Emerson Y695A Data Sheet

Bulletin 74.2:Y695A

Y695A Series Vapor Recovery Regulators

January 2010

W7381

Figure 1. Y695A Series Vapor Recovery Regulators

Features

•  Precision Control—Large diaphragm area
provides very accurate throttling control at low
pressure settings.

• Easy Conversion—Changes easily from the
Type Y695A to the Type Y695AM with two O-rings
and a machine screw.

•  Rugged Construction—Heavy duty casings and
internal parts are designed to reduce vibration and
shock and give this regulator the ability to
withstand 150 psig (10,3 bar) inlet pressure with
no internal parts damage.

•  Simplicity—Direct-operated, straightforward stem
and lever design minimizes the number of parts
while providing excellent regulation of pressure.

Introduction

The Y695A Series are direct-operated vapor recovery
regulators. These regulators are used to sense an
increase in vessel pressure and vent excessive internal
tank pressure to an appropriate vapor recovery disposal
or reclamation system. They may also be used as
backpressure regulators or relief valves.

www.sherregulators.com

D102595X012

Bulletin 74.2:Y695A

Specications

Available Congurations

Type Y695A: Direct-operated vapor

recovery regulator.

Type Y695AM: Direct-operated vapor recovery
regulator equipped with a blocked throat and O-ring
stem seal. The lower diaphragm casing is tapped
1/2 NPT for control line connection.

Body Sizes

NPS 3/4 or 1 (DN 20 or 25)

End Connection Styles

See Table 1

Maximum Allowable Inlet (Casing) Pressure

(1)

150 psig (10,3 bar)

Maximum Outlet Pressure

(1)

150 psig (10,3 bar)

Maximum Emergency Inlet Pressure to Avoid
Internal Parts Damage

150 psig (10,3 bar)

Control Pressure Ranges

(1)

See Table 2

Flow Coefcients with Fully Open Disk

Cg: 120, CV: 3.43, C1: 35

Flow Capacities

See Table 4

Orice Size

7/16-inch (11 mm)

Construction Materials

See Table 3

Material Temperature Capabilities

Nitrile:

-20° to 180°F (-29° to 82°C)
Fluorocarbon (FKM):
40° to 300°F (4° to 149°C)
Peruoroelastomer (FFKM):

-20° to 300°F (-29° to 149°C)
Ethylenepropylene (EPDM):

-20° to 300°F (-29° to 149°C)

Pressure Setting Adjustment

Adjusting Screw

Spring Case Vent Connection

1/4 NPT

Diaphragm Case Connection

1/2 NPT

Approximate Weight

19 pounds (9 kg)

(1)

1. The pressure/temperature limits in this bulletin and any applicable standard or code limitation should not be exceeded.

Table 1. End Connection Styles

BODY SIZES,

NPS (DN)

3/4 or 1 (20 or 25) NPT

  1.  All anges have 14-inches (356 mm) face-to-face.

Ductile Iron

END CONNECTION STYLES

CF8M

Stainless Steel

NPT, ANSI Class 150 RF,

ANSI Class 300 RF, or PN 16/25/40

(1)

Table 2. Control Pressure Ranges

RELIEF SET PRESSURE RANGE

2 to 7-inches w.c.

3 to 13-inches w.c.

10 to 26-inches w.c.

0.9 to 2.5 psig

1.3 to 4.5 psig

3.8 to 7 psig

1. Spring ranges based on spring case installed pointed down. When installed pointing up, the spring ranges increase by 2-inches w.c. (5 mbar).

