Gorman-Rupp Pumps 62E31-B All serial numbers User Manual

Page 16

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OM−04020

60 SERIES PUMPS

PAGE C − 3

OPERATION

OPERATION

Leakage

No leakage should be visible at pump mating sur-
faces, or at pump connections or fittings. Keep all
line connections and fittings tight to maintain maxi-
mum pump efficiency.

Liquid Temperature And Overheating

The maximum liquid temperature for this pump is
160

_F (71_C). Do not apply it at a higher operating

temperature.

Overheating can occur if operated with the valves
in the suction or discharge lines closed. Operating
against closed valves could bring the liquid to a
boil, build pressure, and cause the pump to rup-
ture or explode. If overheating occurs, stop the
pump and allow it to cool before servicing it. Refill
the pump casing with cool liquid.

Allow an over-heated pump to com-
pletely cool before servicing. Do not re-
move plates, covers, gauges, or fittings
from an over-heated pump. Liquid with-
in the pump can reach boiling tempera-
tures, and vapor pressure within the
pump can cause parts being disen-
gaged to be ejected with great force. Af-
ter the pump cools, drain the liquid from
the pump by removing the casing drain
plug. Use caution when removing the
plug to prevent injury to personnel from
hot liquid.

Strainer Check

A suction strainer was not furnished with this pump
but an 80 mesh screen may have been installed by
the user. Check the screen regularly, and clean it
as necessary. The screen should also be checked
if pump flow rate begins to drop. If a vacuum suc-

tion gauge has been installed, monitor and record
the readings regularly to detect screen blockage.

Pump Vacuum Check

NOTE

Petroleum products are very sensitive to changes
in temperature. Warmer temperatures elevate the
product vapor pressure resulting in low vacuum
readings. Do not mistake temperature problems for
faulty pump installation or performance.

With the pump inoperative, install a vacuum gauge
in the system, using pipe dope on the threads.
Block the suction line and start the pump. At oper-
ating speed the pump should pull a vacuum of 15
to 17 inches (381 to 432 mm) or more of mercury
for petroleum or 20 inches (508 mm) of mercury in
other service. If it does not, check for air leaks in the
seal, gasket, or discharge valve.

Open the suction line, and read the vacuum gauge
with the pump primed and at operation speed.
Shut off the pump. The vacuum gauge reading will
immediately drop proportionate to static suction
lift, and should then stabilize. If the vacuum reading
falls off rapidly after stabilization, an air leak exists.
Before checking for the source of the leak, check
the point of installation of the vacuum gauge.

STOPPING

Never halt the flow of liquid suddenly. If the liquid
being pumped is stopped abruptly, damaging
shock waves can be transmitted to the pump and
piping system. Close all connecting valves slowly.

If the application involves a high discharge
head, gradually close the discharge
throttling valve before stopping the pump.

After stopping the pump, shut off the incoming
power and lock it out, or take other action to ensure
that the pump will remain inoperative.

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