FLOW AND DIFFUSION IN SELF-ASPIRATED REVERSE FLOW JET LOOP REACTOR

1 INTRODUCTIONGas and liquid distributions in a self-aspirated reverse flow jet loop reactor dependchiefly on the aspiration and the breakup against gas phase by the liquid nozzle aswell as the redistribution in the draft tube.It has also been noted that effective diffu-sion or backmixing in the reactor has great influence on the flow and mass transferrates.In this case,accurate descriptions about the fluid flow and diffusion conditions inthe reactor are most necessary for effective amplification of them.

LOCAL NONLINEAR CHARACTERISTICS OF GAS LIQUID SOLID THREE PHASE SELF ASPIRATED REVERSED FLOW JET LOOP REACTOR

Hursts rescaled range (R/S) analysis and Wolfs attractor reconstruction technique have been adopted to estimate the local fractal dimensions and the local largest Lyapunov exponents in terms of the time series pressure fluctuations obtained from a gas liquid solid three phase self aspirated reversed flow jet loop reactor,respectively.The results indicate that the local fractal dimensions and the local largest Lyapunov exponents in both the jet region and the tubular region inside the draft tube increase with the increase in the jet liquid flowrates and the solid loadings,the local fractal dimension profiles are similar to those of the largest Lyapunov exponent,the local largest lyapunov exponents are positive for all cases,and the flow behavior of such a reactor is chaotic.The local nonlinear characteristic parameters such as the local fractal dimension and the local largest Lyapunov exponent could be applied to further study the flow properties such as the flow regime transitions and flow structures of this three phase jet loop reactor.

LOCAL CHAOS CHARACTERISTICS IN A SELF ASPIRATED REVERSED FLOW JET LOOP REACTOR

The local chaos characteristics of the time series pressure fluctuations of gas liquid two phase flow in a self aspirated reversed flow jet loop reactor are studied by the deterministic chaos analysis technique. It is found that the estimated local largest Lyapunov exponent is positive in all cases and the profile is similar to that of the local fractal dimension in this reactor. The positive largest Lyapunov exponent shows that the reactor is a nonlinear chaotic system. The obvious distribution indicates that the local nonlinear characteristic parameters such as the Lyapunov exponent and the fractal dimension could be applied to further study the flow characteristics such as the flow regine transitions and flow structures of the multi phase reactors.

FRACTAL STUDIES IN A SELF-ASPIRATED REVERSED FLOW JET LOOP REACTOR

1 INTRODUCTIONSelf-aspirated reversed flow jet loop reactors,characterized by a well defined flow pat-tern,well better dispersing effects,relatively low power consumption and a high masstransfer coefficient,are widely used in chemical engineering,especially in biochemicalengineering.The characteristics of such reactors are highly random or stochastic due tothe influence of a variety of phenomena such as jetting and bubbling of the

LOCAL LIQUID-PHASE OHARAOTERISTIOS OF THE SELF-ASPIRATED REVERSED FLOW JET LOOP REAOTOR

The local liquid--phase characteristics of the gas--liquid two-phase and gas--liquid--solid threephase self-aspirated reversed flow jet loop reactor with a concentric gas--liquid injection nozzle were studied experimentally. They facilitate the evaluation of local phenomena. The local instantaneous liquid velocities at different axial positions of the reactor were measured by using the modified pilot tube.The local liquid-phase turbulent structural parameters such as time-averaged velocity. turbulent nuctuating velocity and turbulent micro scale were calculated with the aid of the statistical theory of turbulence. In particular, effects of liquid jet flowrates and solid loadings on the profiles of the liquid--phase turbulent structural parameter both in the jet effective region and in the tubular region inside the draft tube were discussed.

三相下喷式环流反应器的传质性能

在三相非牛顿型流体体系中，对下喷式环流反应器传质特性进行了实验研究。讨论了表观气速、能量耗散速率、导流筒直径与反应器直径比、喷嘴直径、导流筒下端距反应器底部的距离、固体装填量、羧甲基纤维素钠（ＣＭＣ）溶液浓度及其流变特性对它的影响。实验结果表明，容积传质系数随表观气速和能量耗散速率的增加有所增加，在实验条件下，发现最优的导流筒直径与反应器直径比在０．４～０．４５这一范围、固体装填量大约为３％（体积百分比）、导流筒下端距反应器底部的距离为０．０８ｍ左右。同时提出了容积传质系数的经验关联式。

下喷自吸环流反应器内气相局部流动特性

The local gas phase flow characteristics of the gas-liquid two phase selfaspirated reversed flow jet loop reactor such as the radial profiles of gas holdup,bubble mean velocity and bubble size,using a miniature dual-sensor resistivity probe,were studied experimentally.A new digital processing method,based on threshold combinations of level and slope,was proposed for phase identification by the resistivity probe.In particular,the effects of the liquid jet flowrates on the local gas phase flow parameter profiles in the jet region and the tubular flow region inside the draft tube were discussed.

带导流筒的下喷环流反应器的模拟及研究

本文通过引入二维拟均相κ－ε模型方程，建立了描述气液下喷环流反应器内管流区流体流动规律的数学模型，并进行了求解，模型值与试验值吻合较好。以空气－水－玻璃球为研究物系，对有导流筒的下喷式环流反应器中局部液相性能进行了较深入研究。

三相下喷式环流反应器的气含率和传质性能

在三相非牛顿型流体体系中，对下喷式环流反应器的气含率和传质特性进行了实验研究。讨论了气速、液速、导流筒直径与反应器直径比、固体装填量、羧甲基纤维素钠溶液浓度及其流变特性对它们的影响。实验结果表明，气含率和传质系数随气速的增加而增加，而液速对其影响较小。在实验条件下，发现最优的导流筒直径与反应器直径比在０．４～０．５这一范围，最优的固体装填量约为φ＝０．０３，同时提出了气含率和容积传质系数的经验关联式。

下喷自吸环流反应器内局部气泡平均直径及其径向分布

The local bubble diameter profiles of the gas-liquid two-phase self-aspirated reversed flow jet loop reactor were studied experimentally by using internal camera CCD bubble measuring technology. The experimental results show that the local Sauter bubble diameter profile decreases with increasing liquid jet flowrates and nozzle diameter in both the jet region and the tubular flow region inside the draft tube. Bubble diameter profiles follow inverse Gaussian Distribution in the jet effective region while inverse parabolic distribution in the tubular flow region inside the draft tube.

