低阶煤油泡浮选过程特征及其动力学研究
[Abstract]:China is rich in low-rank coal resources, accounting for about 45.68% of China's coal resources. Clean and efficient development and utilization of low-rank coal resources is of great significance to energy security and economic development in China. At present, the mineralization mechanism of low-rank coal and oil bubbles is still unclear, and the variation characteristics of low-rank coal flotability are lack of in-depth understanding. The characteristics and kinetics of oil bubble flotation process were studied in depth, and the mechanism of low-rank kerosene bubble flotation was discussed. The theoretical basis and technical support were provided for the industrialization of low-rank coal flotation. The oxygen-bearing functional groups on the surface of coal slime are mainly hydroxyl-OH and Ether-Bonded C-O, and a small amount of carboxyl O=C-O and carbonyl C=O. Impurity minerals in low rank coal are mainly quartz, kaolinite and muscovite, and other minerals are less. The contact angle of coal slime is 40.8 degrees, belonging to medium floatable slime. The optimum technological parameters of low-order kerosene bubble flotation were obtained by single factor test and Box-Behnken test. The optimum conditions of bubble flotation were as follows: the speed of flotation machine was 2152.50r/min, the dosage of collector was 4.35kg/t, the slurry concentration was 56.00g/L, and the aeration capacity was 0.22m3/h. The maximum combustible recovery was 96.53%. The minimum reagent consumption of low-order kerosene bubble flotation was explored. By optimizing the dosage of model parameter collector, the maximum combustible recovery rate was 84.32% when the minimum reagent dosage was 2.32 kg/t, the conventional flotation method was 50 kg/t, the concentrate yield was 68.62%, and the combustible recovery rate was 88.18%. The flotation efficiency of low-rank coal and the consumption of collectors are improved obviously. From the point of view of flotation rate, the flotation characteristics of bubbles, cold oil bubbles, hot oil bubbles and slime oil bubbles with different particle sizes are studied. The results show that the flotation rate constant of conventional flotation decreases with the flotation time, while the flotation rate of oil bubbles decreases with the flotation time. The atomization is favorable for the collector to disperse evenly in the pulp, and the flash at high temperature is more conducive to the formation of oil bubbles and the mineralization of particles and bubbles. The flotation process of low-rank coal by ordinary bubble is close to the classical first-order flotation kinetic model. By adding a time parameter t*, the adaptability of the flotation kinetic model to the oil bubble flotation process is improved, and the low-rank kerosene bubble flotation rate is more in line with the revised one. The mechanism of oil bubble flotation behavior was studied from the point of view of oil bubble characteristics, kinetics and thermodynamics. The results show that the stability of oil bubble is stronger, the entrainment effect of oil bubble flotation water is smaller, and the number of bubbles can be reduced by introducing flash hydrocarbon collector. The smaller the bubbles are, the shorter the induction time is. The shorter the induction time is, and the shorter the induction time is, the higher the adhesion probability is. The smaller the mineralization barrier between the particles and the bubbles, which is beneficial to the adhesion process.
【学位授予单位】:中国矿业大学
【学位级别】:硕士
【学位授予年份】:2017
【分类号】:TD94;TD923
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