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机构地区:[1]上海华谊集团技术研究院,上海200241 [2]华东理工大学化学工程联合国家重点实验室,上海200237
出 处:《过程工程学报》2011年第6期901-906,共6页The Chinese Journal of Process Engineering
摘 要:研究了383mm的浅层鼓泡塔内高径比(H/DT)、气体分布器、固体浓度(Cs)对气含率和临界悬浮气速(Ugc)的影响.结果表明,当H/DT<1.5时,随H/DT增大,气含率增大,而Ugc明显下降;当H/DT>1.5时,气含率减小,Ugc变化不大,优化的H/DT约为1.5.采用四管管式气体分布器,当环径比(d/DT)为0.4时,Ugc最小.气含率随Cs增大而减小,Cs超过15%(φ)时,Ugc随Cs变化不大.最后,推导得到Ugc的经验关联式,可为工业反应器提供一定指导.The influences of aspect ratio(H/DT) ,gas sparger and solid concentration(Cs) on gas holdup and critical gas velocity of solid suspension(Ugc) were investigated in a 383 mm i.d. three-phase shallow bubble column. The results show that when H/DT is smaller than 1.5,gas holdup increases and Ugc decreases with the increase of H/DT. However,when H/DT is larger than 1.5,the effect of H/DT on Ugc is insignificant. Gas sparger has great effect on Ugc,when d/DT is equal to 0.4,the value of Ugc is minimum. Gas holdup decreases with the increase of Cs. The effect of Cs on Ugc is insignificant,when Cs is larger than 15%(φ) . Finally,the empirical correlation is proposed to describe their quantitative effects on Ugc to give some physical insights into the experimental phenomenon.
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