Prediction model of ash fusion temperature and viscosity in coal gasification
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摘要: 根据煤灰中硅铝含量及硅铝比对煤灰进行分类研究, 构建了灰熔融点和黏度与组分关系的优化模型, 并对宽组分范围的煤灰熔点、黏度关系进行探讨。获得了更加精确的灰熔点预测模型, 全液相温度模型预测误差为±40 ℃, 实验值和预测值的标准误差为25 ℃。采用修正的Urbain模型和Roscoe模型相结合, 模型预测值和实验值吻合较好, 低黏度下对数黏度的预测值和实验值误差为±0.1;高黏度下黏度的预测值和实验值误差为±0.2。结果表明, 基于煤灰组分分类的拟合结果优于涵盖宽组分的模型。Abstract: Based on classification of silica and alumina content and silica alumina ratio in coal ash, optimized prediction models of coal ash melting point and viscosity related to ash components were built. Their relationship in a wide range of ash components was also discussed. An ash fusion temperature prediction model based on liquidus temperature from FactSage Thermodynamic software demonstrates accuracy improvement with error of less than ±40 ℃ and deviation of 25 ℃. The combination of Urbain and Roscoe model results in viscosity prediction error between prediction and experiment results within ±0.1 for relative low viscosity and ±0.2 for relative high viscosity. The results show that components classification model obtains better results than wide-covered model. Thus a better understanding of ash fusion mechanism is provided and gives reasonable guidance for blending and additives added to coal.
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Key words:
- coal gasification /
- ash fusion temperature /
- viscosity /
- prediction model
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表 1 煤灰样品中氧化物含量变化范围
Table 1 Content range of oxides in coal ash samples
Content w/% SiO2/Al2O3 SiO2 Al2O3 Fe2O3 CaO MgO K2O Na2O TiO2 Minimum 8.2 5.67 1.35 0.28 0.34 0.04 0.04 0.15 1.06 Maximum 66.7 37.57 41.88 46.88 13.06 3.9 4.73 3.09 6.94 表 2 煤灰分类依据
Table 2 Classification of coal ash
Classification Accordance of classification Sample numbers High silica and alumina coal ash SiO2+Al2O3 > 80% 30 Medium silica and alumina coal ash 60% < SiO2+Al2O3 < 80% 47 Low silica and alumina coal ash SiO2+Al2O3 < 60% 17 High silica alumina ratio coal ash SiO2/Al2O3 > 3 14 表 3 熔点预测模型
Table 3 Ash fusion temperature prediction model
Ash classification Viscosity prediction equation Correlation coefficient High silica and alumina coal ash FT=0.962tliq-58.5 0.91 Medium silica and alumina coal ash FT=0.677tliq+298.5 0.93 Low silica and alumina coal ash FT=0.823tliq+111.4 0.90 High silica alumina ratio coal ash FT=0.925tliq+241 0.92 表 4 灰熔点预测能力对比
Table 4 Prediction accuracy of ash fusion temperatures
Model Correlation coefficient Standard deviation t/℃ This research 0.91, 0.93, 0.90, 0.92 25 Jak 0.76 64 Chen wenmin - 47 表 5 黏度模型灰成分
Table 5 Coal ash components in viscosity model
Coal ash Components content w/% SiO2/Al2O3 SiO2 Al2O3 Fe2O3 CaO MgO K2O Na2O TiO2 SiO2+Al2O3 Huangkuang 56.34 31.23 2.65 2.17 0.70 1.62 0.67 1.16 87.57 1.80 Bai 56.30 31.22 3.60 1.87 0.71 2.00 0.65 1.25 87.52 1.80 Yuwu 57.12 29.59 2.74 1.92 0.64 2.01 0.78 1.11 86.71 1.93 Wangzhuang 53.94 32.49 3.74 2.42 0.75 1.43 0.64 1.20 86.43 1.66 Anrui 45.18 36.11 8.52 1.32 0.66 1.30 0.32 1.21 81.29 1.25 Banjiao 66.24 14.79 4.09 7.14 1.30 1.49 0.82 0.88 81.03 4.48 Tongdaxinjing 42.70 35.03 6.52 5.48 2.16 0.94 0.22 1.39 77.73 1.22 4# 56.04 21.13 4.52 5.83 2.18 1.72 0.52 1.12 77.17 2.65 Cilinshan 45.34 30.87 7.48 7.40 0.46 0.46 0.04 0.97 76.21 1.47 Tianye1 52.09 20.15 7.58 7.78 2.70 2.18 0.76 0.98 72.24 2.59 Tianye 51.28 20.05 8.14 8.02 2.93 2.26 0.82 0.92 71.33 2.56 Yuncheng 45.22 7.89 28.4 5.12 3.18 0.94 0.78 0.46 53.11 5.73 6# 32.70 19.54 4.08 18.38 6.71 0.72 3.17 0.93 52.24 1.67 Tongliao 29.68 11.48 14.77 16.12 5.30 0.42 1.73 1.01 41.16 2.59 表 6 修正的Urbain模型参数
