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Home My WebLink AboutRISK MANAGEMENT (NO DATE) INSTALLATION,OPF.RATION 8~ MAINTF' NANCF. INSTRUCTIONS V- NOTCH CHLORINATOR.. SERIES V-75 .... · . .. - ...~t~ .-. ~,, 7:~..... ~ .... :~.,,~.~:.. ::. L.. ~, . . ~ WALLAEE [ TIERNAN 25 MAIN STREET, BELLEVILLE, NEW JERSEY 07109 · .. BOOK NO. WEB. 910.175. :.. '- .... 8L77 .JEB 910. V-75 C" OR,NATOR · ' TABLE OF CONTENTS TITLE DRAWING/TEXT PAGE 9ery-lmportant Information 3 Pages Regiona) Offices. 1.010-1 Introduction V75-1 Typical Installation-3 to 200 lb/24 hr 913.061 Typical Installation-250 to 500 Ib/2'4 hr 913.O62 Typical Installation-Connections to Ton Container 913.063 Typical Installati'on-COnnection"to ManifOlded Ton Containers 913.064 Performance-Operating Water Requirements 910.175.1 Performance-Operating Water Requirements 910.175.2 Performance-Injector Operating Water 910.175.3 Instal 1 at ion 910. 175-3 Installation 910.175-4 Installation 910.175-5 Installation 910.175-57 Preparation for Operation 910.175-6 Preparation for Operation 910.175-10 Operation 741-8 Flow Diagram 25.150.I81.011 Theory of Operation V75-8 Service Notes-General Care of Equipment 910.175-I1 Service Notes-General Care of Equipment 910.175-12 Service Notes-General Care of Equipment 910.175-13 Service Notes 910.175-9 Service Notes 910.175-14 Service Notes 910.175-15 Troubleshooting with a Manometer and Vacuum Gauge V75-10 Troubleshooting with a Manometer and Vacuum Gauge V75-11 Troubleshooting with a Manometer and Vacuum Gauge V75-12 -~, Troubleshooting with a Manometer and Vacuum Gauge V75-13 Troubleshooting with a Manometer and Vacuum Gauge V75-14 Troubleshooting with a Manometer and Vacuum Gauge V75-15 Troubleshooting with a Manometer and Vacuum Gauge V75-16 Troubleshooting with a Manometer and Vacuum Gauge V75-17 Troubleshooting wi'th a Manometer and Vacuum Gauge V75-18 Service Notes 661-1~ Parts-UXA, UXB23766 V-75 Chlorinator 25.150.20.017A&B Parts-U23841 Pressure Regulating-Pressure Relief Valve 25 150.002.O22 Parts-U23842 Pressure Regulating-Pressure Relief Valve 25 150.002.032 Parts-U23153 Vacuum Regulating-Vacuum Relief Valve 25 150.03.021 Parts-U19200 Injector Body 25 150.06.012 Parts-Chlorine Rotameter Component's 25 150.21.011 Parts-V-50, V-75 Injector Throat and Tailpiece Details 25 150.26.021 Parts-Auxiliary Cylinder Valves 50 150.01.011 Parts-Plastic Main Connection for 3/4" or l" Solution Lines with Corporation Cock 50.845.06.011 Parts-Main Connection.for 1" Solution Line and 1-1/2" Main Connection 50.845.06.012 Parts-Main Connection For 3/4" or 1" Solution Lines and 3/4".or 1" Main Connection 50.845.06.032 Spare Parts List 910.175 SPL Chlorine Pamphlet NSM 73-11004 Chlorine Manual Booklet /~ I"NOT_~E: Numbers appearing in the lower margin of. each page are for identification . ~%~,L_e, purposes only and are not intended as numer~'cally consecutive page numbers. iE ~', .. VERY IMPORTANT INFORMATION This page provides in brief a summary of information of rgent importance relative to. SAFETY - INSTALLATION - OPERATION - AINTENANCE, Important information related to SAFETY of Chlorination equipment installations' is provided in the following listed sec- tions of the Chlorine Institute Manual. In the interest ofSAFE operations this information must be read, understood and practiced by equipment operators and their supervisors: Employee SAFETY ~ Training Sec. 6, Pg. 21 Medical Aspects & First Aid Sec. 7, Pg. 23 Emergency Measures Sec. 3, Pg. 16 Health Hazards Par. 1.4, Pg. 4 Other Hazards Par. 1.5, Pg. 4 Using Containers Par. 2.2.5 Pg. 9 With respect to the format used in this Inst~ruction Man- ual, information of particular importance to the equipment operator is highlighted by the use of the words "NOTE", "CAUTION" & "WARNING", each having the particular significance listed below: INOTE: Information of particular importance related to equipment operation. I CAUTION.. Lack of observance of this information wi ll result in equipment malfunction or damage. WARNING:LACK OF OBSERVANCE OF THIS INFORMATION CAN RESULT IN A HAZARD TO PERSONNEL & EQUIPMENT, THE ENTIRE CONTENTS OF THIS MANUAL AND THE CHLORINE INSTITUTE MANUAL SHOULD BE THOROUGHLY REVIEWED AND UNDERSTOOD PRIOR TO INSTALLING AND OPERATING THE EQUIPMENT, VII-lB VERY IMPORTANT INFORMATION CAUTION: At time of initial installation, when chlorine supply lines have been disconnected for any reason and on a routine daily basis, thoroughly check all joints, connections, and equipment for possible chlorine leaks and immediately correct any that may be found. WARNING: DO NOT TOLERATE ANY CHLORINE LEAKS. AS SOON AS THERE IS ANY INDICATION OF THE PRE- SENCE OF CHLORINE IN THE AIR, TAKE IMMEDIATE STEPS TO CORRECT THE CONDITION. CHLORINE LEAKS NEVER GET SETTER. CHLORINE LEAKS ALWAYS GET PROGRESSIVELY WORSE IF THEY ARE NOT PROMPTLY CORRECTED. CAUTION: The two most common causes of chlorine piping leaks are: 1. Re-use of gaskets. This should never be done. Always have an adequate supply on hand and use new gaskets. 2. Improperly made-up threaded joints. See Chlorine Institute Manual pg. 20 sec. 4.3.3- Installation. IWARNING: DO NOT STORE OR FEED AMMONIA GAS IN THE SAME ROOM WITH CHLORINE. CONTACT OF THE GASES MAY RESULT IN AN EXPLOSIVE MIXTURE. WARNING: TO ENSURE PROPER AND SAFE OPERATION OF THIS EQUIP- MENT, USE ONLY W&T LISTED PARTS EXCEPT FOR COMMER- CIALLY AVAILABLE PARTS WHICH ARE IDENTIFIED ON PARTS LISTS. THE USE OF UNAPPROVED PARTS CAN RESULT IN EQUIPMENT MALFUNCTIONS HAVING HAZARDOUS CONSEQUENCES. Vll-2B VERY IMPORTANT INFORMATION NOTE: Do not discard this instruction book upon com- pletion of installation. Information provided is essential to proper & safe operation and maintenance. NOTE: Additional or replacement copies of this instruction book are available from: Wallace & Tiernan Division Pennwalt Corporation 25 Main Street Bel]evi]]e, New. Jersey 07109 Additional or replacement copies of the CHLORINE MANUAL are available.from: The Ch]orine Institute, Inc. 342 Madison Avenue New York, N. Y. ]00]7 NOTE: In an effort to make product improvement availa- ble to W&T customers as quickly as possible, pro- gressive changes in design may be incorporated into W&T products from time to time that are not in~ediately reflected in the instruction book. If such a change has apparently been made in your equipment and does not appear to be reflected in your instruction book, contact your local H&T Sales Office for information. Please note that equipment serial number is essential for effective communication and proper equipment identification. VlI-3D REGIONAL OFFICES INSTALLATIONi~, OPERATION, MAINTENANCE AND SERVICE INFORMATION Direct'any questions concerning this equipment which are not answered in the instruction book to the Reseller from-whom the equipment was purchased. If the equipment was purchased directly from Wallace & Tiernan Division, PENNWALT Corporation, contact the nearest office indicated below. UNITED STATES ATLANTA KANSAS CITY ~uite 350 P. 0. Box 875 1800 Century Blvd., N.E. Shawnee Mission, KS 66201 Atlanta, GA 30345 (913) 384-3933 (404) 876-443) BOSTON LOS ANGELES P. O. Box 6 .. P.O. Box 1858 Wa)pole,~ MA 02081 West Covina, CA 91793 (617) 762-1620 (213) 962-2472 CHICAGO PHILADELPHIA 2540 South 27th Ave. P.O. Box 385 Broadview, IL 60153 Wayne, PA 19087 (31·2) 626-8593 (215) 687-4240 CLIFTON PITTSBURG 642 Broad Street 98 Vanadium Road Clifton, NJ 07013 Bridgeville, PA 15017 (201) 472-7300 (412) 563-2800 DALLAS SAN FRANCISCO Suite 500 Suite 210 2949 Stemmons Freeway (I-35E) 881 Sheath Lane Dallas, TX 75247 San Bruno, .CA 94066 (214) 631-3680 (415) 871-1220 CANADA If the equipment was purchased directly from Wallace & Tiernan Division, Pennwalt of Canada Limited, contact the nearest office indicated below. ALBERTA NOVA SCOTIA 207 Fourteenth St., N.W. P.O. Box 3350 Calgary, Alberta T2N IZ6 South Postal Station (403) 283~0573 Halifax, Nova Scotia B3J 3J1 (902) 423-1522 BRITISH COLUMBIA ONTARIO ~7'0 Granville Street 925 Warden Ave. Vancouver, British Columbia Scarborough, Ontario MIL 4C5 (604) 682-4829 (416) 751-7561 MANITOBA QUEBEC )04-1280 Archibald Street. Room 207 Winnipeg, Manitoba R2J OZ3 4280 Blvd. Metropolitan East (204) 256-6004 Montreal, Quebec HIS IA2 (514) 729-2856 1.OIO-1E -~ : INTRODUCTION This instruction book provides installation, operation and maintenance instructions for the Wallace & Tiernan V-75 Chlorinator. This equipment is designed to control and mete~ the flow of 'chlorine, sulfur dioxide* or carbon dioxide* gas, to mix the gas with water and deliver the resultant solution to the point of application. .A simple manual adjustment permits s~tting_J:_he feted ra?___~_e a~t.any value within.the ranqe of the chlorinator. Once set, the feed rate remains constant unless manually changed by the operator. A glass tube rotameter .indicates the feed rate. . Your V-75 Chlorinator has been carefully assembled and tested. Proper installation and routine maintenance will insure op. timum operation and long life. NOTE: Thoroughly review the entire contents of both this book and the CHLORINE MANUAL (or its equivalent for other gases) be- fore installing and operating the equipment. Of necessity, more information may be given than applies to a particular installation and the reader should determine and disregard that which does not apply. While the manual is written in terms of chlorination, it may be applied to sulfur dioxide or carbon dioxide by substitution of the word Sul- fonator or Carbon Dioxide Feeder for Chlorinator, as applicable. Parts data will be correct for the application specified. *NOTE: If this equipment is to be used for sulfur dioxide of carbon dioxide, you must obtain the appropriate manual from your local gas supplier. TECHNICAL DATA Accuracy 4% of indicated flow rate Capacities Chlorine 3 to 500 Ib/24 hr Sulfur Dioxide 3 to 475 lb/24 hr Carbon Dioxide 3 to 390 lb/2h hr Feed Range 20 to 1 for any one rotameter Pressure at point of 'm'75 Ps[..~rnax.'~with flexible polyethetene application ..pipe- ~60.~~psi maximum using high pressu~ -hose or rigid pipe for='the chlorine =solution line Injector Water Supply 25-300 psi at 35°-70°F. 25-65 psi at 130°F max. V75-1G TYPICAL V-75 V-NOTCH CHLORINATOR INSTALLATION .3 To 200 Lb./24 Hr. 913. 061 (~ SIJ~mORT I~ CONDUIT OR sE.lEs v-~5 RECOMMENDED U 10119 HOSE CLAMF : ::'" RP68-4~20 ~e" PLASTIC 'r'L~NG SAFETY VENT(15 ET. LG.} CHLORINATOR P ~so?s S~CER MOUNTING DETAIL ®SUP.ORT ,. WCUUM GAU~E OR TROUGH ~ ' RP68-4105 ~/4" FLEXIBLE PLASTIC '- ~" --PIPE CHLORINE SOLUTION DISCHARGE .,'""-" P ZIIII-WIRE ~ .~ U lot20 NOSE CLAMP p ~5461oSCREEN ///~'" ( GAUGE,a~,'*STR AiNER · GASKET 3f4" INJECTOR WATER SUPPLY ~ SOLENOID VALVE ONLY - UX_ 495- ~ O.D. FLEXIBLE CONNECTION HEATER ~ ~ RUN WITH DOWN GRADIENT BACK TOWARD \ CYLINDERS. NO TRAPS. LEAD GASKETS '. NOTE--- LEtO G~SffET P~$19 NEOUIRED 247S-15/1~ O.D. ~r E~CN UN/ON CONNECT/ON· 2519 _35~ O.O. V~Z~UUM SWITCH (FOR WI~/NG SEE 50116.05.007~} )115 VOLT POWER SUPPLY AUXILIARY CYUNDER / "- VALVE [UNION TYPE) / i U 10120 · HOSE CLAMP . / · / -~ ADAPTER / NOTE--- CHLORINE CYLINDERS ~R~S 50-345 ~0 ~ ACCESSORY ITEM ~NISH~D ON~ ~ ~ ///' AND AS CHECKED ON THIS DRAWING. ~US~ T~' W~HES ON ""-- ~ION, ~ENCH ~ ~81NG ~T ~RN/SHED 8Y WS~ S~ATIQ~Y WHILE V~ ~ M~N~ (e.