Document vM9eVjD8oERrd1qzMqYwb7QY

BREATHING AIR MODIFICATIONS CLASS "A" DESIGN ABERDEEN PVC PLANT MAY 27, 1980 WORK BY: Bruce Vick Process Engineer REVIEWED BY: V. E. Messick ' Sr. Process Engineer I, APPROVED BY: ronreich Chief Process Engineer VAB.0001028442 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 4 4 VAB.0001028443 K BREATHING AIR MODIFICATIONS CLASS "A" DESIGN ABERDEEN PVC PLANT I. INTRODUCTION Breathing Air Modifications, 1980 Capital Budget, Item A-23, will improve and upgrade the current breathing air system at the plant. The modifications to the existing system include replacement of the existing air-water separator with a vertical air-water separator with an internal mesh pad. The new air-water separator was sized using the TSO program "Drumsize". The existing F-5 reactor near the emission recovery system will be cleaned and used as the breathing air receiver. In the event of compressor failure, the F-5 reactor will provide breathing air to 8 men for 37 minutes. To further insure adequate water removal from the fresh breathing air supply, coalesing filters will be placed inline on the branches of the breathing air to the different areas of the plant. For location of these filters, refer to the Breathing Air Modifications Plot Plan (Figure 2). * VAB.0001028444 *A A BREATHING AIR MODIFICATIONS CLASS "A11 DESIGN ABERDEEN PVC PLANT II. 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 BTend, Plasticizer, VCM tank farm, and the old and new reactor modules. The vinyl area of the plant creates the largest demand for breathing air due to possible VCM exposure by operating personnel. The design basis for the breathing air modifications is 6 SCFM per user.^' 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. 8 Users X 6 SCFM = 48 SCFM (Max.) User (1) CLASS "A" PROCESS DESIGN, BASIS OF BIDS ISSUE, PVC CAPACITY REPLACEMENT; ABERDEEN, MS. VOLUME I, PAGE 64. VAB.0001028445 * BREATHING AIR MODIFICATIONS CLASS "A" DESIGN ABERDEEN PVC PLANT III. PROCESS DESCRIPTION Modifications to the existing Breathing Air System include the replacement of the existing air-water separator and the installation of new coalescing filters at different points in the breathing air system to remove condensed water from the breathing air line. 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 pfoces?)water v ^ as seal water to compress the air. The seal water amfl^ompressed 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 the new airwater separator, WS-101. 