Document MKL4XB48jaw3bLDmnkM1Rkm7
BREATHING AIR MODIFICATIONS
CLASS "A" DESIGN ABERDEEN PVC PLANT
JULY 24, 1980
WORK BY:
l/fcA
Bruce Vick Process Engineer
REVIEWED BY: Senior Process Engineer
APPROVED BY: R. A. Frohreich Chief Process Engineer
VAB.0001027823
Jerry Roberts
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VAB.0001027824
BREATHING AIR MODIFICATIONS CLASS "A" DESIGN
ABERDEEN PVC PLANT
TABLE OF CONTENTS
I. INTRODUCTION II. DESIGN BASIS III. PROCESS DESCRIPTION IV. EQUIPMENT SPECIFICATIONS V. INSTRUMENT SPECIFICATIONS VI. PROCESS PIPING SCHEDULE VII. WORK LIST VIII. DRAWINGS
A
VAB.0001027825
BREATHING AIR MODIFICATIONS
CLASS "A" DESIGN ABERDEEN PVC PLANT INTRODUCTION Breathing Air Modifications, Item A-23 of the 1980 Capital Budget, will improve and upgrade the current breathing air system at the plant. The modifications to be done to the existing system include the replacement of the existing air-water separator with a vertical, ASME code stamped air-water separator with an internal mesh pad. The new air-water separator was sized using the TSO program "Drum Size". To further insure adequate water removal from the fresh breathing air supply, coalescing filters will be placed inline on the branches of the breathing 'air lines to the different areas of the plant. Air bleeding points will be installed in the breathing lines. The bleeding points will allow continuous bleeding of the breathing air lines to reduce water condensation in the breathing air system.
VAB.0001027826
BREATHING AIR MODIFICATIONS
CLASS "A" DESIGN ABERDEEN PVC PLANT
DESIGN BASIS
The breathing air system at the Aberdeen Plant supplies air to the different areas of the plant which include Line I, Line III, Dry Blend, Plasticizer, VCM Tank Farm, and the old and new reactor
modules.
The vinyl area of the plant creates the largest demand for breath ing air due to possible VCM exposure by operating person
The desiqn basis for the breathing air modifications iso SCF per ..cor (n
Maximum Breathing Air Usage
The breathing air system will experience a maximum of 8 users
during periods of peak loading. This would occur at a time when
a reactor in both the old and new reactor units was down for
maintenance and VCM was being unloaded at the VCM tank farm
simultaneously
m
8 Users x 6 SCFM _ User
SCFM (max.)
1 Class "A" Process Design, Basis of Bids Issue, PVC Capacity
Replacement; Aberdeen, MS Volume I, Page 64.
BREATHING AIR MODIFICATIONS
CLASS "A11 DESIGN
ABERDEEN PVC PLANT
III. PROCESS DESCRIPTION
Air enters through the existing inlet stack at ambient conditions. Air flows through the inlet filter to existing compressor C-101. C-101 is a Nash liquid ring compressor which uses process water as seal water to compress the air. The seal water and compressed air are discharged into an existing two inch line that is to be tied into new line 2-AI-101, which is the inlet to new air-water separator, l'S-101 .
4*
Seal water supplied to the compressor is separated from the com pressed air in the air-water separator. The existing level probe on the existing air-water separator will be relocated to WS-101 to drain water from the air-water separator. The water will drain through line l-AU-103 as separator blowdown. Line l-AU-103 is insulated and electric traced for freeze protection. Safety valve, SV-101, on WS-101 will be set to relieve internal pressure at 85 psig.
Air from WS-101 is discharaed into line 2-AI-102. Line 2-AI-102 ties into the existing breathing air header. Air flows through the existing breathing air header to the existing F-5 reactor. The existing F-5 reactor is to be cleaned out for use as the breathing air receiver. In the event of compressor failure, the F-5 reactor will provide 8 men breathing air for 37 minutes.
Existing pressure switch, PSL-101, which is presently located on the existing air receiver at the compressor station is to be relocated to WS-101. At a pressure of 45 psig, PSL-101 will send a signal to the existing red flashing light at the compressor station to notify operating personnel of low system air pressure.
New pressure gauge, PG-101, is available on the F-5 reactor to monitor the internal pressure. From the existing F-5 reactor, breathing air is distributed to the different areas of the plant which include: 1) VCM tank farm, 2) old reactor module, 3) new reactor module, 4) V-ll dryer building, and 5) the compound, plasticizer, and V-10 dryer buildings.
VAB.0001027828
BREATHING AIR MODIFICATIONS
CLASS "A" DESIGN
ABERDEEN PVC PLANT
HI. PROCESS DESCRIPTION - (continued)
In order to remove any water that condenses in the breathing air lines, coalescing filters will be installed in the different breathing air branches that distribute breathing air to the plant. The coalescing filters will be installed in the follow ing breathing air lines:
1) breathing air header that distributes fresh air to the V-10 dryer building, compound, dry blend, and plasticizer,
2) breathing air header to the new reactor module, 3) breathing air line to the V-10 dryer building, 4) the breathing air line to the VCM unloading area, and 5) the breathing air line to the V-11 dryer baghouses.
