期刊文献+

焙烧温度对高温Mn-Fe-Ca脱硫剂脱硫性能的影响 被引量:3

EFFECT OF CALCINATION TEMPERATURE ON DESULFURIZATION PERFORMANCE OF Mn-Fe-Ca SORBENTS FOR HOT GOAL GAS DESULFURIZATION
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摘要 采用机械混合法制备了Mn-Fe-Ca脱硫剂,通过XRD,SEM和H2-TPR等手段研究了焙烧温度对脱硫剂的织构、物相和还原性能的影响,并在固定床反应器中考察了焙烧温度对脱硫剂脱硫性能的影响.结果表明,1 050℃下焙烧后的脱硫剂有较好的机械强度和脱硫性能,脱硫精度最高可达4×10-6,硫容量可达33.3%.焙烧温度的改变,可以改变脱硫剂的微观结构和反应活性. Desulfurization of coal-gas at high temperature is the critical technology improving energy utilizing efficiency. Mn-Fe-Ca sorbents were prepared by mixing methods and effect of calcination temperature on texture, phase, reducibility of Mn-Fe-Ca sorbents was investigated by XRD, SEM and H2-TPR. The effect of calcination temperature on desulfurization performance of Mn-Fe-Ca sorbents were studied in fixed bed reactor. The experimental results show that H2S could be desulfured to 4×10^-6 and sulfur content was 33.3% by the sorbents calcined at 1 050℃ which also had good mechanical intensity and desulfurization performance. The change of calcination temperature can effects the micro-structure and reactivity of the sorbents.
出处 《煤炭转化》 CAS CSCD 北大核心 2009年第2期45-49,共5页 Coal Conversion
基金 国家高技术研究发展计划(863)项目(2006AA11A189) 上海市科学技术委员会重点项目(06DZ12212) 先进钢铁材料技术国家工程研究中心资助项目(中050209)
关键词 锰基脱硫剂 高温煤气 焙烧温度 脱硫性能 manganese-based sorbent, hot gas, calcination temperature, desulfurization performance
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参考文献13

  • 1Tamhankar S S,Bagajenicz M,Gavalas G R et al. Mixed-oxide Sorbents for High-temperature Removal of Hydrogen Sulfide [J].Ind Eng Chem Process Des Dev, 1986,25 : 429- 436.
  • 2Flytzani S M,Gavalas R G,Tamhankar S S. High Temperature Regenerative H2S Sorbents. US Patent:4729889[P]. 1989.
  • 3Lee H S,Kang M P,Rhee Y M. Effect of Fe2Oa Additive on Reactivities of CuO-based Sorbents[C]. The 7th International Joint Symposium of Beijing University of Chemical Technology and Chungnam National University, Beijing, China, 2001:14- 18.
  • 4Mojtahedi W,Salo K, Abbasina J. Desulfurization of Hot Gas in Fluidized Bed with Regenerable Zinc Titanate Sorbents[J]. Fuel Process Technol, 1994,37 : 53-65.
  • 5Lew S,Sarofim A F,Flytzani S M. The Reduction of Zinc Titanate and Zinc Oxide Solids[J]. Chem Eng Sci, 1992,47 (6): 1421-1431.
  • 6Jale F A, Ates A. Hot C-as Desulfurization with Vanadium promoted Zinc Ferrite Sorbents[J]. Gas Sep Purif, 1995,9 (1) :17- 25.
  • 7Lew S, Jothimurugesan K, Flytzani S M. High-temperature H2S Removal from Fuel Gases by Regenerable Zinc Oxide-titanate Dioxide Sorbents[J]. Ind Eng Chem Res, 1989,28: 535-541.
  • 8Lee T J,Kwon W T,Won C C. Study of Regeneration of Zinc Titanate Sorbents for H2S Removal[J]. Korean J Chem Eng, 1997,14 (6) : 513-518.
  • 9祝方,李春虎,樊惠玲,李彦旭.国外高温煤气脱硫剂开发进展[J].煤炭转化,2000,23(2):17-22. 被引量:12
  • 10杜霞茹,黄戒介,房倚天,赵建涛,王洋.高温铁钙基脱硫剂的再生行为研究[J].煤炭转化,2005,28(1):56-60. 被引量:4

二级参考文献13

  • 1李彦旭.铁钙氧化物高温脱硫规律及动力学的研究(博士学位论文)[M].太原:太原理工大学,1999..
  • 2朴玲钰.铁酸锌高温煤气脱硫剂的制备及表征(硕士论文)[M].太原:太原理工大学,1999..
  • 3祝芳.助剂对高温煤气粗脱硫剂的影响(硕士论文)[M].太原:太原理工大学,2001..
  • 4Zeng Y, Zhang S, Groves F Get al. High Temperature Gas Desulfurization with Elemental Sulfur Production. Chemical Engineering Science, 1999,54 : 3007-3017.
  • 5Tamhankar S S, Garimella S, Wen C Y. Kinetics Study on the Reactions Involved in Hot Gas Desulfurization Using a Regenerable Iron Oxide Sorbent Ⅲ Reactions of the Sulfided Sorbent with Steam and Steam-air Mixtures. Chemical Engineering Sciences, 1985,40 (6) : 1019-1025.
  • 6Desal Niraw J, Yang Ralph T. Catalytic Fluidized-bed Combustion Enhancement of Sulfation Calcium Oxide by Iron Oxide.Ind Eng Chem Process Des Dev,1983,22.-119-123.
  • 7Shi Liming, Xu Xuchang. Study of the Effect of Fly Ash on Desulfurization by Lime. Fuel, 2001,80(4):1969-1973.
  • 8White J D, Groves Jr F R, Harrison D P. Elemental Sulfur Production During the Regeneration of Iron Oxide High Temperature Desulfurization Sorbent. Catal Today, 1998(40):47-57.
  • 9曹晏,张建民,王洋,张碧江.高温煤气脱硫技术研究进展[J].煤炭转化,1998,21(1):30-35. 被引量:14
  • 10李愉均.高阶思维视域下的小学科学探究性问题串设计策略[J].中小学教师培训,2012(12):50-53. 被引量:18

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