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 discharged 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. J\t a pressure of 45 psig PSL-101 wi11 send a signal to the existing red flashing light at the compressor station to nntifv~~bperatina personnel of 1nW system air^^p-^j^ res5iuc^--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, 5) the compound, plasticizer, and V-10 dryer building. VAB.0001028446 h BREATHING AIR MODIFICATIONS CLASS UAM DESIGN ABERDEEN PVC PLANT III. PROCESS DESCRIPTION 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 following 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-ll dryer building, 4) the breathing air line to the VCM unloading area, and 5) the breathing air line to the V-ll dryer baghouses. The existing alarm horn at the compressor station will be reconnected to sound in the event of compressor failure, v- . I/*- A VAB.0001028447 m BREATHING AIR MODIFICATIONS CLASS "A11 DESIGN ABERDEEN PVC PLANT EQUIPMENT SPECIFICATIONS Item No. WS-101 TP-101 F-101 F-102 F-103 F-104 F-105 Service Air-Water Separator Drain Trap Coalescing Filter Coalescing Filter Coalescing Filter Coalescing Filter Coalescing Filter Location 2-AI-101 F-5 Reactor 1-AI-105 I-AI-113 l-AI-109 l-AI-117 l-AI-121 VAB.0001028448 * uem^/ry i 2__________________________________________ ____________________________________________________________ :I ;\ O. 323 y` . L........................... alores: X ' k * ' * t #1 t * # Cl} W5 -to( ro s/faj /a/r&/e*Ys4 L *77<^A/ >/?> O. C2^i VU5 tot ro (3) /of ____ Z22_ & ^/?f=iE7ir /?>(= f /?^/77= CoS)f= VACV& J-/CS / r/?r7?'<^> 1 1 11 1 11 I 11 1 1 1 9 plant ir&M NO SERVICE ENGINEERING CENTER PONCA CITY. OKLAHOMA IPCCt P (CATION SHUT PROJECT K/> r?CAj forJ NO . I OATS MAOC BY APPOBY B M NO W O NO tNO NO OtO NO P O NO 221 fit** 1\ i * \ b K i } i * 1 1 > ! MEET A BULLETIN CDT-1 AUTOMATIC CONDENSATE DRAIN TRAPS for Compressed Air Systems 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- m 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 .. v .I r -.s* v. ^ ^ f : ^ =&t\: : W ' * 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. VAB.0001028452 4t TRIP-L-TRAP FEATURES: Designed for heavy duty servicebuilt 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. A% CLOSED POSITION (6) PISTON (1 0) PISTON CYLINDER (11) BLEED HOLE ENGINEERING DATA ' 1 : --WL-j.L;?' la. ; . i,hmhi '- g: i i-juwmst t :'i Min/Max - / t. Operating ' Model .> . , ` ` > ; Temp. Biw : :;: : . PSIBf : C Primary Materials Of Construction Shell (eternals Omchaige Pr Nominal Op. .e.1. ra 1tCs.io- ' n1!'1 L 'L\ i Capacity*1 .; ^ * *V* ^ * - "' x' ' li ' | 505 505HP 10/300 .69/21 Carbon Steel, Stainless 190cc 35/150 1.7/65.6 Steel Steel, Brass, .4 pints 10/500 .69/3$ Delrin, Nylon 190cc/min 11.4 liters/hr 3 gals/hr. 505SS 10/300 .69/21 304 Stainless Steel, 190cc 35/150 1 7/65.6 Stainless Viton .4 pints 505HPSS 10/500 .69/35 Steel 190cc/min 11.4 liters/hr 3 gals/hr Mas. Capacity* : 1140cc/min 68.4 liters/hr 18 gals/hr 1140cc/min 68.4 liters/hr 18 gals/hr Carbon Steel, Stainless 1514cc 1514cc/min 9084cc/min 506 10/300 .69/21 35/150 1.7/65.6 Steel Steel, Brass, 3.2 pints 90.6 liters/hr 544.8 liters/hr Delrin, Nylon 24 gals/hr 144 gals/hr "Traps are designed to operate at one discharge per minute for one year before rebuilding is required. Operation at more than one discharge per minute may require more frequent rebuilding. VAB.0001028453 SNAP-TRAP SNAP-TRAP CaOutNoMmNaStAiTc1 i. J Hi Am HANKiSON $arrtH. :h4 v A wmig *1t>a4o# *0023 for MANUAL Off AUt CLDSC * - ^ 0N 1^14 |f*. 