[1] Verzicco, R., Fatica, M., Iaccarino, G., and Orlandi, P. Flow in an impeller-stirred tank using an immersedboundary method. AIChE Journal, 50(6):1109–1118, 2004.
[2] Sbrizzai, Fabio, Lavezzo, Valentina, Campolo, Marina, and Soldati, Alfredo. Direct numerical simulation of turbulent particle dispersion in an unbaffled stirred-tank reactor. Chemical Engineering Science, 61:2843–2851, 05 2006.
[3] Derksen, J.J. Highly resolved simulations of solids suspension in a small mixing tank. AIChE Journal, 58(10):3266– 3278, 2012.
[4] Joshi, Jyeshtharaj B., Nere, Nandkishor K., Rane, Chinmay V., Murthy, B. N., Mathpati, Channamallikarjun S., Patwardhan, Ashwin W., and Ranade, Vivek V. Cfd simulation of stirred tanks: Comparison of turbulence models. part i: Radial flow impellers. The Canadian Journal of Chemical Engineering, 89(1):23–82, 2011.
[5] Hartmann, H., Derksen, J. J., and van den Akker, H. E. A. Macroinstability uncovered in a rushton turbine stirred tank by means of les. AIChE Journal, 50(10):2383–2393, 2004.
[6] Bakker, A. and Oshinowo, L.M. Modelling of turbulence in stirred vessels using large eddy simulation. Chemical Engineering Research and Design, 82(9):1169 – 1178, 2004. In Honour of Professor Alvin W. Nienow.
[7] Yeoh, S.L., Papadakis, G., and Yianneskis, M. Determination of mixing time and degree of homogeneity in stirred vessels with large eddy simulation. Chemical Engineering Science, 60(8):2293 – 2302, 2005. 5th International Symposium on Mixing in Industrial Processes (ISMIP5).
[8] Sungkorn, R., Derksen, J.J., and Khinast, J.G. Modeling of aerated stirred tanks with shear-thinning power law liquids. International Journal of Heat and Fluid Flow, 36:153 – 166, 2012.
[9] Sungkorn, R., Derksen, J. J., and Khinast, J. G. Euler– lagrange modeling of a gas–liquid stirred reactor with consideration of bubble breakage and coalescence. AIChE Journal, 58(5):1356–1370, 2012.
[10] Zhang, Qinghua, Yang, Chao, Mao, Zai-Sha, and Mu, Junjuan. Large eddy simulation of turbulent flow and mixing time in a gas–liquid stirred tank. Industrial & Engineering Chemistry Research, 51(30):10124–10131, Aug 2012.
[11] Mathpati, C. S. and Joshi, J. B. Insight into theories of heat and mass transfer at the solid−fluid interface using direct numerical simulation and large eddy simulation. Industrial & Engineering Chemistry Research, 46(25):8525– 8557, Dec 2007.
[12] Ranade, V.V., Perrard, M., Le Sauze, N., Xuereb, C., and Bertrand, J. Trailing vortices of rushton turbine: Piv measurements and cfd simulations with snapshot approach. Chemical Engineering Research and Design, 79(1):3 – 12, 2001.
[13] Jones, Raymond M., Harvey, Albert D., III, and Acharya, Sumanta. Two-Equation Turbulence Modeling for Impeller Stirred Tanks . Journal of Fluids Engineering, 123(3):640– 648, 03 2001.
[14] Ranade, Vivek V., Tayalia, Yatin, and Krishnan, H. Cfd predictions of flow near impeller blades in baffled stirred vessels: Assessment of computational snapshot approach. Chemical Engineering Communications, 189(7):895–922, 2002.
[15] Kálal, Zbyněk, Jahoda, Milan, and Fořt, Ivan. Modelling of the bubble size distribution in an aerated stirred tank: Theoretical and numerical comparison of different breakup models. Chemical and Process Engineering, (No 3 September):331–348, 2014.
[16] Numerical Study of Single Phase Liquid Mixing in Stirred Tanks Fitted With Rushton Turbine and Flotation Impeller, vol. Volume 7A: Fluids Engineering Systems and Technologies of ASME International Mechanical Engineering Congress and Exposition, 11 2013. V07AT08A047.
[17] Lane, G.L., Schwarz, M.P., and Evans, G.M. Numerical modelling of gas–liquid flow in stirred tanks. Chemical Engineering Science, 60(8):2203 – 2214, 2005. 5th International Symposium on Mixing in Industrial Processes (ISMIP5).