Also, air bleeding points will be installed in the breathing air system. The bleeding points will allow a constant flow from the breathing air system. For location of the bleeding points see Figure 2.
A
VAB.0001027829
BREATHING AIR MODIFICATIONS
CLASS "A" DESIGN ABERDEEN PVC PLANT
EQUIPMENT SPECIFICATIONS Item No. F-101 F-102 F-103 F-104 F-105 MP-10I TP-101 VJS-101
Service Coalescing Filter Coalescing Filter Coalescing Filter Coalescing Filter Coalescing Filter Mesh Pad Drain Trap Air-Water Separator
Location I-AI-105 l-AI-113 1-AI-I09 l-AI-117 1-AI-121 WS-101 F-5 Reactor 2-AI-10I
VAB.0001027830
CONOCO
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ENGINEERING CENTER
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The Hankison line of compressed air/ gas condensate drain traps automat ically collect and discharge entrained moisture and oil from separators, receiver tanks, intercoolers, aftercool ers, dryers, filters, drip legs, and other equipment in compressed air systems that require drainage of condensates.
These traps bring production costs down by eliminating the loss of expen sive compressed air when petcocks are continuously bled and the man hours wasted when equipment and air lines are manually drained. And because they're automatic, there's no need to worry that unattended drain lines will back up and interrupt production.
PILOT VALVE MAGNET
BULLETIN CDT-1
AUTOMATIC CONDENSATE DRAIN TRAPS for
Compressed Air Systems
r
ORDINARY TRAP
DISCHARGE PORT
HANKISON SNAP-TRAP HANKISON TRIP-L-TRAP
Ordinary Traps vs. Hankison Traps
Ordinary compressed air condensate traps suffer from two problems: 1. They leak and lose a great deal of expensive plant air. 2. They clog and, therefore, do not function at all.
The basic reason these compressed air traps leak and clog is related to their fundamental design. In ordinary traps, power to open and close the discharge valve is supplied by the float. This causes the area of the discharge orifice in the discharge valve to be small in order to minimize the force which must be overcome by the float. This small orifice can easily become clogged by oil sludge, pipe scale, and other contaminants.
Ordinary traps also have a tendency to discharge constantly. They are designed so that the float rises as the
water level rises, gradually opening the discharge valve. The discharge valve remains open just long enough to dis charge condensate at the same rate at which it collects in the trap. This con stant flow causes cutting and erosion of the valve seat. Damage to the valve seat leads to further leakage. This, of course, results in more air loss.
The Hankison TRIP-L-TRAP* and SNAP-TRAP* are not wholly depen dent upon the weak buoyant forces developed by the float to open the discharge valve. As the condensate in the trap rises, the float does not im mediately rise, but is held firmly in place by a magnet. When the buoyant force of the float overcomes the mag netic force of the magnet, the float rises and trips a pilot valve open. The
pilot valve allows line pressure to enter a piston chamber and pneumatic power supplies the force to open the discharge valve. Valve operation by pneumatic power permits the use of a large dis charge orifice. This allows the trap to flush away deposits and "crud" that might otherwise accumulate and clog the discharge orifice. When condensate has been discharged, the pilot valve closes, and line pressure forces the discharge valve shut. Line pressure then holds the valve shut until the next operation. This snap open, snap shut design plus the positive sealing of the discharge port eliminates "valve chat tering" and costly leakage problems . . . leakage problems which cause exces sive wear and subsequent trap failure.
L
VAB.0001027835
f pi
TRIP-L-TRAP
FEATURES:
Designed for heavy duty service-- built to handle moisture and oil emulsions that cause most other traps to fail
Long life--Repair Parts Kits are available for rebuilding traps when necessary
Reliable--only two moving parts Impervious to synthetic lubricants Maximum working pressures to
500 PSIG All stainless steel models available Patented Design (U.S. Patent
#3,635,238)
OPERATION:
As the condensate begins to rise in the
Trip-L-Trap, the float (1) remains in
place, held by the magnet (2) mounted on the valve stem (3). As the condensate
level in the trap rises, the buoyant force of the float overcomes the hold
ing force of the magnet TRIPPING the pilot valve {4) open. A counter weight
on the float arm (9) helps to speed up
the motion of the float arm. The pilot valve mechanism is pro
tected from contaminants by a baffle
in the trap shell. Air enters the pilot
valve (4), flows down through the
hollow valve stem (5), and up under the piston (6) in the piston cylinder {10).
This air pressure forces the piston
assembly to move upward opening the main discharge valve (7). The conden
sate is forced into the main discharge
valve and out the condensate discharge outlet. {The viton seal on the valve stem
prevents condensate from reaching the piston chamber).
When sufficient condensate has
been discharged, the float drops caus
ing the pilot valve (4) to close. The
closing action is increased by attraction
of the float arm (9) and the magnet (2).