~. CHAIN) AS TO PBEVENT THEI~ ~ING K~KED OV~. ~ ~ W~NI~' T~ VENT LI~E MUST TERMINATE CAN. T CAU~ DAMAGE OR IN~RY ~ PVR~NNEL. ~ ~T TER~T~ WALLACE [ TIERNAN ~ DIVISION 25 MAIN STREET, BELLEVILLE. NEW JERSEY 07109 C~T .0. 913 .~' ~ TYPICAL VT5 V-NOTCH CHLORInaTOR INSTALLATION 250 To 500 Lb./2q-Hr. 913. 062_ [ 4 ) MOUNTING HOLES ~ ~-T FOR 5/16" BOLTS Q SUI~RT IN CONDUIT OR TROUGH PfPE SAFETY VENT { 15 FT~ LG.) FLOOR StJ~ IN CONDUIT CHLORINATOR OR TROUGH MOUNTING DETAIL fp-zIIII-wIRE ~. ' VACUUM P':55461-SCREE"] 'x~"' ' ~" STRAINER & SHUT-OFF VALVE P-2519-LEAD \ ~ I'INJECTOR WATER SUPPLY SAFETY "'x 1~ ONLr FOR/NTE~IITT~NT VENT ~ 5T~V~r- 570P OPERA77ON) ~'~HEATER ~) lib VOLT POWER SUPPLY UX_493 FLEXIBLE CONNECTION- RUN WITH DOWN GRADIENT RP68-4106 F' FLEXIBLE PLASTIC PIPE BACK TOWARD CYLINDERS. CHLORINE SOLUTION DISCHARGE NO TRAPS LEAD GASKETS P-251! U-$707 HOSE CLAMP (2) P-2476 -~5/~' O.D. CHAIN 3-AUXILIARY CYLINDER P47206 ADAPTER// VALVE(UNION TYPE) P48124 t'PVC MAIN CONNECTION-~ NOTE--- · TO REPLACE CYLINDER ~ DISCONNECT Al' THIS JOINT [] ACCESSORY ITEM FURIVISHEO OIVLY IF SPEC/F/CAttY LISTED IN QUOTATION A/VD AS CHECKED ON THIS DRAWING. ~ NOT FURtV/SHED 8Y W 8 Y 'WARNING; THE VENT LINE MUST TERMINATE IN AN AREA WHERE G,4S FUMES CANNOT CAUSE DAMAGE OR INJURY TO PERSONNEL. DO NOT TERMINATE THE VENT LINE AT ,4 LOC,4TION ROUTINELY USED BY PERSONNEL SUCH AS WORK AREAS OR PATHWAYS NOR NEAR WINDOWS OR VENTILATION SYSTEM INTAKES. ~ USE TWO WRENCHES ON AlL UNION CONNECTIONS, CAUTION: WRENCH ~CHLORINE CYL/IVDERS MUST BE SECURED IN SUCH A MANNER ON TUBING NUT MUST BE HELD ( e.~. CHAIN) AS TO PRE//E/VT THEIR 8SING KNOCKED OVER. STA~'IONABY WHILE FAIllE NUT IS TURNED. ( TUSIIVG NUT IS BRAZED TO TUBINg.) WALl.gEE TIERNAN DIVISION · 25 MAIN STREET. BELLEVILLE, NEW JERSEY 07109 cAr .o 913.062 REVISED AND AS CHECXED ON THIS DRAWING. TUBING NUT MUST BE HELD STATIONARY . I I I WHIL~ VAL~E NUT IS TURNED. ~TUBING . I --~- . OR TROUGH RECOMMENDED FO~ CHLORIN~ CONNECTIONS ALSO . WHERE GAS FUMES CANNOT CAUSE DAMAGE OB INJURY TO P~RSONNEL. DO NOT TERMINATE TH~ ' VENT LINE AT A LOCATION ROUTINELY USED BY ' VENT PERSONNE~ SUCH AS WOrK A~EAS O~ PATHWAYS NO* NEA~ WlNDOWS OR VENTILATION ~ M MOUNTING DETAIL SYSTEM INTAKES. ~ ~ P 2519 LEAD ~ FOAS~ET VACUUM GAUGE RP68-4106 I" FLEXIBLE PLASTIC ,o. GAUGE, I" STRAINER SHUT-OFF VAWE I" INJECTOR WATER SUPPLY SOLENOID mLVE (REQUI~ED FOB INTERMITTENT ) CHLORINE TON CONTAINER 50-165C FEET LONG FLEXIBLE CONNECTION P 47206 P-48124 PVC EA~ ~/THD~A~ ~ HEATER CONNECTION MAIN CONNECTION CONN~CTIO~ MUST B~ MAD~ VAL~E AS ILLUSTRATED' 115V 50/60Hz POWER SUPPLY (4)MOUNTING HOLES-~..~_~.~ ~ FOR 5.1; "OLTS ~ECI~ L Y LISTED ~ ~ TATION ~T FU~I~D BY W~T ~E~E ~ SEA~L~ ~TE~L S~T/~ARr WHI~ VA~ ~r IS ~RI~ V ~ED, (~NG NUT IS ~AZED C~TOR FLOOR ~CIFY LE~ WHEN ~[R/NG. P ~519 LEAD / ~ c~E C~CT~S AZSO ~S~ CHLORINATOR ~E c4~ ~. 9~,o~ a z~o.~o MOUNTING DETAIL WARNS: THE VENT L/NE MUST TERMINATE IN AN ARE4 PIPE CHLORINE SmUTION ~HERE G~S FUMES CAN. T CAUSE DAMAGE ~ IN~RY ~ PER~NEL. DO ~T TERMINATE THE VENT LINE AT U-~707 HOSE CLA~P A L~ATION R~TINELY ~ED BY PERSONNEl SUCH ~S WORK AREAS OR PATHWA~ ~R NEAR ~IN~S OR 6AU6[. I" STRAINER 8 VENTILAT~N SYSTEM iNTAKES. SHUT-OFF VALVE ~,",6,10,OR 15 FEET CP~ 115 ~LT ~ER S~LY ~WAR~ ~UX_235 4 OR6 FEET C~.' G~ ~H~ LAMP ~NNECTION MUST ~ MAD[ U~ER VALVE A~ ILLUSTRATED. P472~ ~HEADER GUARD :~.: 35-312L 35-312LI 70-242K 85-242K~ 100-242K 120-242K 150-242K 185-242K 210-242J 230-242J 265-242J 40-312L 50-312L 70-312L 105-312L 150-312K 175-312K 210-312K 130-312K 245-312~ 40-242K , 45-242K i105-165H 95-193J; 115-193J 170-165H 190-165H 225-165H 280-165H 260-193H~ 290-193H ~ 30-312L 30-312L, 00-193J 60-242K 70-242K 14,5-193J 175-193J 200-193H 230-193H 225-242J: 255-242J 50-242K 40-312L 60-312L 110-242K 135-242J 160-242J 190-242J 205-312K 240-3121, 35-312L 90-312K 110-312K 140-312K 175-312K ~ 50-193,J 55-193J 75-165H 75-193J 100-165H 180.-140G 190-140G 235-140G 300-120F 255-165G 295-165G 275-242J - 30-242K 35-242K 60-193J 45-242K! 95-193J 135-165H 170-165G 195-165G 275-140G 235-193H 270-193Hi 270-312K 00 20-312L 25-312L 40-242K 35-312L 60-242K 120-193J 145-193H 170-193H 225-165G 215-242J 245-242J 30-312L 50-312K 95-242J 120-242J 155-242J 205-193H 205-312K 230-312Ki 80312K 110-312K 140-312K 185-242J; ~ ..~_.,~ ~.~ ' 75-312K ~,:?.~','i~i 40.193J 40-193J 55-165H 65-165H 125-140G 145'140G 210-120F 255-120F 290-120FI 260-140F 300-140F 270-193G 22-242K 30-242K 55-193J 65-193J 90-165H 125-165G 180-140G 200-140F 225-140FI 255-165G 290-165G 270-312K '.-_,-~'~'"~ 'mm~lm~dl~ 20-312L 20-312L 35-242K 40-242K 80-193J 110-193H 150-165G 180-185G 220-165G 220-193G 240-193G 260-242H 20-312L 25-312L 55-242K 90-242J 135-193H 170-193H 200-193H 205-312K 230-242H 50-312K ,75-312K 120-242J 150-242H 175-312K 200-242H 230-312K 110-312K 140-312K 170-242H :' :-" 45-165H 45-165H 50-165H 80-140G 130-120F 150-120F 190-120F 280-99E 290-99E 255-140F 290-140F 295-165F 25-193J 35-193J 40-193J 80-185H 95-140G 135-14OO 155-140F 230-120F 275-120F 250-165F 265-165F 270-193G 19-242K 22-242K 30-242K 50-103J 75-185H 110-165G 145-165G 180-1,40F 220-140F 210-193G 240-193G 270-312K ZW 15-312L 17-312L 20-312L 35-242K 70-193J 10~-193H 130-193H 175-165G 215-165G 200-242H 230-312K 255-242H .... , :-, ~ 25-312L 50-242K 85-242K 115-242J 180-193G 180-193G 200-312K 225-242H 45-312K 75-312K 105-312K 140-242H 170-242H 135-312K 170-312K :~¥.~, ffi 40-140G 45-140G 75-~20F 85-120F 95-120F 135-120F 170-09E 215-99E 260-99E 300-99E :290-120E 290-165F '~ 25-165H 35-165H 45-140G 55-140G 75-140G 115-140F 170-120E 190-120E 220-120E 260-120E 285-140F :270-193G ~'?~:~ ,~,d~ lO-lg3J 30-~93~ 40-185H 55-165H 70-185G 100-165G 145-14OF 175-140F 210-140F 250-140F 1255-165F 1270-312K '~'~::' II~ 15-242J 10-242J 35-193J 45-193J 65-193J gs-lg3H 135-165G 160-165F 190-165F 220-165F 235-193G 255-242H : 18'312L 25-3~2L 40-312K 75-312K 105-242H 135-242H 185-242H 200..312K 225-242H .~ ./.,?,,:.;~.. 105-312K 135-312K 170-312K 195-242H : ~:/' .j 30-~20F 40-120F 70-ggE 70-99E 95-99E 125-ggE 255-7OC 275-70C 300-70C 255-ggD 285-990 '290-185F ' ' 25-140G 30-140G 45-120F 60-120F 80-120F 110-120E 165-990 190-99D 220-99D 235-120E 270-120E 285-193G -~' ~ 20-165H 25-165H 40-140G 45-1,40F~ 65-140F 105-140F 140-120E 170-120E 205-120E 215-140E 260-140E 255-242H ~ ~BM 17-193J 20-193J 30-~85H 40-165H, 55-185G 95-~65F 140-140F 170-140F IgS-140E 210-185F :245-165F 270-312K ,-,.- a~ 11-242J 15-242J 35-193J 35-103JI 55-193J 80-193G 120-165F 145-165F 180-165F 200-193G 230..312K 10-312L 14-312K 18-242J 25-242J! 40-242J 75-242H 110-193G 140-193G 170-193G 200-312K 225-193G Bill 17-312K 25-3~2K 40-312K 70-312K 105-242H 135-312K 170-312K 195-242H 225-242H 105-312K 130-242H 185-242H · ~ ' 45-99E 50-99E ~120-7OC 130-70C 155-70C 190-70C 225-70C 255-70C 280-70C 245-GGD 2?5-GgD 285-188F .~i ' 30-120F 35-120F 55-OOE 80-~9E 80-09E 110-99D 140-99D 175-99D 210-900 235-120E 270-120E 270-312K 24.140G 25-140<3 40-120F 50-120F 70-120F 105-120E 135-120E 170-120E 205-120E 210-140E 240-140E 270-312K 5 20-165H 24-165{3 30-140G 40-14OF 55-140F gs-140F 130-140F 155-~4OE 185-140E 210-185F 240-~85F 280-193G 15-193H 18.103H 30-165G 40-165G 55-165G 85-165F 115-165F 145-165F 180-165F 200-193G 230-312K 255-242H 10-242J 12-242J 25-193H 30-193H 45-193G 80-193G 110-193G 135-193G 170-312K 200-312K 225-193G 10-312L 11,.312K 18-242J 25-242J 40-242J ZS-242H I05-242H 135-312K 165-183G IgS-242H 225-242H 15-312K 25-312K 40-312K 70-312K 105-312K 130-242H 165-242H 65-?0C 65-?0C 75-70C ~'-OO-?OC 115-70~ ~50-?0C ~85-70C 220-?0C 285-?0C 285-;'0B 300-?0B 300-990 30-OOE 35-99E 40.9gEi 55-90E 75-99D 105-99D 130-99D 185-99D 205-99D 240-99D 275-990 285-185F 22-120F 25-120F 35-1201! 45-120F ~5-120E 95-120E 130-120E 155-120D 180-120D 210-120D 240-140E 270-140E N 15-~40G 2-140G 30-140~ 40-140F 55-140F gO-140E 115-~40E 145-140E 180-~40E 210-140E 240-~eSF 285-120D 15-165F 20-165F 25-165; 35-~85F 50-165F 80-165F 110-165F 145-165F 175-165F 210-185F 235-170D 260-193G 10-193H 15-193H 20-1931. 30-193H 45-193H 80-193G 110-193G 135-193G 165-193G 200-193G 225-193G 255-242H 10-242H 12-242H ~8-242H .25-242H 40-242N 70-242H 100-242H 130-242H 180-242H 195-242H 225-242H -- 45-70C 50-70C 55-70C /u-~u~., gO-70~., 125-70C 160-70B 185-70B 210-70B 240-70B 275-70m 285-165F 20-99D 25-990 30-gOD 40-090 55-ggO 90-ggo 125-99D 150-99C 175-g9C 205-99C 240-165F 270-g9C ~0 19-120E 23-120E 30-120E: 40-120E 55-120E 90-120D 115-120D 145-120D 175-120D 205-120D 235-99C 270-140E 15-140G 20-140G 25-140G 35-140E 50-140E! 80-140E 110-140E 145-140E 170-140E 205-140E 235-120D 265-120D 12-165F 18-165F 20-165F 30-165F 45-~65F 75-~65F ~10-165F 140-165F 170-185F 205-~65F 235-140E 30-70C 40-70C 45-70C 55-70C 80-70C 1 i5-70C 145-70B 170-70B 200-70B 235-70B 270-70B 270-140E m,~ 20-ggD 24-990 30-ggD 40*ggD 55-990 g0-ggc 120-99C 150-g9C 175-99C 205-99C 235-120D 265-120D 15-120E 18-120E 24-120E 35-120E 50-120E 85-120D 115-120D 145-120D 175-120D 205-120D 235-140E 260-99C 15-140F 15-140F 20-140F 30-140E 45-140E' 80-140E 110-140E 145-140E 170-140E 205-140E 230-99C 24-70C 30-70C 35-70C 40-70C 60-70C 100-70B 125-70B 160-70B 195-70B 225-70B 265-70E~ 265-120D 15-990 ~0-ggO 24-990 30-ggO 45-ggC 75-99C 110-ggC 140-120D 170-120D 205-1200 235-120D 280-9gC ~0 13-120D 15-120D 20-1200 30-120D 45-120D 75-1200 110-120D 140-140E 170-140E 205-140E 235-140E, 13-140F 15-140F 20-140F 30-140E 45-140E 75-140E ~05-140E 135-99C 165-99C 200-99C 230-g9C 0 2.S $ 10 20 .40 60 80 100 120 140 160 BACK PRESSURE - PSI USE OF TABLE: The figures in the table indicate the 910.175.3 shows that under the above conditions the minimum inlet water pressure required for each injector 120. injector throat will use less than half as much water throat and tailpiece combination. For example: To feed as the 193 throat. 100 pounds of chlorine per day against a 10 psi back .pressure, the table indicates that60 psi inlet pressure NOTE: V-50 maximum capacity limited to 100 lb ~s required with a 120F injector and only 35 psi inlet' chlorine per 24 hours. pressure is required with a 193J injector. Reference to , INJECTOR SELECTION WALLACE TIERNAN v-50 & v-75 CHLORINATORS - . DIVISION 2 5 MAIN STREET. BELLEVILLE. NEW JERSEY 07109 910.175.1 "~d ;, us~ Revised 9-75 CI"ILORINB BACK PRESSURB--POUNDS PER ~U~R INCH ~ED RATE LB/~4 ~ IN~CTO~ DATA 0 . 5 1~ l- 20 ~ ~ 80 10o 1~0 ~4o 10 .~e~g Wat~ ~I 15 85 110 135 165 200 230 260 I~or N~ ~D ~D ~D ~D ~D 99C ggC 99C 99C 99C 9g 20 ~ Wat~ PSI 20 30 ~ 55 90 120 150 175 205 230 260 I~t~ N~ 99D ~D ~D 99D ~D 9gD ~C 120D 120D ~ 120D -120 30 O~ W~ ~I 20 30 ~ 55 90 125 150 175 205 ~5 265 ~ W~ GPM 1.4 1.7 1.9 2~ 2.9 3.5 3.8 6,0 6,5 7,0 Znj~ ~ 193H 193H ~' I~F 99D ~D ~P 120D 120P 120D 120 ~ ~g W~ ~I 10 20~ 55 10S 130 165 180 210 235 265 O~ Wi~ G~M 3.5 4.8 4.4 3.2 3.5 4.0 6.1 6.6 7.0 7.4 ~: 75 ~ W&~ ~Z 16 25 30 55 95 130 155 185 245 250 280 ~g W~ GPM 4.4 S.5 ~ 4.4 5.8 6.7 7.4 8.0 7.1 9.4 I~ N~ 242] 2¢2] 242], ~42J 165~ 140F 140F 165F lg3G 193G 193G 150 ~ We~ ~ 15 19 30 45 100 145 175 1~ 200 235 270 z~ N~ 242K 242K 242K 24'2J 193H 193H 16SG 165G 193G 193G 193Q 2~ ~ Wa~ ~I 19 30 35 S0 10S ~30 175 215 210 240 270 ~K We~ QPM 7;4 9.2 10.0 ~2.0 11.2 t2.S tL0 12.0 16.0 17.0 18.2 [ I~ N~ 242K 242K ' 242K 242K 242~ 242~ 193H 193H 193G 193G 242H 2~ ~ w,t~ ~z 22 3s 40 ss go 120 170 - 200 220 240 260 ~ we~ GPM 7.9 10.0 10.9 12.5 16.0 18.5 14.5 15.5 16.2 17.0 / I~ N~ 242K 242K 242K 242K 242J 242~ 193H 193H 193H 193H 242] 3~ ~ Wa~ ~ 30 40 45 ~ 95 120 170 205 235 ~ 270 ~ Wn~ GPM 9.2 10.9 ll.S 13.2 16.5 18.5 14.5 15.6 16.6 18.2 28.0 ~'~ 1~ H~ 242K 242K 242K 242K 242K 242J 2427 ~93H 193H 193H ..