下喷自吸环流反应器内液相局部流动特性

对下喷自吸环流反应器内气－液两相流和气－液－固三相流体系的液相局部流动特性进行了深入的实验研究。采用改进皮托管法和线。线双探针电导法分别对液相瞬时速度和液含率进行了微机在线测量，并借助湍流统计理论对液格局部流动参数（液相平均速度、液相湍动速度、湍动微尺度）和局部液含率进行了统计分析和处理，着重讨论了喷射液体流量和固体粒子加入量分别对喷射有效区和导流筒内管流区液相局部流动参数和液含率的影响。

环管喷射反应器气相流动数值模拟

利用三维k -ε湍流模型 ,建立了数值解法和计算程序 ,对环管喷射反应器混合室流动场进行了冷态数值模拟研究。模型成功地预报了混合室流动特性以及气流平均速度和压力的分布。为环管喷射反应器的设计、放大提供了理论依据。

下喷自吸环流反应器中气-液局部相际传质模型

引言 下喷自吸环流反应器是在结合喷射、环流、自吸等优点基础上而开发出的一种新型高效反应器,开展该反应器内局部气液传质模型的研究,对于该反应器的优化设计及放大具有极重要的理论意义.多年来,经典传质理论的不足与局限都在经历不断的修正与改进.其中。

倒喷射式环流反应器的研究

本文以空气-水为体系,研究了倒喷射式环流反应器的气含率,传质特性与其操作参数的关系,并从能耗方面对该反应器进行了初步评价。

下喷式环流生化反应器性能初探

本文以摸拟生物流体——不同浓度的 CMC 水溶液-空气为实验体系,考察了气速、液速等操作条件以及体系物性对下喷式环流反应器流体力学和传递特性的影响,提出了气含率及容积传氧系数的计算关联式ε_G=1.605n^(5·080)·((ρ_Gμ_G)/(ρ_Lμ_L))^(-0·3784).Fr_G^(0·3078)·Fr_L^(0·1918)Sh=8.669×10~6 n^(1·589).Sc^(0·3537).Re^(0·4718).Fr_G^(0·09944).Fr_L^(1·403)为该反应路的进一步研究及其工程放大设计提供了依据。

下喷式环流反应器研究进展

下喷式环流反应器在工业上的应用越来越广泛,深入研究下喷式环流反应器的设计、应用以及工业放大意义重大。概述了下喷式环流反应器的研究现状及最新进展。分析了下喷式环流反应器特性参数气含率、传质系数、循环液速和混合时间的影响因素,对反应器结构、流体特性和操作参数等因素的影响规律进行了归纳,提出了目前研究领域存在的问题,并进行了展望。

连续三相喷射环流反应器的实验和数值模拟

利用Pavlov管和电导探针分别测量含小颗粒(Stokes数小于1.0)的连续气液固三相喷射环流反应器内轴向液速和气体体积分数分布.提出大气泡-小气泡-浆态相三相流体力学模型,以模拟三相喷射环流反应器的流体力学行为,对大气泡相和小气泡相分别考虑尾涡加速和气泡阻碍效应并修正其曳力.对于上升区和下降区,流场模拟结果均与实验结果较吻合.利用模型预测不同固体体积分数下的气体体积分数与轴向液速分布,结果表明,在考虑的固体体积分数范围内,气体体积分数随固体体积分数增加而下降,液体循环速度随固体体积分数增加而略有上升,其原因主要是反应器内平均气泡直径随固体体积分数增加而增大,进而导致气泡浮升速度加大并增强周围流体的加速运动.

喷射环流反应器内宏观混和特性研究

通过实验分析研究了喷射环流反应器内宏观混和特性各影响因素的作用。分别采用水,水-细沙,丙三醇溶液等为实验物料,测定宏观混和时间和内循环液速。通过调整外循环流量大小和喷嘴位置,记录各混和特性的变化。结果表明:不同物料下,外循环流量对混和时间和内循环液速的影响都很大,混和时间均随循环流量的增大而缩短,内循环液速随着循环流量的增大而增大;不同物料下,喷嘴位置对混和时间的影响很小,而对内循环液速的影响较大。

逆向与正向结合的导叶式混流泵叶片系统反求设计

以某型混流式核主泵的叶轮叶片和导水机构叶片为研究对象,采用在逆向设计的基础上,正向设计校核迭代的技术来探索一条不破坏产品的前提下反求导叶式混流泵的复杂叶片系统的曲面几何数据方法。在不能获取叶片系统的完整曲面数据的情况下,采用叶片数字化设计方法建立沿回转流面上叶型曲线为参数线以便于修改控制的原始叶片系统的近似三维曲面几何模型,并将该模型与其他过流部件组成泵的全流道模型,在0.2~1.2Qd(设计流量)范围进行泵的全流道流场数值模拟,预测计算出外特性,再与原泵的试验外特性对比,以评估反求的叶片系统流道曲面的准确性。工程应用实践表明,该方法既保证了反求精度又较好地解决了泵的叶片系统反求设计问题。