直流电晕放电诱导自由基簇射烟气脱硝试验和机理研究
详细信息    本馆镜像全文|  推荐本文 |  |   获取CNKI官网全文
摘要
本文首先评述了各种烟气脱硝技术,并阐述了电晕放电脱除烟气中NO_x的研究成果以及对放电机理的研究状况。
     研究了以NH_3为自由基源物质的烟气脱硝过程。研究表明,烟气湿度对放电的发展起抑制作用,但适当的烟气湿度对提高氮氧化物脱除效率有促进作用,烟气含湿量在10%左右时,单位能量脱除的氮氧化物量最多,是脉冲电晕法的两倍。烟气温度对放电过程影响不明显,但是,烟气温度提高对氮氧化物的脱除不利。烟气流量对放电过程影响较小。氮氧化物脱除率随流量增加而降低,但是提高烟气流量可以提高能量的利用率,烟气在反应器内的停留时间为5~7.5s比较合适,通过进一步延长停留时间来达到进一步提高脱除率是不经济的。烟气中氮氧化物浓度的增加会降低脱除效率,但能量的利用效率会相应提高。减小电极间距将降低起晕电压和击穿电压,加大极间距有利于获得更高的放电功率。
     用O_2+H_2O混合气体簇射结合碱液化学吸收,对烟气中氮氧化物的脱除进行了研究。如果水蒸气体积百分比适量,可以产生稳定的流光电晕。在反应器内,NO主要有两条转化途径,一是被氧化成NO_2,后又与OH自由基反应生成HNO_3,另一途径是与OH自由基反应,生成HNO_2。反应器内的主要反应产物为HNO_3,最高DeNO_x效率达70%以上。增加电极中氧气的湿度可提高反应器内的DeNO_x效率。NaOH溶液对NO的吸收率小于30%,而对NO_2的吸收率在90%以上。经过NaOH溶液吸收后,烟气总DeNO_x效率最高可达90%。Ca(OH)_2溶液对NO_2的吸收比较充分,因此,以传统湿法(半干法)烟气脱硫系统作为电晕放电氧化氮氧化物所产生的氧化产物的吸收系统是可行的。
     采用模拟电荷法和复变换对静态边缘电场进行了模拟。通过模拟,从理论上证明本文实验方案是可行的,并且得到了静态电场的求解方法,为下一步的工作奠定了基础。在静电场模拟中,还求解出流光电晕放电的临界点,为蒙特卡罗法模拟流光电晕放电提供了基准点。
     采用蒙特卡罗法针对本文实验系统进行了流光电晕放电的模拟。模拟结果表明,电子的能量在不同的空间位置分布不同,靠近正极,高能态电子数量有增加的趋势。空间电场因空间电荷的累积而扭曲,在靠近正极附近的区域,电场比拉普拉斯电场强度有所降低,而靠近负极处,电场强度相应增强。由于电场扭曲,流光电晕呈脉冲形式出现,电流也呈脉冲形式。
     初步计算了自由基簇射过程中各种自由基的单位能量产率。计算结果证明,在自由基簇射系统中,烟气中N_2的分解率较小,而O_2和H_2O分解率相对较高。
     计算了NO_x在反应器内的氧化效率,理论与实验值基本吻合。计算了功率
    
