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Bray/mccannalok hpbv – dynamic torques – Bray 40_41 User Manual

Page 13

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Bray/McCannalok HPBV – Dynamic Torques

All information herein is proprietary and confidential and may not be copied or reproduced without the expressed written consent of BRAY INTERNATIONAL, Inc.
The technical data herein is for general information only. Product suitability should be based solely upon customer’s detailed knowledge and experience with their application.

Dynamic : 13

1. Subchoked Liquid Flow, Line-size Valve.

Example Calculations:

Data:

A 24” class 150 McCannalok is to be installed in a 24”

line carrying water. It has been determined that the flow

is not choked and the following pressure drops through

the valve have been calculated:

• 75 psi with the valve 20 degrees open

• 70 psi with the valve 30 degrees open

• 35 psi with the valve 40 degrees open

• 3.5 psi with the valve 55 degrees open

• 1.1 psi with the valve 60 degrees open

• .20 psi with the valve 70 degrees open

• .05 psi with the valve 80 degrees open

• .03 psi with the valve 90 degrees open

Estimate the maximum dynamic torque in Lb-inches for the valve
considering installation with the seat retainer upstream.

Td = Ct D³

p

Substituting produces following results:

20 degrees, Td = .020 x 24³ x 75 = 20,700 Lb-inches,
(tends to close the valve)

30 degrees, Td = .027 x 24³ x 70 = 26,100 Lb-inches

40 degrees, Td = .046 x 24³ x 35 = 22,300 Lb-inches

55 degrees, Td = .078 x 24³ x 3.5 = 3,800 Lb-inches

60 degrees, Td = .086 x 24³ x 1.1 = 1,300 Lb-inches

70 degrees, Td = .100 x 24³ x .20 = 300 Lb-inches

80 degrees, Td = .032 x 24³ x .05 = 20 Lb-inches

90 degrees, Td = -.369 x 24³ x .03 = -150 Lb-inches,
(tends to open the valve)

Thus the peak dynamic torque will occur between 30 and 40 degrees open.
Verify dynamic torque at 35 degrees:

Approximate pressure drop = (70+35)/2 = 52.5 psi.

At 35 degrees: Td = .037 x 24³ x 52.5 = 27,000

Lb-inches

The peak dynamic torque of approximately 27,000

Lb-inches

occurs at about 35 degrees open.

When sizing the valve operator, total torque must be considered. The total torque when the disc is in the seat con-

sists of seating torque, stem packing torque, eccentricity torque and stem bearing torque. The total torque when

the disc is in the seat is published as seating/unseating torque (see pages 1-6. When the disc is out of the seat, total

torque consists of dynamic torque, stem packing torque, and stem bearing torque.

2. Choked Gas Flow, Reduced-size Valve.

Example Calculations:

20” (DN 500) class 300 McCannalok butterfly valve is installed in a 600 mm (24”) line flowing air and the disc is

set at 45 degrees. The flow is choked. A pressure gauge tapped into the pipe just above the upstream reducer shows

24.5 bar.

Estimate the dynamic torque in N-m, given that the seat
retainer is installed downstream.

D = 500 mm

Fk = 1.0

Ct = .114

Y = .667 for choked flow

p1 = 24.5 + 1.0 = 25.5 bar absolute, (1 atm. = 1.013

bar, i.e. about 1.0 bar)

xt at 45º = .35

Calculations:

p = p1 Fk xt Td = .0001 Ct D³ Y

p

p = 25.5 x 1.0 x .35 = 8.9 bar Td = .0001 x .114 x 500³ x .667 x 8.9 = 8,500 N-m

Thus the dynamic torque at 45º open is about 8,500 N-m, and acts to close the valve.

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