Friction losses in valves and fittings for power-law fluids
Authors:
Open Access
- 1 October 2003
- journal article
- Published by FapUNIFESP (SciELO) in Brazilian Journal of Chemical Engineering
- Vol. 20 (4) , 455-463
Abstract
Data on pressure drop were obtained in stainless steel, sanitary fittings and valves during laminar and turbulent flow of aqueous solutions of sucrose and xanthan gum, which were selected as model fluids. The rheological properties of these solutions were determined and the power-law model provided the best fit for experimental data. Friction losses were measured in fully and partially open butterfly and plug valves, bends and unions. Values of loss coefficients (k f) were calculated and correlated as a function of the generalized Reynolds number by the two-k method. The model adjustment was satisfactory and was better in the laminar flow range (0.976 < r² < 0.999) than in the turbulent flow range (0.774 < r² < 0.989). In order to test the adequacy of the results for predicting loss coefficients during flow of real fluids, experiments were conducted with coffee extract. Comparison between experimental and predicted loss coefficients showed very good agreementKeywords
This publication has 12 references indexed in Scilit:
- ELEVATION ON BOINLING POINT OF COFFE EXTRACTBrazilian Journal of Chemical Engineering, 2002
- RHEOLOGICAL PROPERTIES AND FLUID DYNAMICS OF COFFEE EXTRACTJournal of Food Process Engineering, 2001
- RESISTANCE COEFFICIENTS OF FITTINGS FOR POWER‐LAW FLUIDS IN LAMINAR FLOWJournal of Food Process Engineering, 2001
- Non‐newtonian liquid flow through globe and gate valvesThe Canadian Journal of Chemical Engineering, 1994
- Non-newtonian liquid flow in bendsThe Chemical Engineering Journal, 1991
- COMPARISON of FRICTION FACTOR EQUATIONS FOR NON‐NEWTONIAN FLUIDS IN PIPE FLOW1Journal of Food Process Engineering, 1986
- Pressure Drop Across Valves and Fittings for Pseudoplastic Fluids in Laminar FlowTransactions of the ASAE, 1984
- Flow of dilatant (shear‐thickening) fluidsAIChE Journal, 1971
- Turbulent flow of non‐newtonian systemsAIChE Journal, 1959
- Direct Determination of the Flow Curves of Non-Newtonian Fluids. II. Shearing Rate in the Concentric Cylinder ViscometerJournal of Applied Physics, 1953