~ ~ ~ Wn~ ~l ~ 50 ~ 70 110 145 1~ 230 260 290 _~;i~ I~ ~ 242K 242K 242K 242K 242K 312K 312K 312K r 312K 312K ~:~i[~ 5~ ~a~ Wa~ ~l 45 70 85 100 120 130 IS0 175[ 210 245 :~ ~ Wm~ GPM 1!.4 14.0 15.8 17.0 18.5 31.0 33.5 36.0 39.5 42.5 :=;~,i NOTES ~i 1. "BACK PRESSURE" is the w'es- --'ii~i sure al: point o£ application plus or ~:~: ". , . m/nus difference in elevation be- .- - ~ poiat o~ application and : ~ chlorismtor room floor plus friction .... - .,: , - lmm in aolugon line ~nd di~usor. .... 2. "IHIBCTOR lqtJ'MBER' is · W~T refeee~ce.fot identification ....... only. -.,a; 3. "OPERATING WATER PSI" iili 10 water pre,mire at injector inlet. r E T. OPERATING WATER REQUIREMENTS AVERAGE CONDITIONS FOR · ,,,! I WALLACE . E, TIERNAN /V-50, V-75',CHLORINATORS ~!t.~, , DIVISION , , , 910.175.~ INJECTOR OPERATING WATER , PERFORMANCE I 70 _ 60 50-- 40 3O 3 1 0.9 0.8 · 0.7 0.6 0'510 20 30 40 50 60 80 100 200 300 400 500 INITIAL OPERATING WATER PRESSURE (P.S.I.G.) NOTE: lO~e SAFETY FACTOR INCLUDED I~ W/~i.,I../~I::E F., TIERNP. N DIVISION 910.175.3 2,5 MAIN STREET. BELLEVILLE, NEW JERSEY 07109 ISSUE DATE I NSTALLAT ION LO CAT I 0 N Keep the following requirements in mind when selecting a location for the installatlon: ..................... 1. An adequate supply of clean water.is required togperate the j ecto r. 2. Install the chlorine solution discharge line to the po. lnt of appli- cation as directly as possible, A short run with a minimum of fitt'ings is desirable (most direct route). 3. Locate chlorine cylinders so as to require a minimum of handling. Support in such a manner as to prevent their being knocked over. Both in operation and in storage give the cylinder the protection measures described in the CHLORINE MANUAL-STORAGE, page 8. 4. Convenient access for operation, routine maintenance, and service is essential. WARNING: THE CHLORINATOR MUST BE VENTED TO OUTSIOE ATMOSPHERE. THE VENT LINE MUST TERMINATE IN AN AREA ~(HERE GAS FUMES CANNOT CAUSE DAMAGE OR INJURY TO PERSONNEL, DO NOT TERMINATE THE VENT LINE AT A LOCATION ROUTINE- LY USED BY PERSONNEL SUCH AS WORK AREAS OR PATHWAYS NOR NEAR WINDOWS OR VENTILATION SYSTEM INTAKES. INJECTOR WATER. SUPPLY The table on 910.175.2 will be used .to determine the injector throat and tailpiece to be installed in the injector. For example: The chlorinator is to feed lO0 lbs of chlorine per 24 hr. into the main where the. pressure is 40 pounds per square inch. From the table we find that the injector number is 14OF (the throat is #140 and the tailpiece is F) and also that our operating water pressure must be at least lO5 pounds per square inch. Note that the table is only a general guide. Your dealer may select, other combinations better suited to your specific installation. Install the parts as shown on the injector parts drawinq. After you have determined that the water supply is adequate, mount the chlorinator. Spacers P38078 are furnished for use between 'the chlorinator panel and the wall. As shown in the typical installation ' drawings connect a water supp]y line tO ~-+--~T~'~,- ~ the plastic pipe coupling below the in- ' -:- · jector. Install a shut-off valve and ~'-o' RECOMMENOEO strainer in this water line. If the chlo- rinator is to be operated intermittently in conjunction with a pump, install a .,,i,./.~~, ....... solenoid valve in the water line. A CHLORINATOR water pressure gauge .is desirable but MOUNTING DETAIL not requi red, , 9]O. 175-3G I NSTALLAT I ON .C__HLORINE SOLUTION DISCHARGE LINE For chlorinators of 3 to 200 pound per 2h hr capacity, 25 feet of 3/4- inch flexible plastic pipe is furnished for the solution discharge line. This line must be securely installed with clamps U10120 on adapter P47206 at the ectors and also at the main-connection For chlorinators of 250 to 500 pound per 24 hr capacity, 1-inch flexible :-!plastic pipe is required. This line must be secured both at the tailpiece ..... and the main connection with a clamp u3707. In all cases the solution discharge line must be supported and protected to avoid mechanical damage or kinking between the injector and the point of application. POINT OF APPLICATION ~..,-. Open Well - If the chlorine solution is to be applied in a basin, f~ume, channel, etc. where .there is no pressure, the plastic pipe need only be sup- ported so that the ~ree end is submerged completely (12-inch minimum depth) ~'~? and is located in a non-stagnant area. ~"~-"~ Main Connection - If the chlorine solution is to be applied in a main, · a 1-inch NPT tap or tee is required in the main. The solution tube should project into the approximate center of the main If the tube is too long it may be short'en by sawing off a portion. 'VENT Screw the hose adapter (packaged with the mounting spacers) into the opening at the top left of the chlorinator. A.15 ft.-length of 3/8-1nch plastic tubing is furnished for the vent line. It must be connected to the hose adapter with clamp UlOl19 and run to a point outside the building where a possible discharge of chlorine gas will not be objectionable. The line must run on a continuous gradient without traps and down toward outside atmosPhere. The free end must point down and be protected by screen P35461 secured with wire P21111. Where traps are unavoidable or a down gradient is not possible, provisions for condensate removal must be installed at low points (drip leg). WARNING: THE CHLORINATOR MUST BE VENTED TO OUTSIDE ATMOSPHERE. THE VENT LINE MUST TERMINATE IN AN AREA WHERE GAS FUMES CANNOT CAUSE DAMAGE OR INJURY TO PERSONNEL. DO NOT TERMINATE THE VENT LINE AT A LOCATION ROUTINELY USED BY PERSONNEL SUCH AS WORK AREAS OR PATttWAYS NOR NEAR WINDOWS OR VENTILATION SYSTEM INTAKES. IWARNING:~ CHLORINE CYLINDERS MUST BE SECURED IN SUCH A MANNER (e.g. CHAIN) AS TO PREVENT THEIR BEING KNOCKED OVER. 910.175-4G · I NSTALLAT I ON CHLORINE SUPPLY Position the chlorine cylinder and remove the hood. If an escape of gas, from the cap is detected check to see that the cylinder valve is closed before proceed ing. ............... WARNING: IF LEAKAGE DOES NOT RESPOND.TO NORNAL TIGHTENING -. PROCEDURE, TREAT THIS CONDITION AS AN EMERGENCY AND TAKE APPROPRIATE ACT ION. Insert a 15/16-inch gasket P2476 in the auxiliary cylinder valve~,f-u~.rtish- ed and connect the valve to the cylinder. Run a flexible connection U49~rom the auxiliary cylinder valve to the chlorinator. ~ill be'-necess'ar~Y'~o re- move a plug at the chlorinator to make this connection. Use new gaskets P2519 at both ends of the connection and always use 2 wrenches to avoid twisting the tubing. If you have a lO0 pound or ]arger chlorinator, cylinders of ch)orlne should be connected as shown on the 'Typical Installation" drawings. ! WARNING: DO NOT OPENTHE CYLINDER VALVE AT THIS TIME. SEE I PREPARATION FOR OPERATION. NOTE: The rate of withdrawal from a 150 pound SO2 cylin- der is 20 pound/24 hours; from a ton container 225 pound/24 hours. This is about one-half the with- drawa] rate of chlorine from the same size containers. Approximately twice the number of gas valves and fittings will be required for an SO2 installation as would be required for a chlorinator installation of like maximum capacity per 24 hours. LEAD ~ASKE?$ ~ ..~,>,~', ~ ! ROTANETER For protection in shipment, the rotameter and associated parts were re- moved after the chlorinator was factory tested. These parts, are separately packaged and should be assembled and installed as indicated. j! 910. 175-$C ~ I NSTALLAT I ON ETEI~ (Cont' d) / TO ~E~V~ ~OT~T~" 9~0.175-57 PREPARATION FOR OPERATION When all connections specified under INSTALLATION have been made, check the chlorinator as follows:~' .~ . I. With chlorine supply shut off, be sure there is water at the point 'i~ .... of appllcation ready for chlorination 2. Turn on the water supply to the injector. An indication of proper injector operation can be o§tained b~ removing the rotameter and holding a finger over the port where the top of the rotameter normally joins the head block. Slight suction should be felt. 3. ~hile .~ h& d:njector 'i S' oPe ~t'[ n~~' fi~d 'the '~'h'lor i ne supp ~rve the' floa~ in"the'~6tamete'r ~';'i'f "i't is 'not pesting on the bottoni~t~p, a.vacuum leak ahe~g" of the'ZF~tameter.L.i~.'indicated,~:'~-If thls'~'is observed may be ~'n ~n~'~ ~he~O-~:~l-O~i~'g~:,l!A~s: a. Through the seat in the chlorine pressure regulating-pressure relief valve. This can be determined by holding a finger over the safety vent connection. Refer to SERVICE NOTES for correction. b. Past the gasket (6) at the bottom of the diaphragm ~nit (3) on the chlorine pressure regulating-pressure relief valve. This may be cor- rected by tightening the diaphragm unit or replacing the gasket. c. Past the seat (4Al in the chlorine pressure regulating-pressure re- lief valve. This can be corrected by tightening the clamplng nut (ll). d. At the ring gasket P 44121 at the bottom of the rotameter. This can be corrected by proper lubrication of the ring gasket with a film of silicone grease and making sure that the rotameter is seated on the ring gasket. 4. Check the following to be sure all connections are tight: a. The extension chamber (32). b. The gasket P 44122 at the bottom of the vacuum r'egulating-vacuum re- lief valve. c. The connections of both ends of the plastic tubing on the gas dls- charge line to the injector. NOTE: Vacuum leaks ahead of the rotameter will result in ~ errors in chlorine Feed. Vacuum leaks after the rotameter (as listed in Step 4 above) may impair the performance of ~he injector. . .. Turn off the water supply to the injector. ~I0.175-6~ PREPARATION FOR OPERATION 6, Rech'eck the connections in the chlorine supply to see that all have ~een made up. Ensure that the auxiliary cylinder valves are closed. Open one main cyl,nder valve sl,ghtly and check for leaks around th,s valve ~escribed in CHECKING FOR CHLORINE LEAKS. If a leak is detected, close the valve i.mmediateIy and do what is necessary to correct the leak. 7, Check the valve on the other cylinders as described in Step 6 above, valve and test all connections in the chlorine lines to the ~hlorinator, If ~ leak is detected shut off the chlorine supply and turn on the injector .. ~ter supply. r ~ARNIN~: DO NOT OPEN ANY CONNECTIONS TO CORRECT THE LEAK UNTIL AFTER THE READ IN~ ON THE CHLORINE PBESSURE ~AU~E REACNES ZERO, 8, Check For leaks in the chlorine pressure regulating-pressure relief valve b~ testing at the vent ~onnection. 9. Turn on the injector water supply and the chlorine supply. Turn the feed rate adjuster knob to the left (unscrew) to obtain maximum feed. If maximum indicated Feed rate cannot be obtained: a. Be sure no vacuum leaks exist. (See Step 4 above). b. Refer to SERVICE NOTES and TROUBLE LOCATING. 910.175-10B ) ?' ' t' ~. OPERAT I ON TO START !. Turn on the water supply to the injector. 