Afshar Ghotli, R. and Abdul Raman, Abdul Aziz and Ibrahim, Shaliza and Baroutian, Saeid and Arami-Niya, A. (2013) Study of various curved-blade impeller geometries on power consumption in stirred vessel using response surface methodology. Journal of the Taiwan Institute of Chemical Engineers, 44 (2). pp. 192-201. ISSN 1876-1070, DOI https://doi.org/10.1016/j.jtice.2012.10.010.
|
PDF (Study of various curved-blade impeller geometries on power consumption in stirred vessel using response surface methodology)
Study_of_various_curved-blade_impeller_geometries_on_power_consumption_in_stirred_vessel_using_response_surface_methodology.pdf - Other Download (641kB) |
Abstract
The geometry of an impeller is a determining factor in power demand, which in turn determines the cost of mixing operation in stirred tanks. In this work, the power requirements for seven types of 6-curved blade impellers of varying curvature angles and central disk sizes, were analyzed via response surface methodology (RSM) and compared to a Ruston turbine. The experiments were conducted using water as the working fluid in a standard mixing vessel. Power consumptions were measured using a load cell arrangement for a wide range of speeds in both aerated and un-aerated conditions. The data revealed that the power number (NP) of the elliptical shape curved blade was 2.8 whereas for CB180°, CB160° and CB140° were respectively 21, 32 and 75 higher. Furthermore, the power number values for the impeller with a 3/4D central disk size was approximate 3.4, while the impellers with 1/2, 1/4 and without central disk were respectively 15, 20 and 23.5 higher. The results under different gas flow rates illustrated the power reduction of the curved blades impellers, both various central disk sizes and curvature angles, were in the range of 1-20 meanwhile the Rushton turbine was in the range of 5-45. Curvature angle and central disk size found as the significant parameters through variance analysis (ANOVA). The results also indicated that the significance of the central disk size was less than the other variables. The R-squared values indicated a fitting of the models with the experimental data. In conclusion, the curved blade impellers were found to have lower power consumption in both aerated and un-aerated conditions in comparison with the Rushton turbine. © 2012 Taiwan Institute of Chemical Engineers.
Item Type: | Article |
---|---|
Funders: | UNSPECIFIED |
Additional Information: | Export Date: 13 February 2014 Source: Scopus Language of Original Document: English Correspondence Address: Arami-Niya, A.; Department of Chemical Engineering, Faculty of Engineering, University of Malaya, 50603 Kuala Lumpur, Malaysia; email: arasharaminiya@yahoo.com References: Paul, E.L., Atiemo-Obeng, V.A., Kresta, S.M., (2004) Handbook of industrial mixing, , John Wiley & Sons, Inc, New Jersey; Buwa, V., Dewan, A., Nassar, A.F., Durst, F., Fluid dynamics and mixing of single-phase flow in a stirred vessel with a grid disc impeller: experimental and numerical investigations (2006) Chem Eng Sci, 61 (9), pp. 2815-2822; Khare, A.S., Niranjan, K., An experimental investigation into the effect of impeller design on gas hold-up in a highly viscous Newtonian liquid (1999) Chem Eng Sci, 54 (8), pp. 1093-1100; Ranade, V.V., Mishra, V.P., Saraph, V.S., Deshpande, G.B., Joshi, J.B., Comparison of axial flow impellers using a laser Doppler anemometer (1992) Ind Eng Chem Res, 31 (10), pp. 2370-2379; Montante, G., Mostek, M., Jahoda, M., Magelli, F., CFD simulations and experimental validation of homogenisation curves and mixing time in stirred Newtonian and pseudoplastic liquids (2005) Chem Eng Sci, 60 (8-9), pp. 2427-2437; El-Hamouz, A., Cooke, M., Kowalski, A., Sharratt, P., Dispersion of silicone oil in water surfactant solution: effect of impeller speed, oil viscosity and addition point on drop size distribution (2009) Chem Eng Process, 48 (2), pp. 633-642; Bujalski, W., Nienow, A.W., Chatwin, S., Cooke, M., The