Table 6 Modified Urbain model parameters
j i 0 1 2 3 bi0 0 12.45 35.21 -46.21 156.33 biC, j 1 -3.78 23.55 -49.09 33.90 2 4.02 -22.04 35.98 -17.89 biM, j1 1 -17.09 -22.34 37.65 -19.22 2 27.90 -122.88 179.01 -90.2 biK, j1 1 13.09 69.07 132.90 -65.90 2 -6.55 22.52 -1.87 -89.08 biN, j1 1 10.77 -31.39 -10.33 59.90 2 -11.21 -1.33 134.44 -190.22 biT, j1 1 23.33 -129.3 198.2 -104.43 2 -34.76 165.22 -276.9 155.5 表 7 基于组分分类的黏度预测模型
Table 7 Viscosity prediction model based on composition classification
Object Model High silica alumina ratio coal ash;
high silica and alumina coal ash;See Table 6 high temperature melting zone of
medium silica and alumina coal ashSolid precipitation zone of medium
and low silica and alumina coal ashηe=η(1-1.211θ)-2.5 -
[1] LOLJA S A, HAXHI H, MARTIN D J. Correlations in the properties of Albanian coals[J]. Fuel, 2002, 81(9): 1095-1100. doi: 10.1016/S0016-2361(02)00032-7 [2] 姚星一, 王文森.灰熔点计算公式的研究[J].燃料化学学报, 1959, 4(3): 216-223. http://www.cnki.com.cn/Article/CJFDTOTAL-RLHX195903003.htmYAO Xing-yi, WANG Wen-sen. Study on the empirical equations for calculating the fusion temperature of coal ash[J]. J Fuel Chem Technol, 1959, 4(3): 216-223. http://www.cnki.com.cn/Article/CJFDTOTAL-RLHX195903003.htm [3] WINEGARTNER E C, RHODES B T. An empirical study of the relation of chemical properties to ash fusion temperatures[J]. J Eng Power, 1975, 97(3): 395-403. doi: 10.1115/1.3446018 [4] SEGGIANI M. Empirical correlations of the ash fusion temperatures and temperature of critical viscosity for coal and biomass ashes[J]. Fuel, 1999, 78(9): 1121-1125. doi: 10.1016/S0016-2361(99)00031-9 [5] ÖZBAYOGLU G, ÖZBAYOGLU M E. A new approach for the prediction of ash fusion temperatures: A case study using Turkish lignites[J]. Fuel, 2006, 85(4): 545-552. doi: 10.1016/j.fuel.2004.12.020 [6] 陈文敏, 姜宁.煤灰成分和煤灰熔融性的关系[J].洁净煤技术, 1996, 2(2): 34-37. http://www.cnki.com.cn/Article/CJFDTOTAL-JJMS199602011.htmCHEN Wen-min, JIANG Ning. Relation between the coal ash composition and fusibility[J]. Clean Coal Technol, 1996, 2(2): 34-37. http://www.cnki.com.cn/Article/CJFDTOTAL-JJMS199602011.htm [7] HUGGINS F E, KOSMACK D A, HUFFMAN G P. Correlation between ash-fusion temperatures and ternary equilibrium phase diagrams[J]. Fuel, 1981, 60(7): 577-584. doi: 10.1016/0016-2361(81)90157-5 [8] GRAY V R. Prediction of ash fusion temperature from ash composition for some New Zealand coals[J]. Fuel, 1987, 66(9): 1230-1239. doi: 10.1016/0016-2361(87)90061-5 [9] HURST H J, NOVAK F, PATTERSON J H. Phase diagram approach to the fluxing effect of additions of CaCO3 on Australian coal ashes[J]. Energy Fuels, 1996, 10(6): 1215-1219. doi: 10.1021/ef950264k [10] JAK E. Prediction of coal ash fusion temperatures with the FACT thermodynamic computer package[J]. Fuel, 2002, 81(13): 1655-1668. doi: 10.1016/S0016-2361(02)00091-1 [11] SONG W J, TANG