2. Turn on the chlorine'gas supply. 3. Adjust the feed rate as desired. Rotation of the knob to the left increases the feed rat~. TO STOP i~.. For Short Period: `·... l. Turn off the injector water supply. ~"' For Extended Period: ). Turn off the chlorine supply. 2.Wait until the chlorine pressure gauge reads zero and then turn off the injector. INTERMITTENT START-STOP OPERATION Operation of the Chlorinator in synchronism with a pump or other appara- tus may .be accomplished by installing an electrically operated solenoid valve in the injector water supply line and connecting it so the valve is open when the pump is running and closed when the pump is shut down. CHANGING CYLINDERS CAUTION: When changing a chlorine cylinder, it is of the utmost importance that air is hot allowed to enter chlorine lines due to the corrosion problem encountered when am- bient air is mixed with dry chlorine. Therefore, all disconnections must be closed off to prevent entrance of air. It is unnecessary to shut off injector when changing a Cylinder. To re- place a cylinder, observe the following: ). Close cylinder valve and auxiliary cylinder valve. 2. Disconnect the auxiliary cylinder valve from the cylinder val've using wrench W&T Part No. P8201 3. If necessary connect or disconnect the auxiliary cylinder valve from the copper· tubing, use two wrenches W&T Part No. P8200. i!~ CAUTION: Avoid any turning of the nut brazed to the tubing as ; ~.; twisting the tubing even slightly sets up stresses :!',;, which become increaslngly susceptible to corrosion. ~t'~..,,,, WARNING: CHLORINE CYLINDERS MUST BE SECURED (e.g. WITH CHAIN) SO I .. AS TO PREVENT THEIR BEING KNOCKED OVER.. CHLORINE PRESSURE .~ /[,~ REGULATING -': PRESSbRE VACUUM REGULATING- 'RELIEF VALVE VACUUM RELIEF VALVE r'~l' PRESS. ~ ORiFiCE a~"TOae"WATER VACUUM -~ ~ Z ' (Mz~v. ~o Psz) ~"MERCU~r VACUUM , ~° ~m,,,=, ~ CHLORINEiNLETS (~8 "~IATER VACUUM) i FEED RATE Z ADJUSTER O INJECTOR WATER :... SUPPLY INLET ~ THEORY OF OPERATION .. GENERAL OPERATION Wallace & Tiernan chlorinators are designed to control and indicate the rate of flow of chlorine, to.~provide a simple means of setting the feed rate at any value within the range of the machine, to mix the chlorine gas with water, and to deliver the resultant solution to the point of application. ........ ~-' l~~ the V-notch Chlorinator described in this manual, the function of the injector is to produce a vacuum to draw chlorine gas from the chlorinator and to mix this gas with the water flowing thru the injector. The ball check and diaphragm check are built into the injector to prevent a back flow of water into the chlorinator if injector water supply is shut off with pressure on the injector discharge or injector discharqe line becomes restricted. Proper operation of the injector is dependent on the inlet pressure being sufficient- ly higher than the discharge pressure. The vacuum regulating-vacuum relief valve throttles the injector vacuum to maintain the proper operating vacuum on the downstream side of the V-notch variable orifice. , Chlorine gas under pressure enters at the chlorine inlet, and passes into the lower side of the chlorine pressure regulating-pressure relief valve. At this point, the gas pressure is reduced to less than atmospheric pressure be- cause the valve will not open unless a vacuum is produced by the injector. This provides a controlled vacuum on the upstream~side of the V-notch variable orifice. If, ~or any reason, the valve passes chlorine gas when the vacuum is not produced, the diaphragm will be raised from the stem to permit this gas to pass out the vent. From the pressure regulating-pressure relief valve chlorine gas passes thru a rotameter (feed rate indicator) causing the Float to indicate the rate of flow on an easily read scale. The rate of flow is controlled by the posi- tion of the V-notch variable orifice across which a constant differential at less than atmospheric pressure is maintained by the combined operation of the vacuum regulating-vacuum relief valve and the ~ressure regulating-pressure re- lief valve. In the event of failure of the chlorine supply, the vacuum regulating. vacuum relief va)ve tends to close. If the throttling valve does not provide a complete shut-off, the d~aphragm is pulled downward by the vacuum thus per- mitting air entering thru the vacuum relief port to pass the seat in the cen- ter of the diaphragm to satisfy the vacuum produced by the injector. V75-8A SER¥1CE NOTES i ~ GE_.~NERAL CARE OF. EQU ~PMENT The maintenance of any chlorinator is simplified if certain general pre- cautions are taken. These are usually easy to accomplish and will eliminate he3.1 costly maintenance and repairs by providing good operating condi, tions. The Ce ~i : sugoested precautions are as followsr . ~:, CHECKING FOR CHLORINE LEAKS he :' r CAUTION: While dry chlorine in non-corrosive, moist chlorine is / :nd [ extremely corrosive to common metals such as brass or ~nd steel. _ the WARNING: DO NOT TOLERATE ANY CHLORINE LEAKS. THEY ALWAYS GET PROGRESS/VELY ~,/ORSE AND MUST BE PROMPTLY CORRECTED. A small bottle of ammonia (initial supply) is furnished with each W&T 'Chlorinator For checking leakage oF chlorine gas at joints, valves etc. Hold !i:!';' the moistened dauber clo~e to the joint or suspected leakage area. If leakage i'. "exists, a white cloud will form. When a leak is found, immediately shut off to i?:.'chiorine gas supply and remove the escaped Qas by ventilation. At e- .r WARNING: CHLORINE GAS MUST BE VENTED TO OUTSIDE ATMOSPHERE. THE VENT LINE MUST TERMINATE IN AN AREA WHERE GAS FUMES CAN- ble NOT CAUSE DAMAGE OR INJURY TO PERSONNEL. DO NOT TERMI- is .NATE THE VENt LINE AT A LOCATION ROUTINELY USED BY PER- to SONNEL, SUCH AS ~,ln~K AREA OR PATHWAYS OR NEAR WINDOWS OR VENTILATION SYSTEM INTAKES. Eliminate the leak before proceeding. te i- Check chlorine connections For leaks once a day. Green or reddish de- ~ ~osits on metal parts indicate possible chlorine leaks. When any connection is Lhe broken even for a short time, the o~)~,~;nqs must be plugged to prevent the en- e- trance of moisture which, when mixed with chlorine oas, corrodes metal parts. No chlorine odor should be in evidence around equipment except when a joint is temporarily opened. le / NOTE: For leak testify(l, ~se Commercial' 26° Baume aqua - [ ammonia. Household ammonia is not strong enough. I MOISTURE . CAUTION: When any connection is broken even for a short time, plug the resultant openings immediately to prevent the entrance of moisture. Moisture must be excluded from any part oF'the equipment which is normally ex- posed to dry chlorine only. While dry chlorine is non- corrosive, moist chlorine is extremely corrosive to common metals such as brass or steel. 910.175-11A SERV I.CE NOTES GENERAL CARE OF EQUIPMENT (Cont'd) ~/ATER LEAKS NOTE: As a matter of routine maintenance, no water leaks should be tolerated~ All water leaks should be stopped as so,on as they are discovered. PLAST lC PARTS ..... Whenever threaded plastic parts are assembled, use silicone grease on the threads to prevent the parts from freezing together. In general, do not use tools to make up plastic connections. Make this type of connection by hand only. SULFUR DIOXIDE LEAKS The presence of a leak is indicated by odor. The location may be detect- ed by using the dauber moistened in a strong solution of aqua ammonia. Dense white fumes form near the leak in the presence of ammonia. CARBON DIOXIDE LEAKS Carbon Dioxide is colorless and odorless Leaks may be detected by the . application of soapy water to suspected areas or by means of commercially available detectors. Consult your gas supplier for additional information. CLEAN lNG CHLORINATOR PARTS If the rotameter tube, the rotameter f)oat, the V-notch plug or any valve seats become contaminated with impurities sometimes found in chlorine, remove and clean them. Most of the residue that accumulates on the chlorinator parts in contact with chlorine gas can be removed with warm water and a detergent. If further cleaning is necessary, metal, glass, and ceramic parts may be washed in a solvent such as perchloroethylene or trichloroethane (methyl chloroform). These solvents are available from most industrial chemical supply houses. Clean plastic parts only with warm water and a detergent followed by denatured alcohol, if necessary. All traces of solvent and moisture must be removed from parts which come in contact with chlorine before being returned to service. Do not use heat on plastic parts. WARNING: WHEN USING SOLVENTS, WORK IN A WELL VENTILATED AREA. I AVOID PROLONGED 0R REPEATED BREATHING OF SOLVENT VAPORS. ! SERIOUS HEALTH HAZARD. TOOLS When working with screws, bolts, nuts and other hardware, use the proper size tools to avoid damage to screw beads, nuts etc. This precaution wil) make it easi.er to remove these parts when necessary. 910. 175-12B SERVICE NOTES GEN~ERAL CARE OF.EQUIPMENT (Cont'd) A supply of gaskets must alwags be kept on hand so that all gasketed joints can be maintained ~n good condition. A regular replacement program on gaskets will do much to eliminate operating diff[¢u.lties. I WARNING: NEVER REUSE LEAD GASKETS WHICH ARE REMOVED FROM A JOINT. ALWAYS REPLACE WITH A NEW LEAD GASKET. 910.175-13A SERVICE NOTES.. INJECTOR The injector is a highly important part of the chlorinator since proper operation of the machine depends on good injector performance. The initial selection of injector parts has been explained in the INSTALLATION section of this manual. If operatin9 difficulties are encountered after the chlorina tor has been in operation, study Dwg. 25.150.26.02l and become completely familiar with the assembly of the injector. The following check lists points out some of the factors which may produce faulty injector action: 1. Dirty Water Strainer The strainer is required in the water line ahead of the injector to avoid plugging of the injector throat ports by foreign material. If sufficient material is allowed to build up on the strainer surface, the resultant pressure drop across the strainer reduces the injector operating water pressure. If the pressure drop is excessive, the in- jector will not be able to induct the required chlorine flow. Regu- lar periodic inspection and cleaning of the strainer will eliminate this possibility. 