[18] Murthy, B.N., Deshmukh, N.A., Patwardhan, A.W., and Joshi, J.B. Hollow self-inducing impellers: Flow visualization and cfd simulation. Chemical Engineering Science, 62(14):3839 – 3848, 2007.
[19] Chtourou, Wajdi, Ammar, Meriem, Driss, Zied, and Abid, Mohamed. Effect of the turbulence models on rushton turbine generated flow in a stirred vessel. Open Engineering, 1(4):380 – 389, 01 Dec. 2011.
[20] Ammar, Meriem, Driss, Zied, Chtourou, Wajdi, and Abid, Mohamed S. Effects of baffle length on turbulent flows generated in stirred vessels. Central European Journal of Engineering, 1(4):401, Aug 2011.
[21] Ammar, M., Chtourou, W., Driss, Z., and Abid, M.S. Numerical investigation of turbulent flow generated in baffled stirred vessels equipped with three different turbines in one and two-stage system. Energy, 36(8):5081 – 5093, 2011. PRES 2010.
[22] Jenne, Marc and Reuss, Matthias. A critical assessment on the use of k–ff turbulence models for simulation of the turbulent liquid flow induced by a rushton-turbine in baffled stirred-tank reactors. Chemical Engineering Science, 54(17):3921 – 3941, 1999.
[۲۳] پهلوانی, صادق, هاشمآبادی, سید~حسن, و حیدری, امیر. شبیهسازی CFD هیدرودینامیک راکتورحبابی- دوغابی همزندار تولید ترفتالیک
اسید پتروشیمی شهید تندگویان. پژوهش نفت, 24(79):83--94, 2014.
[24] Launder, B. E. Current capabilities for modelling turbulence in industrial flows, pp. 37–59. Springer Netherlands, Dordrecht, 1991.
[25] Hanjalić, K. Advanced turbulence closure models: a view of current status and future prospects. International Journal of Heat and Fluid Flow, 15(3):178 – 203, 1994.
[26] Aghbolaghy, Mostafa and Karimi, Afzal. Simulation and optimization of enzymatic hydrogen peroxide production in a continuous stirred tank reactor using cfd–rsm combined method. Journal of the Taiwan Institute of Chemical Engineers, 45(1):101 – 107, 2014.
[27] Vlček, Petr, Skočilas, Jan, and Jirout, Tomáš. Cfd simulation of a stirred dished bottom vessel. Acta Polytechnica, 53, 12 2013.
[28] Han, Ying, Wang, Jia-Jun, Gu, Xue-Ping, and Feng, LianFang. Numerical simulation on micromixing of viscous fluids in a stirred-tank reactor. Chemical Engineering Science, 74:9 – 17, 2012.
[29] Wucherpfennig, Thomas, Krull, Rainer, and Esfandabadi, Manely. Agitation induced mechanical stress in stirred tank bioreactors-linking cfd simulations to fungal morphology. JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 45:742–748, 01 2012.
[30] Abu-Farah, L., Al-Qaessi, F., and Schönbucher, A. Cyclohexane/water dispersion behaviour in a stirred batch vessel experimentally and with cfd simulation. Procedia Computer Science, 1(1):655 – 664, 2010. ICCS 2010.
[31] Gillis, Paul, Hommersom, Gerrit, and Schäfer, Matthias. A comparison of several cfd approaches for predicting gasliquid contacting in a cylindrical tank agitated with a single rushton turbine. vol. 448, 01 2002.
[32] Kerdouss, F., Bannari, A., Proulx, P., Bannari, R., Skrga, M., and Labrecque, Y. Two-phase mass transfer coefficient prediction in stirred vessel with a cfd model. Computers & Chemical Engineering, 32(8):1943 – 1955, 2008.
[33] Wodołażski, Artur. Cfd-population balance modelling of catalyst particles in solid-liquid rushton turbine-agitated tank reactor in scale-up study. Powder Technology, 313:312 – 322, 2017.
[34] Kamla, Y., Bouzit, M., Hadjeb, A., Arab, I. M., and Beloudane, M. Cfd study of the effect of baffles on the energy consumption and the flow structure in a vessel stirred by a rushton turbine. Mechanika, 22:190+, 2020/8/30/ 2016. 3.
