Bu öğeden alıntı yapmak, öğeye bağlanmak için bu tanımlayıcıyı kullanınız: http://hdl.handle.net/11452/23542
Başlık: Determination of resistance coefficient and turbulent friction factor in non-circular ducts
Yazarlar: Uludağ Üniversitesi/Mühendislik Mimarlık Fakültesi/Makine Mühendisliği Bölümü.
Umur, Habib
6602945164
Anahtar kelimeler: Thermodynamics
Engineering
Friction factor
Resistance coefficients
Valves
Turbulent flows
Non-circular ducts
Flow
Annuli
Duct
Flow resistance
Friction evaluation
Pipe fitting
Pipe flow
Turbulent flow
Valve
Ducts
Equations of motion
Friction
Pipe fittings
Reynolds number
Turbulent flow
Friction coefficient
Non-circular ducts
Pipe flow
Yayın Tarihi: 2000
Yayıncı: Japan Soc Mechanical Engineers
Atıf: Umur, H. (2000). "Determination of resistance coefficient and turbulent friction factor in non-circular ducts". JSME International Journal Series B-Fluids and Thermal Engineering, 43(2), 136-142.
Özet: Static pressures in non-circular ducts and pipe fittings (globe, ball and butterfly valves) have been measured in a closed circuit water channel at the range of Reynolds number from 20 000 to 80 000, which give rise to fully developed turbulent pipe flow, so as to define the friction coefficient (C-f) and resistance coefficients (K). A new proposed equation for friction factor with two new dimensionless parameters as a function of cross sectional area are successfully adopted to fully developed turbulent flow in all cross sections with a precision of better than +/-4%. Measurements showed that friction factors decreased with increasing eccentricity and were in good agreement with the proposed equation. It was also found out that Reynolds number has no effect on resistance coefficients of butterfly, globe and gate valves, but the closing ratio caused K to increase remarkably, and the K value of bends can easily be obtained by an empirical formula based on Moody chart friction factor. Static pressures on front and back sides of the circular disc of butterfly valve decreased with Reynolds number, remained almost constant in the radial direction and increased particularly at closing angles of bigger than 60 degrees, where flow rate starts to decrease sharply.
URI: https://doi.org/10.1299/jsmeb.43.136
https://www.jstage.jst.go.jp/article/jsmeb1993/43/2/43_2_136/_article
http://hdl.handle.net/11452/23542
ISSN: 1340-8054
Koleksiyonlarda Görünür:Scopus
Web of Science

Bu öğenin dosyaları:
Dosya Açıklama BoyutBiçim 
Umur_2000.pdf803.4 kBAdobe PDFKüçük resim
Göster/Aç


Bu öğe kapsamında lisanslı Creative Commons License Creative Commons