2. Installation of Injector The injector must be assembled as.shown on Dwg. 25.150.26.021. If faulty injector action is suspected inspect the gaskets and re- place them if there is any doubt about their condition. '3. Plugging of the In~ector Ports The injector will not operate satisfactorily unless all the ports are clear. This point is easily checked by visual inspection after the throat has been removed. If the injector water supply contains appreciable amounts of manganese or iron, these may deposit out on the throat over a long period and eventually interfere with the injector action. Such deposits are readily recognizable by their black or reddish color. They may be removed by immersing the throat in dilute (I0%) hydrochloric acid (known commercially as muriatic acid). WARNING: WHEN USING HAZARDOUS MATERIAL, OBSERVE ALL SAFETY PRECAUTIONS RECOMMENDED BY THE MATERIAL MANUFACTURER/ SUPPLIER. CHLORINE PRESSURE REGULATING-PRESSURE RELIEF VALVE If a vacuum leak'is detected in this valve as described' in Step 3a under PREPARATION FOR OPERATION and the valve plug P38054 is in good condition, check the seat in the center of the diaphragm unit UXA17643. If cleaning the seat does not correct the condition, interchange this unit with the identical part in the vacuum regulating-vacuum relief valve. Be sure each valve is assembled exactly as shown in the parts drawings. · SERVICE NOTES IDENTIFICATION OF SIMILAR PARTS ICAUTION: Certain parts are similar in appearance and can be physically interchanged. Doing so will result ~n malfunction. I. The plugs on top of the chlorine pressure regulating-pressure relief and vacuum regulating-vacuum relief valves, if interchanged, will create a potential hazard because the safety vent line cannot be con- nected to the correct point. 2. The vacuum regulating-vacuum relief valve must be assembled with the heavier spring P37699 on the bottom. 3. The spring P37683 in the chlorine pressure regulating-pressure relief valve resembles the spring P34588 in the injector but is made of lighter wire. NOTE: It is strongly recommended that only one unit be dis- assembled at a time and that it be reassembled exactly as indicated on the appropriate drawing. VACUUM REGULATING-VACUUM RELIEF VALVE The force exerted by the spring P37699 has been factory set by the in- stallation of spacers P41851 (zero to 5 as required) so that the maximum possible vacuum in the chlorlnator is 46-50 inches of water. With a suitable manometer or vacuum gauge connected to the head block in place of plug P38047 or plug P31295, this vacuum may be measured by shutting off the chlorine gas supply while the chlorinator is operating and then observing the manometer. In the event of the installation of a new spring P37699, a change in the number of spacers may be required. Each spacer added increases the vacuum by 2 inches of water. CAUTION: No more than five spacers may be used. ! PREPARATION FOR WINTER SHUT-DOWN If the chlorinator is to be shut-down for an extended period during freezing weather, the following procedure must be followed: 1. Operate the injector with the chlorine supply turned off until the chlorine pressure gauge reads zero. 2. Shut off the water supply and drain the line to the Chlorinator. 3. Drain the solution discharge line, and prevent any water flow into discharge line. 4. Remove the 1/4-inch pipe plug P31295 at the'bottom of the injector. Insert a pencil or similar object in the hole to unseat t'he ball check and drain any water in the valve. Replace the pi~g after draining. 910.175-14B '~ SERVICE NOTES PREPARATION FOR WINTER SHUT-DOYAN (Cont'd) NOTE: If the chlorinator is to be removed For storage, plug ~ the chlorine~inlet block with the plugs P250 shipped with the machine and seal all chlorine lines with rubber stoppers to prevent the entrance of atmospheric moisture-during the storage'period: ......... NOTE: If a pump is furnished, follow pump manufacturers instruc- tlons for shut-down. :.i ':. i: 910. 175ff15A TROUBLE-SHOOTING W OH TER ~ACUUMGAUGE.':':'~,~;~' '"' ,'~ ' Basic !. Measure the vacuum over the full range of gas flow. (Low, half and full feed)'. Instructions: 2. Compare what you measure with figures given below. If the figures are right, leave that component alone and check the next element. 3. Make additional checks (if necessary) to pin-point the problem. 4. Refer to detailed instructions for component disassembly and repair, if this check list indicates such work is appropriate. WARNING: TURN OFF WATER SUPPLY AND CHLORINE GAS SUPPLY AND RELIEVE PRESSURE IN LINES BEFORE PERFORMING ANY DIS- ASSEMBLY OPERATIONS FOR TROUBLESHOOTING PURPOSES. CHLOR I NATOR T YP I CAL VALUES OPERATING PROBABLE WHAT TO HOW TO FOR PROPER SYMPTOMS CAUSE MEASURE MEASURE OPERATION REMEDY Chlorina-. Insuffi- Injector Connect a vacuum Require 5" mer- Remove the throat and railway and tor will cient vacuum gauge of mercury cury minimum clean or (if necessary) replace the not feed injector manometer' to the for dynamic (gas parts. Clean the Y strainer in the at all- vacuum plugged i/4" port flowing) condi- water line Check the solution (no fora- on the.left side tions, discharge line for accumulation of meter in- of the injector, foreign material, hose kinks or a dication) -' If no gauge or partially closed valve. With gauges, -OR- manometer is With gas shut measure operating water pressure and will not available, re- off should see pressure at the point of applicat~n. come up move line from 25" to 28" mer- Compare with data in instruction to ful.i vacuum regulating cury static book. If system has a booster pump, feed. valve to injector, vacuum, check pump for wear, build-up of (Gas sup- Turn on water deposits and air leaks. If it is a ply to supply and place new installation, ensure that there chlorina- wet thumb over is no elbow or reducing coupling tor is inlet to injec- immediately downstream of the OK.) tot. Vacuum jector railway. Run full size pipe should pull straight up at least 18" before thumb down firm- any elbow or reducer, or use poly ly and raise a pipe and arrange in a 'smooth curve, "bump" on thumb, up, over and down, as required. NATOR ' TYPICAL VALUES OPERATING PROBABLE WHAT TO HOW TO FOR PROPER SYMPTOMS CAUSE MEASURE MEASURE OPERATION REMEDY Chlorinator Clogged CPAV Connect a single '17~' to 22"~ H20 Clean CPRV cartridge (valve either does CPRV vacuum, leg water mano- vacuum for low unit). Clean high pressure not feed at -OR- meter to the l/q" capacity machines gas line, chlorine inlet all or only clogged gas plug opening just , block and high pressure tube at low rates line will below the CPRV '10" to 15~' H20 .to cartridge. refuses to not 1et gas diaphragm. Close vacuum for high feed at high through fast chlorine cylinder capacity machines Tlghten gasketed joints or rates, enough to valve. Rotameter replace gaskets or diaphragm' Injector satisfy de float should drop unit as indicated by tests vacuum OK. mand to bottom stop, at left. Adequate fOR- If it does not, chlorine, in CPRV not it indicates an *See Addendum cylinders, opening due air leak upstream Chlorine to an air of the rotameter. pressure leak from a Remove vent line gauge may perforated and close off show a de- diaphragm or pressure relief creasing a gasket nipple with fin- reading when which' is de- get. If float then higher feed fective or = drops it indicatei rates are oUt of place a defective dia- attempted, phragm, or the stem plug Is not sealing. If it does not drop a bad or missing ... gasket under CPRV diaphragm unit or .. on top of CPRV dicated.~ CHLORINATOR TYPICAL VALUES OPERATING PROBABLE WHAT TO HOW TO FOR PROPER SYHPTOMS CAUSE MEASURE MEASURE OPERATION REMEDY Chlorinator '~[CPRV not CPRV vacuum. Connect a single '17" to 22" H20 Clean CPRV cartridge. feed OK at throttling (Probably leg water mano- vacuum for low high rates sufficiently too low at meter to the 1/4' capacity machines. but will not (held open low feed plug opening ]us! control at by a parti- rates), below the CPRV *10" to 15" H20 iow rates, cle of fer- diaphragm, vacuum for high. ric chloride capacity machines.! rust or dirt etc.); too much gas *See Addendum Rotameter Air leak up- See if float Visual - Check CPRV diaphragm, in- float does stream of is "alive" appearance, cluding center seal to PVC not drop all rotameter (i.e., spin- plug on top of CPRV stem.' the way to -OR- ning or free Check pressure relief spr!ng the bottom dirty fora- floating in- Check CPRV diaphragm gasket. stop when the meter, dicating air Check CPRV cartridge gasket. gas is shut flow) or, it. Clean the rotameter. off at the drops to a cylinder and constant' the injector point and is is operating. "dead" (in- dicating binding by dirt or fOr- eign matter) CHLORINATOR TYPICAL VALUES OPE~TING PROBABLE ~HAT TO HON TO FOR PROPER SYHPTOHS CAUSE HEASURE REASURE OPERATION REHEDY Rotameter Contaminat- - Visual - RemOve V'Notch assembly and float does ion in V- clean V-shaped groove in not rise and Notch plug. Notch plug. (A tooth brush fall uniform- and warm water are usually ly in propor- 'effective. Do not scrape or tion to V- scratch groove with a sharp- Notch knob edged tool.) rotation but ~jumps" up or down sharply :with a small change in V- .. N~tch settin~ ..... Hachlne vents ~lrty CPRV Cartridge ~ith injector off Should be c~- Clean CPRV cartridge Check ' chlorine, cartridge shut-off and gas turned on pletely tight, spring, stem and seat. Re- -OR- quality, r~ove CPRV dia- No continuing place any parts that are de- defective phragm unit. white fumes on fective. Assemble upside [ CPRV spring Check with a~on- a~onia test. down to be sure of proper -OR- ia to see if gas engagement.of parts. Look in. CPRV stem is c~ing through to cartridge inlet nipple to rod not in see if stem rod is centered. center hole ~ARNIN~: USE PRe'- of cross- TECTIVE GAS NASK shaped guide DURING THIS TEST piece. AND VENT THE GAS FRO~ THE AREA THOROUGHLY BEFORE RENOVING ~ASK OR RESUMING OPERA- ~"~ TIONS AFTER RE- PAIR. ~.~ ~ ,, ;'¥ . ~ .. - . i CHLORINATOR TYPICAL VALUES , OPERATING PROBABLE WHAT TO HOW TO FOR PROPER SYMPTOMS CAUSE MEASURE MEASURE OPERATION REMEDy Chlorinator Air leak up- CPRV vacuum Connect a single *17" to 22" H20 For air leaks, check: feed OK but stream of and vacuum leg water mano- vacuum at the Pressure relief spring. cylinder rotameter level under meter to the 1/4' CPRV for low CPRV diaphragm, includidc weight loss- -OR- vacuum re- plug opening just capacity machines center seal to PVC plug as shown by vacuum lev- gulating below the CPRV on top of CPRV stem. scale does els are in- valve diaphragm; then *10" to 15" H20 CPRV diaphragm gasket. not agree correct and to the 3/8" plug vacuum at the CPRV cartridge gasket with rota- have changed opening just be- CPRV for high If CPRV vacuum is outside meter indi- the density Iow the vacuum capacity machines specification limits, replac( cations mui- of the gas regulating valve, cartridge spring. If regu- tiplied by being fed. *32" to 38" H20 fated vacuum is outside.spec- time at each vacuum at the va- ification limits, add or re- setting. * cuum regulating move shims under spring. The valve, effect is 2" H20 higher va- . . cuum per shim added. If sprint · See Addendum is defective,replace spring and re-shim to correct va- cuum level. No Injector Injector See if air Place wet finger There should be Remove injector from the vacuum at gas diaphragm is leaking over center hole no air entering chlorinator. Disassemble in- inlet to in- check valve -into inje¢- in rear injector at this point, jector and examine diaphragm, jector. Oper- not opening, tot at rear. cover plate, center plug, O-ring and larg~ ating water diaphragm-to-housing sealing pressure and ring. Replace parts as discharge necessary. pressure both OK. InJector throat and taiiway clean O-rings good. Line to point of appllca- ; tion is clear. '~N[rORINATOR TYPICAL VALUES OPERATING PROBABLE WHAT TO MOW TO FOR PROPER SYMPTOMS CAUSE MEASURE MEASURE OPERATION REMEDY Chlorinator Vacuum regu- Regulated Connect a single *32" to 