cashco POSR-2 Installation, Operation & Maintenance Manual Download Page 2

IOM-POSR-2

2

10.   See Figure 2 for installation ori en ta tion 

for hor i zon tal or vertical piping. For best 
per for mance Cashco rec om mends in stall ing 
in a well drained horizontal pipe, prop er ly 
trapped.

Position “H”:  Horizontal Pipe. Re quires 

user to in stall sensing line on down stream 
pip ing.

Position “VD”:  Vertical pipe with down wards 

flow direction. Requires user to install 
sensing line on down stream pip ing.

Position “VU”:  Vertical pipe with up wards 

flow di rec tion. Pilot valve and main valve 
shipped as separate units. Re quires user 
to install pilot valve at down stream pipe tap 
with a pipe nipple (not provided), provide 
and install tub ing (4 tube fittings and two 4 
ft (1.2 m) lengths of 1/4" OD copper tubing 
supplied) to load ing cham ber tap and to 
P

1

 body tap from pilot valve.

11.  Recommended installation is with pilot valve 

spring chamber vertical upwards.  Orient such 
that the spring chamber vent hole does not 
collect rainwater or debris.

12.  Regulators are not to be buried underground.

13.  For insulated piping systems, rec om men da tion 

is to not insulate regulator.

This increases the loading pres sure on the 
main valve’s plug and opens valve.  Partially 
closing the pilot valve’s plug will reduce its flow 
to less than the amount bleed ing downstream, 
and allows the loading pres sure on the main 
valve’s piston to decay, allowing partial closing 
of the main valve’s plug. This continues until 
steady-state is de vel oped.

4.  The pilot valve’s diaphragm(s) senses the 

down stream (P

2

) pressure and compares the 

force generated to the force developed by the 
pilot’s range spring.

5.  If, during operation, the downstream (P

2

pres sure falls below the pilot valve’s setpoint, 
the main valve’s piston senses the reduced 
pres sure on its underside and instantly moves 
down,  increasing the flow through the main 
valve.  At the same time, the pilot valve senses 
the reduced pressure and the pilot valve’s 

SECTION III

7.  In placing thread sealant on pipe ends prior to 

en gage ment, assure that excess material is 
removed and not allowed to enter the reg u la tor 
upon start-up.

8.  Flow Direction.  Install so the flow direction 

match es the flow arrow on the body. 

 
  9.  The POSR-2 comes factory piped between the 

pilot supply and pilot loading.  Install an external 
sensing line from the 1/4" NPT con nec tion 
opposite the factory piped pilot load ing port 
to a point downstream at gauge location; use 
1/4" OD metal tubing for dis tanc es 4 ft (1.2 m) 
or less, and 3/8" OD metal tubing (requires 
1/4" x 3/8" tubing adapter) for distances 
greater than 4 ft. (1.2 m).  The sensing line 
should always be sloped down ward so that 
condensation will drain away from the pilot.  
If regulator pipe line is ex pand ing to a larger 
pipe line, always connect sens ing line to the 
larger pipe line.

III. PRINCIPLE OF OPERATION

A. General:

1.  The POSR-2 pilot obtains its operating me di um 

from the main valve body inlet.  Down stream 
pressure (P

2

) registers on the un der side of 

the main valve’s piston and the pilot valve’s 
diaphragm(s).

2.  The loading pressure on the top side of the 

main valve’s piston is an intermediate pres sure 
higher than the downstream (P

2

) pres sure by 

the sum of the pressures required to overcome 
the main valve’s plug unbalance force and the 
piston spring’s force.

3.  The pilot has a bleed orifice that continuously 

bleeds part of the loading medium down stream.  
In op er a tion, the pilot valve’s plug can flow 
more medium than is bleeding down stream.  

          CAUTION

DO NOT HYDROSTATIC TEST THROUGH AN IN STALLED 
UNIT, INCLUDING PILOT; ISOLATE BOTH PILOT AND MAIN 
VALVE  FROM TEST.  The upper range spring pressure 
level listed on the nameplate is the rec om mend ed “upper 
operative limit” for the sens ing diaphragm(s) in the pilot.  
Higher pres sures could cause internal damage.  In addition, 
note on the name plate that the Inlet and Outlet pressure 
and tem per a ture ratings are at different levels.

Summary of Contents for POSR-2

Page 1: ...et pressure gauge should be located approximatelytenpipediametersdownstream and within sight 5 All installations should include a downstream relief device if the inlet pressure could exceed the pressu...

