DING Kaili;HU Chen;DENG Xianhe;School of Chemistry and Chemical Engineering,South China University of Technology;In order to investigate the heat transport characteristics of activated coke particles in moving bed,heat transfer experiment has been conducted,using tube and shell heat exchanger as the main process. Heated air and activated coke particles showed in a countercurrent flow mode in the heat exchanger. According to variable-controlling approach,the temperature difference ΔT_mand heat load Q caused by heat transfer,total heat transfer coefficient K of different experimental conditions,such as different wind speedu_s,the outlet temperature of hot air when the activated coke particles began to unload T_(air)and speed of unloaded activated coke particles v_pwere determined. The results indicated thatu_smade a big difference on ΔT_m,and the greateru_s,the bigger Q and K,closely related to the power ofu_swith n =0. 64. With theu_sreaching to 16 m / s,v_pbecoming 150 kg / h and T_(air)turning into 40 ℃,the total heat transfer coefficient highly reached to 9. 32 W /( m~2·K). With the rising T_(air),There was no obvious change in ΔT_m,a smaller value in Q and K,when negligible variation in K ranged from 70 ℃ to 80 ℃. Moreover,as v_pincreased,ΔT_mslowly increased,at the same time Q and K increased linearly. Higher than7. 5 W /( m~2·K),K increased linearly by 0. 9 W/( m~2·K) with each 50 kg/h rises,which displayed an observable effect on totality.
2016 01 v.22;No.101 [Abstract][OnlineView][HTML全文][Download 1112K]