38" H20 NOTE: The heavy spri~'g"sh~! does not feed lating valve vacuum leg manometer at vacuum for Iow be under the diaphragm; the Gas supply spring bro- the 3/8" plug Dp- capacity machines light spring on top. OK. CPRV ken or de- ening just below If defective, replace vacuum clean, fective or the vacuum regu- *qS" to 50" H20 regulating spri'ng. Note thin V-Notch is inadvertant- lating valve dia- vacuum for high gray PVC shims on vacuum re- clean. Rota- ly left out. phragm, capacity mach]ne~ gulating valve seat. Each meter clean. Fails to shim added raises the vacuum Injector va- lift vacuum approxlmatelyi2" H20. Adjust cuum OK. regulating *See Addendum to about 35" N20 at a flow Injector valve stem in the mid-range of the rota. check is Dp- out of seat ~eter. ening proper- so gas can- lY- not flow to inj,ectpr.' Air is detec- Exhausted or Regulated Same as above. Same as above. If gas is exhausted, connect ted leaking restricted vacuum a new cyl-inder. If gas flow in via the gas supply . is restricted, clean gas center hole -OR- line and/or CPRV cartridge. in the plug Defective If vacuum relief spring, O- at the top of vacuum re- ring or diaphragm unit are the vacuum lief spring defective, replace parts as regulating -OR- necessary. valve dla- Defective O- NOTE: Gasket is required un- phragm unit.' ring on va- der diaphragm unit when re- cuum regu- installed~ lating valve stem -OR-. Hole in dia- phragm. CHLORINATOR TYPICAL VALUES " OPERATING PROBABLE WHAT TO HOW TO FOR PROPER SYMPTOHS CAUSE MEASURE MEASURE OPERATION REMEDY ,. Rotame~er tube Occasional - - - Clean rotameter tube and float. Warm water ~shows green- reliquifi- and detergent generally sufficient. White, slimy or browr cation of powdery deposits of hexachlorethane orihex- oily stains, chlorine achlorcyclohexane are not water-soluble. A fine white, in high For these, use (in a well-ventilated a~ea) powdery depos pressure a chlorinated solvent ~uqh~aA'~c~l"O~othen~; it forms in- tubing. ~~~erchlorethyiene to dissolve t~ side tube and Also, chlo- on float. RD- rine con- . tameter needs taminants WARNING: WHEN USING SOLVENTS, WORK IN A~ cleaning .too dropping WELL-VENTILATED AREA. AVOID PROLONGEO often, out of gas BREATHING OF SOLVENT VAPORS. DO NOT USE flow adja- CARBON TETRACHLORIDE AS THE VAPORS ARE A cent to SERIOUS HEALTH HAZARD. first majo~ drop in Follow'with a warm water flush and allow tc pressure dry before re-installation. with insuf' ficient Arrange position of chlorinator so that in- temperature let block is higher than connection point to keep on cylinders or manifold. Shape tubing for them in the a continuous uphill slope from cylinder to vapor stat( chlorinator (no dips or traps). Place cyl- inders so that they will not be warmer thar the chlorinator (not near a radiator, nor ,, so that sun shine~ on them). l~ne s~ that it might occa~i_~Ql,~b. Ll: 1ed (for_ example~ p~st'a cool, drafty_~n- Adder aline : pro~lgm~.ocaKi.~.~U~~all elec~c ~hlorine inlet bl~ck ~arm~ the ~a~ an~ Gel s pass ~st~ck~sal~~ and other contam- inants ~t~~R~ccurring in the 'CPRV or rotameter, , CHLORINATOR TYPICAL VALUES OPERATING PROBABLE WHAT TO HOW TO FOR PROPER SYHPTOHS CAUSE HEASURE HEASURE OPERATION REHEDY 'V-Notch is Build-up of No measure- - - Remove entire V-Notch assem- difficult to chlorine ments re- bly. Soak in warm water for iturn or move contaminant quired, about two minutes. Unscrew Iby rack and residue on red knob until' threads just ~plnlon. V-Notch plug disengage. Remove screw and ;When forcilby shaft is washer which hold knob to V- imoved, an air binding In Notch shaft. Unscrew and re- leak is de- the'seal move seal clamp. Withdraw V- tected. Rack -OR- Notch plug with seal and O- teeth are has been ring. broken, forced past the seal, Clean plug. stretching It open. Lubricate plug with a light film of silicone grease. Re- assemble all Parts, tighten- lng seal clamp just enough ,: to give a smooth, firm, slid. lng on the plug. Replace seal if damaged. Replace rack or pinion if teeth are broken. NOTE: Running plug up and down through its full range once a month will m~wlpe off~ . any beginning residue befor~ I it becomes a sticky or hard, ~" resistant accumulation. 'CHLORINATOR TYPICAL VALUES OPERATING PROBABLE WHAT TO HOW TO FOR PROPER SYMPTOMS CAUSE MEASURE MEASURE OPERATION REMEDY !High cylinder CPRV vacuum CPRV vacuum, water manometer, lO" to 15" H20 Check that flow deflector ~ressure (a- to high. vacuum. (of PVC or TFE) is over cart bove 80 psi) tridge stem when removing unable to CPRV diaphragm. Reposition feed 500 lb/ as necessary. Check that 24 hr with 5' pressure relief spring is Hg. Injector not corroded. Replace if 'vacuum. corroded. NOTE: Pressure relief spring -~-37700) for Iow capacity machine has a lower load than .the correct spring (P- 48661) used in high,capacity --~ machines. Addendum: Chlorinators are available in : iow and high capacities--zero : to 200 Ib/24 hr, and O to 500 Ib/24 hr respectively. " SERVICE NOTES I~PO~TA~T SAFETY I~ST~TIONS FO~ A~XlLIA~Y ~YLINDER VALVE This valve operates under full cylinder pressure and its construction must be und.erst~d. The physical 'details of the valve are illustrated below. NOTE; Packing nut P29~8 is. equipped with a left-hand thread ~nd, therefore, is tightened by turning, counterel°ck~ise. To tighten the packing while the valve is under pressure first re~ve wlve h~ndle ~2~7 ~r~ the valve stem ~2~ and valve bod~ by rotat~n~ it ~untercIockwise (right-hand thread). Use a small wrench, not over six inch- -es long, on the packing nut P29~8 to avoid damage to the threads. Turn pack- lng nut counterclockwise to tighten. IWARNING: UNDER NO CONDITION SHOULD THE PACKING NUT BE REMOVED ~ILE THE VALVE IS UNDER PRESSURE. If a new packing is required, close the main cylinder valve and relieve gas pressure in the line connected to the auxiliary cylinder valve. After a n~ packing has been installed, the valve handle must be engaged on both the valve st~ and the valve body. The valve stem should seat before the handle covers ail the threads on the valve body. If the handle travels too far, re- ~ve it, push the stem in slightly, re-engage the handle, and close the valve. Readjust the st~ as required ~o that about one thread on the valve body is exposed ~en the valve closes. Ensure that stem packing is leak-tight by testing with a~nia solution. 661-16J · '" :; ,, SERIES V-75 V--NOTCH CHLORINATOR PARTS .,{ UXA 2.,:3766 ' 41 4:> SECTION A-A ~TAME~R INLET UNIT ~ECTI~ 60 Ur/ON / 4~ INLET C~ECTION FRO~ VIEW SlOE VIEW WALLACE DW~S~O, 25.150.20.017 A MA~N STREET. BELLEVILLE, NEW JERSEY 07109 ,s~ 4 ~TE 5-77 !,S, ERIES V-75 V-NOTCH CHL INATOR UXA £3766 .. UXB 23766 KEYPART NO. NO, QTY. DESCRIPTION ~">' 1 P 31295 2 1/~" PLASTIC PIPE PLUG :;.~ 2 PE 5~97 2 BOLT, CHEX.HD. BRONZE) 5/16-18 X 1-1/~"LG. 3 PE 2~75 2 3/16" WASHER (BRASS) ~,~'2~,~ 4 P 3807~ ! SHIELD 5 UXA 17649 1 HEAD BLOCK ','i~, 6 P 47777 1 PANEL *' :;'~" 7 U__25841 1 PRESSURE REGULATING-PRESSURE RELIEF VALVE .... ~~ (3 TO 200 P,P.D.) (SEE DNG. 25,150.02.022) U 23842 I PRESSURE REGULATING-PRESSURE RELIEF VALVE (250 TO ~00 P.P.D,) (SEE DNG. 25,150.02,032) ;~;*; 8 U 17826 I TUBE CONNECTION" -- 9 P 26088 ~ UNION NIPPLE 10 P 221~3 3 UNION NUT ;.,.. ' 11 P 250 2 PLUG · ~ ,~ 12 P -2519 ~ LEAD GASKET ~'~ 1~ P '~BOS1 1 SPACER BLOCK 14 P 38050 ! CHLOE[NE INLET BLOCK ~'~:,.~ 15 P 37662 I SEAL COLLAR 16 P 37548 2 MACH.SCRE~ (FIL.HD.S.S.)~iO-~4Xi-1/2"LG. .~.:.: 17 U 22~64 I ROTAMETER BLOCK & PIPE: UNIT- i~[~~ 1918 PP 3788038047 11 SPRING3/8" PLASTIC PIPE PLUG ~:.' 2120 ~)5OI84~8978 22 ROD'~SCRE~ (HEX.HO.,N~N)~/8"-~ Xl"~ ~,~. 22 U 19200 I INJECTOR (SEE D~G. 25.150.06.012) ~,~.,' 23 P ~[86 i DISCHARGE LiNE (~ TO 200 P.P.D.) P b8123 i DISCHARGE L~NE (250 TO 500 P.P.D.) (~75 P.P,D. 2~ U ~7805' I C~O~INE PRESSURE GAUGE g DIAPHRAGM : 25 [ CHLORINATOR ROT~ETER UNIT (SEE D~G. 25,150,21.011) I SULFONATOR ROT~ETER UNIT (SEE D~G. 60.~JI.01.101) 26 P ~9185 2 ~/8' TUBE X 1/~' PIPE ~LF UNI~ ; ';~'~ ~ 0 R e a890~ 2 1/2" TUBE X 1/~' P~PE ~LF UNION . ~,. 27 P 27593 2 . GASKET (~ TO 200 PPD) P 2759~ 2 GASKET (250 TO 500 28 P 27598 2 COUPLING NUT (3 TO 200 PPO) P 27597 2 COUP[i~ NUT (2~0 TO ~00 PPO) 29 2 SPACER (SEE TABLE BELOW) ~0 _U2~15~ I VACUUH REGU~TZNG-VACUU~ RELIEF VALVE '~SEE D~G. ~1. P ~7657 1 ORIFICE ~2 P ~81~8 1 EXTENSION CH~BE~ FP 57~5 [ '0" RING ~BUNA-N) U~[FORH SIZE NO, 21~ -,. 3b P ~127 I "V' NOTCH PLUG '. [' ~5 P ~5]0 [ PLUG SEAL GASKET :;.'~*' ~6 P 26k82 / 1 ~"O"RING (BUNA-N) ~/BnZ.D.XZ/2"O.D. ~N[FORN SIZE NO. 012 ~7 P ~7663 '**'.1 C~NP[NG SCRE~ ~8 P }5124 [ MACH.SCRE~.CRD.HD.MONE~IB-~2X1/2"LG. $9 P ]5121 [ ~8 ~ASHER (M~) .~* bO U 20~20 1 NIPPLE UNIT 41 P'38061 2 C~MP .~2 P 165~2 ~ HEX.NUT (~NEL~ ~ P 165~6 b 1/b" ~ASHER (MONEL~ ~"~: P 39~71 I 1" X ~/~' P~STIC PIPE COUPLING (250 TO 500'P.P.D.) :~".. ~5 P ~8060 2 SUPPORT BRACKET ~6 P ~777~ b. CARRIAGE 5OLT CRD.HD.MONE~ 1/k-20X2-~/~nLG. ~.'~ ~7 P ~8056 ~ P~ST]C NUT, ~8 P ~8597 ~ CLA~P ~:-,. 50 PE [09~6 3 HEX.NUT (BRASS) 5Z P 38596 ~ BRACKET ~' 52 P ]75~7 2 CARE]AGE BOLT ,~',' 5~ P ~8072 2 PLASTIC NUT ~' 5~ R ~2525 ~ CL~P~NG NUT 55 P ~122 1 RING GASKET (HYPALON) I"I.D.XI-I/~"O.D. ~6 P~ ~0~ ' I MOUNTING P~TE ~7 P ~1077 I FEED RATE ADdUSTER KNOB 58 P 1~102 ~ I/~ LOCKWASHER 59 P 2i)71~ ~ 1/~" SHAKEPROOF WASHER P 50185 2 ~REW (HEX. HD., NYLON) 5/IB'LI~ X L* 1~67 ~ CAUTION LABEL WALLACE E, TIERNAN ---- IViSl r !E_T~,~_E._L.L._EVLLE NEWJE~;~'~ ISSUE 4 DATES-Z6 25.150.20.._01.7__B · ¢.,:','U23841 PRESSURE REGULATING-PRESSURE RELIEF VALVE PARTS i:,I,: " Used In V-Notch Chlorinator F KEY NO. PART NO. qtY. DESCRIPTION 1 P 2118~. I ADAPT~R, 1/¥~ PIPE X 5/B't HOSE 2 PXA 37688 ! PLUG : , 5 UXA 176~5 I DIAPHRAGM UNIT .- U 176a6 I INLET VALVE, INCLUDES 'aA THRU ad' : ~ P al??5 I SEAT ac u [76~?. ~ STEM UNrT ..// aD P a~79a I LOCKNUT bE P k1776 I BODY aF P ~7683 1 SPRING aG _.e_~_?ss[ ~ SPRinG SEAr a~ P ~60'8S 1 UNION NIP.LE ad P 22135 I UNION NUT ~ s . 377oo I SPRING ~ .~_~h~12~ 2 GASKET 7 P 5805a ! VALVE PLUG 8 P 51295 1 1/4" PLASTIC PIPE PLUG g P b033~ ! GASKET II P 2519 1 GASKET aaor, r- -- ~ ~ITY--3 TO200 LB.~R ; ~E~T ,, ow~s~o.. 25.150002.022 25 MAIN STREET, BELLEVILLE, NEW JERSEY 07109 ' ~E I DATE 8-77 U23842 PRESSURE R~ULATING-PRESSURE RELI~vALVE PARTS 1, ..' Used In V-Notch Chlorinotor ~A P ~1775 1 SEAT ~B P ~1777 i FLANGE kC U ~7~k7 I ~M UNIT _ NOTE- - - ~ W/~I..I..Ar:E E. TIE,NAN ~ ' 25 150 002 032 ,,, DIVISION, 25 MAIN STREET. BELLEVILLE. NEW JERSEY 07109 ~ 1 ~fE 8-T7 '.,~ ,~U- . VACUUM -VACUUM ' VALVE PARTS ii "'~ Used In V-Notch Chlorinator PXA-:$768 7 'VENT PLUG ':~ }]~ ~ 17643, DIApH.RAGM UNIT P-37699 SPRING " · ,';.' Pz48125 STEM P241851 SP~R (5 MAX.) '-' :;~' ' (SEE INSTRUCTION 800K -'~ P-38047 318" PLASTIC . . -:-- ~' PIPE PLUG -.- GASKET <~ U-17647.. SEAT {S-PO0 PRO.] U-18075 SEAT lP50-500 P.P.O.) & IvOrp41~T OF u-2s/55 25 MAIN STREET. BELLEVILLE. NEW JERSEY 07109 ISSUE 2 DAT~ 11-75 ° INJECTOR COVER . P 50286-"0" RING > ... U-17639- DIAPHflACI,4 .. I/2" PiPE PLUG · o STEM INSI'41.L r~r~ c~+~o~/~r 645 INL£r I/4." PVC PII~ PLUG& - SPRING ~u,~Nc .... ~'XA-376q3 - CLAMPING COLLAR P'376~2 - (P-52003-BODY · /"WATER INLET CONNECTION A SECTION "A-, P-4oqoo-oIAPHRAGM PLU8 I/4"PVc PiPE PLUG P-3~SI ' RING GASKET BALI., P-,76.9 - SC.EW INJECTOR. BODY ($/~-16X IS/~ LG) ~ BALL SEAT& P-~e~oo - WASHER . P-1654~ - HEX. NUT (8) ' ~ PART OF REORDERING UNIT U23960/ V-NOTCH CHLO ATOR PARTS · ' Chlorine Rotameter Components ~ , --' ~ '~ ~ ~ ~ .... '~ u'll ~ ~ 500 POUNDS ~ ~ ]',:' - ~ PER DAY P-~I~I RING GAS ~W VANE 200 ~ 500 LBS. ROTAMETER MAXIMUM CAPAC I~ FLOAT LBS. COMPL~E ~R 24 H~. ~ UNIT TUBE PART NUMBER ~RIPTION TOP BOSOM ~.