With the pilot valve shut, the air supply
to the piston (6) is cut off. Pressure on the float arm causes the piston assembly
to return to its original position closing
the main discharge valve. A small bleed hole (11) in the piston cylinder (10)
enables air pressure in the piston cylinder to dissipate to the atmosphere. Air pressure in the trap housing creates a positive seal between the discharge valve and outlet eliminating air leakage between cycles.
All models can be blown down manually by opening a petcock.
Model 506 Trip-L-Trap incorporates a second float to increase condensate discharge cycle time. A skim tube "sweeps out" any oil slick that might form on the surface of the liquid inside the trap.
MODEL 505
MODEL 506
(9) FLOAT ARM
(4) PILOT VALVE
(2) MAGNET BAFFLE
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(3) VALVE
(7) MAIN
STEM
SPARGE (5) HOLLOW
VALVfc VA|_VE STM
(1) FLOAT
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CLOSED POSITION
OPEN POSITION
ENGINEERING DATA
(6) PISTON (10) PISTON CYLINDER (11) BLEED HOLE
Model
..................
. j
--LL&k
505
505HP
Mm/Max
Operating
Preacwa
I
PSI6 Bar,.
Min/Max Operating
Temp.
QF C
10/300 .69/21
35/150 1.7/65.6 10/500 .69/35
Primary
Material*
Of Construction
Discharge
par Operation
Shell
(Menials
.. v ' y
Carbon Steel, Stainless Steel Steel, Brass,
Oelfin, Nylon
190cc 4 pints
505SS 10/300 .69/21
304 Stainless Steel,
35/150 1.7/65.6 Stainless Viton
505HPSS 10/500 .69/35
Steel
190cc .4 pints
Carbon Steel, Stainless 1514cc 506 10/300 .69/21 35/150 1.7/65.6 Steel Steel, Brass, 3.2 pints
Delrin, Nylon
Nominal
Capacity*
r---.
190cc/min 11.4 liters/hr
3 gats/hr.
190cc/min 11.4 liters/hr
3 gals/hr
1514cc/min 90.8 liters/hr
24 gals/hr
NMI
Max. Capacity*
-V
114Gcc/min 68.4 liters/hr
18 gals/hr
1140cc/min 68.4 liters/hr
18 gals/hr
90$4cc/min 544.8 liters/hr
144 gals/hr
Traps are designed to operate at one discharge per minute for one year before rebuilding is required. Operation at mon than one discharge per minute may require more frequent rebuilding.
VAB.0001027836
SNAP-TRAP
SNAP-TRAP
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FOR MANUAL DRAIN
CLOSE -
- OPiN
1^1. N1W< !.** f*S
CAOUNTODEMNASTEICft
J HB DRAW
HANKISON
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rOR MANUAL ORA*
CLOS1 -
- OP*N
MODEL 503 and 504
MODEL 507 and 508
ENGINEERING DATA
1 ' _l" (J
Model
S03{1) 507 (2) 504(1) 508 (2)
Min/Max Operating Pressure PSI6 BAR
20/150 1 4/10.3
20/175 1.4/12.1
Mie/Max Operating Tamp. F c
35/120 1.7/48.9
35/120 1.7/48.9
Siiiiili
Polycarbonate Polycarbonate (3) Buna N Seals
Metal w/ sightglass
Oelrin Viton Seals
^M-i-. . y
-
sm**.
:t3
:V
l ll'l'i lil tfM
2 Da 04 pints
20cc/min
1.2 liters/hr -3 gals/hr
(1) Top inlet connection.
(2) Bottom inlet connection
(3) Metal bowl guards are available.
OPERATION:
As condensate begins to rise in the SNAP-TRAP, the float (1) remains in place, held by the magnet (2) and metal
washer (11). When the buoyant force of the float overcomes the magnetic force of the magnet, the pilot valve (3) opens, allowing line pressure to enter
the main discharge chamber (4) caus ing the piston (5) to snap downward opening the main discharge chamber. Condensate is forced through a stain less steel filter (6) and fluted ports into the lower portion (7) of the chamber and is discharged through the outlet (8).
When sufficient condensate has been discharged, the float drops closing pilot valve (3). Excess air in the
discharge chamber is bled off through orifice (10), which is protected by a filter (1 2), and the piston returns to the
closed position. Pressure in the lower portion of the chamber creates
positive sealing of the discharge port. There is no air leakage between cycles. The pilot valve mechanism is pro
tected from contaminants by baffle (13). Models 503 & 504 can be blown
down manually by turning the knurled outlet connection (8). This causes the entire mechanism to move upward, allowing the condensate to flow through the manual drain passage (9) to the outlet (8). Models 507 and 508 have a separate manual drain.
