CB780E/CB784E RELAY MODULES WITH VALVE PROVING
750-234
47
32-00150—03
Table 16. VPS Worksheet Example.
a
Divide inches w.c. by 27.7 to get psi.
b
Divide Btuh by 1000 to get cf/hr for natural gas or by 2550 to get cf/hr for LP gas.
Calculation of Valve Train Volume:
X = V1 + V2 + (A x L ÷ 144)
X = 0.0218 + 0.0238 + (3.356 x 1.75 ÷ 144) = 0.0864.
Calculation of Valve Proving Test Time:
Test Time = 187,000 x (P x X ÷ C)
Test Time = 187,000 x (2 x 0.0864 ÷ 2500) = 12.9 sec.
Round up to 13 seconds; enter 13 seconds into the VPS
Setup.
Table 20. VPS Worksheet.
a
Divide inches w.c. by 27.7 to get psi.
b
Divide Btuh by 1000 to get cf/hr for natural gas or by 2550 to get cf/hr for LP gas.
Item
Description
Information
Lookup Table
Results
Formula Item
V1
Upstream Valve Volume
940-04544
0.0218
V1
V2
Downstream Valve Volume
940-04539
0.0238
V2
D
Pipe Size NPT (in.)
2 in. NPT
3.356
A
L
Pipe Length (ft)
1.75 ft
—
1.75
L
P
Valve Inlet Pressure (psig)
a
2
—
2
P
C
Burner Maximum Firing (cf/hr)
b
2.5 mbtu
—
2500
C
Table 17. V1 Upstream Volumes for Valves.
Models
Pipe Size NPT
(inches)
Size
On/Off
POC
940-04543
1-1/2
0.0218
940-04539 940-04544
2
0.0218
940-04540 940-04545
2-1/2
0.0227
940-04541 940-045262 3
0.0227
940-04409 940-04451
4
0.0779
Table 18. V2 Downstream Volumes for Valves.
Models
Pipe Size NPT
(inches)
Size
On/Off
POC
940-04543
1-1/2
0.0238
940-04539 940-04544
2
0.0238
940-04540 940-04545
2-1/2
0.0245
940-04541 940-045262 3
0.0245
940-04409 940-04451
4
0.0801
Table 19. Schedule 40 Pipe Internal Cross-Sectional
Area.
Pipe Size NPT
(Inches)
Cross-Sectional Area
(Sq. In.) “A”
1-1/4
1.498
1-1/2
2.036
2
3.356
2-1/2
4.788
3
7.393
4
12.730
Item
Description
Information
Lookup Table
Results
Formula Item
V1
Upstream Valve Volume
V1
V2
Downstream Valve Volume
V2
D
Pipe Size NPT (in.)
A
L
Pipe Length (ft)
—
L
P
Valve Inlet Pressure (psig)
a
—
P
C
Burner Maximum Firing (cf/hr)
b
—
C