2. Do not use Fluorocarbon (FKM) diaphragm with these springs at diaphragm temperatures lower than 60°F (16°C).

(5 to 17 mbar)
(7 to 32 mbar)
(25 to 65 mbar)

(0,06 to 0,17 bar)
(0,09 to 0,31 bar)
(0,26 to 0,48 bar)

(1)(2)

(1)(2)

SPRING PART

NUMBER

1B653827052
1B653927022
1B537027052

1B537127022
1B537227022
1B537327052

SPRING COLOR SPRING WIRE DIAMETER FREE LENGTH

Red

Olive drab

Yellow

Light green

Light blue

Black

0.085-inch

0.105-inch

0.114-inch

0.156-inch

0.187-inch

0.218-inch

(2,2 mm)
(2,7 mm)
(2,9 mm)

(4,0 mm)
(4,8 mm)
(5,5 mm)

Hastelloy® C

ANSI Class 150 RF

3.625-inches

3.75-inches

4.188-inches

4.060-inches

3.938-inches

3.980-inches

(92,1 mm)
(95,2 mm)
(106 mm)

(103 mm)
(100 mm)
(101 mm)

2

Bulletin 74.2:Y695A

Type Y695A

Type Y695A

MXXXX

January 2010

Type Y695A

INLET PRESSURE
OUTLET PRESSURE
ATMOSPHERIC PRESSURE

Table 3. Construction Materials

BODY SPRING CASE DIAPHRAGM CASE DISK HOLDER DIAPHRAGM DISK

Ductile iron,

CF8M Stainless steel,

or Hastelloy C

Ductile iron or

CF8M Stainless

steel

Table 4. Y695A Series Capacities

SPRING RANGE,

PART NUMBER, AND COLOR

2 to 7-inches w.c. (5 to 17 mbar)

1B653827052

Red

3 to 13-inches w.c. (7 to 32 mbar)

10 to 26-inches w.c. (25 to 65 mbar)

1B653927022

Olive drab

1B537027052

Yellow

0.9 to 2.5 psig (0,06 to 0,17 bar)
1B537127022

Light green

1.3 to 4.5 psig (0,09 to 0,31 bar)
1B537227022

Light blue

3.8 to 7 psig (0,26 to 0,48 bar)
1B537327052

Black

Ductile iron,

CF8M Stainless steel, or

Hastelloy C

SET PRESSURE

2-inches w.c.

(5 mbar)

4-inches w.c.

(10 mbar)

10-inches w.c.

(25 mbar)

15-inches w.c.

(37 mbar)

1 psig

(0,07 bar)

2 psig

(0,14 bar)

5 psig

(0,34 bar)

316 Stainless steel

or Hastelloy C

MINIMUM BUILDUP TO

WIDE-OPEN

1.5-inches w.c.
(3,7 mbar)

1.5-inches w.c.
(3,7 mbar)

2.3-inches w.c.
(5,7 mbar)

3.4-inches w.c.
(8,5 mbar)

0.40 psig

(0,03 bar)

0.88 psig

(0,06 bar)

1.66 psig

(0,11 bar)

VACUUM OUTLET

Nitrile (NBR),

Fluorocarbon (FKM), or

Nitrile (NBR) with bonded

Teon (PTFE)

PRESSURE

0 psig

(0 bar)

2.5 psig

(0,17 bar)

5 psig

(0,34 bar)

0 psig

(0 bar)

2.5 psig

(0,17 bar)

5 psig

(0,34 bar)

0 psig

(0 bar)

2.5 psig

(0,17 bar)

5 psig

(0,34 bar)

0 psig

(0 bar)

2.5 psig

(0,17 bar)

5 psig

(0,34 bar)

0 psig

(0 bar)

2.5 psig

(0,17 bar)

5 psig

(0,34 bar)

0 psig

(0 bar)

2.5 psig

(0,17 bar)

5 psig

(0,34 bar)

0 psig

(0 bar)

2.5 psig

(0,17 bar)

5 psig

(0,34 bar)

SPECIFIC GRAVITY NITROGEN

Nitrile (NBR),

Fluorocarbon (FKM),

Peruoroelastomer (FFKM), 

Teon (PTFE), or 

Ethylenepropylene (EPDM)