PISTON CLOSED POSITION
(11) METAL WASHER
FEATURES:
Economical--for light to medium duty service
Models with clear polycarbonate bowls for easy viewing of condensate level and trap operation {not for use on systems where synthetic com pressor lubricants are used)
Models with metal bowls and sight glass available for use on systems using synthetic lubricants
Models with top inlet connection or bottom inlet connection (ideal for receiver tanks) available
Patented Design (U.S. Patent #3,993,090)
Tested for over a million cycles
PILOT VALVE
-13) BAFFLE
(2) MAGNET
(1) FLOAT
(4) MAIN
DISCHARGE CHAMBER
(12) ORIFICE FILTER
(10) ORIFICE (5) PISTON (7) LOWER PORTIONOF THE CHAMBER
(6) STAINLESS STEEL FILTER
(8) OUTLET
PISTON OPEN
POSITION
VAB.0001027837
INSTALLATION:
Inlet Piping:
Trap should be installed below level of device being drained to allow conden sate to flow into the trap by gravity. Strainers to protect the trap from undue particulate contairtination and isolation valves to permit quick and easy trap servicing are useful accessories.
Drain Line: A line is recommended from the trap discharge to drain. As the trap dis charges condensate at system pres sure. the discharge line should be anchored to prevent movement.
Dimensions
Model
Inlet A B Conn. Drain
(NPTF) Conn.
503, 504 3%" 6%"
5Ae" Tube
Typical Installations:
TOP INLET CONNECTION TRAPS
il1;. ."Tit
B
f,K yy '
.vV; 'r
BOTTOM INLET
CONNECTION TRAPS
507, 508 3h" 7"
505, 505HP, 505SS, 7"
505HPSS
1 506 7"
8lA" 1 3X"
H"
34"
1"
%" NPTF %" NPTF A" NPTF
' -: ' '-.-vs-
503. 504
Choosing the Correct Size HANKISON Trap
B
Is: ' r v- ..
' .-I;-::'1
iA
507' 508
TA U' ii'i
Ml f: SiSj;
. .=-'1
B
505, 505 HP. 505 and 505 HPSS
i: -
:L':^ -
A'1:
-^.3 .IJC
: _ v? v ' t7-
B
506
I. To determine how much condensate forms in a given area of your compressed air system: A) Measure the temperatures of the com pressed air ENTERING and EXITING a system component (receiver tank, aftercooler/separator, etc.) or length of pipe line on which you wish to install a trap.
system. Do not use any reheated air temperatures. CJ Determine amount of condensate formed per minute for each SCFM of air flow by subtracting amount found in l,B,1 from amount found in l,B,2.
D) Determine total amount of condensate
formed by multiplying value calculated in I.C above by your system's flow rate in SCFM.
II. Select the proper model Hankison trap for your system by referring to the Capacity section of the Engineering Data tables inside this bulletin.
B) Refer to Graph 1) Locate ENTERING compressed air tem perature at bottom of graph; move vertically to curve corresponding to your system's operating pressure; move horizontally to left side of graph and read amount of water condensed in cubic centimeters per minute (cc/min.) per SCFM of air flow.
O$
Li.
QC
<
LL
O
CO
SYSTEM OPERATING PRESSURE
Note: If the temperature of the ENTERING air is to the right of the intersection of the applicable pressure curve and the temper ature line on the bottom of the graph (for example 148F at 100 PSIG), use zero as the value for step l,B,1 and proceed to step l,B,2.
2) Locate EXITING compressed air temper ature at bottom of graph; move vertically to curve corresponding to your system's operating pressure; move horizontally to left side of graph and read amount of water condensed in cubic centimeters per minute (cc/min.) per SCFM of air flow.
0LU.
*
C
*
E
is
Q
LU
CzO
LU
oz o
0
QC LU
1
300 PSIG
Note: Value of EXITING air temperature should be based on the coldest temperature to which the air has been cooled in the
32 50 70 90 110 130 150 170 190 COMPRESSED AIR TEMPERATURE (F)
HANKISON CORPORATION, Canonsburg, PA 15317,Phone: 4.12/745-1555, Telex: 81-2452, Cable HANKORP
PRICE AND ORDERING INFORMATION AVAILABLE FROM:
A
HANKISON
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MEMPHIS, TENN.
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(SOI) 767-7894
VAB.0001027838
OpintoH in H R A
HANKISON *
Bulletin 3400-1
CENTRIFLEX'
Compressed Air Separator/Filter
Efficient Separation and 3 Micron Filtration In One Compact Housing
SEPARATION-
The First Stage
A unique stainless steel separator core, using the principles of centri fugal force and impaction, is 99% efficient in removing particles 10 microns in size and larger.
The reusable cartridge type separator is completely removable for easy cleaning.
FILTRATION-
The Second Stage
A replacement filter sleeve, which fits over the separator core, assures absolute removal of solids and liquids 3 microns and larger in size.
Solids removal--finer filtration at less cost
The filter sleeve, constructed of an in-depth arrangement of glass fibers, has a high percentage of void spaces, allowing it to accumulate 3 to 4 times more particulates than coarser sur face (pore) type filter element materials such as porous metal and plastic. Also the in-deptt\ arrangement of fibers resists clogging due to gummy residues and sticky lacquers which are frequently present in compressed air systems and readily adhere to and foul surface type filters. This ability to accumulate large amounts of solid particles and resist clogging means that there is only a gradual increase in pressure drop across the filter, resulting in a long operating life and less oper ating cost.
