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Discharge Piping | Stuffing Box

EXTERNAL-INJECTION LIQUID-SEAL PIPING

a)  A tapped hole is supplied in the stuffing box  
 

directly over the seal cage to introduce a clean,  

 

clear sealing liquid.  The stuffing box must at  

 

all times be supplied with sealing liquid at a  

 

high enough pressure to keep the box free from  

 

foreign matter, which would quickly destroy the  

 

packing and score the shaft sleeve.  The sealing  

 

liquid must be left on even when the pump is  

 

shut down, unless the casing is isolated from  

 

the discharge pressure.

 
b)  Only a sufficient volume of  sealing liquid to   
 

create a definite direction of  flow from the    

 

stuffing box inward to the pump casing is    

 

required, but the pressure is important.

c)  We recommend that piping supplying sealing  
 

liquid of  stuffing box be sized to supply a    

 

sufficient  volume of  water at the required    

 

pressure, based on the location of  the pump  

 

(or pumps) with respect to the liquid source.  A  

 

small pipe can be utilised for the connection to  

 

the stuffing box.  A valve should be installed to  

 

adjust and regulate sealing liquid and a gauge  

 

installed to check pressure.

d)  External sealing liquid should be adjusted to  
 

the point where packing runs only slightly    

 

warm, with a very slow drip from the stuffing  

 

box. Excess pressure from an external source  

 

can be very destructive to packing.  More  

 

 

pressure is required, however, for abrasive 

 

slurries than for clear liquids.  Examination of   

 

the leakage  will indicate whether to increase  

 

or decrease external pressure.  If  slurry is    

 

present in the leakage, increase the pressure  

 

clear liquid drips from the box.  If  the drippage  

 

is corrosive or harmful to personnel, it should  

 

be collected and piped away.

e)  A common error is to open the external piping  
 

valve wide and then control the drippage by   

 

tightening the packing gland.  Actually, a  

 

 

combination of  both adjustments is essential  

 

to arrive at the optimum condition.  The life of   

 

packing and sleeve depends on this careful    

 

control more than any other factor. 

 

STUFFING BOX

 

Contaminants in the pumped liquid must not enter 
the stuffing box. These contaminants may cause 
severe abrasion or corrosion of  the shaft, or shaft 
sleeve, and rapid packing or mechanical seal 
deterioration; they can even plug the stuffing box 
flushing and lubrication system. The stuffing box 
must be supplied at all times with a source of  
clean, clear liquid to flush and lubricate the pack-
ing or seal. The most important consideration is to 
establish the optimum flushing pressure that will 
keep contaminants from the stuffing box cavity. If  
this pressure is too low, fluid being pumped may 
enter the stuffing box. If  the pressure is too high, 
excessive packing or seal wear may result; and 
extreme heat may develop in the shaft causing 
higher bearing temperatures. The most desirable 
condition, therefore, is to use a seal water pressure 
slightly above the maximum stuffing box pressure.

STUFFING BOX OPERATING PRESSURE

 - The 

actual stuffing box pressure operating pressure 
may be obtained by installing a pressure gauge on 
the box.  This should be done with an extra seal 
cage temporarily replacing the two rings of  pack-
ing in the bottom of  the box to obtain a more 
accurate gauge reading.  Gauge readings should be 
taken with the pump running under various head 
and capacity conditions.  The pressure of  the 
flushing or lubrication water can then be set at a 
value 5 to 10 psi above the maximum expected 
stuffing box operating pressure.  Even under the 
best conditions, a properly packed stuffing box 
should be watched closely.  If  pressure conditions 
change slightly there will be resistant change in 
packing “seating” which should be compensated 
by a change in gland adjustment.

FLUSHING AND LUBRICATION WATER

 – The 

recommended method to minimise error in 
regulating flushing water is the “Controlled 
Pressure System”.  Most important is the pressure 
reducing valve which may be adjusted to a value 
slightly exceeding the stuffing box operating 
pressure.  A flow indicating device that will serve to 
indicate a failing of  the bottom packing rings 
allowing leakage into the pump. is advisable eith 
this arrangement, the packing gland need s to be 
tightened only against the lowest necessary 
pressure.  The “out” connection from the stuffing 
box should be closed with this system.  Longer 
packing life and less frequent adjustment are 
possible with the “controlled pressure system” 
properly installed and operated.