CAPACITIES IN

SCFH (Nm3/h) OF 0.97

280

(7,50)

1180

(31,6)

1520

(40,7)

350

(9,38)

1200

(32,2)

1530

(41,0)

520

(13,9)

1250

(33,5)

1570

(42,1)

640

(17,2)

1300

(34,8)

1600

(42,9)

940

(25,2)

1450

(38,9)

1720

(46,1)

1360

(36,4)

1730

(46,4)

1940

(52,0)

2110

(56,5)

2330

(62,4)

2470

(66,2)

INLET PRESSURE
OUTLET PRESSURE
ATMOSPHERIC PRESSURE

B2648

Figure 2. Y695A Series Operational Schematic

3

Bulletin 74.2:Y695A

Table 5. Materials Compatibility

Material

CORROSION INFORMATION

Material

Fluid

Cast or

Ductile Iron

Carbon Steel

Acetic Acid (Air Free)
Acetic Acid Vapors
Acetone
Acetylene
Alcohols

Aluminum Sulfate
Ammonia
Ammonium Chloride
Ammonium Nitrate
Ammonium Sulfate

  Ammonium Sulte

Beer
Benzene (Benzol)
Benzoic Acid
Boric Acid

Butane
Calcium Chloride (Alkaline)
Carbon Dioxide (Dry)
Carbon Dioxide (Wet)

  Carbon Disulde

Carbon Tetrachloride
Carbonic Acid
Chlorine Gas (Dry)
Chlorine Gas (Wet)
Chlorine (Liquid)

Chromic Acid
Citric Acid
Coke Oven Gas
Copper Sulfate

  Ether

Ethyl Chloride
  Ethylene
  Ethylene Glycol

Formaldehyde
Formic Acid

Freon (Wet)
Freon (Dry)

  Gasoline (Rened)

Glucose
Hydrochloric Acid (Aerated)

1. Monel is a trademark of International Nickel Co.

2. Hastelloy is a trademark of Stelite Div., Cabot Corp.

I.L.

I.L.

C

C

C

C

A

A

A

A

A

A

C

C

A

A

C

C

A

C

C

C

C

C

B

B

A

A

C

C

C

C

A

A

B

B

A

A

C

C

A

A

B

B

C

C

A

A

C

C

C

C

C

C
C

A

A

C

C

B

B

C

C

A

A

A

A

B

B
C

B

B

B

B

A

A

A

A

C

C

S41600

Stainless Steel

Stainless Steel

CF8M or S31600

S30200 or S30400

B

B
A
A
A
A

A
A
B
A
B

A
A
A
A
A

A

C

A
A
A

B
B
B

C
C

C

B
A
B
A

A
A
A
A
B

B
A
A
A

C

C

A

C

A

A

A

A

A

A

A

C

A

A

B

C

A

C

A

C

A

B

A

B

A

A

A

A

A

B

A

A

B

C

A

A

A

A

A

B

B

C

B

A

B

C

C

C

C

C

B

C

A

B

A

A

B

A

A

A

A

B

A

A

A

A

A

A

B

C

A

I.L.

A

I.L.

A

A

A

A

C

C

(2)

C

(1)

®

®

Monel

Stainless Steel

Hastelloy

B

A

A

A

A

A

A

A

A

A

B

A

A

A

B

A

C

A

A

A

C

A

A

A

A

A

A

A

A

A

A

A

A

A

A

A

A

A

B

A

A

A

A

A

A

A

C

B

C

A

A

A

B

A

B

A

C

A

A

A

A

A

A

A

A

I.L.