4|l> H-phH-; V 4. PAfMtl <** CAOUNTDOEMNASTAITCE OffAIN MNKiSQN ., ... _/' Mi mtt * mm ?,g .1"^ 3003 ROW MANUAL DRAIN CLQtA * * OPN MODEL 503 and 504 pmncmjy||k^L^^| IWMfii MODEL 507 and 508 ENGINEERING DATA Model 503(1) 507 |2) WlH|l| Min/Max . :> . L Operating :sa Prewar PS 16 MM# Afl nil iii Vn dieeiii i ( I> `i M Hi/Max Operating ; '% Temp. <T C 20/150 1.4/10.3 35/120 1.7/48.9 504(1) 20/175 1.4/12.1 35/120 1.7/48.9 50B (2) S3-? .. .......................................................................... . -3. iCfl:iji?',. - :'pf*iM*S?i! .- ------------------------- -- - - Polycarbonate Polycarbonate (3) Buna N Seals Metal w/ sightglass Delrin Viton Seats Discharge p#r.,'"'i| ". Operation . V V.-.--- - ? . . b-1 . .4.1,, v V-ri!!*. --iwiiii I l'i 20cc 04 pints 20cc/min 1.2 liters/hr .3 gals/hr |1| Top inlet connection. (2) Bottom inlet connection. 13) Metal bowl guards are available 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 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 (12), 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. 1-<:*: i - -f,, >h'-. . ,J- s.:- v - ' rt, :... 1 ' - -J>C PISTON CLOSED POSITION (11) METAL WASHER PILOT VALVE -13) BAFFLE (2) MAGNET .nfj !-. is_: r?.> wmi&=--s 1 V - +. ,i. lv^. : f < i. n, : .' - CONDENSATE t 'y r.-^VS- y-. v M /-j--: -\-A' X'- (9) MANUAL DRAIN PASSAGE (1) FLOAT V i- r <.. (4) MAIN tv s :o; DISCHARGE CHAMBER l! I T: .4 IIlit- J .S! (12) ORIFICE FILTER t i :v.V v~.V- . t: (10) ORIFICE (5) PISTON v .> (7) LOWER PORTION OF THE CHAMBER (6) STAINLESS STEEL FILTER (8) OUTLET PISTON OPEN POSITION VAB.0001028454 INSTALLATION: Typical Installations: Inlet Piping: Trap should be installed below level of device being drained to allow condensate to flow into the trap by gravity. Strainers to protect the trap from undue particulate contamination 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*6" K2" yl6" Tube 507, 508 3 % " 7" ?6" NPTF BOTTOM INLET CONNECTION TRAPS V pi *- . -.V:- ., r,, ' y-. " . jL i: "'Vv^SV-y'' -.vi;: : :/' B 505. 505HP, 505SS, 7" 505HPSS 00 l\> li" NPTF jL-yi-aPc't.wk-'-'A j`j. :F.Vrx: -i:::V j-.--v.ss 506 7" 13%" 1" X" NPTF 503* 504 Choosing the Correct Size HANKISON Trap 507' 508 505, 505 HP. 505 SS, and 505 HPSS 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, after- cooler/separator, etc.) or length of pipe line on which you wish to install a trap. system. Do not use any reheated air temperatures. C) 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 l,C above by your system's flow rate in SCFM. tl. 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. 