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快速流化床提升管中气固流动行为的非线性分析 总被引:8,自引:7,他引:1
对φ100mm×16m、FCC固体颗粒的快速流化床提升管内环-核流动区局部颗粒含量脉动行为进行了非线性分析,用Kolmogorov熵表征了其气固流动行为.结果表明,Kolmogorov熵沿提升管环-核流动区径向有3个显著变化区域,以此为依据将提升管环-核流动区的气固流动行为沿径向分成3个流域:单颗粒随机运动控制的核心流域;单颗粒混沌控制的过渡流域;边壁控制的环形流域.同时,从颗粒对垂直气固流动系统中气固湍动程度影响的角度,解释了Kolmogorov熵的径向分布特征及其与流动结构的关系. 相似文献
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T. Dyakowski S. J. Wang D. Geldart M. S. Beck 《Chemical Engineering Communications》1999,175(1):117-130
The dynamic characteristics of gas-solid flow patterns within a circulating fluidized riser have been investigated using an electrical capacitance tomography system. The tomograms show both an instantaneous and an average in time solids' distribution in the riser cross-section. The effects of gas superficial velocity and solids circulating fluxes on the flow behaviour were measured and the results compared with data from the existing literature. 相似文献
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与气固并流上行提升管反应器相比,气固并流下行管反应器的轴向气固返混明显降低,而径向气固混和仍然相当大,因而有利于提高气固快速反应的转化率及选择性。本文在分析下行流化床反应器内气、固混合机理的基础上,比较了有关气、固混合的研究方法及结果,并比较了提升管和下行管的不同混合现象,旨在促进对这一课题更加深入系统地研究,以适应循环床下行管反应器设计、放大和模型化的迫切要求。 相似文献
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综述了循环流化床提升管和下行管气固两相流动模型研究的现状在对这些模型分类评述的基础上,给出了可用于描述下行管反应流动规律的一维两相和地维两相流动模型,为下行管反应器的设计,放在提供了理论依据。 相似文献
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This paper presents an experimental study on the flow patterns of FCC particles in a 140 mm ID Circulating Fluidized Bed with concurrent upflow and downflow gas-solid suspension. Based on the distribution of local particle velocity and particle concentration measured by a Fiber-Optical Probe Laser Doppler Velocimeter and a Fiber Optical Probe System respectively, the different flow patterns of local particls concentration, local particle velocity, local particle fluctuating velocity and sectionally average particle velocity in concurrent upflow and downflow gas-solid system have been investigated. It is found that the particle flow in the concurrent downflow is much more uniform radially than that in the concurrent upflow riser. The investigation of flow patterns in different flow systems is of significance to the development of a new gas-solid reactor. 相似文献
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薛惠芳 《化学反应工程与工艺》1992,8(3):302-307
颗粒速度是快速流化床内重要的流体力学参数,直接测定是困难的,一般都是通过测定其他参数,来计算颗粒的速度。本研究在内径6.6cm 和9.7cm,高3m 的快速流化床内测定颗粒的轴向滞留量分布及压头损失,分析床层内颗粒速度及其影响因素,对三种不同颗粒进行测定,将实验数据进行关联,得出颗粒速度的关联式:适用范围:气体流速:1.4~6.0m/s颗粒循环速度:30~130kg/m~2·s颗粒终端速度:0.133~0.880m/s将实验值与计算的结果比较,基本一致。故可认为该式在实验范围内,可用于推算快速流化床内的颗粒速度。 相似文献
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采用稳态吸附方法,测定了示踪剂在下行式流化床反应器中的轴向浓度分布,并与理论分布进行拟合,利用Marquardt法,求取了不同操作条件下的轴向扩散系数与气固传质系数,藉以揭示并流下行循环流化床反应器中的气固传质特性.基于实验结果,通过因次分析与线性回归,得到了轴向扩散系数Ea及传质系数KFa与操作条件的经验关联式:Pe1≡(Luf)/Ea=0.226Re0.499PΘ-0.302Pe2≡uf/(KFa.L)=0.000185Re0.618pΘ-0.983Θ≡Gs/(ufρp)=us(1-ε)/(ugε)关联式与实验数据拟合较好. 相似文献
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本文在φ140mm的气固并流下行快速流化床中,研究了颗粒浓度及颗粒速度的径向分布随操作气速、颗粒循环速率以及床层轴向位置的变化规律。并探讨了颗粒质量通量的径向分布及颗粒流动的均匀性,表明在相同操作条件下,下行快速流化床中气固流动远比上行快速流化床均匀。 相似文献
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论述了快速床区流体动力学的结构,研究了快速床区纵向和横向悬浮密度分布的规律及相应的计算公式。对影响快速床区动力学结构的主要因素,如固体颗粒的循环率、气体速度等进行了试验研究,对循环流化床锅炉的设计和运行有一定的指导意义。 相似文献
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本文在一高8m,直径186mm 的快速流化床中采用小型电加热探头测定了床层与换热面之间的局部传热系数,实验中通过将探头向上和向下设置考察了探头设置方向对局部传热系数的影响,实验表明探头在床中的设置方向不同将对传热系数的测定值产生一定的影响:另外在同一床层浓度下,操作气速和固体循环速率的变化将对传热系数产生直接的影响 相似文献
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This paper presents an experimental study on the axial and radial distributions of heat transfer coefficients in a fastfluidized bed operated at ambient temperature.The following formula is recommended to correlate the local heat transfer coefficients in fast fluidized beds:where a,n_1 and n_2 are functions of radial positions. 相似文献
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V. V. Basava Rao Ch Sailu D. Krishna Sandilya 《Chemical Engineering Communications》2007,194(3):353-367
A liquid-solid circulating fluidized bed (LSCFB) is operated at high liquid velocity, where particle entrainment is highly significant and between the conventional liquid fluidized bed and the dilute phase liquid transport regimes. LSCFB has potential applications in the fields of food processing, biochemical processing, and petrochemical and metallurgical processing. It is well known that the flow characteristics in a liquid-solid circulating fluidized bed are different from those of a conventional liquid-solid fluidized bed. The limited studies available in literature do not provide complete understanding of the flow structure in this typical regime.
In the present work, experiments were carried out in a 0.0762 m ID and 3 m height laboratory-scale liquid-solid circulating fluidized bed apparatus by using various solid particles and tap water as fluidizing medium. In the experimental setup, two distributors (specially designed) were used to monitor solid circulation rate in the riser. The effects of operating parameters, i.e., primary liquid flow rate in the riser (Up), solid circulation rate (Gs), and particle diameter (dp), were analyzed from the experimental data. Finally, a correlation was developed from the experimental data to estimate average solid holdup in the riser, and it was compared with present experimental and available data in the literature. They agree well with a maximum root-mean-square deviation of 7.83%. 相似文献
In the present work, experiments were carried out in a 0.0762 m ID and 3 m height laboratory-scale liquid-solid circulating fluidized bed apparatus by using various solid particles and tap water as fluidizing medium. In the experimental setup, two distributors (specially designed) were used to monitor solid circulation rate in the riser. The effects of operating parameters, i.e., primary liquid flow rate in the riser (Up), solid circulation rate (Gs), and particle diameter (dp), were analyzed from the experimental data. Finally, a correlation was developed from the experimental data to estimate average solid holdup in the riser, and it was compared with present experimental and available data in the literature. They agree well with a maximum root-mean-square deviation of 7.83%. 相似文献