A

A

A

A

A

A

A

A

A

A

A

A

C

B

Fluid

Cast or

Carbon Steel

Hydrochloric Acid (Air free)
Hydrogen
Hydrogen Peroxide

  Hydrogen Sulde (Liquid)

Magnesium Hydroxide

Methanol

  Methyl Ethyl Ketone

Natural Gas
Nitric Acid

  Petroleum Oils (Rened)

Phosphoric Acid (Air Free)
Phosphoric Acid Vapors
Potassium Chloride
Potassium Hydroxide
Propane

Silver Nitrate
Sodium Acetate
Sodium Carbonate
Sodium Chloride
Sodium Chromate

Sodium Hydroxide
Stearic Acid
Sulfur
Sulfur Dioxide (Dry)
Sulfur Trioxide (Dry)

Sulfuric Acid (Aerated)
Sulfuric Acid (Air Free)
Sulfurous Acid
Trichloroethylene
Water (Boiler Feed)

Water (Distilled)
Water (Sea)
Zinc Chloride
Zinc Sulfate

- - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - -

A+--Best possible selection
A--Recommended
B--Minor to moderate effect. Proceed with caution.
C--Unsatisfactory
I.L.--Information lacking

I.L.

C

C

A

A
A

C

C

A

A

A

A

A

A

A

A

C

C

A

A

C

C

C

C

B

B

B

B

A

A

C

C

A

A

A

A

C

C

A

A

A

A

A

C

A

A

A

A

A

A

C

C

C

C

C

C

B

B

B

C

A

A

B

B

C

C

C

C

Ductile Iron

Stainless Steel

CF8M or S31600

S30200 or S30400

C

C

A

A

A

A

A

A

A

A

A

A

A

A

A

A

A

B

A

A

A

A

B

A

A

A

A

B

A

A

A

A

B

A

A

A

B

B

A

A

A

A

A

A

A

A

A

A

A

A

C

C

C

C

B

B

B

A

A

A

A

A

B

B

C

C

A

A

®(1)

S41600

Monel

Stainless Steel

Stainless Steel

C

C

A

A

B

A

C

C

A

A

A

A

A

A

A

A

C

C

A

A

C

B

C

C

C

B

B

A

A

A

B

C

A

A

B

A

B

A

A

A

B

A

B

B

A

A

B

A

B

A

C

C

C

B

C

C

B

A

B

A

B

A

C

A

C

C

B

A

(2)

C

®

Hastelloy

B
A
B
A
A

A
A
A
B
A

A

I.L.

A
A
A

A
A
A
A
A

A
A
A
A
A

A
A
A
A
A

A
A
A
A

- continued -

Principle of Operation

Y695A Series vapor recovery regulators are used to
maintain a constant blanket (inlet) pressure or vessel

pressure with the outlet owing to a system whose 

pressure is lower than the inlet (see Figure 2).

4

When vessel pressure increases above the setpoint
of the regulator due to pumping in or thermal heating,
the force of the control spring is overcome by pressure
acting on the diaphragm. This moves the disk away

from the orice, allowing gas to ow from the vessel 

to the vapor recovery system. As vessel pressure is

Table 5. Materials Compatibility (continued)

Fluid

Acetic Acid (30%)
Acetone

  Alcohol (Ethyl)

Alcohol (Methyl)
Ammonia (Anhydrous)

Ammonia (Gas, Hot)
Benzene
Brine (Calcium Chloride)
Butadiene Gas
Butane (Gas)
Butane (Liquid)

Carbon Tetrachloride
Chlorine (Dry)
Chlorine (Wet)
Coke Oven Gas

  Ethyl Acetate

  Ethylene Glycol

Freon 11
Freon 12
Freon 22
Freon 114

Gasoline
Hydrogen Gas

Hydrogen Sulde (Dry)
  Hydrogen Sulde (Wet)

Jet Fuel (JP-4)

Natural Gas
Natural Gas + H2S (Sour Gas)
Nitric Acid (20%)
Nitric Acid (50 to 100%)
Nitrogen

Oil (Fuel)
Propane
Sulfur Dioxide
Sulfuric Acid (to 50%)
Sulfuric Acid (50 to 100%)

Water (Ambient)
Water [at 200°F (93°C)]
Water (Sea)

