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INSTRUMENT LETTER IDENT :ATION TABLE PIPING SYMBOLS FlRST4.ETTER SUCCEEDING4ET7ER✓S MEA8t1Rm ORREADOUT OR INITIATING PABNVE OUTPUT -c _w BALL VALVE (N.O./N .C .) fl r FLEXIBLE CONNECTION/HOSE M� MAG (MAGNETIC) FLOW METER VARIABLE WXMER FUNCTION FUNCTION WIOOF1ER AAM MUFTIS STAGE A Analysis B Burner Combustion -04--►/- GATE VALVE ( N .O. /N.C.) SIF-- UNION V-CONE FLOW METER VACUUM VESSEL i } 7 DIFFUSER C Conhd D Dtffwwtid 3-WAY VALVE (FAIL OPEN TO -- -- FLANGE CONNECTION rl VARIABLE AREA FLOW INDICATOR E Vobge geK (pllrt y PATH SHOWN BY ARROW) Elenmt CONCENTRIC REDUCER/ z CUHAMBEROXIDATION F Flay Ram Ralb (Fraction) -1�)- CHECK VALVE INCREASER CALIBRATION COLUMN i 00000 O Glow. vl&Mrkg L11.ia 00000 Device GLOBE VALVE QUICK DISCONNECT COUPLING CARBON ADSORPTION VESSEL H Hud High My I Gamont (ElaWfol) hdh�br larddar ALTER ower Sun -I Y'i H 1 I- BUTTERFLY VALVE (N.O./N .C .) ® BUTTERFLY GATECATALYST BED J P K Time, Tbro Time Ram Cadrtl SbOon Schedule of Charrgo STATIC WATER LEVEL L level Llslld Low SELF ACTUATED PRESSURE ® FILTER/SILENCER M Mannantm Mldole, CONTROL VALVE BLOWER SEDIMENT COLLECTION/ II Imanrelw CONE- BOTTOM TANK SEPARATION TANK O 8u Raetrktlon AIR FILTER/DRYER p N t7n Ipayeyam Point (TM) PRESSURE CONTROL VALVE CENTRIFUGAL PUMP Caluwcdon O Ouendly Intawam, Tomihe -}^�{- - PLUG VALVE (N .O./N.C.) �L AIR LUBRICATOR R Radiation Reoord 9Sw11rh.Speed, FmquwcV Safety METERING PUMP T Temperature Transmit RELIEF VALVE U Multivadeble WWW cion MuMenabn Ab1NRnalon FLAME ARRESTOR V Vbradon, VaNe, DengCLOSE-TOP TANK OR DRUM &, II II II II II Mochmial Lrva aM MOTOR ACTUATED NVQ/\ PROGRESSIVE CAVITY PUMP An*Ws S SOLENOID ACTUATED W Waiyd, Foy WN HEAT EXCHANGER X Urdamlbad XAdaa AXIS Undl8Unclassifieded Unclassified Unda.eteed SPRING-OPPOSED, SINGLE- Y Event, Siam or YA % Rotary, Compute, L-L3 ACTING CYLINDER ACTUATOR �C AIR COMPRESSOR PUMP Preseme Convert T Z Position, ZAds Driver, Acbelor, Oimeralon UndeseiBed Reel A ANTI -SIPHON/VACUUM RELEASE AIR RECEIVER TANK Conhal FJermerd a 0 n DOUBLE DIAPHRAGM PUMP STACK EXAMPLE NOTES FOR TABLE e4 AIR RELEASE 1 , ANY UNASSIGNED LETTER IS DEFINED FIRST LETTER AS A USERS CHOICE LETTER WHICH IS LIQUID RING PUMP INTENDED TO BE USED TO COVER SP-xx SAMPLE PORT SUCCEEDING LETTER MEAN114G FOR A PARTICULAR PROJECT. OR MODIFIER MODIFIER 2, 7C IS USED TO REPRESENT ANY 'SPECIAL' FUNCTION OR VARIABLE AND xx(t ) MAY BE DEFINED AS FOLLOWS: SIG NAL (z) DISTINGUISHING CHARACTER SPECIAL FUNCTION OR VARIABLE INSTRUMENT OR FUNCTION SYMBOLS PROCESS DESIGNATORS SIGNAL DESIGNATORS IDENTIFICATION USED TO DENOTE MORE THAN SSG SONIC SIGNAL GENERATOR DIRECT PROCESS CONNECTION AJ ANALOG INPUT ONE IDENTICAL INSTRUMENT PH PH PRIMARY PROCESS LINE (LIQUID) INTHESAMELOOP SG SPECIFIC GRAVrrY (VAPOR) PNEUMATIC BINARY SIGNAL .AO ANALOG OUTPUT TAG NUMBER O FIELD LOCATED INSTRUMENT PRIMARY PROCESS LINE (VA _ - - - - - - • - - • - • - - ' AUXILIARY PROCESS LINE (LIQUID) ELECTRIC ANALOG SIGNAL DI DIGITAL INPUT NORMALLY NOT ACCESSIBLE TO OPERATOR _ . - . _ . - . - . - . _ AUXILIARY PROCESS LINE (VAPOR) -\- - ELECTRIC BINARY SIGNAL DO DIGITAL OUTPUT AS PACKAGED PROGRAMMABLE LOGIC CONTROLLER (PLC) OR DIGITAL CONTROL AS AR SUPPLY LINE 'ti ELECTROMAGNETIC OR SONIC SIGN,L (NOT INTEGRAL TO CONTROL SYSTEM IA INSTRUMENT AIR SUPPLY UNE GUIDED) PIPING CODES INDICATES SOURCE/DESTINATION PROCESS EQUIPMENT AND DRAWING WHERE STARTED CU COPPER OR CONTINUED GCS GALV. CARBON STEEL STREAM IDENTIFIER (VAPOR) PE POLYETHYLENE O STREAM IDENTIFIER (LIQUID) PVC POLY VINYL CHLORIDE 40 SCHEDULE 40 PIPE 80 SCHEDULE 80 PIPE PROCESS STREAM CHARACTERISTICS Vepar conunaadarr m h pprm,r C« ow"redone are In % w yl Tare Tool Cama Saaem oeevgdom R" Casdlltar c72-0CE 1 ,1-0(a Cmmr+de HV0C4 Bac ne AVOCs Meln r oxygen DhAde IIJ Dual Phase Emallon Wok 75 =wrr% �W Hg, 7W F 121 8A 918 111.1 02 8.8 2A 18.3 18 ❑B VepmUgtdd Separator (V-1) EBluent 75 odym -20' Hg. 700' F 4.3 10.0 95A 120.1 02 10.3 240 18.3 1 .8 © MUSSAmp OMBwr (V-0) EBFrra 150 ecK 25 pelp, Ar F 0.04 DDt 0.05 0.14 0 0 0 21 0 QD Cortdasllon Chamber (E3) Inluard 225 sdm, 2 prig, 300' F 1.5 3.3 319 40.7 0.1 34 0.8 1940 0.5 © Ca Musdon Chamber (E•3) E}dard 225 sdr4 0.5 Paige 950' F 0.0 0.11 19 1 .21 0.0 0.1 0.0 17.9 211 Liquid Catpntretlar an In mfco¢arwAeer COKarCidkne are In rrarlflJJrlerOarf V11TA TOW TOW 060001 Hy*ombm Sheem Dwalplon Flow CondC7 ,one o1,2AXE Z Cldr orms HV001 Bene AVOCe Fud M6mn 7D8 Hertbmr- Fe . Mn - ® Duel Phue Ex1racflon Web 20 gpm. ,20' Hg, 70' F 879 423 103A 253.4 25 149 293 512 1185.8 4932 24 08 VaportL$gA Sspaaeor (V-1 ) Bkmt 20 gpme -2W Hg, TW F 89 42 10,3 25.3 023 1.8 289 48.7 11888 483.2 24 © mw* Ewamon Weft (EWP-07m) bAtrad 10 mm, 1 pale, TO' F 8.3 16A 23 39,1 OA 0,0 OA 0.0 111040 475,0 0.0 (0] MueFShgs DFOaser (V4)) Wkwt 30 amm I peq, 70' F 8.8 82 7.7 299 0.15 1.1 18.7 324 11812 487.1 1 .8 P.EV DATE REVISION APPRtD FRT BY Q MuIti.Sm" Dlf tmir (VA) Ellkanr 30 Wm 30 prig, 7W F 1.3 12 0.014.b 0.02 0.18 18.7 324 1127.1 479.0 09 REV OF GAC (V-11n2) OW" 3D Wm. 25psige700F es 45- ms <t 1127 479 0.5 LEGEND TO PROCESS DIAGRAMS Concentration sinam Y to Marinate Cancenitsu n level PAX) far the oo rommi, SNEEr NONE C. VONSETiFJI C. VONSTLZTEN D-8032.25-04 Nola Conoentretlom d oordenr'unte stwn erns mgeded b De encaarlWad durbq arYartem eterbq. Averspa online o now Antli0 s are agarmd b be sppn drnd* 40% of 8a In" ocrloenhatlorl. I. of 19 1 / 13/98 A CJIDdBUAKIR, PE J. OUINN, PF b 8032.25 IF SHEET IS LESS THAN 22x34- DUAL PHASE EXTRACTION SYSTEMCbwrAcW Additions �saPDta¢ Injection Rats �� Tangaah" T IS A REDUCED - T�( M UNION PACIFIC RAIL YARD F, _ y f mant SCALE REDUCED ACCORDICRDINCLY, Ei.\111 TRACY, CALIFORNIA HCL bNerSon (0.4% HCL Beurdon) 358 rtiDMarhrinb err 215 rrdllRara4glr 50 pog 7W F m\cm\Owcs\e032\25\e03225a4.avc 72lVIROt4NQrNCAL RESOURCES MANAGEAffiQT