APPENDIX A – MODEL 1200A PRESSURE/VACUUM RELIEF VALVE 10
APPENDIX B – MODEL 1220A PRESSURE/VACUUM RELIEF VALVE 11
APPENDIX C – MODEL 1260A PRESSURE RELIEF VALVE 12
APPENDIX D – MODEL 1300A VACUUM RELIEF VALVE 13
APPENDIX E – MODEL 1360A VACUUM RELIEF VALVE 14
APPENDIX F – MODEL 2300A PRESSURE RELIEF VALVE 15
The Groth Model 8860 Back Pressure Regulator controls upstrea m pressure in a process line such as
an anaerobic digester gas control system. The pressure setting is obtained by adjustable spring
compression and opening is caused by upstream pressure acting on a large diaphragm. A visible scale
indicates approximate set pressure. Springs are available for various standard and special set
pressure ranges.
The regulator must be maintained by a knowledgeable valve technician. It should only be assembled
under clean conditions, preferably in a shop environment. Carefully read and understand this manual
before attempting to adjust set pressure or flow capacity, or repair the regulator.
For information not contained in this manual, please contact:
The Groth Model 8860 Back Pressure regulator is a high capacity, low pressure in-line pressure relief
valve. It controls upstream pressure by discharging excess vapor downstream.
When the diaphragm force, due to upstream pressure, equals the spring compression, the regulator
begins to open. Opening is controlled to accommodate the required vapor flow. Full capacity is
achieved at 15-25% over-pressure [above set pressure]. When system pressure returns to set
pressure or below, the regulator closes.
Upstream vapor pressure, acting on a large diaphragm, forces the regul ator open at the specified set
pressure. For best performance, set pressure should be sensed at a remote location at least ten pipe
diameters upstream from the regulator. The upstream pressure acts on the lower surface of the
diaphragm. The upper side of the diaphragm must be vented to atmosphere.
Set pressure is determined by the compression of the spring; the greater the compression of the
spring, the higher line pressure required to overcome the spring force. The scale located on the
regulator is a close approximation of the set pressure. A manometer is recommended for a high
accuracy reading of the set pressure. The manometer should be plumbed upstream of the Back
Pressure Regulator, at lease ten pipe diameters.
The seat and disc are lapped flat surfaces with metal to metal contact.
III. SAFETY WARNINGS
This section is intended as an overview of safety guidelines that should be followed during the
installation, operation and maintenance of the Groth Model 8860 Back Pressure Regulator. To
understand the context of these warnings and instructions, read and understand this complete manual.
In the event of an actuator diaphragm failure, the regulator will fail in the CLOSED position.
Vapor flow will be shut off. WITHOUT PROPER PIPELINE PRESSURE SENSING, EXCESSIVE
PRESSURE CAN BE REACHED.
Regulator flow capacity is based on a fully open regulator flowing air or a vapor with SG=0.7.
Consult factory for capacity under other conditions.
DO NOT attempt to re-adjust the set pressure beyond the limits specified in Table 3.
The regulator is to be connected to the upstream line with a minimum .31" ID tubing sense line.
This line must be kept open and unobstructed to ensure that the regulator senses the actual
line pressure. Long sense lines may require a larger diameter and care must be taken DURING
INSTALLATION to assure that the line is self-draining.
DO NOT attempt to remove the regulator from the line or perform field repairs in line without
first isolating the regulator from both upstream and downstream systems.
The regulator body and actuator housing are exposed to process vapors. Observe all safety
precautions as specified on the Material Safety Data Sheet(s) for the prod uct(s) that are in the
system.
The vent on the upper actuator housing must be clean and open to the atmosphere and SHALL
be inspected periodically.
The recommended set pressure range of the regulator spring is stamped on the namep l ate.
Never adjust a spring for a set pressure beyond its design range as specified in Table 3.
Exceeding the spring upper limit may compress the spring to its solid height, and prevent the
regulator from opening. Setting it below the lower limit may prevent the regulator from closing
fully at the required pressure.
PROCESS PIPING IS TO BE CLEAN AND FREE OF WELD SLAG. WELD SLAG OR OTHER
DEBRIS COULD BLOCK THE SENSE LINE OR DAMAGE THE REGULATOR SEATING SURFACE.
DO NOT LIFT THE BACK PRESSURE REGULATOR FROM THE ADJUSTMENT SCREW. IF
LIFTED FROM THIS LOCATION, THE ADJUSTMENT SCREW MAY BE PERMANENTLY
DAMAGED.
USING AN IMPROPER PRESSURE SENSING LINE CAN RESULT IN LIMITED OR NO
FUNCTIONALITY OF THE REGULATOR. RECOMMENDED SIZE FOR THE PRESSURE SENSING
LINE IS AT LEAST .31”. THIS LINE MUST REMAIN FREE OF DEBRIS AND ANY TYPE OF
OBSTRUCTION.