A+--Best possible selection
A--Recommended
B--Minor to moderate effect. Proceed with caution.
C--Unsatisfactory
I.L.--Information lacking

Neoprene

(CR)

C
B
A

A+

A

B
C
A
B
A
B

C
C
C
C
C

A

B
A+
A+

A

B

A

A

B

C

A

A

B

C

A

B

A

B

A

B

C

A

C

FLUID INFORMATION

Nitrile
(NBR)

B
C
A
A
C

C
C
A
C

A+

A

C
C
C
B
C

A
A
A
C
A

A+

A
C
C
A

A+

B
C
C
A

A+

A
A
C
C

C
A
B

Material

Fluorocarbon

(FKM)

B
C
B
C
C

C
A
B
B
A
A

A
A
A

A+

C

A

A+

B
C
B

A
A
C
C
A

A
C
A
A
A

A
A
A
A
A

A
A
B

Bulletin 74.2:Y695A

Peruoroelastomer

(FFKM)

A
A
A
A
A

A
A
A
A
A
A

A
A
A
A
A

A
A
A
A
A

A
A
A
A
A

A
A
A
A
A

A
A
A
A
A

A
A
A

Ethylenepropylene

(EPDM)

A
A
A
A
A

B
C
A
C
C
C

C
C
C
C
B

A
C
B
A
A

C
A
A
A

I.L.

C
C
C
C
A

C
C
A
A
B

B
A
A

reduced, the force of the back disk spring causes the

disk to move toward the orice, decreasing the ow of 

gas out of the vessel. As vessel pressure drops below
the setpoint of the regulator, the disk will seat against

the orice, shutting off the ow of gas.

Sizing Vapor Recovery Systems

To determine the capacity required, you must consider
the amount of blanketing gas that must be displaced

from the tank when either lling the vessel with liquid 

(pump-in) or the expansion of tank vapors during
atmospheric thermal heating.

Using the established procedures from American
Petroleum Institute Standard 2000 (API 2000),

determine the required ow rate for outbreathing.

For liquids with a ash point below 100°F (38°C) or a 

normal boiling point below 300°F (149°C), multiply the
calculated outbreathing requirements in Table 6 by 2.0
as indicated in footnote 1 from Table 6.

5

Bulletin 74.2:Y695A

Table 6. Flow Rate Conversions (Gas ow required to displace
blanketing gas with pump-in of liquid.)

MULTIPLY MAXIMUM

PUMP RATE IN

U.S. GPM
U.S. GPH

Barrels/hour

Barrels/day

1.  For liquids with a ash point below 100°F (38°C) or normal boiling point below 300°F 
(149°C), multiply the above calculated outbreathing requirement by 2.0.

2. To convert to Nm³/h multiply SCFH by 0.0268.

BY TO OBTAIN

8.021

0.1337

5.615

0.2340

SCFH air

required

(1)(2)

  1.  Determine the ow rate of blanketing gas displaced 

when liquid is being pumped in (see Table 6).

  2.  Determine the gas ow rate due to “outbreathing” 

caused by atmospheric thermal heating (see
Table 7).

3. Add the requirements of steps 1 and 2 and select
a vapor recovery regulator size based on total
capacity required from Table 4.

Sample sizing problem for vapor
recovery applications:

Vessel capacity . . . . . . 1000 barrels (42,000 gal)(159 000 liters)

Pump in capacity . . . . . . . . . . . . . . . . . 20 GPM (75,7 l/min)

Inlet pressure source . . . . . . . . 60 psig (4,14 bar) nitrogen

Desired blanket setpoint . . . . . . . . 0.5-inches w.c. (1 mbar)

Desired vapor recovery setpoint . . . 2-inches w.c. (5 mbar)
Vapor recovery vacuum source . . . 5-inches Hg (169 mbar)

Fluid . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . Hexane

Boiling point . . . . . . . . . . . . . . . . . . . . . . . . . . 155°F (68°C)

  1.  From Table 6 the desired air ow rate due to pump 

in equals 20 GPM (75,7 l/min) x 8.021 x 2 = 321
SCFH (8,60 Nm3/h) air.

