آمار

تعداد نشریات11
تعداد شماره‌ها228
تعداد مقالات2,324
تعداد مشاهده مقاله3,712,577
تعداد دریافت فایل اصل مقاله2,721,700
Mashaei, P. R. Mashaei, Hosseinalipour, S. M., Esmailpour, K.. (1392). Numerical investigation of thermal mixing of shear thinning fluids in one-way opposing jets. فناوری آموزش, 3(2), 95-103. doi: 10.22061/jcarme.2014.63
P. R. Mashaei Mashaei; S. M. Hosseinalipour; K. Esmailpour. "Numerical investigation of thermal mixing of shear thinning fluids in one-way opposing jets". فناوری آموزش, 3, 2, 1392, 95-103. doi: 10.22061/jcarme.2014.63
Mashaei, P. R. Mashaei, Hosseinalipour, S. M., Esmailpour, K.. (1392). 'Numerical investigation of thermal mixing of shear thinning fluids in one-way opposing jets', فناوری آموزش, 3(2), pp. 95-103. doi: 10.22061/jcarme.2014.63
Mashaei, P. R. Mashaei, Hosseinalipour, S. M., Esmailpour, K.. Numerical investigation of thermal mixing of shear thinning fluids in one-way opposing jets. فناوری آموزش, 1392; 3(2): 95-103. doi: 10.22061/jcarme.2014.63

Numerical investigation of thermal mixing of shear thinning fluids in one-way opposing jets

Journal of Computational & Applied Research in Mechanical Engineering (JCARME)
مقاله 2، دوره 3، شماره 2 - شماره پیاپی 6، فروردین 2014، صفحه 95-103    اصل مقاله (1.2 M)
نوع مقاله: Research Paper
شناسه دیجیتال (DOI): 10.22061/jcarme.2014.63
نویسندگان
P. R. Mashaei Mashaei؛ S. M. Hosseinalipour* ؛ K. Esmailpour
CAE Lab & CFD Center, School of Mechanical Engineering, Iran University of Science and Technology (IUST), Tehran, 16765-163, Iran
تاریخ دریافت: 10 تیر 1391،  تاریخ بازنگری: 19 تیر 1392،  تاریخ پذیرش: 26 تیر 1392 
چکیده
In recent years, impinging streams have received increasing interest for their high efficiency in heat and mass transfer. This numerical study was conducted to investigate flow and heat transfer characteristics of one-way opposing jets of non-Newtonian fluids. Effects of Reynolds number impinging angle, momentum ratio and flow behavior index on mixing index were evaluated. The results showed improvement of thermal mixing due to an increase in Reynolds number, flow behavior index and momentum ratio in impinging zone. This study also demonstrated that thermal mixing along the channel increased as the Reynolds number and momentum ratio decreased. Nevertheless, augmentation of the flow behavior index resulted in higher thermal mixing along the channel. The impinging angle had no significant effect on thermal mixing along the channel; but, with increasing impinging angle, thermal mixing improved in the impinging zone.
کلیدواژه‌ها
Opposing streams؛ Mixing index؛ Non-Newtonian؛ Flow behavior index؛ Impinging angle
مراجع
[1] A. Tamir, “Processes and phenomena in impinging-stream reactors”, Chemical Engeniring Progrgress, Vol. 85, No. 9, pp. 53-61, (1989).

[2] T. Kudra, A. S. Mujumdar, “Impingement stream dryers for particles and pastes”, Drying Technology, Vol. 7, No. 2, pp. 219-266, (1989).

[3] A. Tamir, Impinging-Stream Reactors: Fundamentals and Applications, Elsevier, Amsterdam, (1994).

[4] S. M. Hosseinalipour, A.S. Mujumdar, “Flow, heat transfer and particle drying characteristics in confined opposing jets: A numerical study”, Drying Technology, Vol. 13, No. 3, pp. 753-781, (1995).

[5] Y. Berman, A. Tamir, “Experimental investigation of phosphate dust collection in   impinging streams”, The Canadian Journal of Chemical Engineering, Vol. 74, No. 6, pp. 817-821, (1996).

