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流化床快速制不定形活性焦脱除烟气中SO_2的研究 被引量:3

Study on SO_2 removal from flue gas by active coke prepared from fluidized bed reactor
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摘要 利用大型流化床制得了适用于脱除烟道气中二氧化硫的不定形活性焦ACA,并对其进行了特性分析,在固定床上考察了不同条件下脱除SO2的性能。与硫容相近的商业活性焦ACB的脱硫性能对比,发现其脱硫性能较好。实验结果表明,在烟气中的二氧化硫的体积分数为0.05%~0.12%,反应温度为80℃~100℃,空速(GHSV)为1200h-1,O2的体积分数为6%,水蒸气为10%的情况下,活性焦ACA保持SO2脱除率在90%以上达5h。再生循环脱硫实验表明,活性焦ACA具有良好的再生脱硫活性。 A kind of active coke (AC-A) for SO2 removal from flue gas was directly produced from a large scale fluidized bed gasifier. The desulphurization behavior and characteristics of the active coke (AC-A) were investigated under different conditions and compared with a commercial active coke ( AC-B ) with approximate saturated sulphur capacity. It is found tht adsorption temperature has complicate effect on the adsorption behavisot of AC-A produced. AC-A has a maximum sulfur removal ability at 100 ℃. It is not surprised to see a short adsorption period of AC-A with the increase of gas hourly space velocity (GHSV) or SO2 concentration. There are suitable values of oxygen concentration ( about 6% ) and steam concentration (about 10% ) for AC-A to obtain high sulfur removal ability. AC-A prepared shows higher desulfurization ability than commercial AC-B at the same adsorption conditions. Meanwhile, the desulphurization ability of regenerated active coke AC-A is also better than that of regenerated AC-B after every regeneration courses. This kind of active coke can be potentially used in the flue gas desulfurization, though efforts are needed to modify it.
出处 《燃料化学学报》 EI CAS CSCD 北大核心 2005年第4期465-469,共5页 Journal of Fuel Chemistry and Technology
基金 国家自然科学基金(90210002)~~
关键词 活性焦 脱硫 再生 流化床 active coke removal of SO2 regeneration fluidized bed
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  • 1赵修松,蔡光宇,王作周,杨永和,王清遐,罗静慎,盛世善,陈恒荣.活性炭催化剂上SO_2转化活性中心的研究[J].环境化学,1993,12(3):194-199. 被引量:18
  • 2前田勇 田中五夫.-[J].别册化学工业,1971,15(3):305-312.
  • 3渡部俊雄 田中建夫.-[J].化学装置,1988,(5):114-114.
  • 4植田腾.-[J].别册化学工业,1971,15(3):313-313.
  • 5八○二组.-[J].催化学报,1982,3(2):198-198.
  • 6-.化学工程手册(第一版)[M].北京:化学工业出版社,1989,10.10-80.
  • 7[1]LU G Q, DO D D. Preparation of economical sorbonts for SO2 and NOx removal using coal washery reject[J]. Carbon, 1991, 29(2):207-313.
  • 8[2]Knoblauch K, Richter E, Juntgen H. Application of active coke in processes of SO2 and NOx removal from flue gases[J]. Fuel, 1981, 60(9): 832-838.
  • 9[3]Juntgen H. New applications for carbonaceous adsorbents[J]. Carbon, 1977, 15(5):273-283.
  • 10[4]Carrasco-Marin F, Ultrera-Hidalgo E, Rivera-Utrilla J, et al. Adsorption of SO2 in flowing air onto activated carbons from olive stones[J]. Fuel, 1992, 71(5):575-578.

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  • 1刘卉卉,宁平.磷矿浆催化氧化湿法脱硫研究[J].化工矿物与加工,2005,34(7):12-14. 被引量:13
  • 2郑仙荣,李春虎,房靖华.改性半焦脱除烟气中SO_2的研究[J].环境污染与防治,2005,27(7):498-500. 被引量:7
  • 3马双忱,赵毅,马宵颖,郭天祥,刘皓磊,姚为方.微波诱导催化还原脱硫脱硝实验研究[J].中国电机工程学报,2006,26(18):121-125. 被引量:40
  • 4Ma H B, Chen P, Zhang M L, et al. Study of SO2 removal using non-thermal plasma induced by dielectric barrier discharge (DBD) [J]. Plasma Chemistry and Plasma Processing, 2002, 22 (2) : 239 -254.
  • 5Kanungo S B, Das R P. Extraction of metals frommanganese nodules of the Indian Ocean by leaching in a - queous of sulfur dioxide [J]. Hydrometallurgy, 1998, 20, 135-146.
  • 6Davini P. Desulfurization properties of active carbons obtained from petroleum pitch pyrolysis [ J]. Carbon, 1999, 37 (9) : 1 363-1 371.
  • 7Rubio B, Izquierdo M T. Low cost adsorbents for low temperature cleaning of flue gases [ J ]. Fuel, 1998, 77 (4) : 631 - 637.
  • 8Rubio B, Izquierdo M T. Influence of low-rank coal char properties on their SO2 removal capacity from flue gases: I. Nonactivated chars [J]. Carbon, 1997, 35 (7): 1 005-1 011.
  • 9Davini P. Desulfurization properties of active carbons obtained from petroleum pitch pyrolysis [ J ]. Carbon, 1999, 37 (9): 1363-1 371.
  • 10Davini P. Adsorption of sulfur dioxide on thermally treated active carbon [ J]. Fuel, 1989, 68 ( 1 ) : 145 - 148.

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