
Bulletin 71.2:EZH and EZHSO
12
MECHANISM BOX
FIRST-STAGE
RESET PIN (WHITE)
SECOND-STAGE
RESET SHAFT
W8128
E0565
Figure 9. Slam-Shut Device in Open Position Figure 10. Slam-Shut Device in Closed Position
SETPOINT
ADJUSTMENT RING
TRAVEL STOP
See Figures 9 and 10 for the difference between the
device in open and closed positions. See Figure 11
for Type EZHOSX Installation Schematics. For more
information about the Types EZHOSX and EZHSO-OSX,
contact your local Sales Of ce.
Capacity Information
Note
EZH and EZHSO Series fl ow capacities are
laboratory veri ed; therefore, they may
be sized for 100% fl ow using published
capacities as shown. It is not necessary to
reduce published capacities.
Tables 17 through 20 show the natural gas regulating
capacities of the EZH and EZHSO Series regulators at
selected inlet pressures and outlet pressure settings.
Flows are in thousands of SCFH at 60°F and 14.7 psia
(or in thousands of Nm³/h at 0°C and 1.01325 bar) of
0.6 speci c gravity natural gas.
To determine equivalent capacities for air,
propane, butane or nitrogen, multiply the capacity
by the following appropriate conversion factor:
0.775 for air, 0.628 for propane, 0.548 for butane
or 0.789 for nitrogen. For gases of other speci c
gravities, multiply the given capacity by 0.775 and
divide by the square root of the appropriate speci c
gravity. Then, if capacity is desired in Nm³/h at 0°C and
1.01325 bar, multiply SCFH by 0.0268.
To nd approximate regulating capacities at pressure
settings not given in Tables 17 through 20 or to nd
wide-open ow capacities for relief sizing at any inlet
pressure, perform one of the following procedures. Then
convert using the factors provided above, if necessary.
Critical Pressure Drops
For critical pressure drops (absolute outlet pressure
equal to or less than one-half of absolute inlet
pressure), use the following formula:
Q = (P
1
)(C
g
)(1.29)
Non-Critical Pressure Drops
For pressure drops lower than critical (absolute outlet
pressure greater than one-half of absolute inlet pressure).
Q =
520
GT
C
g
P
1
SIN
3417
C
1
∆P
P
1
DEG
where,
Q = gas ow rate, SCFH
P
1
= absolute inlet pressure, psia (P
1
gauge + 14.7)
C
g
= regulating or wide-open gas sizing coef cient
G = gas speci c gravity of the gas
T = absolute temperature of gas at inlet, °Rankine
C
1
= ow coef cient
∆P = pressure drop across the regulator, psi
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