Experimental study on micromixing characteristics of novel large-double-blade impeller
Introduction
Agitation is widely used in many aspects of process industries such as chemical engineering, pharmaceutical, food, metallurgy, papermaking and sewage treatment. Impeller, as the core part of stirring equipment, directly determines the mixing effects and power consumption, therefore significantly affects the performance and economical efficiency of the whole mixing system. Consequently, the optimization design and selection of efficient impellers have especially prominent and practical meanings (Zlokamik, 2001).
Conventional impellers are characterized by their simple structures, easy operation and relatively mature design approaches. Nevertheless, because of their single function, such impellers are only applicable to particular technological processes. For systems with variable working conditions, they can׳t meet the requirements at different stages well, whether they are low-viscosity impellers (which are applicable to low-viscosity systems) or high-viscosity impellers (which are applicable to high-viscosity systems). For this problem, there are two valid methods being proposed (Chen et al., 2014). The first one is the application of double-shaft mixers. The second one is using single-large-bladed impellers, whose projected area of blade accounts for large proportion of longitudinal area of the whole tank. The typical ones are Fullzone (FZ) impeller, Maxblend (MB) impeller and Sanmeler (SM) impeller. By comparison, the large-blade impellers are more competitive for their simple structures, easy dynamic seal and lower cost of operation and maintenance.
Previous researches on large-bladed impellers concentrated more on their macromixing performance, while micromixing performance was rarely studied. Lianfang Feng, etcetera experimentally studied the performances of MB, FZ, and SM impellers (Gu et al., 2000), and found that at the same Reynolds numbers, MB impeller and SM impeller had the highest and lowest power consumption, respectively. Meanwhile, in a medium-high-viscosity system, mixing efficiency of FZ mixer was the highest and SM mixer performed best at heat transfer. Dohi׳s experimental study focused on power characteristics and solid-liquid suspension performance of MB impeller and FZ impeller in gas-liquid-solid three-phase stirring systems. The minimum impeller speeds of MB and FZ impellers for off-bottom solid suspension and homogeneous solid suspension were measured in aerated and unaerated systems, and were compared with that of a triple-impeller system composed of two four-pitched blade downflow disk turbines (DTs) at middle and upper positions and one Pfaudler type impeller at lower position (Dohi et al., 2004). The results showed that MB and FZ impellers were proved to have better solid-liquid suspension performance, particularly MB impeller. Yao, etcetera numerically investigated the macromixing performances of MB impeller and DHR impeller, and found that MB impeller had better dispersion and mixing performances, especially in the grids region (Yao et al., 2001).
However, in practical production, large-blade impellers are mainly used in rapid-reaction situations in process industries. And earlier studies indicated that the final product quality of rapid reactions was closely associated with micromixing effects. Villermaux, etcetera concluded that micromixing performances influenced polymer׳s molecular mass distribution (Villermaux and Blavier, 1984). According to Pohorecki׳s research, micromixing could control precipitating particle size distribution during the reaction process (Pohorecki and Baldyga, 1988).
When intrinsic rate of the reaction is approximate to or faster than the stirring rate, the reaction will have already or nearly been completed before the reactants reach molecular-scale homogenization. In such situations, actually, the rapid reaction proceeds in a local inhomogeneous state, thus influencing the distribution and quality of the reaction products and the system stability. That is why micromixing affects rapid reaction processes.
Therefore, considering the application status, research status of large-blade impellers in rapid reactions and the effects of micromixing on the products of rapid reactions, it is extremely essential for micromixing performances of large-blade impellers to be studied. In this article, the micromixing performance of the novel LDB impeller in viscous systems was experimentally studied, providing guidance for optimization design of impellers and mixing operations.
Section snippets
Structure of LDB impeller
LDB impeller, a new type of wide-adaptability stirrer based on FZ and MB impellers, is composed of upper and lower blades fixed on stirring shaft by upper and lower shaft sleeves. As shown in Fig. 1 (Xu and Lin, 2011), the two blades are arranged with certain axial distance and angle, both of which have symmetrical grids. The upper blade is equipped with extension plate at the lower tips, while the lower blade, whose bottom shape matches the structure of channel-head, has flanged plates in the
Experimental setup
The experiment was conducted in a PMMA stirred tank with a diameter of 380 mm, equipped with standard elliptical head in the bottom. During the experiment, the stirred tank, with 418 mm high liquid level, had two feeding points of F1, F2 and one sampling point P positioned at the same location as F1. Their specific locations are shown in Fig. 2. The novel LDB impeller was employed. And for reference, FZ and DHR impellers which have wide applications in viscous systems were also used. Structures
Influence of feeding time on segregation index
During the experiment, the iodide-iodate parallel competing reaction system was adopted to study impellers’ micromixing characteristic. Considering that too high adding speed of H+ would cause fluidic macromixing to make a difference in the experimental results, the impact of macromixing on reaction product distribution must be eliminated beforehand. It was demonstrated that prolonging feeding time continuously played a significant part in removing macromixing effects on segregation index (Cui
Conclusion
The LDB impeller is a novel type of impeller developed from FZ and MB impeller. It combines both advantages of the two kinds of impellers and has good adaptability in different viscous systems and under different fluid regimes. The iodide-iodate competing parallel reaction system was adopted to study its micromixing effects, the results are shown below:
- (1)
Segregation index decreases with the increasing feeding time. When feeding time is greater than the critical one, the segregation index Xs tends
Nomenclature
flanged plate width, mm
initial reactant concentration, mol/L
- C
distance from the tank bottom, mm
mass concentration of the malt syrup
impeller diameter, mm
space between upper and lower blades
stirring speed, rpm
stirring power, W
- =
power per unit volume, W.m-3
Reynolds number
micromixing characteristic time, s
kinematic viscosity, m2.s-1
segregation index
mole fraction
value of Y in instantaneous reactions
number of grids
angle between upper and lower blades, °
energy dissipating rate, m2
Acknowledgments
This work was financially supported by the National Natural Science Foundation of China (21206144) and the Program for Zhejiang Leading Team of S&T Innovation (2011R50005).
References (21)
- et al.
Mixing and fast chemicalreaction-I: test reactions to determine segregation
Chem. Eng. Sci.
(1981) - et al.
Power consumption and solid suspension performance of large-scale impellers in gas–liquid–solid three-phase stirred tank reactors
Chem. Eng. J.
(2004) - et al.
A new parallel competing reaction system for assessing micromixing effciency experimental approach
Chem. Eng. Sci.
(1996) - et al.
Characterisation of micromixing effciency by the iodide-iodate reaction system.part I: experimental procedure
Chem. Eng. Sci.
(2000) - et al.
Extension of a chemical method for the study of micromixing process in viscous media
Chem. Eng. Sci.
(1997) - et al.
Characterisation of micromixing effciency by the iodide-iodate reaction system.part II: kinetic study [ J]
Chem. Eng. Sci.
(2000) - et al.
Free radical polymerization engineering-I: a new method for modeling free radical homogenous polymerization reactions
Chem. Eng. Sci.
(1984) - et al.
Numerical investigation on dispersive mixing characteristics of MAXBLEND and double helical ribbons
Chem. Eng. J.
(2001) Mixing and selectivity of chemical reactions
Org. Process Res. Dev.
(2003)- et al.
Development and research progress in mixers with broad adaptability to viscosity
Chem. Eng. Mach.
(2014)