Flow Rate Measurement of Non-Newtonian Fluids through Sharp Crested Notches

被引:0
|
作者
Khahledi, Morakane [1 ]
Haldenwang, Rainer [2 ]
Chhabra, Raj [3 ,4 ]
机构
[1] Cape Peninsula Univ Technol, Civil Engn & Surveying Dept, ZA-7530 Cape Town, South Africa
[2] Cape Peninsula Univ Technol, Dept Civil Engn Civil Engn & Surveying, ZA-7530 Cape Town, South Africa
[3] Indian Inst Technol IIT Kanpur, Dept Chem Engn, Kanpur 208016, Uttar Pradesh, India
[4] Cape Peninsula Univ Technol, ZA-7530 Cape Town, South Africa
关键词
Sharp crested notches; non-Newtonian fluids; Rheology; Coefficient of discharge; Laminar flow; Turbulent flow; POWER-LAW; FRICTION; LAMINAR;
D O I
10.1061/(ASCE)HY.1943-7900.0000941
中图分类号
TU [建筑科学];
学科分类号
0813 ;
摘要
Sharp crested notches, particularly rectangular and V-shaped ones, have been used to measure the flow rate of water in open channels for a long time. However, they have not been used to measure the flow rate of non-Newtonian fluids. The aim of this work is to explore the possibility of extending their range of application to non-Newtonian fluids, especially for rectangular and V-shaped notches. An experimental facility in the flow process research laboratory was used to perform the extensive tests reported herein. The notches and an in-line tube viscometer were calibrated using water. The in-line tube viscometer was used to determine the fluid rheology. Three different types of non-Newtonian fluids [namely, aqueous solution of carboxymethyl cellulose (CMC) solutions and water-based suspensions of kaolin and bentonite] were used as model test fluids. The experimental values of the coefficient of discharge (C-d) were plotted against three different definitions of the Reynolds number denoting different underlying physical ideas. In the laminar conditions, the discharge coefficient exhibited the classical dependence on the Reynolds number with slopes of approximately 0.43-0.44. On the other hand, the discharge coefficient was nearly constant in the turbulent flow regime. Single composite power-law function was used to correlate the present C-d - R for each of the two notch shapes used here. Using these correlations, the C-d values could be predicted to within +/- 5% for the rectangular and the V notches. (C) 2014 American Society of Civil Engineers.
引用
收藏
页数:9
相关论文
共 50 条
  • [1] Flow Rate Measurement of Non-Newtonian Fluids through Sharp Crested Notches (Oct 6, 10.1061/(ASCE)HY.1943-7900.0000941, 2014)
    Khahledi, Morakane
    Haldenwang, Rainer
    Chhabra, Raj
    JOURNAL OF HYDRAULIC ENGINEERING, 2023, 149 (10)
  • [2] Modeling the Flow of Non-Newtonian Fluids Through Sharp Orifices
    Rituraj
    Vacca, Andrea
    JOURNAL OF FLUIDS ENGINEERING-TRANSACTIONS OF THE ASME, 2018, 140 (05):
  • [3] Flow of non-Newtonian fluids
    Avram, Marius Andrei
    Avram, Marioara
    Iliescu, Ciprian
    Bragaru, Adina
    2006 INTERNATIONAL SEMICONDUCTOR CONFERENCE, VOLS 1 AND 2, 2007, : 463 - +
  • [4] FLOW OF NON-NEWTONIAN FLUIDS THROUGH POROUS MEDIA
    SAVINS, JG
    INDUSTRIAL AND ENGINEERING CHEMISTRY, 1969, 61 (05): : 8 - &
  • [5] Flow of non-Newtonian fluids through eccentric annuli
    Luo, Yuejin
    Peden, J.M.
    SPE Production Engineering, 1990, 5 (01): : 91 - 96
  • [6] FLOW OF NON-NEWTONIAN FLUIDS THROUGH HELICAL COILS
    RAJASEKHARAN, S
    KUBAIR, VG
    KULOOR, NR
    INDIAN JOURNAL OF TECHNOLOGY, 1970, 8 (11): : 391 - +
  • [7] Flow of Newtonian and non-Newtonian fluids through fixed stratified layers
    Sabiri, N.-E.
    Comiti, J.
    Canadian Journal of Chemical Engineering, 1997, 75 (06): : 1030 - 1037
  • [8] Flow of Newtonian and Non-Newtonian Fluids Through Packed Beds: An Experimental Study
    Kaur, Navdeep
    Singh, Raveena
    Wanchoo, R. K.
    TRANSPORT IN POROUS MEDIA, 2011, 90 (02) : 655 - 671
  • [9] Flow of Newtonian and Non-Newtonian Fluids Through Packed Beds: An Experimental Study
    Navdeep Kaur
    Raveena Singh
    R. K. Wanchoo
    Transport in Porous Media, 2011, 90 : 655 - 671
  • [10] The flow of non-newtonian fluids through filter gauze packets
    Kiljanski, T
    Dziubinski, M
    PRZEMYSL CHEMICZNY, 2003, 82 (8-9): : 1209 - 1211