
Bulletin 71.4:EZH
3
Principle of Operation
A pressure relief valve is a throttling pressure control device
that opens and closes to ensure the downstream pressure
does not rise above a predetermined pressure. Fisher
®
relief valves cannot be used as ASME safety relief valves.
A backpressure regulator is a device that controls and
responds to changes in the upstream pressure. It functions
the same as a relief valve in that it opens on increasing
upstream pressure.
Relief Valve
As long as the inlet pressure is below the set pressure, the
pilot control spring keeps the pilot valve plug closed. Inlet
pressure passes through the restrictor and registers as
loading pressure on the main valve diaphragm chamber.
Force from the main spring, in addition to pilot loading
pressure, provide loading pressure to keep the main valve
diaphragm and plug assembly tightly shut off. When the
inlet pressure rises above the set pressure, the pressure
on the pilot diaphragm overcomes the pilot control spring
and opens the pilot valve plug. The pilot then exhausts the
loading pressure from the main valve diaphragm chamber.
The pilot continuously exhausts gas when the inlet pressure
is above the set pressure. The inlet pressure unbalance
overcomes the main spring force and opens the diaphragm
and plug assembly.
As the inlet pressure drops below the set pressure, the pilot
control spring closes the pilot valve plug and the exhaust
to atmosphere stops. Force from the main spring, along
with pilot loading pressure, pushes the diaphragm and plug
assembly onto the knife-edged seat, producing tight shutoff.
Backpressure Regulator
As long as inlet pressure remains below setpoint, the
pilot control spring keeps the pilot valve plug closed. Inlet
pressure passes through the upper port around the upper
portion of the valve plug and then through the hollow
passage in that valve plug. Force from the main spring,
in addition to pilot loading pressure, provide downward
loading pressure to keep the main valve diaphragm and plug
assembly tightly shut off. When inlet pressure rises above
the set pressure, pressure on the pilot diaphragm overcomes
the control spring to close the upper port and stroke the
valve plug to open the lower port. The pilot exhausts loading
pressure from the main valve diaphragm chamber. Inlet
pressure unbalance overcomes the main spring force to
open the diaphragm and plug assembly.
While the main valve is throttling, the upper port of the pilot
stays closed. The pilot exhausts only when it repositions the
main valve. As inlet pressure drops below setpoint, the pilot
control spring overcomes the diaphragm force to stroke the
valve plug down to close the lower port and open the upper
port. Force from the main spring, along with the pilot loading
pressure, pushes the diaphragm and plug assembly onto the
knife-edged seat, producing tight shutoff.
Capacity Information
Note
EZH Series ow capacities are laboratory
veried; therefore, it may be sized for 100%
ow using published capacities as shown. It is
not necessary to reduce published capacities.
Table 7 show the natural gas regulating capacities of the
Type EZH relief or backpressure regulator 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 specic 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 specic
gravities, multiply the given capacity by 0.775 and divide by
the square root of the appropriate specic 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 Table 7 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 coefcient
G = gas specic gravity of the gas
T = absolute temperature of gas at inlet, °Rankine
C
1
= ow coefcient
P = pressure drop across the regulator, psi
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