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利用导热油换热技术回收焦炉上升管余热 被引量:1

Recovery of waste heat from ascension pipe by heat transfer oil
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摘要 焦炉荒煤气温度达700-800益,因此利用导热油换热技术对上升管余热进行回收利用。实践证明,导热油换热回收上升管余热系统运行稳定、安全性好、可靠性高、实用性强。 The temperature of raw gas from coke oven reaches 700~800°C,therefore it is necessary to utilize the waste heat from ascension pipe by heat transfer oil.After put into operation,this approach proves stable,safe,reliable and practical.
作者 冯敏超 杨丽 Feng Minchao;Yang Li(TangShan Vocational College of Science and Technology,Tangshan063001,China)
出处 《燃料与化工》 2022年第4期52-53,共2页 Fuel & Chemical Processes
关键词 上升管 余热回收 导热油 Ascension pipe Waste heat recovery Heat transfer oil
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  • 1陈维汉.一种考虑综合性能优化的换热器热设计方法(一)[J].化工装备技术,2006,27(4):35-43. 被引量:6
  • 2李铁,李伟力,袁竹林.用不同辐射模型研究下降管内传热传质特性[J].中国电机工程学报,2007,27(2):92-98. 被引量:29
  • 3Cao Y, Wang Y, Riley J T, et al. A novel biomass air gasification process for producing tar-free higher heating value fuel gas[J]. Fuel Processing Technology, 2006,87(4) : 343 - 353.
  • 4Dogru M, Midilli A, Howarth C R. Gasification of sewage sludge using a throated downdraft gasifier and uncertainty analysis[J ]. Fuel Processing Technology, 2002,75( 1 ) : 55 - 82.
  • 5Dogru M, Howarth C R, Akay G, et al. Gasification of hazelnut shells in a downdraft gasifier[J]. Energy, 2002,27 (5):415-427.
  • 6Pathak B S, Patel S R, Bhave A G, et al. Performance evaluation of an agricultural residue-based modular throat-type down-drairt gasifier for thermal application[J]. Biomass and Bioenergy, 2008,32(1) : 72 - 77.
  • 7Seshadri K S. Effects of temperature, pressure and carrier gas on the cracking of coal tar over a char-dolomite mixture and calcined dolomite a fixed-bed reactor[J]. Industrial & Engineering Chemistry Research, 1998, 37 ( 10 ): 3830 -3837.
  • 8Hesp W R, Waters P L. Thermal cracking of tars and volatile matter from coal carbonization [J]. Industrial & Engineering Chemistry Product Research & Development, 1970,9(2) : 194 - 202.
  • 9Doolan K R, Mackie J C, Tyler R J. Coal flash pyrolysis secondary cracking of tar vapours in the range 870- 2 000 K [J]. Fuel, 1987,66(4):572-578.
  • 10Stiles H N, Kandiyoti R. Secondary reactions of flash pyrolysis tars measured in a fluidic bed pyrolysis reactor with some novel design feature[J]. Fuel, 1989, 68(3) : 275 - 282.

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