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 I.B.1 and proceed to step 1,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. O cc < oLL CO tr LU CL *- C E_ ou O LU Vi UzJ O O CC LU 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 n rr: iL * * D: - i - ^ A^ P ' i ^j T. , \ f` -** rTM 1 \ 1 fp ' ' \T" H ki 4 * F I i . MEMPHIS, TEMM. -"7 (901) 767-7894 VAB.0001028455 Printed in U S A. CONOCO V PLANT /&*#/><r*J ITEM NO SERVICE ENGINEERING CENTER PONCA CITY. OKLAHOMA SPECIFICATION SHEET PROJECT * ft A F E NO DATE MAOE BY APP'O BY f/' 8 M NO . W O NO INO NO REO NO P O NO b -/O f -A P^4t?n,u comfouto >, Afc2i2l / V/6G^,sry' &r- r~sfrUJ>P /44/BPiAl n&snouzb CLg/kJ .s/' ----- Rt.rg,< T~ / ( ro,/7y?7 r1 A-J ZX=> ft /u L<OQy 1 7^5 (SsrS s) 2-4 ^,50^ CO O &* CoaJ DgA)^ g 2. Ps//- 0,5. K/OOC 02__ rc^yipAndij V<Q / Cc//d C r< 'fc77<z t Zcr. /2*sZ> 7>rt= Oc>i&bt//uij MEET ViABDJQQ1Q28456 .ft'*i n 4 mmm r ***- In <> RfYAB.0001038459 m rw Y^B.0001028460 M k cciNO(:o r ENGINEERING CENTER AM.NO T m ijmiiQi CONOCO PLANT ITEM NO SERVICE ENGINEERING CENTER PONCA CITY. OKLAHOMA SPECIFICATION SHEET PROJ JT7&9* A/O.. .nstc lot o*4: Af E.N * - OATE . O NO MAOE I APP 0 BY 'i ^ INO NO REO NO M NO P O NO ss&r/?77c*fs '-SO 8&e.&n*tA/6* Atfc CiajB. /t-e 7?AE M/c TRajk m/?r &1/AS 7Z> vc TSirff* /Vq&wi/U- Ifre^urz . PZiCt fijgflMYtAL. Ci C/clow?^^g' SCf^y) A/orrrtfH- D^Sl6(d J /rl/rtr 7~sfn/i> jC-P tV &ewtotjen =5^ P'S foMAgAf Q&ancirfi /7?Ar&& , A L g/O SiQKl /tftCfcrtf C-ewJ $>7iUi 04*1M f>jU>?f\ tCJAJ G& yv^ QArJ \J j4PPi MEW MH* * MEET VAB.000102B464 I T Bulletin 3400-1 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-deptb, 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 flange opening for models 3407 through 3415. FEATURES: High efficiency separationremoves 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 fi jA.-.-A i IS f ifcH: 1 : >. i jTk ik r-.*... mA .V B c ;;So vJk Lg|r:^;0 j0> 60 fi - JlijiijiUjjKiiii liiiij;! s!'!l'l!*!1!|| !^!ni Ml: ilIlI !:!!!!:! Hiitfi ii: i S i: Ii i!ii-i''i; nil1 !!!! i\ ii'! ! if 1,1 nl [1.1 1 t''.#tY* i'V 1 > i .l' iI jSii. i,M'j;j*1:: ISiSirii P p- Ail * t 6 AB.0001028466 1 Maximum Flow (SCFM)* 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 2,1 BAR 5.9 13.7 21.5 39.0 78.0 117 234 468 702 936 1170 1870 2570 3280 4450 40 PSIG 2,8 BAR 7.2 16.7 26.2 47.7 95.4 143 286 572 859 1140 1430 2290 3150 4010 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 9420 100 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 13,400 150 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 PSIG 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 80.8 127 231 462 692 1380 2770 4150 5540 6920 11,100 15,200 19,400 26,300 300 PSIG 20.7 BAR 41.2 96.0 151 274 549 823 1650 3290 4940 6590 8230 13.200 18,100 23,000 31,300 Note: Pressure Drop--Separator/Filter--At rated flow conditions, when