期刊文献+

410t/h煤粉锅炉的汞排放及其NID系统除汞特性研究 被引量:7

Characteristics of mercury emission and demercurization property of NID system of a 410t/h pulverized coal fired boiler
下载PDF
导出
摘要 对配备有NID系统的410t/h燃煤电站锅炉的煤、底渣、飞灰进行取样,测定了样品中汞的含量。采用Ontario-Hydro方法测定了NID前和ESP后烟气中汞的形态。实验结果表明,汞主要以飞灰形式排放,占总汞量的90%,烟气汞占10%。NID前和ESP后的烟气中,汞的浓度分别为21.3μg/m^3~22.4μg/m^3和1.93μg/m^3~3.67μg/m^3,说明该NID系统对烟气中汞具有相当高的脱除效率,达到83.6%-90.9%。对汞的化学形态研究表明,NID前烟气汞主要以Hg^2+形式存在,占气态汞量的67%;ESP后烟气中Hg^2+占气态汞量的71.8%-85.1%,Hg^0的含量为零,说明烟气中Hg^0在NID系统中经历一系列的氧化还原反应后.被氧化成Hg^2+并吸附脱除。 Coal, slag, and fly ashes were sampled from a 410 t/h utility boiler with the equipment of NID ( Novel Integrated Desulfurization) system and mercury concentrations of these samples were determined. Ontario-Hydro method was applied to determine mercury speciation in flue gas before NID and after ESP. The experimental data indicate that the majority of mercury goes into fly ash. The ratio of mercury quantity in fly ash to total combustion product is about 90% , while that in flue gas is about 10%. The results also show that before NID and after ESP, the gaseous mercury concentration in the flue gas is about 21.3 μg/m^3 - 22. 4 μg/m^3 and 1. 93μg/m^3 -3.67 μg/m^3 respectively, indicating that the NID system has quite high mercury removal efficiency up to 83.6% - 90.9%. The percentage of Hg^2+ which is the main mercury speciation in flue gas before NID is about 67%. The percentage of Hg^2+ in flue gas after ESP is about 71.8% -85.1%, while the content of Hg^0 is zero, indicating that some chemical reactions have been happened to Hg^0 when it passes by NID system. Hg^0 becomes Hg^2+ and is then adsorbed and removed.
出处 《燃料化学学报》 EI CAS CSCD 北大核心 2008年第5期540-544,共5页 Journal of Fuel Chemistry and Technology
基金 国家重点基础研究发展规划(973计划 2006CB200304)
关键词 煤粉锅炉 NID系统 形态分布 脱除效率 pulverized coal fired boiler NID system mercury speciation distribution removal efficiency
  • 相关文献

参考文献16

  • 1THOMAS D B, DENNIS N S, RICHARD A H. Mercury measurement and its controL: What we know, have learned, and need to further investigate [ J ]. J Air Waste Manage Assoc, 1999, 49 (6) : 200-204.
  • 2郭欣,郑楚光,吕乃霞.簇模型CaO(001)面上吸附汞与氯化汞的密度泛函理论研究[J].中国电机工程学报,2005,25(13):101-104. 被引量:26
  • 3任建莉,周劲松,骆仲泱,徐璋,张雪梅.钙基类吸附剂脱除烟气中气态汞的试验研究[J].燃料化学学报,2006,34(5):557-561. 被引量:52
  • 4郭欣,郑楚光,贾小红,林钊,刘亚明.300MW煤粉锅炉烟气中汞形态分析的实验研究[J].中国电机工程学报,2004,24(6):185-188. 被引量:90
  • 5陈进生,袁东星,洪有为,郭娟.烟气催化脱硝装置对多环芳烃排放特性的影响[J].燃料化学学报,2007,35(6):722-726. 被引量:6
  • 6SENIOR C L, SAROFIM A F, ZENG T, HELBLE J J, MAMANI-PACO R. Gas-phase transformations of mercury in coal-fired power plants [J]. Fuel Process Technol, 2000, 63(2-3) : 197-213.
  • 7HALL B, SCHAGER P, LINDQVIS O. Chemical reactions of mercury on combustion flue gases[J]. Water Air Soil Pollut, 1991,56: 3-14.
  • 8TAKAHISA Y, KAZUO A. Mercury emissions from a coal-fired power plant in Japan[J]. Sci Total Environ, 2000, 259: 97-103.
  • 9LEE T G, BISWAS P, HEDRICK E. Comparison of Hg^0 capture efficiencies of three in situ generated sorbents[J]. AIChE J, 2001,47(4) : 954-961.
  • 10CAO Y, CHEN B, WU J, CUI H, SMITH J, CHEN C K, CHU P, PAN W P. Study of mercury oxidation by a selective catalytic reduction catalyst in a pilot-scal slipstream reactor at a utility boiler burning bituminous coal [J].Energy Fuels, 2007, 21( 1 ) : 145-156.

