摘要
主要对SJ型低温干馏炉生产半焦的过程进行了物料、热量衡算及过程能耗分析.结果表明,SJ型内热式低温干馏炉的半焦理论转化率为63.926%,焦油产率为6.079%,煤气产率为598m^3/t;炉体的热效率为88.90%,热工效率为84.08%,且炉体散热损失仅为4.82%,过程能耗在13.38%~17.92%之间,结合所用低变质煤的成分特征,可说明该过程属于低能耗、高产率、高附加值的洁净生产过程,适合该煤种的综合利用.
It's mainly analyzed that the material balance, heat balance calculation and energy consumption of the production process of semi-coke by SJ-low-temperature carbonization furnace. The results showed that, the theoretical semi-coke yield of SJ-low-heat oven is 63. 926 %, tar yield is 6. 079%, gas yield is about 598 m^3/t; with thermal efficiency of 88. 90%, heat efficiency of 84.08%, and heat loss of furnace surface of 4. 82%, and the energy consumption for process is between 13. 38% and 17.92%. Compared the composition characteristics of the low metamorphic coals, it's real a low energy consumption, high-yield, high value-added clean production process for the comprehensive utilization of this coal, which has great guiding significance to the sustainable development of the semi-coke industry in Northern Shaanxi.
出处
《煤炭转化》
CAS
CSCD
北大核心
2009年第2期18-21,32,共5页
Coal Conversion
基金
陕西省“13115”重大科技专项项目(2008ZDKG-46)
关键词
低温干馏炉
物料衡算
热量衡算
能耗
low-temperature carbonization furnace, material balance, heat balance calculation, energy consumption