removing liquids, pressure drop will be less than 1 PSI {.07 bar) nominal (1.6 PSlt 11 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 sleevefs] 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 In/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 3401-3 3402-1 3402-3 3402-5 3402-7 3403-1 3403-3 3404-1 3405-1 3406-1 3407-1 3408-1 3409-1 3410-1 3411-1 3412-1 3413-1 3414-1 3415-1 AUTO DRAIN 3401-2 3401-4 3402-2 3402-4 3402-6 3402-8 3403-2 3403-4 3404-2 (2) (2) (2) 3407-2 (2) (2) (2) (2) (2) (2) 12) (2) MAX. AIR FLOW (SCFM) 100PSIG 15 15 15 15 35 35 35 35 55 55 100 200 300 600 600 1200 1800 2400 3000 4800 6600 8400 11.400 AIR INLET/OUTLET CONNECTION HOUSING (BOWL/VESSEL) TYPE WIDTH (INLET TO OUTLET) & HEIGHT (INS.) %" NPTF %" NPTF %" NPTF %" NPTF %" NPTF %" NPTF l/?" NPTF %" NPTF %" NPTF 1" NPTF 1" N PTF 1%" NPTF iy2" NPTF 2Yz" coupling (3) 2%" coupling (3) 3" coupling (3) 3" flange 4" flange 4" flange 6" flange 6" flange 6" flange (5) 8" flange (6) 8 oz. polycarbonate CD 8 oz. metal w/sight glass 16 oz. polycarbonate 16 oz. metal 16 oz. polycarbonate 16 oz. metal 16 oz. polycarbonate 16 oz. metal 32 oz. metal 32 oz. metal 48 oz. metal 136 oz. metal 205 oz. metal 5" pressure vessel 5" pressure vessel 8" pressure vessel 10" pressure vessel 12" pressure vesse 12" pressure vessel 16" pressure vessel 20" pressure vessel 20" pressure vessel 24" pressure vessel 3% x 6% 3% x 6% 3Ya x 10% 3YaxQ7/8 3Ya x ioa 3% x 9% 3K x 10% 3Kx9% 49/ie x 11 Vt 49Ax m 4%6 x 13Yz 5% x 22% 5K x 30Y 15% x 40% 15%x 42)4 22% x 42% 16% x 44%6 20 x 51% 20 x 51% 24 x 32% 28 x 5914 28 x 59% 33 x 63^16 1% 2% 2% 3% 2Yz 3% 2% 3% 5jj 57/s 9% 18 21 29% 32% 215 325 330 335 430 625 630 1150 MAX. OPERATING PRESSURE (PSIG) MANUAL DRAIN 150 AUTO DRAIN 300 150 300 150 300 300 300 300 300 300 200 (4) 200 (4) 200 (4) 200 (4) 200 (4) 200 (4) 200 (4) 200 (4) 200 (4) 150 175 150 175 150 175 175 175 175 (2) (2) (2) 20_OJ4) (2) (2) (2) (2) (2) (2) ` (2) (2) REPLACEMENT FILTER SLEEVE NO. 0734-1 0734-1 0734-1 0734-1 0734-2 0734-2 0734-2 0734-2 0734-3 0734-3 0734-3 0734-5 0734-6 0734-7 0734-7 0734-72 0734-73 0734-74 0734-75 0734-78 0734-711 0734-714 0734-719 4 c ating temperature of 120F ------------------- -------------- oz. polycarbonate bowl also available with optional metal guard. _ratn plugs standard on models 3405^ 3406 3407-1. and 3408 through 3415. For manual draining a valve is recommended For automatic draining Hankison automatic drain traps are available Model 3407-2 includes, as standard, an integral model 505 Trip-L-Trap' For models 3405. 