2008
DOI: 10.1002/cjce.5450830205
|View full text |Cite
|
Sign up to set email alerts
|

Friction Losses in Valves and Fittings for Viscoplastic Fluids

Abstract: Data on pressure drop were obtained in stainless steel, sanitary fittings and valves during laminar and turbulent flow of aqueous suspensions of sucrose and bentonite. The rheological properties of these suspensions were determined and the Bingham model provided the best fitting with the experimental data. Friction losses were measured in fully‐ and partially‐open butterfly and plug valves, bends and union. Values of loss coefficients (kf) were calculated and correlated as functions of the classical Reynolds n… Show more

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
1
1
1
1

Citation Types

0
6
0
1

Year Published

2009
2009
2022
2022

Publication Types

Select...
6
1
1

Relationship

1
7

Authors

Journals

citations
Cited by 13 publications
(7 citation statements)
references
References 12 publications
0
6
0
1
Order By: Relevance
“…Shear rate range was 0.5 to 300 s -1 and both upward and downward tests were performed in duplicate for each temperature and soluble solids content combination. The experimental procedure was previously tested by a rheological study of ethylene glycol and chlorobenzene (Telis-Romero et al, 2005;Polizelli et al, 2003).…”
Section: Density and Rheological Behaviormentioning
confidence: 99%
“…Shear rate range was 0.5 to 300 s -1 and both upward and downward tests were performed in duplicate for each temperature and soluble solids content combination. The experimental procedure was previously tested by a rheological study of ethylene glycol and chlorobenzene (Telis-Romero et al, 2005;Polizelli et al, 2003).…”
Section: Density and Rheological Behaviormentioning
confidence: 99%
“…For example, the viscosity of the molasses can change under factors such as temperature, time and mass concentration . The high viscosity also limits the flows, interfering in the design of systems such as pipes, valves, pumps, heat exchangers and evaporators . Thus, the knowledge of the factors that influence them would be of value in optimizing these operations .…”
Section: Introductionmentioning
confidence: 99%
“…The flow velocity equation (11) is valid for fully undisturbulent flow in straight horizontal tubes. Real processing system contain many other elements such as valves, tees, elbows etc., which can cause mixing of fluid during flow [21][22][23][24]. In addition, pipe vibration caused by energy inputs from pumps may contribute to mixing.…”
Section: Resultsmentioning
confidence: 99%