~ , P 41212 P 581~1 ~ U 20947 P 44058 P 57702 ~8 DIA. RED ~LL:~?.. I0 UXA 20947 P 44059 P 57702 P 41212 P ~81~1 80 UXB ~947 P 44060 P 5770~ ~ 5/3~ DIA. RED BALL P 41~12 P 58151 ~0 UXC 20947 P 44061 NP 150 . ~/~ DIA. B~CK ~LL P 41212 P ~81]1 50 UXD 20~7 P 4~6~ P ~7705 I/~ DIA. R~ ~LL P 41212 P ~8131 75 UXE 20~7 P 4~63 P ~7706 ~ P 41212 P ~81~1 ,~lA. RED I00 UXF 20947 P 44~64 P ~7706 P 41212 P ~8131 150 UXG 20947 P 44065 P 3T~7 ~ DIA. ~D ~LL P 41212 P 58151 ~00 UXH 20947 P 44066 P 36376 9~ DIA. P 48140 P ~140 GLASS F~AT ~ ~140 P 48140 ~50 UXJ 20947 P 44067 P ~6~76 300 UXK 20947 P 44068 P 38256 5/~ DIA. P 48140 P 48140 400 UXL 20~7 P 44069 P ~8256 GLASS ~AT P ~1~ P 48140 WALLA[E [ TIERNAN o~v~s~o. ,~.. ~ ~..,o-~ 25~ 150.21.011 'MAIN STREET. BELLEV,LLE. NEW JERSEY 07109 ~?~' I NJE THROAT 8~ TAILPIECE AILS PARTS ~_~-~ ,.. Used In V-Notch Chlorinator ~8~s~;. P-38275 RETAINING p47E06-3/4" PIPE X ~/4" HOSE ADAPTER FOR I" FLEXIBLE' 'PLASTIC PIPE "~. Lg~ D~SI~NATION k~ PXD 5.0093 TAILPIECE "0") (L~TTER O~SlaNaTION PXG 50095 TAILPIECE PXJ 50095 TAILPIECE (LETTER OESIGNATION."J") PXK 50095 TAILPIECE ASSEMBLE BEFORE ~ (LEtTeR D~$1GNATION ~K .' ~ LAROER OIA."O" RINO PXE 5~ ~99 'THROAT PXO 50094 · 140 THROAT $/Z~ NUMB~A PXH 50094 ~ 165 THROAT LOC~ rED PXd 50094 ~ 195 THROAT ~ ~IL ~ " PXK 50094 ~ 242 THROAT · SMALLER DIA."O" RING j NOTE--- .-. USE ~99 THROAT WITH "O" TAILPIECE USE ~140 THROAT WITH ~F" T~AILPIECE USE~I65 ~ROAT WITH USE ~1~ ~HDOAT WITH . USE~R~2 THBOAT WITH I~JECTOR BODY "~" TAILP/ECE ~ WHEN REORDERING "0" RINGS SPECIFY U-21275 FOR PAIR. NOT SOLO SEPARATELY. raE W LT WALLACE TIERN'AN ~-- o~v,s,o. 25.150.26.021 ~ll 25 MAIN STREET, BELLEVILLE, NEW JERSEY 07109 ~ssu~ 5 o,~zE 5 -74 AUXILIARY CYLINDER VALVE- UNION .TYPE U 1::'43 CHLORINE U172.21 SULFUR DIOXIDE , .=-~, - AUXILIARY CYLINDER VALVE-YOKE TYPE · m U24948 CHLORINE- 2 U 17g~1 1 V~ ~DY ~ P 2~9 1 5 P q5~ 1 ~[I~6 ~, 6 P ~5~7 1 ~]C ~R 7 P ~ I P~[NG NUT 9 P qS~ 1 ~ PL~ 10 P ~ 1 ~ ~ STOP~R i~ P 529~ I V~ ~Y ~ O 2~16 I ~ ~Y ~ P 16191 ~ ~ ~ ;~' ~ ~ W~LL~CE [ TIERN~N ;~:' DIVISION 50.150.01.011 PLASTIC MAIN CON~CTION PARTS ~'~ I! II II For ;/4 or.ii'l Solution Lines With I Corporation Cock ;' .... ~ P-7468- RING C..~SKET ~ ...: ~r---~- ~r~, ~ ~w~ ~' J / .~ P~ 2635 ' NUT ...... _ ~=~_~-. ~~ ~[~~~/~ ..~ :', ~ P-4373- TAG~ _ "~ U-19259- ~ ~UTION ~BE~ ' ) ~ ~RATI~ ;':t~ ' .~ P-37~-~ N~~ U-~7-~R~ . . ~ U- 1~7- I' CHECK VALVE I" FL~ PL~C ~ OR ~ :~. - P-~498-1' X ~' ~,,~ I' ~I~E ~TIC C~ %-' PI~ ~ HOSE ~ ;::'~ ~ * · ~ ..... PIPE ~TER - · ::. ~ ~.... c~ vALvE ~" HOSE P~T OF ~AT~N ~K ~ U-617 OR U-6~ ~T~ FLEX~B~ PLA~C mpg :?,' ~MUM ~E-140 RS.I. AT~'F OR "*" ~ ~E OF ~E OR : ~18~ ~STIC PI~ WRLLP, CE E TIERNP, N . DIVISION 50.8 45.06.011 MAIN STREET 8ELLEVILLE NEW JERSEY 07109 ~SSUE 7 o,~'r£ 1-72 - MAIN C ECTION PARTS . "For I" Solution Line And I~/~_' Main Connection . ~. · · .~.~. I" FLEXIBLE PLASTIC ./ ., IIIII I II llilllllllll--. ......... .. ~ -'--'--],___~ ..... VALVE P 37857 I" NIPPLE ~i..:!ii !!!-=--~ U 18890 MAIN [~. CONNECTION ?. , :~~ I¢~ N.P.T. ~ P 37900 I ~{~ '/2 x I" COUPLING P 37590 ADAPTER FOR I" FLEXIBLE PLASTIC PIPE OR HOSE CXIUT/ON- FOR P/:i~PER D/SPERS/ON OF SOLUTION, THE END OF TIlE TUBE MUST EXTEND INTO THE MAIN, BUT NOT MORE TNAN APPROXIMATELY MAXIMUM PRESSURE 140 PSI AT 75° F //$ T/YE DIAMETER OF THE MAIN. OR WORKING PRESSURE OF HOSE CUT OFF THE TUBE/F TOO LONG. OR FLEXIBLE PLASTIC PIPE. raE~T- W/'4.LLACE F., TIERNrRN mv,s~om 50.845.O6.012_. 25 MAIN STREET, BELLEVILLE. NEW JERSEY 07109 ~SSUE DATE ~ MAIN CO CTION PARTS 3/" 'i" For '4. Or Solution Lines And~/,~'Or I" Main Connections I" RIGID PLASTIC PIPE U 18967 I" CHECK VALVE ~UXC 21673 I" BALL VALVE ! P 37590 ADAPTER FOR P 37837 I' NI ~., I" ~EXlBLE PLASTIC TION HOSE PiPE ~ .. I" RIGID PLA~IC PIPE :~'~;';~ P 37590 ADAPTER 43468 I" ~UP ''~ I" FLEXIBLE PLASTIC ~ PIPE ~ HOSE ,, [' ~' P 47206 ~" TUnG X 3~ EP~ Z ~ PIPE T~EAD J ~. ADAPTER ' .~ CRUT/ON --- ~E--- .¥' FO~ P~OPE~ DIS~SION OF S~UTION TH~ MAXIMUM P~ESSU~E' 140 ..~ ~ND OF TH~ TUB~ MUST ~XT~ND INTO YS~F OR W~KING ~SSUR~ :. ~ THE MAIN, BU~ NO~ MORE THAN OF FL~IB&E P&~IC APPROXIMATELY ~ THE DIAMETER OF ~ MAIN. CUT OFF THE Y~E IF TOO LON~ r~EN~W~T W/ALLAI:E F., TIERNP, N DIVISION 50.8 4 5.0 6.0 3 2 25 MAIN STREET. BELLEVILLE. NEW JERSEY 07109 ~ssu~ Z D~TE I- 73 SPARE PARTS LIST ALI. ACE & TIERNAN CHLORINATOR SERIES V-50 or V-75 1 Set of Gaskets U-2 ! 247 : ~1 I Diaphragm Unit .. UXA-17643 ~,:, 1 In joet'or Diaphragm U-17639 Tub I e Lubrlcant U-!0242 1 4 oz. Bottle Ammonia Solution U-409 "Commercially available as Dow Corning DC33 Silicone Grease Prices subject to change without notice. 'Prices FOB BellevJlle, N.Jo with ~ull transportation of seller's selection allowed. 910o175 SPL lC \'*,'~'~RJ;'/I'4(~ WITH CtlI. ORINE form dangerous acids. In fact, tl~e first lead to a kind of acne -- symptom of exposure to it is smartinfl and burning of the e¥'es, nose ali~l tJ~roat. Continued ext)oti~.~'a, can cau:.~ imense ControJJingChJorineJJ~lzards f;hl,,rir,(,, a riss thai; is widely dish'ib~ted in coughing(), chest pains. ',md often vomili~g. If . r~t~l~¢ J~J,t' is so reactiue [hat it is rarely (otllid bre,~lhc,i h)fl~ (¢~ui~gl~, t~igh concentr~tio~ts of Are:as in which chloriria is i~,,,,~ ..... ,,s a i,,..,; ~ia~;, J~ k~owf~ as a potential dangffr to chlorine can cause rate,cie crampi~,!l of the stored, or used shoHId be well veridl!,t,..J '. w,Jrl, ei iiealth i~-~ its manu[act'ure arm tl~roat a:nd swull l;he li~i,~s of ai~ [,assafl4s, exhaust vents at .floor level to Ciil,'~rine gas ifself is a pungent, t_.iqt,id cl¢orine pi,;(htces gas i~;l~mdy, if air co~[aininfl chlorJr~e ttus fl~-eel~isl~-y~llow Bas that is more theft twit:(: as spilled. Either the liq,liti or lhe (:ol~ct:Rtl'ated procesg()d so that it doesn't do I~av¥ as air. It is manufactured b¢ passing gas can severely l~tl~'l-~ the skin or ~ho'eyes. the atmosphere. elecllicity through .a solution of ordinary "Freeze I]urrls" can also be caug~:d by the Clflorinest.orageand lablu salt and then is usually compressed to a rapid vaporization of tll,: liquid, areas should have unobstltlc{ed, v,.,:ll ,,,~,t ['.,. liquid for shipping and stora~. The handli~,g Pure chlurJr~e tl~S and liquid :.i~e not emergency exits. Work areas shouhl ah,J usc of both liquid and ~seous chlorine flammable, but they i,r,3(hJce, ilan.'m~ble and emergency gas masks, emergency require close attention to safety precautions ext:,lo~ive mixtures i~ c,.mibinatiol~ with other face-flooding and eye-wa~lih/9 and practices, ct~emic~ds such as hvdrogerh hydroc,~rbons, Workers who for any reason have t-o er,'t~r alcohols and ethers. Becatlso high an area con[ainJn9 a I~iflh contzeiiti'~lioF~ temperatures and p~e~f;ures are prodt~ced in chlorine, or where accidental spillage How Chlorine IsU~ed -. the manufacture of some chlorine occur, should wear protective clothi~g compounds, the~ pro~e~es must bu rigidly gloves arid uric a full-fac~ airline respirator. Chlorine is used in many industries as a con[rolled. bleach to whiten malerials used in paper and lextile industries, such as in making cellulo~ What to Do if Exposed toChlorin8 fibrs for svntl~etic fabrics. Since it is ~lso a Warningsof/ow-Lev6lChlorineExposure powerful disinfectant, it is widely u~d [o If you find d'iat lhe ~ir you are purify drinking water, to disinfect swimn'dng The offensive odor of chloril~o ~tas gives contaminated wid-~ cl~Jo~ilto, hold ~ls, and to treat sewa~, warning of sudden or substantial chlorine until you get the nearest emer~ricy mask Chlorine is widely used in the chemical contamination, but people who are regularly If you have to bread]e l~fore you can get industry for the manufacture of u~ful subjected to chlorine soon Io~ their ability to mask on, take very shallow breaths. chemicals such as solvents, refrj~rant gas~s, smell it at concentrations below th(~se that If even a little chlorine gets in your eyes or plast'ics, rubber products, and bug killers, cause immediate effects. Such a worker can if they are subj~cted to strong concu~Uatio,'~s no longer loll if a Ii[de chlorine is in Ihe air he of the gas, flush them out immediately wiil~ breathes; [his is dangerous because continued lots of wa[er at the face spray. See II~e ttow Il Affects the Body exposure can lead to futm-e respiratory doctor afterwards. disea~s and predispose the wo~ko~ ~o other If liquid chlorine ge'ts on li~e Chlorine is notably irritating to the mucous diseas0 It can aisc) reuuit in c~>rlosiorl of the anywhere, wash !he ar{;a with lots of ~tm~ membranes of the eyes, nose, th~oat and the tootle. Exposure of tl~e ski,-, to Iow water. ¥o(~ (:ai~ rise a mild soap, b~t cJ~¢~'r lungs bucoliC it reacts with body moisture 're corl,,;~,~dliorls of cht,,rine for ,~ Io~fl time can on an ointment or a~'¢ msdicin¢ th~ll WORKING WITH doc[or[ellsyouto. 3. Kn0w his job, hisecluilx~ent, andwhat ' Ch[0r[ne ].o i~i.:alec[ ~gaJnst Iow--level exposure. ~nV he ~ho~iJd do in the event of CUOl'kei' WJiO ddVeJOpS c-Joracne, COn[iI-HJOUS emergency. . hOaddCii,'~S, OF fealir, gsb,'' guil~eral indisl.,asiiion, 4. Be prepared to assist other workers near dlIXieLy, or 5iii[ocatiorl should report [o the Jiila in ca~ of emergency. jJJ~ll][ ilJJl'SO OF (JOG[Of illlF(le(.Jiately. 5. Make Stll'e ventilation systems are fHnctioili ng during work periods. 6. Tell his supervisor aboLit any*hing M~nogemerHResponsi~ilities unusuai concernirlg the u~ of chlorine gas or li(l~lid in his area. 'l'he omj)Joyer I'nLISL take every reasonable 7. Repor[ to tho plant I-ILII~ or doctor any slep Ik, p(evel'VL health Jlazards or accidental UllJiS~l~l or chronic symptoms that J,~j~lJV t(J his workers. Nc) olde with a history feels coLiJd be related to exposure of respiratory illness sho~dd ~ put t() work chlorine. vui~ere he couJcl J~ expcsed to even Iow concentrations of chlorine gas. Those who .. roceive si~ch a job should be given a complete piwsical ~xarnination ~fore starting [o wc)rk ar,d at least al3nuallV tliereafter. Managal~cnL is reslbonsiJ)le.for inspecting and maintainiltg equipment and processes, for i}roviding safety arid emergency equipltient, IISM 73- and for i~]siituting a toni'in,ling progral~i of s:~[e'[y iTainin~]. Employee Responsibilities Each employee must be aware ot: the hazards to health resulting from working wJt~ U. 8. DEPAflTMENT OF · chlorine and how he can ~st reduce the 'HEALTH, EDIJCATION, AND WEI.FARE hazards through safe work practices and Public Health Service sa[ety precautions. In addition, the employee I-tealth Services and should: Mental Health Ad~ninistration Natiom-:l Insti LLI[e ior ("}dC[lpa tional 1. Avoid skin and eye contact with SaietyandlleMth cldorine. 