[6] Y. Berman, A. Tanklevsky, Y. Oren, Tamir A., “Modeling and experimental studies of SO2 absorption in coaxial cylinders with impinging streams: Part I”, Chemical Engineering Science, Vol. 55, No. 5, pp. 1009-1021, (2000).

[7] Y. Berman, A. Tanklevsky, Y. Oren, Tamir A., “Modeling and experimental studies of SO2 absorption in coaxial cylinders with impinging streams: Part II”, Chemical Engineering Science, Vol. 55, No. 5, pp. 1023-1028, (2000).

[8] B. Yao, Y. Berman, A.  Tamir, “Evaporative cooling of air in impinging streams”, AIChE Journal, Vol. 41, No. 7, pp. 1667-1675, (1995).

[9] J. C. Roy, C. Bertrand, G. L. Palec, “Numerical and experimental study of mixed and forced convection in a junction”, International Journal of Heat and Mass Transfer, Vol. 37, No. 11, pp. 1985-2006, (1994)

[10] S. M. Hosseinalipour, A. S. Mujumdar, “Flow and Thermal Characteristics of Steady Two-Dimensional Confined Laminar Opposing Jets: Part I. Equal Jets”, International Communication of Heat Mass transfer, Vol. 24, No. 1, pp. 27-38, (1997).

[11] S. M. Hosseinalipour, A. S. Mujumdar, “Flow and Thermal Characteristics of Steady Two-Dimensional Confined Laminar Opposing Jets: Part II. Unequal Jets”,International Communication of Heat and Mass transfer, Vol. 24, No. 1, pp. 39-50, (1997).

[12] S. M. Hosseinalipour,  A. S. Mujumdar, , “Comparative evaluation of different turbulence models for confined impinging and opposing jet flows”, Numerical Heat Transfer, Part A: Application, Vol. 28, No. 6, pp. 647- 666, (1995).

[13] S. Devahastin, A. S. Mujumdar, “A numerical study of flow and mixing characteristics of laminar confined impinging streams”,Chemical Engineering Journal, Vol. 85, No. 2-3, pp. 215-223, (2002).

[14] H. J. Poh, K. Kumar, H. S. Chiang, A. S. Mujumdar, “Heat transfer from a laminar impinging jet of a power law fluid”, International Communications in Heat and Mass Transfer, Vol. 31, No. 2, .pp. 241-249, (2004).

[15] A. Chatterjee , S. C. Dhingra , S. S. Kapur, “Laminar impinging jet heat transfer with a purely viscous inelastic fluid”, Numerical Heat Transfer, Part A: Applications, Vol. 42, No. 1-2, pp. 193-213, (2002).

[16] C. Srisamran, C. Devahastin, “Numerical simulation of flow and mixing behavior of impinging streams of shear-thinning fluids”, Chemical Engineering Science, Vol. 61, No. 15, pp. 4884-4892, (2006).

[17] A. Cavadas, F. T. Pinho, J. M. Campos  , “Numerical Investigation of the Flow Field in Confined Impinging Jets of  Non  Newtonian  Fluids”,  The XVth    International Congress on Rheology, pp. 165-167, (2008).

[18] K. F. K. Adane , M. F. Tachie , “PIV study of laminar wall jets of non-Newtonian fluids”, Journal of Fluids Engineering, Transactions of the ASME, Vol. 132, No. 7, pp. 0712011-0712018, (2010).

[19] M. Moradi, G. Etemad, A. Moheb  , “Laminar flow heat transfer of pseudoplastic fluid through a double pipe heat exchanger”, Iranian Journal of Chemical Engineering, Vol. 3, No. 2, pp. 13-19, (2006).

[20] A. Kumar, M. Bhattacharya, “Teransient temperature and velocity profile in canned non-Newtonian liquid food during sterilization in a still-cook retort”, International Journal of Heat and Mass Transfer, Vol. 34, No. 7, pp. 1083-1096,(1991).

[21] ANSYS, Ver. 5.4, User Manual, SAS Co, (1998).

آمار
تعداد مشاهده مقاله: 3,220
تعداد دریافت فایل اصل مقاله: 1,956


سامانه مدیریت نشریات علمی. طراحی و پیاده سازی از سیناوب