency and reduced 26.5% of the energy consumption at 6 kV with a gasflow rate of 11.8 m3/h.The energy consumption of the two-stage system at 6 kV reduced 26.5%. ACF could remove the SO2 and O3, no SO2 and O3 were detected before the breakthrough time of ACF for H2S.The breakthrough time of ACF for H2S was prolonged from 2 to 16 times by NTP at the input voltage range from 3 to 7 kV.
|
Published: 01 December 2010
|
|
低温等离子体吸附两段式系统降解硫化氢
为了克服单一低温等离子体(NTP)降解硫化氢(H2S)能耗高和副产物排放的问题,采用低温等离子体活性炭纤维(ACF)吸附两段式系统降解硫化氢,考察不同充电电压两段式系统与单一低温等离子体系统对H2S降解率及副产物的影响,分析低温等离子体与活性碳纤维协同降解硫化氢的机理.研究表明:两段式系统能够显著提高H2S的去除率、降低能耗、去除副产物,并能延长ACF的穿透时间,增加吸附反应H2S的容量.当气体流量达到11.8 m3/h、充电电压为6 kV时,两段式系统能使H2S的去除率提高15%,能耗节省26.5%,ACF能够有效地去除SO2和O3,在ACF穿透前气流出口检测不到污染物;当充电电压从3 kV升高到7 kV时,ACF的穿透时间延长2到16倍.
|
|
[1] BOUZAZA A, LAPLANCHE S, MARSTEAU. Adsorptionoxidation of hydrogen sulfide on activated carbon fibers: effect of the composition and the relative humidity of the gas phase[J]. Chemosphere, 2004, 54(4): 481-488.
[2] MIKHALOVSKY S V, ZAITSEV Y P. Catalytic properties of activated carbons.1.Gasphase oxidation of hydrogen sulphide[J]. Carbon, 1997, 35(9):1367-1368.
[3] CANELA M C, ALBERICI R M, JARDIM W F. Gasphase destruction of H2S using TiO2/UVVIS[J]. Journal of Photochemistry and Photobiology A: Chemistry, 1998,112(1): 73-80.
[4] HUTTENHUIS P J, AGRAWAL N J, HOGENDOOM J A, et al. Gas solubility of H2S and CO2 in aqueous solutions of Nmethyldiethanolamine[J]. Journal of Petroleum Science and Engineering, 2007, 55(1/2): 122-134.
[5] YI H H, TANG X L, NING P, et al. Liquid phase catalytic oxidation of lowconcentration H2S in cerium doped absorption solution[J]. Journal of Rare Earths, 2007,25(suppl.): 253-256.
[6] LIMTRAKU S, ROJANAMATIN S, VATANATHAM T, et al. Gaslift reactor for hydrogen sulfide removal[J] Indusrial & Engineering Chemistry Research, 2005,44(16 ): 6115-6122.
[7] DENIS J. Pulsed corona discharge for hydrogen sulfide decomposition[J]. IEEE Transactions on Industry Applications, 1993,29 (5): 882-886.
[8] LI K T, YEN C S, SHYU N S. Mixedmetal oxide catalysts containing iron for selective oxidation of hydrogen sulfide to sulfur[J]. Applied Catalysis A: general, 1997,156(1): 117-130.
[9] TSAI C H, LEE W H, CHEN C Y, et al. Difference in conversions between dimethyl sulfide and methanethiol in a cold plasma environment[J]. Plasma Chemical and Plasma Process, 2003,23(1): 141-157.
[10] SOBACCHI M G, SAYELIEV A V, FRIDMAN A A, et al. Experimental assessment of pulsed corona discharge for treatment of VOC emissions[J]. Plasma Chemical and Plasma Process, 2003,23(2): 347-370.
[11] WANG X P, YAN N Q, JIA J P, et al. Removal of hydrogen sulfide in waste gases by pulse discharge plasma[J]. Chemical Industry and Engineering Progress, 2005, 25(3): 278-231.
[12] SHI Y, RUAN J J, WANG X, et al. Decomposition of mixed malodorants in a wireplate pulse corona reactor[J]. Environmental Science & Technology, 2005, 39(17): 6786-6791.
[13] RUAN J J, LI W, SHI Y, et al. Decomposition of simulated odors in municipal wastewater treatment plants by a wireplate pulse corona reactor[J]. Chemosphere, 2005,59 (3): 327-333.
[14] SHI Y, WANG X, LI W, et al.Evaluation of multiple corona reactor modes and the application in odor removal[J]. Plasma Chemistry and Plasma Processing, 2006,26(2): 187-196.
[15] YAN K, HEESCH E J M, PEMEN A J M, et al.From chemical kinetics to streamer corona reactor and voltage pulsed generator[J]. Plasma Chemistry and Plasma Processing, 2001, 21(1): 107-137.
[16] METTS T A, BATTEMAN S A. Effect of VOC loading on the ozone removal efficiency of activated carbon filters[J]. Chemosphere, 2006,26(1): 34-44.
[17] MASUDA J, FUKUYAMA J, FUJII S. Ozone injection into an activated carbon bed to remove hydrogen sulfide in the presence of concurrent substances[J]. Journal of the Air & Waste Management Association, 2001, 51(5): 750-755. |
|
Viewed |
|
|
|
Full text
|
|
|
|
|
Abstract
|
|
|
|
|
Cited |
|
|
|
|
|
Shared |
|
|
|
|
|
Discussed |
|
|
|
|