Моделювання гетерогенних систем (рідина-рідина) у мікрореакторах
DOI:
https://doi.org/10.15587/2313-8416.2014.30735Słowa kluczowe:
мікрореактор, мікроканал, процес функціоналізації, поверхня кремнезему, CFD-моделювання, гетерогенна система, мініатюризаціяAbstrakt
В даній роботі було розглянуто представлені в літературі математичні моделі гетерогенних систем (рідина-рідина) в середовищі мікроканалів. На основі узагальнених даних обґрунтовано доцільність застосування мікрореактора для проведення процесу функціоналізації поверхні кремнезему і синтезу інноваційних матеріалів. Наступним етапом даного дослідження є розробка математичної моделі процесу та її реалізації в спеціальному програмному середовищі.
Bibliografia
Iarylin, R., Herbst A. (2012). Nepreryvnye protochnye mikroreaktory [Continuous flow microreactors]. Microreactors and nanotechnology, 44–49.
Kashid, M. N., Gupta, A., Renken, A., Kiwi-Minsker, L. (2010). Numbering-up and mass transfer studies of liquid–liquid two-phase microstructured reactors. Chemical Engineering Journal, 158 (2), 233–240. doi: 10.1016/j.cej.2010.01.020
Mills, P. L., Quiram, D. J., Ryley, J. F. (2007). Microreactor technology and process miniaturization for catalytic reactions – A perspective on recent developments and emerging technologies. Chemical Engineering Science, 62 (24), 6992–7010. doi: 10.1016/j.ces.2007.09.021
Zub, Yu. L., Kessler, V. G. (2008). Design of Functionalized Polysiloxane Adsorbents and their Environmental Applications. Proceding of ARW NATO, 29.
Zub, Yu. L. (2010). Funkcionalizovani orhanokremnezemy: syntez, bydova, fizyko-himichni vlastyvosti [Functionalized organosilicas: synthesis, structure and physicochemical properties]. Kharkiv, 603.
Hernandez Carucci, J. R., Eränen, K., Murzin, D. Yu., Salmi, T. O. (2009). Experimental and modelling aspects in microstructured reactors applied to environmental catalysis. Catalysis Today, 147, 149–150. doi: 10.1016/j.cattod.2009.07.034
Yeung, K. L., Zhang, X., Wai, N. L., Martin-Aranda, R. (2005). Experiments and modeling of membrane microreactors. Catalysis Today, 110 (1-2), 26–37. doi: 10.1016/j.cattod.2005.09.020
Yang, B., Yuschak, T., Mazanec T., Lee Tonkovich, A., Perry, S. (2008). Multi-scale modeling of microstructured reactors for the oxidative dehydrogenation of ethane to ethylene. Chemical Engineering Journal, 135, 147–152. doi: 10.1016/j.cej.2007.07.050
Kashid, M. N., Agar, D. W., Turek, S. (2007). CFD-modelling of mass transfer with and without chemical reaction in the liquid–liquid slug flow microreactor. Chemical Engineering Science, 62 (18-20), 5102–5109. doi: 10.1016/j.ces.2007.01.068
Qian, D., Lawal, A. (2006). Numerical study on gas and liquid slugs for Taylor flow in a T-junction microchannel. Chemical Engineering Science, 61(23), 7609–7625. doi: 10.1016/j.ces.2006.08.073
Kumar, V., Vashisth, S., Hoarau, Y., Nigam, K. D. P. (2007). Slug flow in curved microreactors: hydrodynamic study. Chemical Engineering Science, 62 (24), 7494–7504. doi: 10.1016/j.ces.2007.06.026
Gupta, R., Fletcher, D. F., Haynes, B. S. (2009). On the CFD-modelling of Taylor flow in microchannels. Chemical Engineering Science, 64 (12), 2941–2950. doi: 10.1016/j.ces.2009.03.018
Kashid, M. N., Renken, A., Kiwi-Minsker, L. (2011). Gas-liquid and liquid-liquid mass transfer in microstructured reactors. Chemical Engineering Science, 66 (17), 3876–3897. doi: 10.1016/j.ces.2011.05.015
Kashid, M. N., Renken, A., Kiwi-Minsker, L. (2010). CFD-modelling of liquid–liquid multiphase microstructured reactor: Slug flow generation. Chemical Engineering Research and Design, 88 (3), 362–368. doi: 10.1016/j.cherd.2009.11.017
Kulkarni, А. A., Gorasia, A. K., Ranade, V. V. (2007). Hydrodynamics and liquid phase residence time distribution in mesh microreactor. Chemical Engineering Science, 62 (24), 7484–7493. doi: 10.1016/j.ces.2007.08.063
Haidarov, V. H., Borovinskaya, E. S., Tomas, A., Holodniv, V. A., Reshetilovskii, V. P. (2013). Modelirovanie reakcii omyleniia etilacetata i izopropilacetata c ychetom hidrodinamiki i trohmernoy modeli reaktora v Ansys Fluent [Simulation of the saponification reaction of ethyl acetate and isopropyl acetate, considering hydrodynamics and three-dimensional model of reactor in Ansys Fluent]. Proceedings of the St. Petersburg State Technological Institute (technical university), 44, 93–96.
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