Data Sheet
Bulletin 71.2:627F
5
Principle Operation
The superior performance of a Type 627F regulator is
due to the amplifying effect of the pilot and the two-path
control system (Figure 2). Changes in outlet pressure
actquicklyonthemainregulatordiaphragmwhich
repositions the valve disk to provide fast response to
systemchanges.Simultaneously,thepilotamplies
system pressure changes to position the main
regulator valve disk for precise pressure control.
Inlet pressure is used for the pilot supply pressure.
Ifdownstreamowincreases,loweringtheoutlet
pressure below the regulator setpoint, pressure on the
pilot diaphragm and the lever side of the main regulator
diaphragm decreases. The pilot opens to supply the
requiredloadingpressureincrease.Theincreased
loading pressure from the pilot overcomes the main
regulator spring force, and the main regulator valve
diskmovesfartheropentosupplytherequiredow.
When downstream pressure increases due to lowered
demand, greater pressure is registered on the pilot
diaphragm and the lever side of the main regulator
diaphragm.Thepilotcloses,andtheexcessloading
pressure bleeds off to downstream, through the pilot
restriction. With the lower loading pressure, the spring
canmovethemainregulatordiskclosertotheorice.
Undernoowconditions,theexcessloadingpressure
bleeds through the pilot restriction to the downstream
system until the loading pressure and outlet pressure
equalize.Themainvalveisclosedbythespringand
the bleed stops.
Installation
The Type 627F regulators may be installed in any
position,aslongasowwillbeinthesamedirection
as that indicated by the body arrow. These regulators
should be installed so that their spring case vents are
protected from anything that might clog them.
Emerson™ provides an instruction manual with
every regulator shipped. Refer to this for complete
installation, operation, and maintenance instructions.
Included is a complete listing of individual parts and
recommended spare parts.
Overpressure Protection
Overpressurizinganyportionofaregulatororassociated
equipmentmaycausepersonalinjury,leakage,or
property damage due to bursting of pressure-containing
partsorexplosionofaccumulatedgas.
To avoid overpressure, provide appropriate pressure
relieving or pressure limiting devices to ensure that
noneofthelimitsinthespecicationssectionis
exceeded.Regulatoroperationwithinratingsdoes
notpreventthepossibilityofdamagefromexternal
sources such as debris in the pipeline. Inspect the
regulator for damage after any overpressure condition.
Refertothereliefsizingcoefcientsinthe
specicationstableandtheCapacityInformation
sectiontodeterminetherequiredexternalrelief
valve capacity.
Capacity Information
Natural gas regulating capacities at selected inlet
pressures and outlet pressure settings are given in
Tables6through8.FlowsareinSCFH(60°Fand
14.7psia)of0.6specicgravitynaturalgas.To
determinetheequivalentcapacitiesforothergases,
multiply the table capacity by the following appropriate
conversionfactor:0.775forair,0.789fornitrogen,
0.625forpropane,or0.548forbutane.Forgasesof
otherspecicgravities,multiplythegivencapacityby
0.775,anddividebythesquarerootoftheappropriate
specicgravity.
Then, if capacity is desired in normal cubic meters
per hour (Nm
3
/h)at0°Cand1.01325bar,multiply
SCFHby0.0268.
Todeterminewide-openowcapacitiesforreliefsizing
use the following formula:
where,
C
1
= C
g
/C
v
(seeSpecicationstable)
C
g
= Gassizingcoefcient(seeSpecicationstable)
G = Gasspecicgravity(air=1.0)
P
1
= Valve inlet pressure, psia
P = Pressure drop across valve, psi
Q = Gasowrate,SCFH
T = Absolutetemperatureofgasatinlet,°Rankine
To obtain the published capacities, the inlet and outlet
pipingshouldbethesameastheregulatorsize.
Q = C
g
P
1
SIN DEG
520 3417 P
GT C
1
P
1