[35] Azargoshasb, Hamidreza, Mousavi, Seyyed Mohammad, Jamialahmadi, Oveis, Shojaosadati, Seyed Abbas, and Mousavi, Seyyed Babak. Experiments and a three-phase computational fluid dynamics (cfd) simulation coupled with population balance equations of a stirred tank bioreactor for high cell density cultivation. The Canadian Journal of Chemical Engineering, 94(1):20–32, 2016.
[36] Murthy, J. Y., Mathur, S. R., and Choudhary, D. Cfd simulation of flows in stirred tank rectors using a sliding mesh technique. 8th European Conference on Mixing, pp. 21–23, Cambridge, UK, 1994. Institution of Chemical Engineers.
[37] Deen, Niels G., Solberg, Tron, and Hjertager, Bjørn H. Flow generated by an aerated rushton impeller: Two-phase piv experiments and numerical simulations. The Canadian Journal of Chemical Engineering, 80(4):1–15, 2002.
[38] Jahoda, M., Tomášková, L., and Moštěk, M. Cfd prediction of liquid homogenisation in a gas–liquid stirred tank. Chemical Engineering Research and Design, 87(4):460 – 467, 2009. 13th European Conference on Mixing: New developments towards more efficient and sustainable operations.
[39] Perng, Chin Yuan, Murthy, J. Y., Calabrese, R. V., and Tatterson, G. B. A moving-deforming-mesh technique for simulation of flow in mixing tanks, symposium, process mixing: chemical and biochemical applications. in AICHE SYMPOSIUM SERIES, Process mixing: chemical and biochemical applications, Symposium, Process mixing: chemical and biochemical applications, no. 293, pp. 37–41, New York, NY, 1992. American Institute of Chemical Engineers;.
[40] Derksen, J. J. Numerical simulation of solids suspension in a stirred tank. AIChE Journal, 49(11):2700–2714, 2003.
[41] Witz, Christian, Treffer, Daniel, Hardiman, Timo, and Khinast, Johannes. Local gas holdup simulation and validation of industrial-scale aerated bioreactors. Chemical Engineering Science, 152:636 – 648, 2016.
[42] Joshi, Jyeshtharaj B., Nere, Nandkishor K., Rane, Chinmay V., Murthy, B. N., Mathpati, Channamallikarjun S., Patwardhan, Ashwin W., and Ranade, Vivek V. Cfd simulation of stirred tanks: Comparison of turbulence models (part ii: Axial flow impellers, multiple impellers and multiphase dispersions). The Canadian Journal of Chemical Engineering, 89(4):754–816, 2011.
[43] Pinelli, D., Montante, G., and Magelli, F. Dispersion coefficients and settling velocities of solids in slurry vessels stirred with different types of multiple impellers. Chemical Engineering Science, 59(15):3081 – 3089, 2004.
[44] Khopkar, Avinash R. and Ranade, Vivek V. Cfd simulation of gas–liquid stirred vessel: Vc, s33, and l33 flow regimes. AIChE Journal, 52(5):1654–1672, 2006.
[45] Khopkar, A. R., Kasat, G. R., Pandit, A. B., and Ranade, V. V. Computational fluid dynamics simulation of the solid suspension in a stirred slurry reactor. Industrial & Engineering Chemistry Research, 45(12):4416–4428, Jun 2006.
[46] Bao, Yuyun, Yang, Jie, Chen, Lei, and Gao, Zhengming. Influence of the top impeller diameter on the gas dispersion in a sparged multi-impeller stirred tank. Industrial & Engineering Chemistry Research, 51(38):12411–12420, Sep 2012.
[47] Zhang, Yanhong, Bai, Yulan, and Wang, Hualin. Cfd analysis of inter-phase forces in a bubble stirred vessel. Chemical Engineering Research and Design, 91(1):29 – 35, 2013
[48] Bao, Yuyun, Yang, Jie, Wang, Bingjie, and Gao, Zhengming. Influence of impeller diameter on local gas dispersion properties in a sparged multi-impeller stirred tank. Chinese Journal of Chemical Engineering, 23(4):615 – 622, 2015.
[49] Bao, Yuyun, Wang, Bingjie, Lin, Mingli, Gao, Zhengming, and Yang, Jie. Influence of impeller diameter on overall gas dispersion properties in a sparged multi-impeller stirred tank. Chinese Journal of Chemical Engineering, 23(6):890 – 896, 2015.