Liquids removal--higher efficiencies from no flow to full flow
By using coalescence to force small droplets to form into larger droplets, the filter media continually collects all liquid droplets 3 microns in size and larger, as well as a portion of smaller droplets. This means that 99% of water droplets and 40% of oil aerosols are collected and dis charged from the system.
The combination of filter sleeve and separator core ensures high effi ciency liquid separation over a full range of flows. There is no reduction in efficiency at less than rated flows, a common occurrence in purely centrifugal separators.
Housing design--features easy installation and maintenance
The in-line, inlet and outlet con nection design reduces installation time and expense. Additional piping to maintain alignment is not required. Cartridge replacement is made easy by removable bowls for models 3401 through 3406 and a convenient -'Bottom flarfge opening for models 3407 through 3415.
FEATURES:
High efficiency separation-- removes 99% of water droplets, 40% of oil aerosols.
Combination of separator core and filter sleeve maintain high efficiency from no flow to full flow.
Replaceable filter sleeve removes 100% of particles 3 microns and larger in size--while giving long sleeve life.
OPERATION
Air enters the top of the Centriflex separator/filter and flows down through the center of the separator core and radially outward. The air is subjected to a strong centrifugal force as it passes through the separator core which is constructed of a pair of stainless steel perforated
tubes. The orifices in the first tube (A) are staggered in relation to those in the second (B). This causes particles 10 microns and larger to continue in a straight course after leaving the inner tube, impacting and impinging on the inside of the outer tube where they form a film which drains to the bottom of the separator core.
The air then passes into the filter sleeve (C) which is composed of an in-depth bed of resin impregnated glass fibers. Solid particles (to 3 microns absolute) are captured and retained here. Liquid aerosols are coalesced on the glass fibers form ing large droplets which move down ward to the bottom of the cartridge where they drain by gravity into the filter housing and are removed from the air system.
This combination of separation and coalescence allows the Centriflex separator/filter to handle large inlet liquid loads (up to 25,000 ppm w/w) while removing 99% of water droplets and 40% of oil aerosols over a full range of flow conditions.
Models from 15 SCFM to 11,400 SCFM
35 SCFM Model 6600 SCFM Model
Maximum Flow (CFM)* at Various Inlet Pressures
MODEL NUMBER
3401 3402 3403 3404 3405 3406 3407 3408 3409 3410 3411
3412 3413 3414 3415
20 PSIG 1.4 BAR
4.5 10.6 16.7 30.3 60.6 90.9 182 364 545 727 909 1450 2000 2550 3450
30 PSIG 1 40 PSIG 2.1 BAR. JJZ& BAR
'72
13.7
16.7
21.5
26 2
39.0
47.7
78.0
95.4
117 143
234 286
468 572
702 859
936 1140
1170
1430
1870
2290
2570
3150
3280
4010
4450
5440
60 PSIG 4.1 BAR
9.8 22.8 35.8 65.1 130
195 391 781 1170 1560 1950 3120 4300 5470 7420
80 PSIG 5.5 BAR
12.4 28.9 45.3 82.6 165 248 496 991 1490 1980 2480
3970 5450 6940
t
9420
ISO PSIG 6.9 BAR
15.0 35.0 55.0 100 200 300 600 1200 1800 2400 3000 4800 6600 8400 11,400
120 PSIG 8.3 BAR
17.6 41.1 64.6 117 235 352 704 1410 2110 2820 3520 5640 7750 9860 13,400
15D PSIG 10.3 BAR
21.5 50.3 79.0 144 287 431 862 1720 2580 3450 4310 6890 9480 12,100 16,400
200 PS !G 13.8 BAR
28.1
65.5 103 187 374 562 1120 2250 3370 4490 5620 8990 12,400 15,700 21,300
250 PSIG 17.3 BAR
34.6
300 PSIG 20.7 BAR
41.2
80.8
96.0
127 151 231 . ***04
462 549
692 823
1380
1650
2770
3290
4150
4940
5540
6590
6920
8230
11,100
13,200
15,200
18,100
19,400 23,000
26,300 31,300
Note: Pressure Drop--Separator/FHter--At rated flow conditions, when removing liquids, pressure drop will be less than 1 PSI (.07 bar) nominal (1.6 PSl M1 bar] for model 3406-1). Further pressure drop will occur only as the filter sleeve(s) become contaminated with solid particles. It is recommended that filter sleeve(s) be replaced for maximum filtration efficiency if pressure drop exceeds 10 PSI (0.7 bar).
^Convert SCFM to Metric Units as follows: 1 SCFM = .472 I n/s based on air measured at 68F (20C) and 29.92 in (760 mm) Hg.