    浙江大学博士学位论文
    为2.5w时不同烟气流速条件下的NO:脱除效率,发现在一定的功率条件下,
    烟气停留时间增加使脱除率提高,但是,降低了能量利用效率。
     预测了当喷嘴气体湿度变化时,反应器内NO、氧化效率的变化,发现当喷
    嘴气体含湿量为9%时,NO:氧化效率最高达90%以上。
     结合传统湿法脱硫脱硝技术,提出了电晕氧化结合传统湿法同时脱除烟气
    中二氧化硫和氮氧化物的工艺流程。
The thesis reviewed every kind of flue-gas DeNOx technologies firstly, and introduced both the research results of removal of the NOX from flue-gas with corona discharge technologies and the research work on discharge mechanism.
    The experiments on removal of NOX from the flue-gas using NH3 as radical resource were carried out. The results showed that water vapor restrains the discharge process, but proper content of water vapor in flue-gas will improve the removal efficiency, the quantity of NOX that removed by unit energy from the flue-gas that contained 10% of water vapor is the highest, and double that of pulsed corona technologies. The temperature of flue-gas affected on the discharge process a little, but high temperature would reduce the removal efficiency of NOX. The flow rate of flue-gas impacted on the discharge faintly. The higher the flow rate of flue-gas is, the higher energy efficiency would be obtained. It is moderate that the flue-gas residues in the reactor for 5-7 seconds. To improve the removal efficiency by the way of lengthening residence time of flue-gas in the reactor is not economical. The removal efficiency would be reduced if the concentration of the NOX increased, the energy efficiency enhanced on the other hand. The shorter distance between the anode and the cathode would result in both lower started corona voltage and lower breakdown voltage. Long distance is beneficial to obtaining high discharge power.
    Removal of NOX from flue-gas by H2O+O2 radical injecting integrating with alkali solution scrubbing is carried out. The steady streamer corona occurred when the water vapor feed into the nozzle electrodes was moderate. Some of the NO will convert into NO2 in the reactor. The NO2 react with OH radicals and convert into HNO3 at the end. The rest of NO in the reactor converts into HNO3 after reacting with OH radicals. Most of the reaction production in the reactor is HNO3. The highest DeNOx efficiency is above 70%. To increase the humidity of the oxygen that feed into the nozzles will improve the DeNOx efficiency. The NO absorbed by NaOH solution was little than 30%, the percent of NO, absorbed by NaOH solution was more than 90%. The overall DeNOx efficiency approached 90% after the flue gas absorbed by NaOH solution and the Ca(OH)2 solution absorbed the NO2 well also. This indicated that to remove the NOX, which is the production of corona discharge, by wet desulfurization system is feasible.
    The electrostatic field of the nozzle brim was simulated with simulation-charge technique and complex transformation. The experiment project was proved to be
    
    
    
    feasible by simulation process. The solution of electrostatic field was approached and this is the foundation of the subsequent research. The critical position, which was the start position of the Monte Carlo simulation of steamer corona discharge, was solved too.
    The streamer corona discharge in the experiment system was simulated with Monte Carlo simulation. The simulation result showed that the electron energy distribution of different positions is different. The quantity of higher-energy electrons near the anode is much more than other positions. The space electric field is distorted because of the charges accumulation. The electric field near the anode is lower than Laplace electric field, and the electric field near the cathode is higher than Laplace electric field. The streamer corona appears as pulse because of the distorted electric field, and the discharge current appears as pulse too.
    The unit energy yield of every kind of radicals in the radical injecting process was computed. The dissociated probability of the N2 in the flue-gas is low, but the dissociated probabilities of O2 and H2O are high comparatively.
    The oxidizing efficiency of NOx in reactor was forecasted, and the computed results are accordant with the experiment results. The removal efficiency of NOx was computed in different velocity flue-gas at a constant power of 5 watt. It was founded that the removal efficiency of NOX increases with the residues ti
引文
1.米都斯,增长的极限,四川人民出版社,1984:6.
    2.岑可法,倪明江,骆仲泱等著,循环流化床锅炉理论设计与运行,北京:中国电力出版社,1997.
    3.刘孜,关于我国NO_x污染指标及控制措施等有关问题的探讨,国家环境保护总局大气噪声处,2000:9.
    4.德利克.埃尔森,Smog Alert,科学出版社,1999:5.
    5. Inventory of U.S. Greenhouse Gas Emissions and Sinks: 1990-1998 EPA-R-00-001 April, 2000.
    6. Simpson, D., Eliassen, A., Tackling multi-effect problem-an iterative approach, The Science of the Total Environment, 1999, 234:43-48.
    7.刘希玲,洪少贤,中国2000年大气氮氧化物污染趋势预测研究,环境科技,1995,12(4).
    8. Mitigation Analysis For Hungary Interim Report Budapest August, 1996.
    9.王兰新,烟气脱硫脱硝的进展,化学研究与应用,1997,9(4).
    10.朱联锡,卢虹等,烟气脱硫脱硝技术进展情况,环境科技,1996,13(2).
    11.陈笃慧,燃煤烟气中SO_2和NO_x的防治,化工环保,1997年,17(5).
    12. Robert Mclnnes, Mary B.Van, Wormer, Cleaning up NOx emissions chemical engineering, 1990, 9.
    13. Lyon,R., Thermal DeNO_x-Controlling Nitrogen Oxides Emissions by a Noncatalytic Process, Environmental Science and Technology, 1987, 21(3):231-236.
    14. Kawamura, K., Hirasawa, A., et al., Pilot plant experiment of NO_x and SO_2 removal from exhaust gases by electron beam irradiation, Radiat. Phys. Chem., 1979, 13:5-12.
    
