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Received April 24, 2016
Accepted August 19, 2016
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Pneumatic transport characteristics of coarse size pulverized coal for the application of fast circulating fluidized bed gasification
Jin Wook Lee†
Seok Woo Chung
Sang Oh Ryu
Ji Eun Lee
Yongseung Yun
Chan Lee1
Yongjeon Kim2
Sungkwang Lim2
Plant Engineering Center, Institute for Advanced Engineering, Yongin 17180, Korea 1Department of Mechanical Engineering, Suwon University, Suwon 18323, Korea 2SK Innovation Global Technology, Daejeon 34124, Korea
jwlee@iae.re.kr
Korean Journal of Chemical Engineering, January 2017, 34(1), 54-61(8), 10.1007/s11814-016-0237-9
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Abstract
The pneumatic transport characteristics of pulverized coal with very coarse grain size were investigated, especially related to fast circulating fluidized bed gasifier. The lock hopper system was used along with the top discharge blow tank technology to examine the transportation characteristics of pulverized coal. The most important factors among the pulverized coal transportation properties were mass flow rate of pulverized coal and the solid loading ratio, which changed with the amount of fluidization nitrogen and differential pressure between injection hopper and gasifier. The mass flow rate of the pulverized coal and the solid loading ratio were linearly proportional to changes in differential pressure, and were inversely proportional to changes in the amount of fluidization nitrogen. In the case of extended transport line, similar feeding characteristics were obtained by increasing the differential pressure while the level of fluidization nitrogen was kept constant. Pressure losses were observed with changes in the mass flow rate of pulverized coal, solid loading ratio, and the transport gas density in horizontal and vertical, both upward and downward, straight pipelines and at bends. Characteristics of pressure losses under various operating conditions were correlated with the nondimensional numbers such as the Reynolds number, Froude number, solid/gas density ratio, and solid loading ratio. Such correlations were reasonably consistent with the experimental results.
Keywords
References
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Mallick S, Modeling of fluidised dense-phase pneumatic conveying of powders, Ph. D. thesis, University of Wollongong, Australia (2009).
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Ratnayake C, Scaling up technique for pneumatic transport systems, Ph. D. thesis, Telemark University College, Norway (2005).
Mills D, Pneumatic conveying design guide, 2nd Ed., Elsevier Butterworth-Heinemann, Gulf Professional Publishing (2004).
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Holdich R, Fundamentals of particle technology, Midland Information Technology and Publishing (2002).
Jo YM, Ray MB, J. Ind. Eng. Chem., 5(1), 32 (1999)
Lee C, Lee J, Kim G, Shin J, Computational analyses on coalconveying pneumatic system, 23rd International Society of Offshore and Polar Engineering, Anchorage, U.S.A. (2013).
Lee C, Lee J, Kim G, Kwon T, Numerical simulations and correlations on the coal-conveying gas flow in pipe for fluidized-bed coal gasification facility, Ecology and Safety 2014, 23rd International Conference, Elenite, Bulgaria (2014).
He CH, Chen XM, Wang JH, Ni HL, Xu YP, Zhou HJ, Xiong YQ, Shen XL, Powder Technol., 227, 51 (2012)
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