HANKISON CENTRIFLEXTM SEPARATOR/FILTERS
MODEL NUMBER
MANUAL DRAIN
3401-1
AUTO DRAIN
MAX. AIR FLOW
(SCFM) @ 100 PSIG
15
AIR INLET/OUTLET CONNECTION
%" NPTF
HOUSING (BOWL/VESSEL)
TYPE
8 oz. polycarbonate (1)
WIDTH (INLET TO OUTLET) & HEIGHT (INS.)
3J4 x 6K
WT. (LBS.)
134
MAX. OPERATING PRESSURE (PSIG)
--I., i,--,
MANUAL AUTO
DRAIN
DRAIN
150
REPLACEMENT FILTER
SLEEVE NO.
0734-1
3401-3
%" NPTF
8 oz. metal w/sight glass 3J4 x 6%
300
0734-1
%" NPTF
16 oz. polycarbonate
3401-4
%" NPTF
16 oz. metal
3J4 x m
0734-1
3402-1 3402-3 3402-5
3402-2 3402-4 3402-6
35
%" NPTF %" NPTF
A" NPTF
16 oz. polycarbonate
3/4 x 10)4
16 oz. metal
3% x 9%
16 oz. polycarbonate
3A x 10%
2A
150
150
0734-2 0734-2 0734-2
3402-7 3403-1
3402-8 3403-2
A" NPTF H"NPTF
16 oz. metal 32 oz. metal
3% x 9% 4^6 x 11 ^
300 175
0734-2
3403-3
1" NPTF
32 oz. metal
4%6x m
3404-1
3405-1
3406-1
3407-1
600
3408-1
(2)
1200
3409-1
(2)
1800
3410-1 (2) 2400
3411-1 (2) 3000 3412-1 (2) 4800
3413-1 (2) 6600
3414-1 3415-1
(2) 8400
(2) 11.400
oi^rat^>q^emj^rature* oM
1" NPTF
48 oz. metal
4M x 13A
0734-3
1A" NPTF
136 oz. metal
5A x 22A
0734-5
1 Vi" NPTF
205 oz. metal
5% x 30A
0734-6
2A" coupling (3)
5" pressure vessel
15% x 40A
200 (4}
0734-7
2A" coupling (3)
5" pressure vessel
4\5%x42A 32%
0734-7
3" coupling (3)
8" pressure vessel
22Ax42% 215 200 (4)
(2)
0734-72
3" flange
10" pressure vessel
16% X 44Me
200 (4)
(2)
0734-73
4" flange
12" pressure vessel
20 x 51%
330 200(4)
(2)
0734-74
4" flange
12" pressure vessel
20 x 51%
335 200 (4)
(2)
0734-75
6" flange
16" pressure vessel
24x 52%
430 200(4)
(2)
0734-78
6'* flange
20" pressure vessel
28 x 5934
625 200 (4)
(2}
0734-711
6" flange (5)
20" pressure vessel
28 x 59%
630 200 (4)
(2)
0734-714
8" flange (6)
24" pressure vessel
33 x 637Ae 1150 200 (4)
(2)
0734-719
i
of 120F (48 9C) are no* recommended since filtration efficiency may decrease Polycarbonate bowls have a maximum
[1) 8 oz. polycarbonate bowl also available with optional metal guard.
(Z) Drain plugs standard on models 3405. 3406. 3407-1, and 3408 through 3415. For manual draining a valve is recommended For automat ic drainina Hankisnn
automatic drain traps are available. Model 3407-2 includes, as standard, an integral model 505 Trip-L-Trap' For models 3405 3406 and 3407-19use TriD-L-
(3) Ranges'S^vaitablTM
,hrPugh 3415 US Trip-L`Trap model 506 Standard Trip-L-Traps have a maximum wooingpressure of300 PSIG (20 7 bar)
(5) 8''>flange'ccmnectioni)ava*'lablereSSlJreS ' 3 PS'G (2'7 b*r) *"* ava"ab,e-1200 SCFM (3408) and lar9er m<*els are ASME code constructed and stamped
(6) 10" ftange connections available.
HANKISON CORPORATION, Canonsburg, Pa. 15317, Phone 1412 J 745-1555, Telex: 81-2452, Cable: HANKORP
PRICE AND ORDERING INFORMATION AVAILABLE FROM:
HANKISON
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VAB.0001027840
rcoi*iC)CO V LA
ENGINEERING CENTER
PONCA CITY. OKLAHOMA SPECIFICATION SHiiT
PLANT
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PROJECT'
ITEM NO SERVICE
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PLANT
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ENGINEERING CENTER
PONCA CITY. OKLAHOMA SPECIF ICATION SHEET
PROJECT
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ENGINEERING CENTER
PONCA Cliv. OKLAHOMA
SPECIFICATION SHEET
/ ^i .rr-'f \ h/c ftsiN'T'
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DATE MADE HY APR O BY
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BREATHING AIR MODIFICATIONS CLASS "A" DESIGN
ABERDEEN PVC PLANT
INSTRUMENT SPECIFICATIONS Item No. CV-101 PG-101 PG-102 PG-I03 PG-104 PG-105 PG-106 PG-107 SV-101 TG-101
Service Control Valve Pressure Gauge Pressure Gauge Pressure Gauge Pressure Gauge Pressure Gauge Pressure Gauge Pressure Gauge Safety Valve Temperature Gauge
Location l-AU-103 F-5 Reactor l-AI-105 l-AI-113 l-AI-109 l-AI-117 l-AI-119 WS-101 WS-101 WS-101
VAB.0001027852
CONOCO
PLANT
ENGINEERING CENTER
PONCA CITY, OKLAHOMA
h
SPECIFICATION SHEET
CONTROL VALVES
PROJECT
1
2
3
4
S
10
11
17 ia
20
21 22
23
24
26
26 27 26
30
GENERAL ITEM NO ft TAG
CL t/-/tV
SCHVICC
LINE StZE MANUFACTURER MODEL NO.