    
    15. 邰德荣,韩宾兵,成都电厂电子束烟气脱硫示范工程,中国电力,1998,31(11) .
    16. Kawamura, K., et al. On the removal of NOX and SO2 in Exhaust Gas from the Sintering Machine by Eletron Beam Irradiation, Radiat.Phys.Chem., 1980, 16:133-138.
    17. Masuda, S., et al., Control of NOX by Positive and Negative Pulsed Corona Discharge, IEEE/IAS Annu. Conf., 1986:1173-1182.
    18. Mizuno, A., et al., A Device for Removal of Sulfur Dioxide Exhaust Gas by Pulsed Energixation of Free Electrons, Proc. of IEEE/IAS, 1984 Annual Conf., 1984:1025-1182.
    19. Tokunaga, O., Suzuki, N., Radiation chemical reactions in NOX and SO2 removals from flue gas, Radiat. Phys. Chem., 1990, 24(1) : 145-165.
    20. Senichi Masuda, Hideyuki Nakao, Control of NOX by positive and negative pulsed corona discharges, IEEE Transactions on Industry Applications, 1990, 26(2) :374-383.
    21. Keping Yan, Hexing Hui, et al., Corona induced non-thermal plasmas: fundamental study and industrial applications, Journal of Electrostatics, 1998, 44:17-39.
    22. Jen-Shih Chang, Phil A. Lawless, Toshiaki Yamamoto, Corona discharge processes, IEEE Transactions on plasma science, 1991,19(6) : 1152-1161.
    23. Tomio Fujii, Removal of NOX by DC Corona Reactor with Water, Journal of Electrostatics, 2001, 51:8-14.
    24. Yamamoto, T., et al., Ttiangle-shaped DC Corona Discharge Device for Melecular Decomposition, IEEE Trans, on Ind. Appl., 1982,25(4) : 743-749.
    25. Chang, J.S., et al., Corona Discharge Processes, IEEE Trans, on Plasma Science, 1991,19(6) : 1152-1165.
    26. Chang, J.S., Hayama, M., Ono, S., Teii, S., Ar-NH3 Mixture gas positive column plasma, Chemical Engineering Science, 1989, 5:351-355.
    27. Bemie M. Penetrante, Mark C. Hsiao, et al., Comparison of electrical discharge techniques for non-thermal plasma processing of NO in N2, IEEE Trans. On plasma science, 1995,23(4) : 679-687.
    28. Mizuno, A., et al., A Method for the Removal of Sulfur Dioxide from Exhaust Gas Utilizing Pulsed Streamer Corona for Electron Energization, IEEE Trans. On Ind. Appl., 1986,22(3) : 512-522.
    29. Rongyi Wang, et al., Apparent Energy Yield of a High Efficiency Pulse Generator With Respect to SO2 and NOx Removal, J. of Electrostatics, 1995, 34:355-366.
    
