石油学报(石油加工)
石油學報(石油加工)
석유학보(석유가공)
ACTA PETROLEI SINICA(PETROLEUM PROCESSING SECTION)
2009年
6期
790-795
,共6页
双组分流化床%大差异颗粒%颗粒一颗粒传热
雙組分流化床%大差異顆粒%顆粒一顆粒傳熱
쌍조분류화상%대차이과립%과립일과립전열
binary mixture fluidized bed%great differential particles%particle-particle heat transfer
以降烯烃催化剂作为大颗粒,FCC催化剂作为小颗粒,将冷的大颗粒加入至热的大、小颗粒双组分全混流化床中,考察流化床中颗粒间混合换热过程.结果表明,在全混流化状态下,流化床密相区内混合颗粒的平均粒径越小、床层气速越高和床温越高,冷、热颗粒间传热系数就越大.用颗粒的努塞尔数Nu_p和雷诺数Re_p关联试验数据时,必须考虑密相床层温度的影响.考虑换热的初始床温和冷颗粒温度后,关联式计算值与实验值的误差不超过30%,可用于双组分流化床颗粒传热系数的计算.
以降烯烴催化劑作為大顆粒,FCC催化劑作為小顆粒,將冷的大顆粒加入至熱的大、小顆粒雙組分全混流化床中,攷察流化床中顆粒間混閤換熱過程.結果錶明,在全混流化狀態下,流化床密相區內混閤顆粒的平均粒徑越小、床層氣速越高和床溫越高,冷、熱顆粒間傳熱繫數就越大.用顆粒的努塞爾數Nu_p和雷諾數Re_p關聯試驗數據時,必鬚攷慮密相床層溫度的影響.攷慮換熱的初始床溫和冷顆粒溫度後,關聯式計算值與實驗值的誤差不超過30%,可用于雙組分流化床顆粒傳熱繫數的計算.
이강희경최화제작위대과립,FCC최화제작위소과립,장랭적대과립가입지열적대、소과립쌍조분전혼류화상중,고찰류화상중과립간혼합환열과정.결과표명,재전혼류화상태하,류화상밀상구내혼합과립적평균립경월소、상층기속월고화상온월고,랭、열과립간전열계수취월대.용과립적노새이수Nu_p화뢰낙수Re_p관련시험수거시,필수고필밀상상층온도적영향.고필환열적초시상온화랭과립온도후,관련식계산치여실험치적오차불초과30%,가용우쌍조분류화상과립전열계수적계산.
With an olefin-reducing catalyst as the large particle and FCC catalyst as the small particle, an experimental investigation on heat transfer characteristics of feeding cold large particles into the heated fluidized binary mixtures of small particles and large particles was conducted in a experimental hot fluidized bed.The particle-particle heat transfer coefficient was measured under operations of different fluidized gas velocities, bed temperatures and large particle mass ratio in bed mixture.The experiments showed that the heat transfer coefficient increased with the increase of fluidized bed temperature, superficial gas velocity and with the decrease of the average particle size of bed binary mixture when the binary mixtures was in full-mixed fluidized state.A new correlation between Nu_pand Re_p of the particles, involving the influences of the temperatures of initial bed mixture and cold feed particle, was put forward, which could predict the experimental data with the error less than 30%.