7. Lots of ways to try
Slide
Rotary
Globe
Swing
Sphere
Diaphragm
Sleeve
Vertical-lift
Operator/actuation
Seating
Action
Direction of flow
Degree of rotation
Allowable leakage
Number of ports
8. But let's try a different way
Slide
Rotary
Globe
Swing
Sphere
Diaphragm
Sleeve
Vertical-lift
Operator/actuation
Seating
Action
Direction of flow
Degree of rotation
Allowable leakage
Number of ports
20. 1: Protecting by stopping (prior to pump)
High risk of clogging
Introduces friction losses
NPSH considerations (raises TDSL)
Net energy impact: Priming protection vs. friction losses
34. 3: Protecting by stopping and throttling
Controlling or dampening pump startup
Controlling or dampening pump shutdown
Immediacy of closure on power loss
47. 5: Managing by stopping and throttling
Solids passage
Tightness of seal
Seating type
Coefficient of friction (Cv) versus clear opening
Ease of seal/seat replacement
54. 6: Energy control to protect (air)
Potential for air accumulation
Head to overcome on startup
Weight of water column if held by vacuum
Sidewall thickness of pipe
Age of pipe
58. 7: Energy control to protect (flow)
Abruptness of startup
Abruptness of shutdown
Momentum of water column
Tendency to vaporize
Pipe friction and tendency to dissipate
68. To recap
Protection by
stopping
Protection by
throttling
Protection by
energy control
Management by
energy control
Management by
throttling
Management by
stopping
69. Questions?
Thank you for coming! Brian Gongol
DJ Gongol & Associates
515-223-4144
info@djgongol.com
70. References
Most valve images are courtesy of GA Industries
All other images are original work by and copyright reserved
to Brian Gongol