foc/j 7?c>/J
Iw/s-io
1 /"
|
1
/ AW -/
| |
SERVICE CONDITIONS FLUID
TEMP PRESS > INLET.t
normal
NORMAL
MAX MAX
75
AP
MIN
NORMAL
MAX
MOLECULAR WEIGHT
SP GH ** 60 F.
WEIGHT
VAPOR IN
VISCOSITY *** F T. 6 P
RATE. NOR . LB HR i
A PI F T.
OUT
I GPM
AO
0,9iC> Cp
HATE MAX LB HR tSCFH) GPM
NORMAL FLOW Cv
BODY
EIQDY SIZE
PORT SIZE
TYPE i ANGLE OR MATERIAL
END CONNECTIONS
BONNET
if
&djL CSjl
LUBRICATOR PACKING TRAVEL INDICATOR
VAL
TRIM
TYPE INNER VAL
NO OF PORTS
PLUG a SEAT MATERIAL
DATE A. F. E. NO W. O. NO REO. NO.
ga\/
1
ACTUATOR
TYPE
FAILURE POSITION
wi cvA\re^r
POSITIONER
input signal
OUTPUT SIGNAL
36 BYPASS
GAUGES
37 MANUFACTURER
38 MODEL NO.
NOT
B. M. NO
INO. NO. P O. NO APP O BY
4 I INDICATES ITEM CmANGCD ON LATEST flCVS'ON. ill INOlCATffc MANUFACTURE* TO GIVE RfQUCSTCD INFORMATION IN HIS QUOTATION
H|. V 7 J4 bj
OF : e00&0-1W027853
CONOCO PLANT
ENGINEERING CENTER
PONCA CITY, OKLAHOMA
SPECIFICATION SHEET
RELIEF VALVES
C PROJ ECT___
GENERAL
1 ITEM NO. ft TAG
RELIEVES EQUIPMENT NO
MANUFACTURER MODEL NO,
SY-/01
V5 -/o /
A.F.E NO
DATE *irU?o
MADE BY APP'D BY B M. NO-
W O. NO INQ. NO* REQ NO P O NO
SERVICE CONDITIONS FLUID
8 REQU1R
CAPACITY
MOL. WT
SP, GR
lO VISCOSITY
1 1 COMPRESSIBILITY FACTOR
12 DESIGN PRESS OF EQUIPMENT
OPERATING
RELIEVING
1 4 TEMP
FLOWING
RELIEVING
1 5 BACK PRESSURE
16 DIFFERENTIAL SET
URE
1 7 ACCUMULATION
1 8 BLOW DOWN
19
BA
20 CODE REQUIREMENT
FIRE2 1 EXPOSED AREA INSULATION THICKN
23 OTHER BASIS
24
IGN DETAt
25 DESIGN TY
2 6 SEAT TYPE
64s
2/.J
es 25 5.5
^SPS( A
27 BONNET l OPEN OR CLOSED t
28 INLET SI2E. RATING FACING
29 OUTLET SIZE. RATING. FACING
30 CALCULATED AREA
3I
ORIFICE LETTER
ACTUAL AREA
MATERIALS
BODY
NNET
SEAT ft DISK
34^
36
GUIDE ft RING
SPRING
E3 E L L G W S
' if /5o&- g.P 2*' i
37 LIFTING LEVER i PLAIN OR PACKED)
38 GAG
39 CODE STAMP 40 CAP t SCREWED OR BOLTED I 4 I OT HER
NOTES
MANUF ACTURER SHALL VERIFY SELECTION OF ORIFICE SIZE AND MATERIALS VALVES SHALL MEET DIMENSION REQUIREMENTS OF API RP- 526 VALVES SHALL MEET TEST REQUIREMENTS OF API RP * 527
SUPPLIER TO COMPLETE FORM BY FURNISHING INFORMATION FOR BLANK SPACES
V I/
"VAD:6Q01027854
OF
REV.