    
    30. Ruinian Li, et al., A Phenomenon of Oxidation in Removal of S02 from Flue Gas by Positive Pulsed Streamer, The 2nd International conference on Applied Electrostatics, 1993:32-38.
    31. Yamamoto, T., et al., Triangle-shaped DC Corona Discharge Device for Molecular Decomposition, IEEE Trans, on Ind. Appl., 1982, 25(4) : 743-749.
    32. Chang, J.S., et al., Corona Discharge Processes, IEEE Trans, on Plasma Science, 1991,19(6) : 1152-1165.
    33. Eliasson, B., et al., Modeling and Application of Silent Discharge Plasma, IEEE Trans, on Plasma Science, 1991,19(2) : 309-323.
    34. Oda, T., et al., Decomposition of Fluorocarbon Gaseous Contaminants by Surface Discharge-Induced Plasma Chemical Processing, IEEE Trans, on Ind. Appl., 1993, 29(4) : 787-792.
    35. Zhang, R.H., et al., Control of Ammonia and Odors in Animal House by a Ferroelectrics Plasma Reactor, IEEE/IAS Annu. Conf., 1994:1545-1549.
    36. Yamamoto, T., et al., Control of Volatile Organic Compounds by an Ac Energized Ferroelectrics Pellet Reactor and a Pulsed corona Reactor, IEEE Trans, on hid. Appl., 1992, 28(3) :528-533.
    37. Loeb, L.B., Electrical Corona, Bereley, CA:Univ. Of California Press, 1965.
    38. Gallimberti, L, A computer Model for Streamer Propagation, J. Phys. D: Appl. Chem., 1972, 5:2179-2189.
    39. James T. Yeh, Warren T. Ma, et al., Integrated testing of the NOXSO process: simultaneous removal of SO2 and NOX from flue gas, Chem. Eng. Comm., 1992, 114:65-88.
    40. Gate Jones, Meeting compliance and profit goals takes ingenuity, fortitude, Emissions Control, 1999:63-65.
    41. Dougtas J. Smith, NOX emission control demands a range of solutions, Power Engineering, 1992:44-47.
    42. ABB Power Plant Laboratories, NOX: U.S. Plants take aim at a moving target, Chemical Engineering, 1994:28-41.
    43. Robert J. Chironna, Boris Altshuler, Chemical aspects of NOX scrubbing, Pollution Engineering, 1999, 4:32-36.
    44. Sirpa K. Nelo, Kalsu M. Leskela, Jorma J.K. Sohlo, Simultaneous oxidation of nitrogen oxides and sulfur dioxide with ozone and hydrogen peroxide, Chem. Eng. Technol., 1997,20:40-42.
    45. Si Noroozi, Fluor Daniel, Urea enhances safety in SCR applications, Power
    
    Engineering, 1993,12:28-35.
    46. David A. Rundstrom, James L. Reese, Catalyst air heater retrofit reduces NOX emissions, Power Engineering, 1992, 8:38-40.
    47. Anderson, C.M., Billings, J.A., Simple calculation measures NH3 slip for cogeneration units, Power Engineering, 1991,4:42-44.
    48. Eric Darmstaedter, Sodium bicarbonate injection: a small-plant SO2/NOX option, Power Engineering, 1990,12:25-27.
    49. Ed Cichanowicz, Selective catalytic reduction controls NOX in Europe, Power Engineering, and 1988:36-38.
    50. Paul Wagner, P.E., Greg Cook, SCR succeeds at Logan generating plant, Power Engineering, 1997,1: 28-32.
    51. Dhali, S.K., et al., Dielectric-barrier Discharge for Processing of SO2/NOX, J. Appl. Phys., 1991, 69(9) : 6319-6324.
    52. Rittenhouse, R.C., Action builds on 1990 clean air act compliance, Power Engineering, 1992,5:21-27.
    53. Nicholas J. Rossi, How to control NOX, Pollution Engineering, 1995,4:50-52.
    54. Kuniko Urashima, Jen-Shih Chang, Tairo Ito, Reduction of NOX from combustion flue gases by superimposed barrier discharge plasma reactors, IEEE Transactions on Industry Applications, 1997, 33(4) :879-886.

© 2004-2018 中国地质图书馆版权所有 京ICP备05064691号 京公网安备11010802017129号

地址:北京市海淀区学院路29号 邮编:100083

电话:办公室:(+86 10)66554848;文献借阅、咨询服务、科技查新:66554700