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Carbonized shrinkage force of anthracite briquette and large tamped coal cake

机译:无烟煤球和大夯实煤饼的碳化收缩力

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During high-temperature treatment, shrinkage stress of high-rank coal briquette often leads to crack formation, affecting the particle size distribution of briquette. Thus the type and formation mechanism of anthracite briquette shrinkage force were evaluated. The calculation methods of carbonized shrinkage forces of anthracite briquette and large tamped coal cake (16780mm* 500mm* 6630 mm) were also established. The results revealed that carbonized shrinkage of anthracite briquette was affected by four forces: thermal shrinkage force of anthracite coal (F-C) and binder (F-B), thermal fusion force (F-F), and thermal traction force (F-T). Below 250 degrees C, F-C, F-B and FT were derived from capillary pressure and surface tension. F-F came from the gravity of softened binder. Between 250 and 750 degrees C, F-C and F-B were both originated from resultant force of thermal depolymerization shrinkage force and volatiles precipitation expansion force. F-F and F-T were provided by co-carbonization products of anthracite coal and binder. Between 750 and 950 degrees C, F-C and F-B was induced by resultant force of thermal polycondensation shrinkage force and gas precipitation expansion force. F-F acted through catalytic effect of the binder on anthracite and F-T no longer provided traction. Four carbonized shrinkage forces of anthracite briquette and tampered coal cake could be calculated according to the equations: F-C = K(C)m(Cp) d(2)R(Cp)/dt(2), F-B = K-B m(BP) d(2)R(BP)/dt(2) F-F = K(B)m(Bp) (d2R)(CB-F)p/dt(2), F-T = K(B)m(BP) d(2)R(CB-T)p/dt(2) and F-cake = yz Sigma(x)(i=1) (F-C + F-B +F-F + F-T)(i). This study provides guidance for high-rank coal briquette production and stretches the mind for parameter calculations of multiphase system during chemical reaction.
机译:在高温处理过程中,高级煤球的收缩应力通常会导致裂纹形成,从而影响煤球的粒度分布。因此,评价了无烟煤团块收缩力的类型和形成机理。建立了无烟煤团块和大夯实煤饼(16780mm×500mm×6630mm)碳化收缩力的计算方法。结果表明,无烟煤球的碳化收缩受到四个力的影响:无烟煤的热收缩力(F-C)和粘结剂的热收缩力(F-B),热熔合力(F-F)和热牵引力(F-T)。低于250摄氏度时,F-C,F-B和FT由毛细管压力和表面张力得出。 F-F来自软化粘合剂的重力。在250至750摄氏度之间,F-C和F-B均来自热解聚收缩力和挥发物沉淀膨胀力的合力。 F-F和F-T由无烟煤和粘结剂的共碳化产物提供。在750至950摄氏度之间,热缩聚收缩力和气体沉淀膨胀力的合力诱发了F-C和F-B。 F-F通过粘合剂对无烟煤的催化作用而起作用,而F-T不再提供牵引力。可以根据以下公式计算无烟煤球和夯实的煤饼的四个碳化收缩力:FC = K(C)m(Cp)d(2)R(Cp)/ dt(2),FB = KB m(BP) d(2)R(BP)/ dt(2)FF = K(B)m(Bp)(d2R)(CB-F)p / dt(2),FT = K(B)m(BP)d( 2)R(CB-T)p / dt(2)和F-cake = yz Sigma(x)(i = 1)(FC + FB + FF + FT)(i)。该研究为高级煤饼生产提供了指导,为化学反应过程中多相系统的参数计算开辟了思路。

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