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Bulletin 74.2:T208
4
CONTROL PRESSURE RANGE
SPRING COLOR
SPRING WIRE DIAMETER SPRING FREE LENGTH
In. w.c. mbar In. mm In. mm
2.0 to 7.0
(1)(2)
5 to 17
(1)(2)
Red 0.085 2.2 3.63 92.2
3.0 to 13.0
(1)(2)
7 to 32
(1)(2)
Unpainted 0.105 2.7 3.75 95.3
10.0 to 26.0 25 to 65 Yellow 0.114 2.9 4.31 109
0.9 to 2.5 psig 62 to 172 Green 0.156 4.0 4.06 103
1.3 to 4.5 psig 90 to 310 Light Blue 0.187 4.8 3.94 100
3.8 to 7.0 psig 0.26 to 0.48 bar Black 0.218 5.5 3.98 101
1. To achieve the published control pressure range the spring case must be installed pointing down.
2. Do not use Fluorocarbon (FKM) diaphragm with these springs at diaphragm temperatures lower than 60°F / 16°C.
Table 3. Control Pressure Ranges and Spring Information
Table 5. T208 Series C
v
Coefcient and Flow Capacity
Table 4. Flow and Sizing Coefcients
ORIFICE SIZE REGULATING WIDE-OPEN
In. mm C
g
C
v
C
1
C
g
C
v
C
1
7/16 11 94 2.7 35.0 97 2.8 35.0
Table 2. Available Construction and Trim Materials
AVAILABLE CONSTRUCTION MATERIAL AVAILABLE TRIM OPTION
Body and 
Casing
Guide Insert, 
Stem and 
Pusher Post
Diaphragm 
Head
Lever 
Assembly
Trim Option 
Code
Diaphragm Material Disk and O-ring Material
Operating Temperature 
Range
Gray cast iron,
WCC Carbon
steel or
CF8M/CF3M
Stainless steel
(1)
316 Stainless
Steel
304 Stainless
Steel
302 Stainless
Steel
Standard Nitrile (NBR) Nitrile (NBR) -40 to 180°F / -40 to 82°C
VV Fluorocarbon (FKM) Fluorocarbon (FKM) 40 to 300°F / 4 to 149°C
TV Fluorinated Ethylene Propylene (FEP) Fluorocarbon (FKM) 40 to 180°F / 4 to 82°C
TN Fluorinated Ethylene Propylene (FEP) Nitrile (NBR) -20 to 180°F / -29 to 82°C
TK Fluorinated Ethylene Propylene (FEP) Peruoroelastomer (FFKM) 0 to 180°F / -18 to 82°C
TE Fluorinated Ethylene Propylene (FEP) Ethylene Propylene Diene (EPDM) -20 to 180°F / -29 to 82°C
1. Pipe nipples and anges are 316 Stainless steel for anged body assemblies.
CONTROL PRESSURE 
RANGE AND 
SPRING COLOR
SET PRESSURE MINIMUM BUILDUP TO WIDE-OPEN VACUUM OUTLET PRESSURE
C
v
COEFFICIENT 
CAPACITIES OF AIR
In. w.c. mbar In. w.c. mbar psig barg SCFH Nm
3
/h
2.0 to 7.0 in. w.c. /
5 to 17 mbar
Red
2.0 5.0 4.02 10
0 0 3.1 192 5.1
2.5 0.17 3.5 1161 31.1
5 0.34 3.5 1488 39.9
4.0 10.0 3.62 9
0 0 2.6 226 6.1
2.5 0.17 3.5 1178 31.6
5 0.34 3.5 1500 40.2
3.0 to 13.0
in. w.c. /
7 to 32 mbar
Unpainted
10.0 25 5.99 15
0 0 2.0 268 7.2
2.5 0.17 3.5 1232 33.0
5 0.34 3.5 1539 41.2
10.0 to 26.0 in. w.c. /
25 to 65 mbar
Yellow
15 37 8.89 22.1
0 0 2.0 331 8.9
2.5 0.17 3.5 1279 34.3
5 0.34 3.5 1574 42.2
0.9 to 2.5 psig /
62 to 172 mbar
Green
1 psig 70 0.78 psig 54
0 0 2.2 499 13.4
2.5 0.17 3.6 1426 38.2
5 0.34 3.6 1687 45.2
1.3 to 4.5 psig /
90 to 310 mbar
Light Blue
2 psig 140 1.49 psig 103
0 0 2.3 752 20.2
2.5 0.17 3.8 1694 45.4
5 0.34 3.7 1904 51.0
3.8 to 7.0 psig /
0.26 to 0.48 bar
Black
5 psig 340 2.79 psig 192
0 0 2.2 1139 30.5
2.5 0.17 3.8 2286 61.3
5 0.34 3.8 2242 60.1
Installation
Install the T208 Series regulator using a straight run pipe of
the same size or larger as the regulator body. Flow through
the regulator body is indicated by the ow arrow attached
to the body. If a block valve is required, install a full ow
valve between the regulator and the blanketed vessel. To
achieve the established regulator capacities, the regulators
should be installed with the spring case barrel pointed down
(See Figure 1).
Emerson Process Management Regulator Technologies, Inc.
(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
Vapor recovery regulators are used to maintain a constant
inlet (blanket) pressure with the outlet owing to a system
whose pressure is lower than that at the inlet. The recovery
regulators are not intended to be used as an ASME certied
relief device for overpressure protection on a tank. They are to
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