Eng-Tips is the largest engineering community on the Internet

Intelligent Work Forums for Engineering Professionals

Register Log in
  • Congratulations waross on being selected by the Tek-Tips community for having the most helpful posts in the forums last week. Way to Go!

Derating of centrifugal slurry pumps

Status
Not open for further replies.
catt

catt

Mechanical
Mar 6, 2003
5
0
0
AU
55% (by mass) slurry with solids sg of 3 and fluid sg of 1.2 (overall density of 1800 kg/m3). In determining the ER and HR using the Warman catalogue, can the value of S (solids sg) be reduced by 3/1.2 to reduce the effect of ER / HR?
 
Status
Not open for further replies.

Similar threads

deepu78
  • Locked
  • Question
Derating of process piping designed to ASME B31.3 2
Replies
6
Views
21
georgeverghese
georgeverghese
samski
  • Locked
  • Question
Hydrophore filling pumps running of curve 1
2
Replies
21
Views
67
LittleInch
LittleInch
BillKapri
  • Locked
  • Question
Flexible Pipes for Centrifugal Pump Vibration 3
Replies
10
Views
50
LittleInch
LittleInch
edison123
  • Locked
  • Question
Centrifugal blower input power vs speed
Replies
5
Views
27
LittleInch
LittleInch
Jharvey2525
  • Locked
  • Question
Seeking Advice on Discharge Pump Flange Loads and Pressure Thrust in Slurry Pump System
2
Replies
33
Views
113
GBTorpenhow
GBTorpenhow
Back
Top