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Содержание CSR

Страница 1: ......

Страница 2: ... 7 MAINTENANCE 8 GENERAL MAINTENANCE AND PERIODIC INSPECTION 8 MAINTENANCE TIME TABLE 8 TROUBLE SHOOTING 9 11 NOTE The information contained in this book is intended to assist operating personnel by providing information on the characteristics of the purchased equipment It does not relieve the user of their responsibility of using accepted engineering practices in the installation operation and ma...

Страница 3: ...ERIAL NUMBER Composed of certain groups of numbers All groups are necessary for identification TYPICAL EXAMPLE P 2081 98 2 MODEL CSR followed by SIZE Composed of three 3 groups of number EXAMPLE 4 x 3 x 11 First number 4 is the ASA suction flange size in inches second number 3 is the ASA discharge flange size in inches the third number 11 is the nominal maximum impeller diameter in inches 3 IMPELL...

Страница 4: ...s condition provides a positive suction head on the pump It is also possible to prime the pump by pressurising the suction vessel When installing the pump consider its location in relation to the system to assure that sufficient Net Positive Suction Head NPSH at pump suction is provided Available NPSH must always equal or exceed the required NPSH of the pump The pump should be installed with suffi...

Страница 5: ...n piping observe the following precautions a If the pump is operating under static lift conditions a foot valve may be installed in the suction line to avoid the necessity of priming each time the pump is started This valve should be of the flapper type rather than the multiple spring type sized to avoid excessive friction in the suction line Under all other conditions a check valve if used should...

Страница 6: ...sion or corrosion of the shaft or shaft sleeve and rapid packing or mechanical seal deterioration they can even plug the stuffing box flushing and lubrication system The stuffing box must be supplied at all times with a source of clean clear liquid to flush and lubricate the pack ing or seal The most important consideration is to establish the optimum flushing pressure that will keep contaminants ...

Страница 7: ...mp NOTE If the pump does not prime properly or loses prime during start up it should be shut down and the condition corrected before the procedure is repeated 5 Pumps moving high temperature liquids Open the warm up valve to circulate liquid for preheating Close the valve after the pump is warmed up 6 Start the pump driver turbines and engines may require warming up consult the manufacturer s inst...

Страница 8: ...ings are running hot over 180 it may be the result of too much lubricant If changing the lubricant does not correct the condition disassemble and inspect the bearings Check grease lubricated bearings for saponification This condition is usually incurred by the infiltra tion of water or other fluid past the bearing shaft seals and can be noticed immediately upon inspec tion since it gives the greas...

Страница 9: ...on will cause pump damage Dismantle pump or use piping hand hole to clean impeller Not enough liquid delivered 8 Air leaks in suction piping 9 Air leaks in stuffing box 10 Speed too low 11 Discharge system head too high 12 Suction lift too high 13 Impeller partially plugged 14 Cavitation insufficient NPSH depending on installation 15 Defective impeller 16 Defective packing If liquid pumped is wate...

Страница 10: ... enough pressure 21 Speed too low 22 Air leaks in suction piping 23 Mechanical defects 24 Obstruction in liquid passages 25 Air or gases in liquid Test in laboratory reducing pressure on liquid to pressure in suction line Watch for bubble formation 26 Excessive impeller clearance 27 Too small impeller diameter probable cause if none of the above See item 5 See item 8 See items 15 16 and 17 Dismant...

Страница 11: ...See item 14 See items 15 16 and 17 See item 18 Use larger driver Consult factory for recommended size Test liquid for viscosity and specific gravity See item 6 Release gland pressure Tighten reasonably If sealing liquid does not flow while pump operates replace packing If packing is wearing too quickly replace scored shaft sleeves and keep liquid seeping for lubrication Check alignment Examine pum...

Страница 12: ...SAM Engineering Pty Ltd 24 Duncan Road Lilianton Boksburg South Africa Tel 27 0 11 823 4250 Fax 27 0 11 823 4943 Email pumps sameng co za www sameng co za ...

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