二级参考文献50

  • 1王宝凤,王刚,李文,陈皓侃,李保庆.亚临界水条件下煤中汞的脱除[J].燃料化学学报,2004,32(5):513-516. 被引量:8
  • 2郭欣,郑楚光,吕乃霞.簇模型CaO(001)面上吸附汞与氯化汞的密度泛函理论研究[J].中国电机工程学报,2005,25(13):101-104. 被引量:26
  • 3[2]PISUPATI S V,WASCO R S,SCARONI A W.An investigation on polycyclic aromatic hydrocarbon emissions from pulverized coal combustion systems[J].J Hazard Mater,2000,74(1-2):91-107.
  • 4[3]CHEN Y,BI X,MAI B,SHENG G,FU J.Emission characterization of particulate/gaseous phases and size association for polycyclic aromatic hydrocarbons from residential coal combustion[J].Fuel,2004,83(7-8):781-790.
  • 5[4]dos SANTOS C Y M,de ALMEIDA AZEVEDO D,de AQUINO NETO F R.Atmospheric distribution of organic compounds from urban areas near a coal-fired power station[J].Atmos Environ,2004,38(9):1247-1257.
  • 6[5]YANG H-H,CHEN C-M.Emission inventory and sources of polycyclic aromatic hydrocarbons in the atmosphere at a suburban area in Taiwan[J].Chemosphere,2004,56(10):879-887.
  • 7[6]LI C-T,MI H-H,LEE W-J,YOU W-C,WANG Y-F.PAH emission from the industrial boilers[J].J Hazard Mater,1999,69(1):1-11.
  • 8[10]KLINGSTEDT F,KALANTAR NEYESTANAKI A,LINDFORS L-E,SALMI T,HEIKKIL(A) T,LAINE E.An investigation of the activity and stability of Pd and Pd-Zr modified Y-zeolite catalysts for the removal of PAH,CO,CH4 and Nox emissions[J].Appl Catal A,2003,239(1-2):229-240.
  • 9[11]KLINGSTEDT F,KALANTAR NEYESTANAKI A,BYGGNINGSBACKA R,LINDFORS L-E,LUNDEN M,PETERSSON M,TENGSTR?M P,OLLONQVIST T,V(O)YRYNEN J.Palladium based catalysts for exhaust aftertreatment of natural gas powered vehicles and biofuel combustion[J].Appl Catal A,2001,209(1-2):301-316.
  • 10[12]GABRIEL J,BALDRIAN P,VERMA P,CAJTHAML T,MERHAUTOVá V,EICHLEROVá I,STOYTCHEV I,TRNKA T,STOPKA P,NERUD F.Degradation of BTEX and PAHs by Co(Ⅱ) and Cu(Ⅱ)-based radical-generating systems[J].Appl Catal B,2004,51(3):159-164.

共引文献170

同被引文献104

引证文献7

二级引证文献73

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部