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(SUPPLIE OTHERS) PRESSURE RELIEF VALVE HAZLETT. H -PVR -1 (BLUE LABEL) URVA14210 Ii:1 1/4' COPPER TUBING LENGTH TO SUIT JOB CONDITION. DRILL 3 TAP VENT PIPE FOR 113 NPT MALE CONNECTOR. r I HOOK N VENT LINE To EITHER PORT MARKED 'LOW PRESS' ] PUT PLUGS INTOPUT ENTERED RREMANNG OPETER INTO ENNRPORT PORTS MARKED 'MGH PRESS' Gasoline Vent Manifold(Exc. Diesel_j p Tank. Level Correction Gage ■■■■■■..u...■■...■.■■■■■■ou■■ddo■orf■■UNN0mom o■m■mmoss oo■uo■■ormenm■■00000unu■■uou■musom■oo■ DISPENSER CANOPY VAPOR RETURN LINE (EXISTING) Moo F -I VAPOR VALVE (P/N II -33000) COAXIAL HOE I SUPPLIED BY OTHERS I Figure (A) (WITH BREAK -AWAY) Diso. Vapor Valve B� reak-away. .4H `�lli5�5 r / TOP VIEW m NEMA 56 MOUNT v )NLS NPT FEM. 8 8 INCL NFD DISPENSER MP ISLAND DISPENSER VACUUM PUMP d MOTOV, -i Ijj INSTALLER:PLACE UNIONS AT ALL PORTS ,TS IN ALLAT�OI N. -OUTLET TO VENT. - FLAME ARRESTOR LL1. INLET FROM ISLAND OESPENSER GROUND MOUNTED VGP-2/2A VAPOR RECOVERY 5Y9TEM • SEE TABLE 71 OF INSTALLATION MANUAL SLOPE SLOPE FROM OTHER DISPENSERS PROCESS UNIT LOOP t )DIN IA LCV PONT SLOPE O D SLOPE IL� Pry VALVE- IVAREC SHOWNI OVERFILL LOOP 20 FT HER. •• COLLECTION UNIT MANIFOLD VENTS TLC GAGE N/ p Q ALTERNATE ATE RETURN PIPING VacuRite Tyip cal Instillation_(Isometric Vieeew) ■■■00000uuru■nu■oo■oou■ouuuuueor■o■o■u■ouo■000■ r EI 3.��•:•tital T GAILY. ItHR 1' PORI AMID CAP AGE AWE 1-1/4 NPT FEM. ■ ■ bUrEET-TT-UNK VE 8L04ET6VEN'r T. ■ i TANK 3t ■ I � i LL. _ J v CHE[N ■ ASSEMBLY NPT FEM. ■ 0I042 3TCET-TO--PROCESSOR UNIT /■ m-vr FRONT VIEW FLAME ARRESTOR WI NIT) TO ELECTRICAL' — CTR) A SIDE VIEW Note_ SCH MA IC 5 Installations with more then 16 ea. fuel hose DWG. 10 I outlets will require two Vapor Collection units. Collection_ Unit_ Detail ■■rn■uuuuomrun■ourmm000■■ro■■ou0000nuou00000u■ 1' sTe' rvv i I I I Lid/'i xS SECT PROCESSING UNIT Thermal _Processin4 Unit DISPENSERS VAPOR FRG4 I I tt PIBW ELNus -------------I-------) NOTE: COMPDNENTS DEPICTED IN HEAVY LINES PART OF HAS STECH ASSEMBLY 01042. PROFILE VIEW VAPOR FROM VAPOR TO COLLECTION COLLECTION UNIT OUTLET UNIT INLET TO LOWEST CCTAFE — 1. NOTE: FOR RETROFR TO NON- MAlfOLCED BALANCE SYSTEM CAP OFF UNUSED LRGTNS OF ENSTNG VAPOR RETURN PRY PLAN VIER NOTE: THE DRAIN CHECK — ALLOWS LIOUID FROM V.R. NOZZLE SIDE TO DRAIN TO STORAGE TANK WHEN COLLECTION UNIT IS OFF. AND TO PREVENT VAPOR FLOW OUT OF STORAGE TANK WHEN COLLECTION UNIT IS ON. P-TrapDra_in Check Installation ■■ommmmm■dvor odorNNE MEN rruoro■ odr■r n■o■ruu000Mumma HASSTECH GRAIN CHECK ABBEABLY .IB42 'OFF' Ill GENERAL INSTALLATION REQUIREMENTS 1. Piping above grade shall be Schedule 40 galvanized pipe. 2. Piping below grade shall be fiberglass or corrosion protected steel. 3. Pipe threads shall be clean cut and coated with pipe Joint sealing compound and tightened to refusal. 4. Piping between Collection Unit and Process Unit to slope down towards Collection Unit. ( Mln. 1/8" per ft.) 5. Collection Unit Inlet and outlet lines shall be sloped to allow drainage of liquid to a storage tank or a dosed sump with access for pump out. ( Min. 1/8" per ft.) 6. Process Unit shall be located outside of classified area if less than 10 feat from Collection Unit. ( See instillation instructions ) 7. Ground mounted Process Unit to have a 12 foot high overfill protection loop ahead of Process Unit. ( See Instillation instructions) B. Ground mounted units to be protected against vehicle damage by bumper posts or other suitable means of protection. 9. Process Unit to be located so as to meet minimum distances to vents and fuel transfer points specified by California State Fire Marshall. 