3406 and 3407-1 use Trin-L- Trap model 505 For models 3408 through 3415 use Trip-L-Trap model 506. Standard Trip-L-Traps have a maximum working pressure of 300 PSIG (20 7 bar) (3) Flanges are available J U ' *ir; is) f SCFM anb lamer8'^ f! ange* ccmri ect Ions3 av^Ji la bl SS U fSS 3 PS'G (2 7 bar) are available 1200 <3408> models are ASME code constructed and stamped (6} 10" flange connections available HANKISON CORPORATION, Canonsburg, Pa. 15317, Phone(412J 745-1555, Telex: 81-2452, Cable: HANKORP PRICE AND ORDERING INFORMATION AVAILABLE FROM: HANKISON \ 'S ` L 1 3a ! J - * 1 r'a\ 'w t '!M1 'nJ. ' VAB.0001028467 BREATHING AIR MODIFICATIONS CLASS "A" DESIGN ABERDEEN PVC PLANT INSTRUMENT SPECIFICATIONS Item No. CV-101 SV-101 Service Control Valve Safety Valve Location WS-101 WS-101 PG-101 PG-102 PG-103 PG-104 PG-105 h PG-106 PG-107 TG-101 Pressure Gauge Pressure Gauge Pressure Gauae ** Pressure Gauge Pressure Gauge Pressure Gauge Pressure Gauge Temperature Gauge F-5 Reactor l-AI-105 l-AI-113 l-AI-109 l-AI-117 l-AI-121 WS-101 WS-101 VAB. OOO1028468 CONOCO PLANT ENGINEERING CENTER PONCA CITY, OKLAHOMA SPECIFICATION SHEET CONTROL VALVES A'c A PROJECT DATE _ A. F. E. NO. W. O. NO REO. NO. MADE BY z /tta B. M. NO. INO. NO. g nP O. NO APP D BY GENERAL 1 ITEM NO S TAG SERVICE 3 LINE SIZE 4 M AMU 1* ACT UHER 5 6I MODEL NO. G>C S?-7?C:*J 1 SERVICE CONDITIONS 7 j FLUID e 1 TEMP F NORMAL MAX. 9 PRESS , INLET., NORMAL MAX TO A P MIN. NORMAL MAX. 1 1 MOLECULAR WEIGHT A P I. 12 SP CM W 60 F. '< F T. 13 14 1 15 j 16 t 17 1 1b WEIGHT ' VAPOR IN OUT VISCOSITY F T. ft P. RATE NOR LB HR iSCFHi GPM HATE MAX LB HR tSCFHI GPM NORMAL FLOW Cv ClA/tV W/S--iOt /" 1 1 1 ~/6>3/ Ad ___________________________ ____________________1 t\J/f fE2f<L 1 go 75 90 85 1 1 III 1 * 1111 AO & O 1 cpo.9<o 1 ________ % H~T 1 1 1 19 [ 20 1 21 1 22 I 23 1 24 1 25 1 26 1 27 I 28 flOOY SIZE BOOT | PORT SIZE TYPE * ANGLE OR GLOBE MATERIAL ENO CONNECTIONS BONNET Cv _ __ LUBRICATOR ] ISO VAL HACKING TRAVEL INDICATOR /" | Cs I I ni - 1 ! ---------------------------!--------------------------- TRIM I 29 TYPE INNER VAL | NO OF PORTS _ ... 1_ 1 1 1 I 30 PLUG ft SEAT MATERIAL I 31 1 J2 TYPE ACTUATOR / // // PkJ|^ Tv j 1 33 1 -j4 FAILURE POSITION 1 mIII in Ifc W) AkjU ^A c tu \T <T [/ |-- \f OPe/J J 1 35 I 3C 1 37 | 38 POSIT IONER K input signal OUTPUT SIG|MAfc*v UYPASS GAUGES manufacturer MODEL NO. ` j 39 NOTES ACCESSORIES ______________________________________ I I INOICMTS ITEM CHANCCD ON LATEST REVISION, tit INDICATE* MANUfCTuHlH TO GIVE KIOUCSTCU INf Mt V / 24 L'J A T ION IN Hit QUOTATION RHRMp mmm or 02346 CONOCO PLANT ENGINEERING CENTER PONCA CITY, OKLAHOMA SPECIFICATION SHEET RELIEF VALVES g PROJECT___ GENERAL t ITEM NO. & TAG RELIEVES EQUIPMENT NO. MANUFACTURER MODEL NO. SV-IOI '/VS -SO/ SERVICE CONDITIONS FLUID REQUIRED CAPACITY MOL. WT. SP. GR ID VISCOSITY 1 I COMPRESSIBILITY FACTOR IGN PRESS OF EQUIPMENT OPERATING RELIEVING TEMP FLOWING RELIEVING BACK PRESSURE DIFFERENTIAL SET RE 17 ACCUMULATION BLOW DOWN A.F.E NO DATE Sjn4?o MADE BY APP'D BY. B. M. NO.. W. O. NO iNQ. NOREQ. NO P. O NO 20 CODE REQUIREMENT 21 EXPOSED AREA FIRE INSULATION THI 23 OTHER BASIS 24 DESIGN DETAI DESIGN TY 26 SEAT TYPE 27 BONNET (OPEN OR CLOSED* 2 8 INLET SIZE. RATING. FACING OUTLET SIZE, RATING. FACING CALCULATED AREA ff !5qU2,%iso*- rZ 3 1 ORIFICE LETTER ACTUAL AREA [ MATERIALS 32 BODY | BONNET 33 SEAT & DISK I \ 1 34 GUIDE ft RING 1 30 SPRING 1 36 BELLOWS _____________________________ _________________________________________________________________ 1 \1 1 | 1 ACCESSORIES : 37 LIFTING LEVER 1 PLAIN OR PACKED! 