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3

PENBERTHY 

MODELS GL AND GH GAS OPERATED JET PUMPS

INSTALLATION, OPERATION AND MAINTENANCE INSTRUCTIONS

4 INSTALLATION

Note:

 The user should refer to the relevant 

technical data sheet or product proposal to 
obtain dimensional information for the specific 
size and model of jet pump.

Check the exploded view (Figure 3) for the 
location of operating, suction and discharge 
connections to insure correct hook up.

4.1 Effect of related piping and precautions

1.  Penberthy models GL and GH gas operated 

jet pumps may be installed and operated in 
any position.

2.  Jet pumps should be installed with pipe and 

fittings which provide minimum resistance 
to fluid flow. Pipe line friction losses must 
always be a consideration when estimating 
jet pump performance.

3.  It is recommended that provisions be made 

for pressure gauge connections near the 
inlet, suction and discharge connections 
of the jet pump. If operating difficulties are 
encountered at any time, it may become 
necessary to install pressure gauges to 
identify the problem.

4.  Steam must not have over 20°F (-7°C) of 

superheat, or performance will differ from 
that published in the relevant technical data 
sheet or product proposal referred to above.

5.  When pumping liquids, suction piping 

should be sized so that the velocity of the 
liquid does not exceed 4 feet per second. 
This is almost always obtained automatically 
when the suction line is the same pipe size 
as the suction connection.

6.  Install a valve in the suction line if it is 

desirable to:

  a.  Prevent contamination of suction fluid by 

the motive fluid at start up.

  b.  Prime a centrifugal pump.
  c.  Throttle suction flow.
7.  When a gas operated jet pump is used to lift 

liquids by suction or vacuum, the jet pump 
should be located as close to the level of 
the liquid as practical. However, any liquid 
entrained into the jet pump, 

other than water 

when using steam as the operating medium

may cause the jet pump to stop pumping, 
resulting in a possible suction flow reversal.

8.  Discharge piping should be sized as short as 

possible and with the least number of turns 
and restrictions. Discharge piping friction 
losses must always be considered when 
estimating jet pump performance. Increase 
discharge line pipe size if necessary to 
minimize loss.

9.  Do not impose system piping loads on a 

jet pump. The unit is NOT designed to be a 
load-bearing fitting.

10. All piping should be clean and free of foreign 

materials which could clog the jet pump.

FIGURE 1
Typical installation schematic gas operated pumping gases

FIGURE 2
Typical installation schematic steam operated pumping water

Motive gas 

valve

Inlet

Discharge

Motive 

pressure

Suction

Suction 

pressure

(vacuum)

Check 

valve

Motive gas 

valve

Suction

Discharge

Motive 

pressure

Foot 

valve

5 OPERATION

5.1 Pre-operational check

1.  Ensure that all installation procedures have 

been completed.

2.  Ensure that any restrictions in the discharge 

line have been removed.

3.  Ensure that any discharge line valves are 

fully open.

4.  Ensure that the suction line valve, if 

installed, is fully closed.

5.2 Operating

1.  Open the motive valve quickly.
2.  Open the suction line valve, if any.
3.  Regulate the discharge pressure as desired 

to a value within the capability published in 
the relevant technical data sheet or product 
proposal referred to above.

4.  For pump priming applications, when 

evacuation is completed, close the suction 
valve and immediately start the centrifugal 
pump. Then shut off the motive valve to the 
jet pump.

Inlet

Summary of Contents for PENBERTHY GL

Page 1: ... for consequential damages It is expressly understood that Emerson is not responsible for damage or injury caused to other products buildings personnel or property by reason of the installation or use of its products This is Emerson s sole warranty and in lieu of all other warranties expressed or implied which are hereby excluded including in particular all warranties of merchantability or fitness...

Page 2: ... malfunction of the jet pump with resulting sudden release of pressure severe physical injury or property damage 2 3 Application data The model GL is intended to operate between 60 psig 410 kPaG and 150 psig 1030 kPaG steam pressure against moderate or zero discharge head The model GH is intended to operate between 20 psig 140 kPaG and 150 psig 1030 kPaG steam pressure against moderate to substant...

Page 3: ...n a gas operated jet pump is used to lift liquids by suction or vacuum the jet pump should be located as close to the level of the liquid as practical However any liquid entrained into the jet pump other than water when using steam as the operating medium may cause the jet pump to stop pumping resulting in a possible suction flow reversal 8 Discharge piping should be sized as short as possible and...

Page 4: ...her than ambient temperature 4 Lower temperature or size larger jet pump 5 Suction piping leaks 5 Tighten fittings 7 DISASSEMBLY REASSEMBLY WARNING Do not proceed with removal of the jet pump from connecting piping unless the jet pump has been relieved of all pressure or vacuum has been allowed to reach ambient temperature and has been drained or purged of all fluids Failure to follow these instru...

Page 5: ... the cost exceed the minimum charge If you return a unit under warranty but it is not defective the minimum charge will apply FIGURE 3 Suction connection Operating connection Discharge connection 10 EXPLODED PARTS DRAWING PARTS LIST Ref nr Item 11 Body 61 Nozzle Neither Emerson Emerson Automation Solutions nor any of their affiliated entities assumes responsibility for the selection use or mainten...

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