10. All lank openings shall be vapor tight with a submerged fill and a positive seating dry break. 11. Pressure Decay Test (GARB TP -201.3) to be performed to ensure system integrity. ( See instillation instructions ) 12. Air -to -Liquid ratio test (CARE TP -210.5 or TP 201.5A) to be performed after installation to verify proper system operation. NOTE: 1. Refer to instillation instructions supplied with unit for specific and detailed directions for instillation of system. 2. Instillation to comply with the following California Air Resources Board Executive Orders A- Phase 1 Vapor Recovery System Tow Point Fill System #G -70-2-G Exi bit #2 B. Phase II Vapor Recovery Line System Manifolded Piping System #G -7043 -AB Exibit #2 C. Phase Two Dispenser Configuration Hasstech VacuRite System #G-70-164 Required Equipment The VacuRite" Vapor Recovery System requires one BASE UNIT for each station and a set of DISPENSER COMPONENTS for each NOZZLE. The BASE UNIT is composed of the following components: City Component 1 Processing Unit (VCP -2 or VCP -2A) I Collection Unit I Electronic Control and Status Panel 1 Pressure Vacuum (Pi Valve 1 Tank Pressure Switch 1 Tank Stick Correction (TSC) Gauge The difference between the VCP -2 and VCP -2A models is the processing unit. The VCP - 2 Proc;ssoc 1. Has multiple burners, and measures 36"06"x96". 2. Has the inlet flame arrestor in the last vertical run at the processing unit. The VCP -2A Processor: 1. Has a single burner, and measures 20"00"02". 2. Has an inlet flame arrestor installed in the processing unit. The following DISPENSER COMPONENTS are required for Ali NOZZLE: Qly Component 1 Nozzle (see Table 12.1 for Manufacturers) 1 HI -Flow Coaxial Hose (see Table 12.1 1 CFC -1 Flow Control Valve A/R CFC -I to 3/4'• Adapter A/R 1/2" a Vapor Hose 1(Per Dispenser) 3/4", 1", or 1 1/2" Flame Arrestor OPTIONAL ITEMS: Out -of -Tank Drain Check In -Tank Drain Check Hose Break-Aways (See Table 123 for Manufacturers) All other items, fittings, interconnecting wire, etc., need to be supplied by the installer. ■ V REMOTE VAPOR PNM I V REMOTE VAPOR PUMP ■ ■ Process Unit Distances CHOOKr GRADE LEVEL CHECK f- -MADE LEVELVALVE Canopy Mounted 0 VALVE : ■ ACCESS ACCESS ■ ■ FORT SEALED CAP ' TO COLLECTION UNITY P1AT SEALED CAP } To COLLECTOR UPT ■ � The distance between the process unit and storage took vents shall be no less than ; 20 tact. ■ s.rMEo To rAvts sono To TNNcs ■ Ground Mounted TANK TANK F,EsAPa TA"` FRssaPE ■ ---•—� VAPORS an The process unit shall be installed no less than 20 feet from a storage tank vent. P B ■ X ■ EHON DI�EFHts DSPETlR1 X TANK' ■ x ■ x LIOUD DRANs ro' x nm x ■ X x THE TANK x x d The process unit shall be elevated according to the following distances from x ■ x x ni77f VALVE X VALVEDMIN PIEVENTING a storage tank vent: B TO BE THE LONEST POINT IN THE VAPOR X AuLDKs RYE I PV'rRS X X X ANY B/�'ZW N ■ ■ Minimum IVACVUM $ DEr ]WIN X x LICUIO TO FLD1 x OW THE SYSTEA AAD ■ ■ x x FREELY To TAli x PRESS ANds. ri Distance Height Ab Ye Ground . ■ x x N I ■x xX X x (SIX X x r greater than 50' 0" ■ x X xx ■ ■ X x x X X x xx : ■ 41-50' 18" an x X x x ia•rRIC ■ X X X LRA L^UAIN ■ ■ ■ 31 -40' 30" i FIGURE 1 FIGURE 2 ■ CFEOC VALVE NO COLLECTION DECK VALVE D. RW CQ.LECTION ■ i 21 - 30• 42" ■ ■ ■ ■ VALVE IS NORMALLY FLOODED AS SHOWN Not less than 20 46" Ref. California State Fire Marshal Regulations as contained in Title 19, Califomia a Administrative Code, Paragraph 1918.63. Vapor Recovery Isolation P -Trap & Check Valve REVISIONS I BY California Petroleum Equipment Inc. P.O. Box 9364 Fresno Calif. 93792 06(209)276-1881 Fax(209)276-1881 Oc. #432613 A B C61 HAZ R