dependency on scale of power numbers of Rushton disc turbines (1987) Chem Eng Sci, 42 (2), pp. 317-326; Karcz, J., Major, M., An effect of a Baffle length on the power consumption in an agitated vessel (1998) Chem Eng Process, 37 (3), pp. 249-256; Chen, Z.D., Chen, J.J.J., A study of agitated gas-liquid reactors with concave blade impellers (2000) Mixing and crystalization, pp. 43-56. , Kluwer Academic Publishers, Malaysia, B.S. Gupta, S. Ibrahim (Eds.); Houcine, I., Plasari, E., David, R., Effects of the stirred tank's design on power consumption and mixing time in liquid phase (2000) Chem Eng Technol, 23 (7), pp. 605-613; Wu, J., Zhu, Y., Pullum, L., Impeller geometry effect on velocity and solids suspension (2001) Chem Eng Res Des, 79 (8), pp. 989-997; Warmoeskerken, M.M.C.G., Smith, J.M., The hollow blade agitator for dispersion and mass transfer (1989) Trans IChemE, 67, pp. 193-198; Mhetras, M.B., Pandit, A.B., Joshi, D., Effect of agitator design on hydrodynamics and power consumption in mechanically agitated gas-liquid reactors (1994) Eighth European conference on mixing; Forrester, S.E., Rielly, C.D., Carpenter, K.J., Gas-inducing impeller design and performance characteristics (1998) Chem Eng Sci, 53 (4), pp. 603-615; Amanullah, A., Serrano-Carreon, L., Castro, B., Galindo, E., Nienow, A.W., The influence of impeller type in pilot scale Xanthan fermentations (1998) Biotechnol Bioeng, 57 (1), pp. 95-108; Cooke, M., Heggs, P.J., Advantages of the hollow (concave) turbine for multi-phase agitation under intense operating conditions (2005) Chem Eng Sci, 60 (20), pp. 5529-5543; Shiue, S.J., Wong, C.W., Studies on homogenization efficiency of various agitators in liquid blending (1984) Can J Chem Eng, 62, pp. 602-609; Weetman, R.J., Oldshue, J.Y., Power, flow and shear characteristics of mixing impellers (1988) Proceedings of 6th European conference on mixing; McFarlane, C.M., Zhao, X.M., Nienow, A.W., Studies of high solidity ratio hydrofoil impellers for aerated bioreactors. 2. Air-water studies (1995) Biotechnol Progr, 11 (6), pp. 608-618; Junker, B.H., Stanik, M., Barna, C., Salmon, P., Paul, E., Buckland, B.C., Influence of impeller type on power input in fermentation vessels (1998) Bioprocess Eng, 18 (6), pp. 401-412; Van't Riet, K., Smith, J.M., The behaviour of gas-liquid mixtures near Rushton turbine blades (1973) Chem Eng Sci, 28 (4), pp. 1031-1037; Galindo, E., Nienow, A.W., Mixing of highly viscous simulated xanthan fermentation broths with the Lightnin A-315 impeller (1992) Biotechnol Progr, 8 (3), pp. 233-239; McFarlane, C.M., Nienow, A.W., Studies of high solidity ratio hydrofoil impellers for aerated bioreactors. 4. Comparison of impeller types (1996) Biotechnol Progr, 12 (1), pp. 9-15; Chen, Z.D., Chen, J.J.J., Comparison of mass transfer performance for various single and twin impellers (1999) Chem Eng Res Des, 77 (2), pp. 104-109; Saito, F., Nienow, A.W., Chatwin, S., Moore, I.P.T., Power, gas dispersion and homogenisation characteristics of SCABA SRGT and Rushton turbine impellers (1992) J Chem Eng Jpn, 25, pp. 281-287; Couper, J.R., Penney, W.R., Fair, J.R., Walas, S.M., James, R.C., W.Roy, P., (2005) Mixing and agitation, in chemical process equipment, pp. 277-328. , Gulf Professional Publishing, Burlington; Arami-Niya, A., Wan Daud, W.M.A., S.Mjalli, F., Abnisa, F., Shafeeyan, M.S., Production of microporous palm shell based activated carbon for methane adsorption: modeling and optimization using response surface methodology (2011) Chem Eng Res Des, 90, pp. 776-784; Alam, Z., Muyibi, S.A., Toramae, J., Statistical optimization of adsorption processes for removal of 2,4-dichlorophenol by activated carbon derived from oil palm empty fruit bunches (2007) J Environ Sci, 19, pp. 674-677; Karacan, F., Ozden, U., Karacan, S.L., Optimization of manufacturing conditions for activated carbon from Turkish lignite by chemical activation using response surface methodology (2007) Appl Therm Eng, 27 (7), pp. 