3Q GAG 1 39 CODE STAMP 40 CAP \ SCREWED OR BOLTED) 41 OTHER j| NOTES MANUFACTURER SHALL VERIFY SELECTION OF ORIFICE SIZE AND MATERIALS VALVES SHALL MEET DIMENSION REQUIREMENTS OF API RP-526VALVES SHALL MEET TEST REQUIREMENTS OF API RP- 527 SUPPLIER TO COMPLETE FORM BY FURNISHING INFORMATION FOR BLANK SPACES Hi v.'. i.' -i : IWIIHIUHU n-im** *MI f r 11 III 1 1 V " "" " 1* 1 I.n --------------------------------------- -------------------------------------------- Nl, 1 1 VAB.0001028470 REV. . -436-S PLANT COhK)CO Tf k. i ENGINEERING CENTER PONCA CITY. OKLAHOMA SPECIFICATION SHEET PRESSURE GAUGES PROJECT- AFX NO _______ OATE MADE BY APP'D BY B M. NO W.O NO (NO. NO. REO NO . P. O. NO 1 TAG INSTRUMENT PERATING (OPERATING 3 -to/ 4 5 /Q7 ~so3 6 7 8 pC? ~ 9 PC? - fo 7 10 11 12 13 14 15 1 16 17 181 19 20 1 1 21 1 1 221 1 23 f24 25 I 26 27 1 I 28 B 29 30 31 1 32 (33 I 34 I 35 I 36 I 37 138 1 39| I " %l/T Pressure /Tvs-surr ^ntlA Q-lgo >-*>&- 0-5^ 0 - S**O' 5*- O-l&o I I I 75 75" -?<> 7s 75 | 80 1 70 I 70 70 7o la I 9o F-^ggACTCC.--------- 1 / ~/?jr-/o5 I f-*?jz-?> 3 I /-4iz-?aQ f~PJZ~ify 1 I l-HX-'Zl I ^5vq/I 1 -1 1 11 | I I ____ 1 11 1 I A 11 -/oz gJl fan Tfcfr !LtL QUOTATION WILL NOT BE CONSIOEREO IF SUPPLIER OOES NOT COMPLETE RIGHT HAND COLUMN. SHEET :YAko(M3V02M71- - V B 3 1 Tfa-iOl 41 5 6 7 8 9 101 111 12 1 1 1 | 1 1 7E-*M0er/?n*r i^uT^ir^zSs i I- *fct___ i i" A | \ASS~tOl (1) ALL GAUGE ELEMENTS TO BE BIMETALLIC UNLESS OTHERWISE NOTED. mum* MnWflWIflJWl T Iff --- -rt ' i ii i i <niii*~-fimi 4 BREATHING AIR MODIFICATIONS CLASS "A" 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, services, line number, insulation requirements, and piping specification. Sample Line Description 2-AI-101-N-M2-1 lL Sample Piping Specification M2-1 i Service Designation Used AU AI Insulation Requirements N E Nominal Pressure Rating M Piping Material Piping Specification Insulation Requirement Line Number Service Nominal Line Size, Inches 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.0001028473 w PROCESS PIPING SCHEDULE * PROCESS ENGINEERING DEPARTMENT Date Project Plant Made By Line Designation Prom Z-&T-JO 2- / e-/v jrcv/or. WS-io 1 Vu6~lOl wft /- tfu-to 3 -erm2-i /-Qui-io4 - ni2-1 / `/?T-/e6-A/-ttfZ~/ ) /-4r-/o<1-N~niZ-t f-4-T. -ftp -*j-m z>f t -ajz-tf f -a(mt- / f/z-Au-\\Z--i*AZ-l t //3 / - f?T-i/4-/d~ %- f / _y?x - ttS-Af'/ttl-f \/ i ~/ZT-it~r ~ rJ-MZ-) / 'At 'tPJ 7t-4-ft4-*X-MZ' "rta-i zo.e+*mi- g&VAt ex&nvtf rttK- LjAj >AjaJ /=-*&/ UM rvfV-to, ptA^ncttti' ccmP. | / -ffT->Q 5 f -&X ~/06 F-fO j_____________ 004/, Uftlfc 1&v-l Q PHo3 F-/C 3 v-fi o^e ^turrv t -fiT -fC/j /-/9JT-//0 ~-/o 3 AUtt-Mir fp Tf4g tHOtX V: F-Vg?Z OX/h> F*i o2 Ajuo [Itt mioCxa / - >9j~ -//? RA TOt V 4-Z- 1\7 /~-i 4- F - >c?4 -- ( Flour Rate Lb/Hr (Hot bpsd: 2 4ypo If dbL(Zw\ it&CFW) 5CFm /_ZSCjPj2^ /2 /2 N 7# 7$ I 6e458 |g><y/sl\O ii3 I 5Q.fe 70 }75 I 0 - 45ff 1|o'm3 1 tyO,*> 7o 1 7? 