Page 2: ...thepilotvalvesenses the reduced pressure and the pilot valve s SECTION III 7 In placing thread sealant on pipe ends prior to engagement assure that excess material is removedandnotallowedtoenterthere...

Page 3: ...SITION H POSITION VU Pilot valve and main valve shipped as two units Installer to connect between pilot valve and main valve for loading and supply tubes POSITION VD Pipe or tubing installed by custom...

Page 4: ...omabove untilflow begins 7 Continue to alternate slowly closing the bypassvalveandthenslowlyopeningtheinlet upstream block valve especially when the downstream piping system isn t pressurized If the o...

Page 5: ...close the inlet upstream block valve Close the outlet downstream valve only if regulator removal is required Close the needle valve on the pilot valve s sensing line 6 Most pilot operated valve operat...

Page 6: ...to remove the bellows 11 in the box below Number of revolutions required to remove bellows 11 ________________ Inspect the bellows 11 for a crack or joint failure where leakage is occurring Replace b...

Page 7: ...uld be protruding bellows 11 Invert bellows 11 with stem extension 10 into body 1 recess Allow stem extension 10 to fall into threaded opening for bellows 11 Align threaded portion of bellows 11 rotat...

Page 8: ...Never replace bolting 17 18 with just any bolting if lost Bolt heads and nuts are marked with specification identification markings Use only proper grades as replacements For the 1 through 2 main val...

Page 9: ...laxed before the stem nut 15 is fully removed 15 Pull cylinder 3 horizontally outwards to removal movingoverheadhoistasnecessary Set cylinder 3 aside 16 Using a needle nose pliers grasp outside lip of...

Page 10: ...ith a clean dry cloth 32 Place cylinder 3 into a strap support and lift withanoverheadhoist Swingcylinder 3 over threaded end of plug stem assembly 7 and lower into the shoulder of bonnet 2 taking car...

Page 11: ...e cylinder 3 to cylinder head 4 ring gasket 13 Align the flat edges ofthecylinderhead 4 tobeinthesameplane as the flange of the body 1 below by rotating the head 4 as necessary 55 Insert the four elon...

Page 12: ...ax the range spring 15 by rotating the adjustingscrew 19 CCW viewedfromabove adjusting screw until fully loose Keep track of the number of revolutions in the box below 2 Place thread sealant on thread...

Page 13: ...ves 2 and 3 Open valve 1 Slowly pressurize the inlet up to 50 psig 3 4 Barg Waitaminimumof10minutes Observe for leakage of bubbles in the water jar If the number of bubbles is greater than the limit i...

Page 14: ...is subsection VIII TROUBLE SHOOTING GUIDE 1 Erratic or Noisy Operation Possible Cause Remedy a Wet steam or condensate at the inlet a Install a steam trap on the inlet side of the regulator b Clogged...

Page 15: ...mn A reflect minimum parts required for inspection and rebuild Soft Goods Kit Those in column B include minimum trim replace ment parts needed plus those Soft Goods parts from column A If the BOM is n...

Page 16: ...IOM POSR 2 16 FIGURE 7 FIGURE 8 ITEM NO DESCRIPTION 19 Pipe Nipple 20 Tube Fitting 21 Tubing 26 90 Elbow 27 90 Street Elbow 28 Union 29 Pipe Nipple 30 Pipe Nipple FIGURE 6...

Page 17: ...Cylinder 4 Cylinder Head 5 Seat Ring 6 Seat Ring Gasket 7 Valve Plug Stem Assy 8 Piston 12 Seal 13 Bonnet Cylinder Gasket 14 Piston Spring 15 Hex Nut 16 Hex Head Bolt 17 Hex Nut 18 Bushing 24 Flange 2...

Page 18: ...y Cap 10 Stem 11 Bellows Subassembly 12 Diaphragm ITEM NO DESCRIPTION 13 Diaphragm Gasket 14 Pressure Plate 15 Range Spring 16 Spring Button 17 Cap Screw 18 Hex Nut 19 Adjusting Screw 20 Adjusting Scr...

Page 19: ...cooling of the process gas depends on the process gas and the inlet and outlet pressures The system designer is responsible for determining whether the process gas temperature may raise under any ope...

Page 20: ...A5 DA6 DA8 DA0 DA1 DAP SAP SLR 1 SLR 2 PTR 1 ALR 1 ULR 1 PGR 1 BQ BQ OPT 45 BQ CRYO 123 123 CRYO 123 OPT 45 123 OPT 46G 123 1 6 123 1 6 OPT 45 123 1 6 OPT 46G 123 1 6 S 123 1 6 S OPT 40 1000HP 1000HP...

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