IV. INSPECTION AND INSTALLATION
The regulator is packaged and supported to prevent damage or contamination during shipment. The
regulator shall also be protected during subsequent handling and storage. Always keep all ports
plugged to prevent intrusion of foreign materials. Before installation, inspect the unit visually. If there
are indications of physical damage or internal contamination, the regulator must be disassembled,
cleaned and inspected before installation. If factory set, the spring adjustment cap must be secure.
Report any shipping damage to carrier.
The regulator must be installed in a horizontal line as shown in Figure 1. Use the actuator housing or
valve body to lift and support the regulator at installation.
1. Aluminum bodies should be connected with flat-faced 150# ANSI flanges using a full-faced gasket.
Mating flanges should be flat within .020", clean, free of scratches, corrosion and tool marks.
2. Steel bodies should be connected with raised-faced 150# ANSI flanges using a full-faced or ring
gasket. Mating flanges should be flat within .020", clean, free of scratches, corrosion and tool
marks.
3. Each valve is leak tested at the factory as part of our standard inspection procedures.
4. Inspect the gasket; make sure that the material is suitable for the service. Gasket dimensions are
listed in Table 1. Full gaskets must be used with flat face flanges. Either full or ring gaskets may be
used with raised face flanges.
5. Lubricate all studs and nuts with an appropriate thread lubricant. If stainless steel fasteners are
used, use an anti-seize lubricant such as moly-disulfide.
6. Align flanges and gaskets. Make sure the flow path is not restricted by valve or gasket
misalignment.
7. Install nuts and lock washers and torque all fasteners to half the value listed in Table 2 below in a
staggered, alternating pattern.
8. Make sure that the flanges are not distorted and that the gasket is evenly compressed.
9. Make up the final torque and check that no further nut rotation occurs at the specified torque value.
Regulator flow capacity is based on a fully open regulator flowing air or a vapor with SG=0.7. Consult
factory for capacity under other conditions.
The regulator sense line is to be connected to the process line at a location at least ten feet upstream
with a minimum of .31" ID tubing. The sense port on the regulator is on the lower surface of the
actuator housing (see Figure 1). This line must be kept open and unobstructed to ensure that the
regulator "senses" the actual line pressure. Long sense lines may require a larger diam eter and care
must be taken to assure that the line is self-draining. For some applications, a nitrogen purge may be
required to ensure that this line remains open. Consult the factory for recommendations for remote
installations or vapors that may cause line obstructions.
All system piping must be free of weld slag and other debris before installing the regulator.
V. OPERATION
The regulator is set at the factory. The pressure setting can be changed while installed in the pro ce ss
piping system. The purpose of the regulator is to maintain set pressure at some point upstream in the
process, such as in the anaerobic digester tank. System pressure shall be monitored at this point.
Set pressure is set at the factory according to purchasing specifications. The range of set pressure for
standard springs are shown in Table 3. Other ranges are available with special spring s. The factory
setting and spring range are shown on the nameplate. The regulator will not function properly if the
setting is outside this range. If higher or lower settings are required, the necessary component s can be
obtained from Groth Corporation.
For in-line adjustment, a visible scale shows the approximate set pressure. From this setting, small
adjustments can be made while observing upstream system pressure. Remove the cap [1] and turn the
adjusting screw counter-clockwise to increase pressure or clockwise to decrease pressure. Replace
the cap when adjustment is complete.
Vapor flowing at line
pressure below specified
set point.
Vapor not flowing at line
pressure above specified
set point.
Gas leaking from upper
vent.
System pressure above
specified operating
range.
System pressure below
specified operating
range.
Flow indicator or vapor
discharge.
Flow indicator or vapor
discharge.
Emission indication
near the regulator.
Observe pressure
indicator during
operation.
Observe pressure
indicator during
operation.
VII. PREVENTATIVE MAINTANANCE
Periodically, while in service, examine the regulator for leakage at bolted connections, adjusting
screws, and vent. Test for process vapor emissions from vent caps.
Periodically, out of service, examine seat and pallet for a smooth surface to ensure proper seating and
sealing. Examine actuator diaphragm for cuts, or unusual wear.
VIII. RECOMMENDED SPARE PARTS
Spring; see Table 3 for correct part number
Vent part number 285320147 (1/4” NPT)
Soft Goods Kit; see Table 4 for correct part
numbers
Damaged seat/disc or setting too low.
If original pressure setting has not been disturbed, remove
regulator and repair.
Damaged diaphragm or pressure setting too high.
If original pressure setting has not been disturbed, remove
regulator and repair.
Inspect the bushings for debris or damage.
Damaged diaphragm.
Remove regulator and replace diaphragm.
Damaged diaphragm or pressure setting too high.
Vapor flow exceeds capacity of regulator.
Damaged seat/disc or setting too low.
Insufficient vapor production.
The nameplate on the Groth Model 8860 Back Pressure Regulator contains the model nu mber, serial
number, set pressure & set pressure range. The model number contains additional information about
material of construction, capacity and options. The following chart will assist in relating the model
number to the specifications of your regulator:
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Model Number Inlet/Outlet Soft
Body Goods
Material