1212-1218; Chen, J.P., Higgins, F.B., Chang, S.Y., Hung, Y.T., Mixing (2005) Physicochem Treat Process, 3, pp. 47-101; Westerterp, K.R., van Dierendonck, L.L., de Kraa, J.A., Interfacial areas in agitated gas-liquid contactors (1963) Chem Eng Sci, 18 (3), pp. 157-176; Guillard, F., Trägårdh, C., Mixing in industrial Rushton turbine-agitated reactors under aerated conditions (2003) Chem Eng Process, 42 (5), pp. 373-386; Edwards, M.F., Baker, M.R., Harnby, N., Nienow, A.W., A review of liquid mixing equipment (1997) Mixing in the process industries, pp. 118-136. , Butterworth-Heinemann, Oxford; (2010) Load cell application and test guideline, , Scale Manufacturers Association (SMA), Columbus, OH, SMA; Birch, D., Ahmed, N., Gas sparging in vessels agitated by mixed flow impellers (1996) Powder Technol, 88 (1), pp. 33-38; Montgomery, D.C., (2001) Design and analysis of experiments, , John Wiley and Sons, New York, USA; Sahu, J.N., Acharya, J., Meikap, B.C., Response surface modeling and optimization of chromium(VI) removal from aqueous solution using Tamarind wood activated carbon in batch process (2009) J Hazard Mater, 172, pp. 818-825; Baroutian, S., Aroua, M.K., Abdul Aziz, A.R., Sulaiman Nik, M.N., A packed bed membrane reactor for production of biodiesel using activated carbon supported catalyst (2011) Bioresour Technol, 102 (2), pp. 1095-1102; Baroutian, S., Aroua, M.K., Abdul Aziz, A.R., Sulaiman Nik, M.N., Potassium hydroxide catalyst supported on palm shell activated carbon for transesterification of palm oil (2011) Fuel Process Technol, 91 (11), pp. 1378-1385; Shafeeyan, M.S., Wan Daud, W.M.A., Houshmand, A., Arami-Niya, A., The application of response surface methodology to optimize the amination of activated carbon for the preparation of carbon dioxide adsorbents (2012) Fuel, 94 (0), pp. 465-472; Vargas, A.M.M., Garcia, C.A., Reis, E.M., Lenzi, E., Costa, W.F., Almeida, V.C., NaOH-activated carbon from flamboyant (Delonix regia) pods: optimization of preparation conditions using central composite rotatable design (2010) Chem Eng J, 162 (1), pp. 43-50; Arami-Niya, A., Abnisa, F., Shafeeyan, M.S., Wan Daud, W.M.A., Sahu, J.N., Optimization of synthesis and characterization of palm shell-based bio-char as a by-product of bio-oil production process (2012) BioRes, 7 (1), pp. 246-264; Bezerra, M.A., Response surface methodology (RSM) as a tool for optimization in analytical chemistry (2008) Talanta, 76 (5), pp. 965-977; Rewatkar, V.B., Rao, K.S.M.S.R., Joshi, J.B., Power consumption in mechanically agitated contactors using pitched bladed turbine impellers (1990) Chem Eng Commun, 88 (1), pp. 69-90; Pacek, A.W., Chamsart, S., Nienow, A.W., Bakker, A., The influence of impeller type on mean drop size and drop size distribution in an agitated vessel (1999) Chem Eng Sci, 54 (19), pp. 4211-4222; Karcz, J., Major, M., An effect of a baffle length on the power consumption in an agitated vessel (1998) Chem Eng Process, 37 (3), pp. 249-256; Vasconcelos, J.M.T., Orvalho, S.C.P., Rodrigues, A.M.A.F., Alves, S.S., Effect of blade shape on the performance of six-bladed disk turbine impellers (1999) Ind Eng Chem Res, 39 (1), pp. 203-213; Nienow, A.W., (1996) Gas-liquid mixing studies: a comparison of Rushton turbines with some modern impellers, , Elsevier, Amsterdam, PAYS-BAS; Karcz, J., Kaminska-Brzoska, J., Heat transfer in a jacketed stirred tank equipped with baffles and concave disk impeller (1994) Eighth European conference on mixing |
Uncontrolled Keywords: | Curved blade impeller; Curvature angle; Central disk size, Power number (NP); Aerated and un-aerated system; RSM |
Subjects: | T Technology > T Technology (General) T Technology > TA Engineering (General). Civil engineering (General) T Technology > TP Chemical technology |
Divisions: | Faculty of Engineering |
Depositing User: | Mr Jenal S |
Date Deposited: | 26 Feb 2014 02:07 |
Last Modified: | 06 Dec 2019 08:16 |
URI: | http://eprints.um.edu.my/id/eprint/9446 |
Actions (login required)
View Item |