Table 7. Gas Flow Required for Thermal Heating (Outbreathing)
per API 2000 (Interpolate for intermediate sizes.)

VESSEL CAPACITY

Barrels Gallons Liters

60
100
500

1000
2000

3000
4000

5000
10,000
15,000

20,000
25,000
30,000
35,000
40,000

45,000
50,000
60,000
70,000
80,000

90,000

100,000
120,000
140,000
160,000

180,000 7,560,000 28 616 000 54,000 (1447) 90,000 (2412)

2500

4200
21,000
42,000
84,000

126,000
168,000
210,000
420,000
630,000

840,000
1,050,000
1,260,000
1,470,000
1,680,000

1,890,000
2,100,000
2,520,000
2,940,000
3,360,000

3,780,000
4,200,000
5,040,000
5,880,000
6,720,000

9500
15 000
79 500

159 000
318 000

477 000
636 000

795 000
1 590 000
2 385 000

3 180 000
3 975 000
4 769 000
5 564 000
6 359 000

7 154 000
7 949 000
9 539 000

11 129 000
12 718 000

14 308 000
15 898 000
19 078 000
22 257 000
25 437 000

SCFH (Nm³/h) AIR FLOW

RATE REQUIRED

Flash point is equal

to or above 100°F

(38°C) or normal

boiling point is

equal to or above

300°F (149°C)

40 (1,07)

60 (1,61)
300 (8,04)
600 (16,1)

1200 (32,2)

1800 (48,2)
2400 (64,3)
3000 (80,4)

6000 (161)
9000 (241)

12,000 (322)
15,000 (402)
17,000 (456)
19,000 (509)
21,000 (563)

23,000 (616)
24,000 (643)
27,000 (724)
29,000 (777)
31,000 (831)

34,000 (911)

36,000 (965)
41,000 (1099)
45,000 (1206)
50,000 (1340)

Flash point is

below 100°F

(38°C) or

normal boiling

point is below

300°F (149°C)

60 (1,61)
100 (2,68)
500 (13,4)

1000 (26,8)
2000 (53,6)

3000 (80,4)

4000 (107)

5000 (134)
10,000 (268)
15,000 (402)

20,000 (536)
24,000 (643)
28,000 (750)
31,000 (831)

34,000 (911)

37,000 (992)

40,000 (1072)

44,000 (1179)
48,000 (1286)
52,000 (1394)

56,000 (1501)
60,000 (1608)
68,000 (1822)
75,000 (2010)
82,000 (2198)

given capacity of nitrogen by 0.985, and divide by the

square root of the appropriate specic gravity of the 

gas required. To determine regulating capacities at
pressure settings not given or to determine wide-open

ow capacities, use the following formula:

  2.  From Table 7 the desired air ow rate = 1000 SCFH

(26,8 Nm3/h) air due to thermal heating.

3.  Total required ow rate = 1000 SCFH (26,8 Nm3/h)
air + 320 SCFH (8,58 Nm3/h) = 1320 SCFH
(35,4 Nm3/h) air. This converts to nitrogen
requirements of 1340 SCFH (35,9 Nm3/h).

Capacity Information

Table 4 gives typical nitrogen regulating capacities at
selected inlet pressures and outlet pressure settings.
Flows are in SCFH at 60°F and 14.7 psia and Nm³/h at

0°C and 1,01325 bar of 0.97 specic gravity nitrogen. 
For gases of other specic gravities, multiply the

6

520

Q = CgP1SIN

GT

3417

C

∆P

Deg.

