Operation
Maximum operating pressure: 150 psig
1. At the beginning of the cycle, the float ball
(4.2) is at its lowest position. The vent
valve (4.4) is open and the pressure valve
(4.3) is closed.
2. The liquid to be pumped enters the pump
tank by gravity through the inlet check
valve. As the pump fills, the float ball (4.2)
rises. The outlet check valve prevents back
flow of liquid into the pump tank from the
downstream side.
3. At the high trip point the mechanism
snaps over center. The compressed coil
spring (4.5) simultaneously closes the vent
valve (4.4) and opens the pressure valve (4.3). The motive gas flows through the pressure valve
(4.3) and pushes the liquid out of the pump tank though the outlet check valve. The inlet check
valve prevents liquid from flowing back into the upstream piping.
4. As the liquid falls, the float ball (4.2) drops. At the low trip point, the mechanism snaps over
center and the compressed coil spring (4.5) simultaneously opens the vent valve (4.4) and
closes the pressure valve (4.3). The pump tank depressurizes as the motive gas is relieved
through the vent valve.
5. After the pressure in the pump tank is relieved through the
vent valve (4.4), flow resumes through the inlet check valve
and a new cycle begins.
Installation
Consult the Installation Drawings for the proper piping configuration for your application.
Please call GESTRA if you are not sure of the
proper configuration.
1. CLEARANCE: Install the pump below the
equipment to be drained. Proper clearance is
required for the pump to fill. The clearance is
the distance between the base of the pump
and the bottom of the equipment to be
drained. The FPS 14 and FPS 23 require a
minimum clearance of 36”.
2. CHECK VALVES: Install the check valves on
the pump tank, with gaskets, making sure the
check valves are installed in the same
direction. The flow direction has been stamped on each check valve and should match the flow
arrow on the front of the tank.
a. Install lower flange bolts and secure with nuts and lock washers.
b. Place the check valve between the flanges from above onto the bottom bolts. Verify the
flow arrows are pointing in the correct direction.
c. Install and center the gaskets on both sides of the check valves.
d. Install the remaining flange bolts, nuts, and lock washers. Tighten evenly in a star pattern.
NOTE: The correct bolts for the different check valves are as follows:
1” RK16A (S.S.) 1/2”-13x3-1/2” (FPS-366)
1” RK44 (Bronze) 1/2”-13x3” (FPS-193)
2” RK16A (S.S.) 5/8”-11x4-1/2” (FPS-313)
2” RK44 (Bronze) 5/8”-11x6” (FPS-034)
3” RK16A (S.S.) 5/8”-11x6” (FPS-034)
3” RK44 (Bronze) 5/8”-11x5” (FPS-071)
e. Connect piping from discharge check valve flange to the condensate return line or other
discharge point
Full Port Isolation Valves are recommended on the pump inlet and outlet to allow the pump to
be isolated for service.
Pressure Gauges are recommended upstream and downstream of the pump for accurate
measurement of actual operating conditions.
NOTE: All isolation valves must be full port in order to achieve rated pump capacity.
3. MOTIVE GAS SUPPLY: Connect the motive gas supply (steam, air, or gas) to the ½” NPT
connection “P” on the top of the cover flange. The motive gas supply line should have a
strainer and a steam trap (GESTRA MK series for steam service) or liquid drainer trap (GESTRA
UNA series for air or gas service) installed before the pump. See installation drawings for the
proper piping of the components for the motive supply.
A Pressure Gauge should be installed on the motive gas supply to verify that there is sufficient
motive gas pressure at the pump. If steam is being used, a siphon loop (pigtail) should be
installed before the pressure gauge.
A Full Port Isolation Valve should be installed on the motive gas supply line to allow the pump
to be isolated for service.
A Union or Flange should be installed between the isolation valve and the pump mechanism to
allow for easy removal of the mechanism for service. This should be installed 14” or more
above the cover flange, or in a horizontal plane outside of the O.D. of the cover flange, for easy
removal.
NOTE: Motive gas pressure should be reduced to the minimum required to both overcome
back pressure and high enough to provide necessary pump capacity.
NOTE: If the motive gas pressure exceeds 200 psig, a pressure-reducing valve (PRV) must be
installed on the motive gas supply line to reduce the pressure to the pump. The PRV should be
installed as far upstream as possible for optimum performance.
A Safety Relief Valve set at or below 200 psig, and a pressure gauge should be installed on the
motive gas supply line to protect the pump should the PRV fail. These items should be installed
downstream of the PRV, and upstream of the pump.
4. RESERVOIR / VENTED RECEIVER TANK: A reservoir or vented receiver tank is always required
ahead of the pump. This is to prevent equipment flooding while the pump is in the discharge
cycle. The actual requirement depends on the application and the type of installation. Please
consult GESTRA if a reservoir or vented receiver is not existing, or has not been specified.
5. VENT LINE: Connect the vent line to the 1” NPT vent connection “V”. This vent line should be
pipe to atmosphere, or back to the equipment to be drained. Application details will determine
how the vent must be piped.
A Tee and Ball Valve should be installed in the vent line for troubleshooting purposes (See
Installation Drawings). This is very important because it will allow troubleshooting of the vent
and pressure valves without removing the mechanism from the tank.
A full port isolation valve should be installed on the vent line to allow the pump to be isolated
for service.
A Union or Flange should be installed between the isolation valve and the pump mechanism to
allow for easy removal of the mechanism for service. This should be installed 14” or more
above the cover flange, or in a horizontal plane outside of the O.D. of the cover flange, for easy
removal.
If the vent line piping needs to be run more than 10 feet, the pipe size should be increased to
greater than 1” in order to prevent restrictions which could reduce the capacity of the pump.
If the vent line is run horizontally, the piping should be pitched so as to be self-draining to
prevent vapor lock.
NOTE: If condensate pressure from the equipment to be drained can exceed pump outlet
pressure under normal operating conditions, a steam trap must be installed after each pump.
This steam trap will prevent steam from blowing though the pump and entering the condensate
return line. Consult GESTRA for the proper steam trap sizing and selection.