436-
CONOCO
ENGINEERING CENTER
PONCA CITY. OKLAHOMA
SPECIFICATION SHEET
PRESSURE GAUGES
PLANT /fes&OG&J/vt
PROJECT-
A.F l NO DATE SftZJJO
MADE BY
APP'D BY Will
B M NO
W. O NO INO NO REQ NO P. 0. NO
1 TAG
INSTRUMENT I OPERATING I OPERATING
3 -'O/ 4 5 ~fC3 6 7 8 P6-'C&
9 PC, - fo 7
10
11
12 13 14
15 16 17
. ...
ire C-}^ha*:
C-iAucx e 0>Aljic,i
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7S
7S '?`5
18 rnr
20
21
22 23 24 25
26 27 28 29 30 31 32 33 |34l______________ 35 [36 | 37
____________* ________________
1
1________________________________________________
| 38] | 39|
[ |
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70 70
7o
7o
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QUOTATION WILL NOT BE CONSIDERED IF SUPPLIER DOES NOT COMPLETE RIGHT HAND COLUMN.
JPM
*
SHEET
OF
rw
PLANT
1 TAG
NO.
3 TTiy ~tO i
CONOCO
ENGINEERING CENTER
PONCA CITY. OKLAHOMA SPECIFICATION SHEET
TEMPERATURE GAUGES
PROJECT
A.F E NO____ DATE 5/i//rO MADE BY APP D BY^YJMA .
B M NO ______
ftfoA,
\ -J * * f
iNO Nu
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SERVICE
TE-i*f/><rr/?rtirc &Aa*.
INSTRUMENT RANGE F (1)
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OPERATE G TEMP. F
LOCATION
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9
10
11 12
13
1-1
15
16 17 18 19 20
\
28
31 32
34 35 36
(11 ALL GAUGE ELEMENTS TO BE BIMETALLIC UNLESS OTHERWISE NOTED 41 42
13
44 45 46 47
49
52
56
QUOTATION WILL NOT BE CONSIDERED IF SUPPLIER DOES NOT COMPLETE RIGHT HAND COLUMN.
SHEET
VAB.0001027856
Of REV.
i
BREATHING AIR MODIFICATIONS CLASS "A11 DESIGN
ABERDEEN PVC PLANT
VI. PROCESS PIPING SCHEDULE
The following piping schedule uses a system of numbers and letters as a line designation. This system denotes the following information: line size, service, line number, insulation requirements, and piping specification.
Sample Line Description
2-AI-101-N-M2-1
- Piping Specification Insulation Requirement
- Line Number - Service - Nominal Line Size, Inches
Sample Piping Specification
* M2-1
{
Service Description Used
AU AI
Insulation Requirements
N E
Nominal Pressure Rating
M
Piping Material
1
First Specification of M2 Group Piping Material Nominal Pressure Rating
Service Utility Breathing Air
No Insulation Electric Traced and Insulated
125 Pound Class
Carbon Steel
VAB.0001027857
PROCESS PIPING SCHEDULE PROCESS ENGINEERING DEPARTMENT
Date
Project Plant
Made By 5*51/
Line Designation
s?r-
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Rate Lb/Hr (Hot BPSD
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7o j 7S 1 45$ I oaSS I 0.784
7o 75 I <ol*S I hoi 1
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^ -i-i.
4
PROCESS PIPING SCHEDULE PROCESS ENGINEERING DEPARTMENT
From
1 I To
ph>s
/ ~AT-1 Zi F -fo S
I
f YX *4A 6.<cu?rs
^VsJ &
/ - RT-iZ 2
0 24*m
Bate
Project
Plant
Made By
BREATHING AIR MODIFICATIONS
CLASS "A" DESIGN
ABERDEEN PVC PLANT
WORK LIST
1. Remove existing air water separator and air receiver from the breathing air station.
2. Remove the activated carbon from the existinci F-5 reactor, and clean the inside of the existing reactor.
3. Fabricate and install the new air water separator, WS-101. Insulate and electric trace the bottom of the separator.
4. Tie outlet from existing compressors, C-101 and C-102, to line 2-AI-101, inlet to WS-101.
5. Tie line 2-AI-102, outlet from WS-101, to the existing three inch breathing air header.
6. Relocate low pressure switch, PSL-101 into existing local control box.
7. Install control valve, CV-101, on the drain line, l-AU-103, from WS-101, and tie drain line into the existing drain at the north end of the compressor station.
8. Reconnect the alarm horn at the local control box and tie in instrument leads from C-101 and C-102.
9. Install coalescing filters F-101, F-102, F-103, F-104, and F-105 on the different breathing air branches. (See Figure 2)
10. Install air bleeding points in the breathing air system. (See Figure 2)
11. Install drain trap, TP-101, on the existing F-5 reactor.
12. The existing level control leg at the breathing air station is to be insulated and relocated to the new air water separator, WS-101.
13. Insulate and electric trace the level control lea from WS-101.
14. Insulate and electrice trace the bottom half of the air water separator, WS-101.
......... .
ilTHii't wi.niMJini PjPPH'IHH
.......
............................. .
.................">................ ..........
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DATE
VAB.0001027861
'IHHcliiHiiiifi... ....................1|r
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VAB.0001027862
d IP' -:h - I- r =-^--- - -1J J - .. -li'-Ir r uj.irri i>->".|.. 'Ur-
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