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G100 Series

©Emerson Process Management Regulator Technologies, Inc., 2001, 2015; All Rights Reserved

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a 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 specifications of such 

products at any time without notice.

Emerson Process Management Regulator Technologies, Inc. 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 Regulator Technologies, Inc. product remains solely with the purchaser.

For further information visit www.fisherregulators.com

LPG Equipment

Emerson Process Management

Regulator Technologies, Inc.

USA - Headquarters

McKinney, Texas 75070 USA

Tel: +1 800 558 5853

Outside U.S. +1 972 548 3574

!

WARNING

Trained personnel should test the back check 

valve in a safe location.
To ensure that the valve is still functional, 

back check closure should be checked 

annually if there is no other regularly 

scheduled test program.

Maintenance

Annually TEST back check valve for closure. Back check valves 

are non-repairable. Replace non-functioning valves.

1.  Brass valves are not suitabe for NH

3

 applications.

2.  Manually operate the back check valve’s poppet 

before installation to assure parts were not damaged in 

shipment or blocked with dirt or foreign material.

3.  Install valve so that arrow points in the direction of flow 

through the valve.

4.  Use pipe dope on the main threads of the valve or 

the pipeline. Polytetrafluoroethylene (PTFE) tape or 

PTFE pipe dope compound is recommended for the 

male threads of the larger valves such as the 2 and 

3 in. sizes.

5.  Test the valve for proper operation after installation and 

before placing the system into full service. To make the 

test, pressure the system through the back check valve 

and then quickly bleed pressure from the valve inlet 

piping. Check for pressure build-up in the inlet piping. 

On soft seated valves, there should be no build-up 

in the inlet side. On metal-to-metal seated valves, a 

slow pressure build-up is permissible. A rapid pressure 

build-up on either valve style indicates that the valve 

has malfunctioned.

SEAT CONSTRUCTION

OUTLET CONNECTION,  

IN.

INLET CONNECTION,  

IN.

PROPANE FLOW CAPACITY AT  

10 psig / 0.69 bar  

DIFFERENTIAL PRESSURE

TYPE NUMBER

Brass

Steel

Metal-to-Metal

3/4 FNPT

3/4 MNPT

21 GPM / 79.5 l/min

G100

- - - -

1-1/4 FNPT

1-1/4 MNPT

55 GPM / 208 l/min

G101

- - - -

2 FNPT

2 MNPT

150 GPM / 568 l/min

G102

G112

2 FNPT

2 FNPT

150 GPM / 568 l/min

G109

- - - -

3 FNPT

3 MNPT

250 GPM / 946 l/min

- - - -

G104

Soft Seat

2 MNPT and 1-1/4 FNPT

2 MNPT

137.5 GPM / 520 l/min

- - - -

G105

2 MNPT

3 FNPT

254 GPM / 961 l/min

- - - -

G106

3 MNPT and 2 FNPT

3 MNPT

254 GPM / 961 l/min

- - - -

G107

Specifications

This section lists the specifications for the G100 Series valve. Factory specifications are stamped on the nameplate fastened on 

the valve at the factory.

Maximum Operating Pressure: 

250 psig / 17.2 bar

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