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作 者:侯彦青[1] 谢刚[1,2] 陶东平[1] 俞小花[1] 李荣兴[1] 宋东明[1,3]
机构地区:[1]昆明理工大学冶金与能源工程学院,昆明650093 [2]云南冶金集团总公司技术中心,昆明650031 [3]昆明冶研新材料股份有限公司,昆明650031
出 处:《中国有色金属学报》2011年第12期3202-3210,共9页The Chinese Journal of Nonferrous Metals
基 金:国家自然科学基金资助项目(50574045)
摘 要:应用有关热力学数据研究了与多晶硅主要生产工艺即西门子法相关的"Si-Cl-H"三元系的复杂化学反应,研究SiCl4氢化转化为SiHCl3过程中可能发生的15个反应,给出15个反应的ΔG mΘ—T图;并确定5个独立的反应,给出这5个独立反应的K pΘ—T图;高温时主反应(1)的K pΘ增长较慢,而反应(2)和(5)的K pΘ快速增大,1 373 K时,主反应(1)的K pΘ较小,为0.157 1。进一步研究温度、压强和进料配比n H 2/nSiCl4对SiCl4氢化率的影响,并绘制出SiCl4氢化率随这些因素的变化曲线。结果表明:当压强和进料配比一定时,SiCl4的氢化率随温度的升高先增加后降低;增大压强或增加进料配比n H 2/nSiCl4都会提高SiCl4的氢化率;SiCl4氢化转化为SiHCl3过程的最佳操作条件为温度为1 000℃,压强为0.3 MPa,进料配比n H 2/nSiCl4为4,在此条件下,SiCl4的氢化率为25.78%。Based on the thermodynamic data for the related pure substances, fifteen possible chemical reactions in the SIC14 hydrogenation system of Siemens process that is one of the main process for the polysilicon production were studied. The AGm curves of the fifteen chemical reactions in the system versus temperature were fitted by the assistant of computer. The values of AGm for most reactions are greater than zero at the range of 973K to 1 773 K. That is to say that the value of equilibrium constant is small. Therefore, the small degree of the reactions was carried on. Five o and temperature was fitted by the independent reactions in the process were decided and the relation between gp assistance of computer based on the thermodynamic data for the related pure substances. The value of Kp for main Kp reaction (1) increases a little at high temperature, but the value of Kp for side-reactions (2) and (5) increase quickly. Besides, the value of Kpe for main reaction (1) is low at low temperature, for example only 0.157 1 at 1 373 K. Therefore, the transformation ratio of SIC14 to SiHCI3 being low is a object!ve fact which can not be changed. Furthermore, the influencing factors, such as the temperature, pressure and feeding mole ratio, on the transformation ratio from SiCI4 to SiHC13 were studied. The diagrams of n-transformation ratio are presented as function of temperature, pressure and feeding mole ration, respectively. The transformation ratio of SIC14 to SiHC13 decreases with increasing the temperature,and the pressure have a positive effect on the transformation ratio. Furthermore, the excess of H2 is necessary in SIC14 hydrogenation system of the modified Siemens process. From the thermodynamic above, The results show that the optimum operation parameters are at 1 050 ℃, 0.3 MPa and feeding mole ratio nH2/nsiCl4 of 4. Under this condition, the transformation ratio from SIC14 to SiHCI3 is 25.78%.
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