P

1

1

Where:

Cg   = gas sizing coefcient from Specications
C1 = Cg/CV or 35 from Specications

  G   = gas specic gravity (air = 1.0)

P

= inlet pressure, psia (add 14.7 psi to gauge inlet

1abs

pressure to obtain absolute inlet pressure)
  Q   = ow rate, SCFH
T = absolute temperature in °Rankine of gas at inlet
(°Rankine = °F + 460)

  ∆P   = Pressure differential across the valve, 

psig (P1 - P2)

Installation

Bulletin 74.2:Y695A

Install the regulator using a straight run of pipe the
same size or larger as the regulator body. Flow

through the regulator body is indicated by the ow 

arrow on the body. If a block valve is required, install a

B

14

(356)

B2441

INCHES

(mm)

A

5.56

(141)

full ow valve between the regulator and the blanketed 

vessel. For proper operation at low setpoint ranges,
the regulators should be installed with the spring case
pointed down.

G F

D

8.38

(213)

DIAMETER

DIMENSIONS, INCHES (mm)

BODY SIZE,

NPS (DN)

3/4,1 (20, 25) 4.0 (102) 4.12 (105) 2.12 (54) 2.25 (57) 6.19 (157) 6.19 (157) 10.38 (264) 10.38 (264) 1.69 (43) 1.69 (43)

A B D F G

Iron

Stainless

Steel or

Hastelloy® C

Ductile

Iron

Stainless

Steel or

Hastelloy® C

Ductile

Iron

Stainless

Steel or

Hastelloy® C

Ductile

Iron

Stainless

Steel or

Hastelloy® C

Ductile

Iron

Stainless

Steel or

Hastelloy® C

Figure 3. Dimensions

7

Bulletin 74.2:Y695A

Ordering information

When ordering, specify:

Application

  1.  Type of gas being controlled (natural gas, air, etc.); 

list any factors such as impurities in the gas that
may affect compatibility of gas with the regulator
trim parts.

  2.  Specic gravity of the gas.

3. Temperature of the gas.

  4.  Range of owing inlet pressures to regulator.

5. Flow rates

a)  Minimum controlled ow
    b)  Normal ow
    c)  Maximum ow

6. Line size and end connection size of adjacent piping.

Regulator

Refer to the Specications table on page 2.  Carefully 
review the description of each specication and make

the desired selection wherever there is a choice.
Always specify the type number.

Industrial Regulators

Emerson Process Management
Regulator Technologies, Inc.

USA - Headquarters
McKinney, Texas 75069-1872 USA
Tel: [phone]
Outside U.S. 1-972-548-3574

Asia-Pacic

Shanghai, China 201206
Tel: [phone]

Europe

Bologna, Italy 40013
Tel: [phone]

Middle East and Africa
Dubai, United Arab Emirates

Tel: [phone]

For further information visit www.sherregulators.com

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business of Emerson Process Management.

The contents of this publication are presented for informational purposes only, and while every effort has been made to ensure their accuracy, they are not to be construed as warranties or
guarantees, express or implied, regarding the products or services described herein or their use or applicability. We reserve the right to modify or improve the designs or specications of such
products at any time without notice.

Emerson Process Management does not assume responsibility for the selection, use or maintenance of any product. Responsibility for proper selection, use and maintenance of any Emerson 

Process Management product remains solely with the purchaser.

Natural Gas Technologies

Emerson Process Management
Regulator Technologies, Inc.

USA - Headquarters
McKinney, Texas 75069-1872 USA
Tel: [phone]
Outside U.S. 1-972-548-3574

Asia-Pacic

Singapore, Singapore 128461
Tel: [phone]

Europe

Bologna, Italy 40013
Tel: [phone]
Gallardon, France 28320
Tel: [phone]

TESCOM

Emerson Process Management
Tescom Corporation

USA - Headquarters

Elk River, Minnesota 55330-2445 USA

Tel: [phone]

Europe

Selmsdorf, Germany 23923
Tel: [phone]

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