1 >-46?\|g>-o//srlL~.|cs> I SO.O "70 1 75 1 62-3 11 i'Ot 1I -- 1 -- "70 1hs Bt p.45^ 1 o<ctf$ 11 <9,7/4 j_J375 70 |175 I <W5if \0`Ot?5 | Q-7$4 I _ 3 3, Zy5 7c> | 7S If V 4581 frQtfsl 0,1$41 3 70 7S I7*01 I f c. 4 r* J r PROCESS PIPING SCHEDULE PROCESS ENGINEERING DEPARTMENT Date Project Plant Made By BREATHING AIR MODIFICATIONS CLASS "A" DESIGN ABERDEEN PVC PLANT v VII. WORK LIST 1. Remove existing air water separator and air receiver from the breathing air station. 2. Remove the activated carbon from the existinq F-5 reactor, and clean the inside of the existing reactor. 3. Fabricate and install the new air-water separator, WS-101. 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, to.WS-101, and tie 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 intothe 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 drain trap, TP-101, on the existing F-5 reactor. n------------------fr.i :. -fta,* h*. -1ft- . ***** -gwimHimiiittmHiK^miittm^ihmi^ .r.. .m-iHiK-'i^aemiiiiiMiii^rfmiiiimirik^ ........................................................... . ...................,'MM:-*m* >' ; iJ: w v^a- "pf*i . 1 miffWiMWiBU fflifftn*IffWtwNWdiMWH 4 < X? If'l A ' *Ml *' -HI ^ ^I?1 4t ' I 'ffl* II- fcOHI ft i-^r' i^M: VAB.0001028477 '`TUlTT'r ............... ..................-Mur---iih-hm U'*--unn- - \i` I,-jHi Hltp :im .`mimhh:*- iT:ri|i .kxi* 'iia* 4 l ! i i i l i i I i i i i i i i i jiliiii^1ttjKmihiik. * . ,IM -i.j-. i. Lf --1H- ir-ll -I lH.-. n. -SJ - J * '1HH NOZZLE SCHEDULE VAB.0001028479 ............ . ......... . ................ Nl ipr: 5 r 1P..L .................... .. I4pa..-.jaa^a|. iifl, ........................ .............. ........................................... ,. "IL..........................................................................................................................................................nmm................................................... .................................. IMMlMlMPim ........................................................................... ... fFn luiMimnmfffmm "......... AB.0001028480 mmmmmmrmm nrnrnmmm wmliiimMiviiiiimiwimvipfiiiiMVBimMmwiimp NMMPPHHMHMHMi "*r-^nipiliinmnpiuqHimnmpHniin'^ini^iiiiiiiiginn I ; VAB.0001028481 wmmrnum' ihiUfc.j. imiihmiL..Jil................. 4>-,HMirnnrn1H ihiUrii. n. j . ..Jill. . m VAB.0001028482 mHHMP nnmimn'^uujnimi::: 'j i. . ,d-i. ,P- . | I** C* I ,1-jip- |ilS- .r dP;J` H t Hull irr. ;i ir^1. 'l-rtP-f'i VAB.0001028483