L H, ZHU X D, WU Y Q, ZHU Z B, KOYAMA S. Prediction of Chinese coal ash fusion temperatures in Ar and H2 atmospheres[J]. Energy Fuels, 2009, 23(4): 1990-1997. doi: 10.1021/ef800974d [12] VARGAS S, FRANDSEN F J, DAM-JOHANSEN K. Rheological properties of high-temperature melts of coal ashes and other silicates[J]. Prog Energy Combust, 2001, 27(3): 237-429. doi: 10.1016/S0360-1285(00)00023-X [13] SONG W, SUN Y, WU Y, ZHU Z, KOYAMA S. Measurement and simulation of flow properties of coal ash slag in coal gasification[J]. AIChE J, 2011, 57(3): 801-818. doi: 10.1002/aic.12293 [14] BAI J, KONG L, LI W. Prediction of slag viscosity under gasification condition[C]. The 2nd International Symposium on Gasification and its Application. Fukuoka, 2010. [15] UNUMA H, TAKEDA S, TSURUE T, ITO S, SAYAMA S. Studies of the fusibility of coal ash[J]. Fuel, 1986, 65(11): 1505-1510. doi: 10.1016/0016-2361(86)90325-X [16] 台培杰.煤灰渣熔融与流动特性及水冷壁气化炉小试热模研究[D].上海:华东理工大学, 2010.TAI Pei-jie. Study on fusibility and fluidity of coal ash slag and hot model of membrane wall entrained-flow gasifier[D]. Shanghai: East China University of Science and Technolgy, 2010. [17] 白进, 孔令学, 李怀柱, 郭振兴, 白宗庆, 尉迟唯, 李文.山西典型无烟煤灰流动性的调控.燃料化学学报, 2013, 41(7): 805-813. http://rlhxxb.sxicc.ac.cn/CN/abstract/abstract18214.shtmlBAI Jin, KONG Ling-xue, LI Huai-zhu, GUO Zhen-xing, BAI Zong-qing, WEI Chi-wei, LI Wen. Adjustment in high temperature flow property of ash from Shanxi typical anthracite[J]. J Fuel Chem Technol, 2013, 41(7): 805-813. http://rlhxxb.sxicc.ac.cn/CN/abstract/abstract18214.shtml [18] ILYUSHECHKIN A Y, HLA S S, ROBERTS D G, KINAEV N N. The effect of solids and phase compositions on viscosity behaviour and Tcv of slags from Australian bituminous coals[J]. J Non-Cryst Solids, 2011, 357(3): 893-902. doi: 10.1016/j.jnoncrysol.2010.12.004 [19] TOPLIS M J, DINGWELL D B. Shear viscosities of CaO-Al2O3-SiO2 and MgO-Al2O3-SiO2 liquids: Implications for the structural role of aluminium and the degree of polymerisation of synthetic and natural aluminosilicate melts[J]. Geochim Cosmochim Acta, 2004, 68(24): 5169-5188. doi: 10.1016/j.gca.2004.05.041 [20] PATTERSON J H, HURST H J. Ash and slag qualities of Australian bituminous coals for use in slagging gasifiers[J]. Fuel, 2000, 79(13): 1671-1678. doi: 10.1016/S0016-2361(00)00032-6 [21] HURST H J, NOVAK F, PATTERSON J H. Viscosity measurements and empirical predictions for fluxed Australian bituminous coal ashes[J]. Fuel, 1999, 78(15): 1831-1840. doi: 10.1016/S0016-2361(99)00094-0 [22] HURST H J, NOVAK F, PATTERSON J H. Viscosity measurements and empirical predictions for some model gasifier slags[J]. Fuel, 1999, 78(4): 439-444. doi: 10.1016/S0016-2361(98)00162-8 [23] HURST H J, PATTERSON J H, QUINTANAR A. Viscosity measurements and empirical predictions for some model gasifier slags-Ⅱ[J]. Fuel, 2000, 79(14): 1797-1799. doi: 10.1016/S0016-2361(00)00043-0 [24] WAANDERS F B, DYK J C, PRINSLOO C J V. The characterisation of three different coal samples by means of various analytical techniques[J]. Hyperfine Interact, 2009, 190(1/3): 109-114. https://www.researchgate.net/publication/253322621_Erratum_to_The_characterisation_of_three_different_coal_samples_by_means_of_various_analytical_techniques