2. Know where emergency equipr,,ent is 1973 kept i,~ his area and how tO use it. II.S. BEPARTMENT OF residence residence ' residence residence ' ' residence - Nearest ~ - F~re sis. lean [~ - Hos.uitaJ ~. - School residence residence - Nearest ~ - Fire stadon ~'~ - HosoitaJ - Scrtool residence PLANZ ROAD WHITE LANE LEGEND ~4 ' i 234 56 78910 rcmTi Fire statJon ~ -Hosi3it;a.l ~i~' School o - Nearest rtL~J - residence AVE. / VIRGINIA AVE. LEGEND residence CALIFORNIA LEGEND ' :~4 5 6 78 910 1~'' Nearest ~ - Fire station - HospitaJ residence AVE. LEGEND residence SC~L~: r'=aoo' LEGEND ~ ~ - ~o~=~, - s~oo, ~ ...... , . Nearest o F~re s~tion '~ ,SC. ALE.' f'=80O' residence LEGEND Nearest ~T~ Fire stolon . . - - ~i ~-~ residence LEGEND [. SC..ALF.: - Ne?est Fire st~ti(~n - HospitaJ School residence CHLORINE pLUME CONFIGURATIONS - NIGHT CONDITIONS Toxic Vapor Limit = 2.5 ppm Chlorine 83 ppm, 396 feet '24 ppm, 988 feet 7 ppm, 2172 feet 5 ppm, 3060 feet 3 ppm, 3947 feet 2.5 ppm, 4243 feet Toxic Vapor Limit = 25 ppm Chlorine 69 ppm, 475 feet [9 ppm, 725 feet 28 ppm, 912 feet 25 ppm, 974 feet At 100 feet down wind, ground level concentrations are only 1.4 ppm compared to the. 970 ppm concentration at the 9 foot high relief vent. Release height and ground level concentrations become approximately equivalent at down wind locations exceeding 350 feet. CHLORINE PLUME CONFIGURATIONS - NIGHT CONDITIONS Toxic Vapor Limit = 2.5 ppm Chlorine 83 ppm, 396 feet 24 ppm, 988 feet 7 ppm, 2~72 feet 5 ppm, 3060 feet 3 ppm, 3947 feet 2.5 ppm, 4243 feet Toxic Vapor Limit = 25 ppm' Chlorine ~69 ppm, 415 feet / ~ \ ~ i ~39 ppm, 725 feet ~ 28 ppm, 912 feet 25 ppm, 974 feet At 100 feet down wind, ground level concentrations are only' 1.4 ppm compared to the 970 ppm concentration at the 9 foot high relief vent. Release height and ground level concentrations become approximately equivalent at down wind locations exceeding 350 feet. CHLORINE PLUME CONFIGURATIONS - NIGHT CONDITIONS Toxic Vapor Limit = 2.5 ppm Chlorine --~83 ppm, 396 feet 988 feet ppm, 2172 feet pm', 3060 feet L~~~~_~~~ 3 ppm, 3947 feet 2.5 ppm, 4243 feet Toxic Vapor Limit = 25 ppm Chlorine ~69 ppm, 475 feet ~3~8P~,725 feet 912 feet 25 ppm, 974 feet At 100 feet down wind,, ground level concentrations are only 1.4 ppm compared to the 970 ppm concentration at the 9 foot high relief vent. Release height and ground level concentrations become approximately equivalent at down wind locations exceeding 350 feet. CHLORINE PLUME CONFIGURATION DAYLIGHT CONDITIONS Toxic Vapor Limit = 2.5 ppm Chlorine 112 ppm, 80 feet 59 ppm, 166 feet 8 ppm, 558 feet ppm, 720 feet 2.6 ppm, 1016 feet Toxic Vapor Limit = 25 ppm Chl. orine 112 ppm, 80 feet ppm, 140 feet 284 feet All distances are measurements from the point of the chlorine release to a point down wind along the center line. The vapor dispersion model predicts that the indicated chlorine concentrations may exist at the given distances across the width of the plume. CHLORINE PLUME CONFIGURATION DAYLIGHT CONDITIONS Toxic Vapor Limit = 2.5 ppm Chlorine ll2.ppm, 80 feet 2.6 ppm, 1016 feet Toxic Vapor Limit = 25 ppm_ Chlorine 11'2 ppm, 80 feet '~/'~ ~ ' ~75 ppm, 140 feet ~ppm, 284 feet Ail distances are measurements from the point of the chlorine release to a point down wind along the center line. The vapor dispersion model predicts that the indicated c~lorine concentrations may exist at the given distances across the width of the plume. residence - Nearest ~'~ - Fire stsdcn [~ - Hosni~ ~. - School residence ' ~,~,,.~- Nearest J~-Fire st~.tion r~ ' Hos.Diml .~- SChool residence residence ,.' - Nearest ~'~ Fire s~.dcn ['~ - HosoitaJ ~. - School ~ · residence - Nearest [~ - Fire station ~-~ - HcspitaJ ~ - Sct~col residence - Nearest [~ - Fire station [~ - Hcs.oitsl ~i~ ' School residence ~--~=' Nearest ~- Fire s~ation ~ - Hos.loitnl ~i~' School residence E. ~IA ~O ~ I AVE. -F_ ~ VIRGINIA AVE. LEGEND - Nearest ~ - Fire stadon ~ - Hospital '~ - School residence CALl FORNIA BRUNDAGE F_ VIRGINIA AVE. LEGEND - Nearest - Fire station Hospital residence CALIFORNIA AVE. _ DRACENA STREET PALM ,v -- ~ BRUNOAGE AVE. COl,.~ STRF. ET $~1~1T,4 ~ R~ILf~,40 YAtTI2 CALIFORNIA WHITE L.~NE ]~- Nearest r~- Fire statien residence SC~L~: ~ PLANZ ROAD c~L ; ~ WHITE LANE LEGEND - Nearest ~ . Fire station ~-~- HospitaJ ~i~ - School a~.i 2,,~. '--3 4 ~ SC, ALE: residence BAKERSFIELD FIRE DEPARTMENT FAX Transmittal COMPANY: 'P/~P-~--S ~;; (2~ FAXNo: FROM: ~ L',~ ~J'~-~ Office of Environmental Services FAX No. {805) 326-0576 · Bus No. {805) 326-3979 1715 Chester Ave. ° Bakersfield, CA 93301 8003.5-A, 8003.6-8003.6.' 1994 UNIFORM FIRE CODE TABLE 8003.5-AmFLAMMABLE COMPRESSED GASES--- DISTANCE FROM STORAGE TO EXPOSURES1 MINIMUM DISTANCE TO BUILDINGS, STREETS, ALLEYS, PUBLIC WAYS OR MAXIMUM AMOUNT PER STORAGE PROPERTY LINES THAT CAN BE MINIMUM DISTANCE BETWEEN AREA (cubic feet) BUILT ON (feet) STORAGE AREAS (feet) x 0.0283 for m3 × 304.8 for mm 0-4,225 5 5 4,226-21,125 10 10 2 I, 126-50,700 15 10 50,701-84,500 20 10 84,501 or greater 25 20 tThe distances can be reduced to 5 feet '1524 mm) when protective structures having a minimum fire resistance of two hours interrupt the line of sight between the container and the exposure. The protective structure shall be at least 5 feet ( 1524 mm) from the exposure. The configuration of the protective structure shall allow natural ventilation to prevent the accumulation of hazardous gas concentrations. 8003.6 Oxidizers. 8003.6.1 Indoor storage. 8003.6.1.1 General. Indoor storage of oxidizers in amounts exceeding the exempt amounts set forth in Section 8001.13 shall be in accordance with Sections 8003.1 and 8003.6.1. Retail display of oxidizers shall be in accordance with Section 8001.12. See also Section 8001.14.3 for storage of oxidizing gases in quantities not exceeding exempt amounts. 8003.6.1.2 Detached storage. Storage of liquid and solid oxidizers shall be in detached buildings in accordance with Section 8003.1.21 when required by Section 8003.1.21. 8003.6.1.3 Distance from detached storage buildings to exposures. In addition to the require- merits of the Building Code, detached storage buildings shall be located in accordance with Tables 8003.6-A and 8003.6-B. TABLE 8003.6-A--CLASS 1, 2 AND 3 OXIDIZER LIQUIDS AND SOLIDS-- SEPARATION OF DETACHED AND OUTDOOR STORAGE FROM OTHER BUILDINGS, PROPERTY LINES, STREETS, ALLEYS, PUBLIC WAYS OR EXITS TO A PUBLIC WAY MINIMUM DISTANCE (feet) OXIDIZER CLASS x 304.8 for mm N.R. = not required. ox,o.z ..,oo,os w .s o. WEIGHT ~ ~ MINIMUM DISTANCE {feet) x 0.4536 for kg ~ x $04.8 for mm Over 10 to~ ~to 1,000 ~ l,~i to 3,~0 / )=¢0~ ,o ?ACP. 300 5,001 to 10,000 400 Over 10,000 As dete~ined by the chief [ 8 003.6.1.4 Liquid-tight floor. In addition to Section 8003. I. 18, floors of storage areas for liquid and solid oxidizers shall be of liquid-tight construction. 1~32 1994 UNIFORM FIRE CODE 8003.6.1.5-8003.6.1.7, 8003.6-D 8003.6.1.5 Smokeand heat venting. Smoke and heat venting shall be provided. The design crite- ria shall be as set forth in the Building Code. 8003.6.1.6 Smoke detection. An approved supervised smoke-detection system shall be installed in liquid and solid oxidizer storage areas. Activation of the detection systems shall sound a local alarm. EXCEPTION: A smoke-detection system need not be provided in detached storage buildings protected by an automatic fire-extinguishing system. 8003.6.1.7 Storage conditions. The maximum quantities per building in detached storage buildings shall not exceed those set forth in Tables 8003.6-C through 8003.6-F. The storage arrangement for liquid and solid oxidizers shall be as set forth in Tables 8003.6-C through 8003.6-F. Class 2 oxidizers shall not be stored in basements except when such storage is in stationary tanks. Class 3 and 4 oxidizers in excess of the exempt amounts set forth in Section 8001.13 shall be stored on the ground floor only. TABLE 8003.6-C~STORAGE OF CLASS 1 OXIDIZER LIQUIDS AND SOLIDS IN COMBUSTIBLE CONTAINERS1 LIMITS (feet) CONDITION x 304.8 for mm ( Piles Maximum length No limit Maximum width 50 Maximum height 20 Minimum distance to next pile 3 Minimum distance to walls 2 Maximum quantity per building No limit IStorage in noncombustible containers or in bulk in detached storage buildings is not limited as to quantity or arrange- ment. TABLE 8003.6-D--STORAGE OF CLASS 2 OXIDIZER LIQUIDS AND SOLIDS1,2,3 LIMITS x 304.8 for mm × 0,4536 for kg CONDITION Segregated Cut Off Detached Piles Maximum height (feet) 10 12 12 Minimum distance to next pile (feet) Footnote 2 Footnote 2 Footnote 2 Minimum distance to walls (feet) 2 2 2 Maximum quantity per pile (tons) 20 50 200 Maximum quantity per building {tons) 200 500 No limit IStorage in noncombustible containers is not limited as to quantity or arrangement, except that piles shall be at least 2 feet (609.6 mm) from walls in sprinklered buildings and 4 feet (I 219 mm) from walls in nonsprinklered buildings; the distance between piles shall not be less than the pile height. 2Aisle width shall not be less than the pile height. 3Quantity limits shall be reduced by 50 percent in buildings or portions of buildings used for retail sales. 1-333 09/24/97 14:17 8805 326 0576 BFD HAZ MAT DIV ~001 *************************** *** ACTIVITY REPORT *** *************************** TRANSMISSION OK TX/RX NO. 3395 CONNECTION TEL 8610864 CONNECTION ID START TIME 09/24 14:13 USAGE TIME 03'20 PAGES 3 RESULT OK CITY of BAKERSFIELD "WE CARE" FIRE DEPARTMENT 2~f01 H STREET S. O. JOHNSON August 24,1993 BAKERSFIELD, 93301 FiRE CHIEF 326-3911 Linda Robinson Bakersfield Recreation Division 4101 Truxtun Ave. ~ Bakersfield, CA 93309 Dear Linda, On August 9, I inspected several of the Bakersfield swimming pool sites to verify implementation of the City's Risk Management and Prevention Program (RMPP) for pool chlorination. It appears that the RMPP has been fully implemented at all of the pool sites with the exclusion of Jefferson. Jerry DeLaurie explained that the conversion to non- gaseous chlorine at Jefferson is complicated some by the size of the pool and the location of equipment at the site. It is important that we work to solve the problems related to converting the system at Jefferson due to the added hazard of subterranean storage of chlorine gas. The Recreation Division needs to consider the options for co0version, develop a schedule for installation and request an extension of time to complete implementation of the RMPP at Jefferson. Because the Fire Department must document the City's compliance with the CA Health and Safety Code regarding the implementation of this RMPP, we must request your response to this letter by October 1, 1993. Please address the extension request to my supervisor, Ralph. Huey. I will be leaving the Bakersfield Fire Department on September 1. It has been a pleasure working with the staff of the Recreation Division over the last several years. Please contact the Hazardous Materials Division at 326-3979 if we can be of assistance. 'Sincerely, Barbara Brenner Hazardous Materials planning Technician cc: Ralph Huey ~ TO: Ralph E. Huey,.~azardous Materials Coordinator FROM: Linda Robinsof~Recreation Supervisor DATE: October 5, 1992 SUBJECT: ELIMINATION OF CHLORINE GAS The City of Bakersfield, Recreation Division is in the process of converting all City owned pools to use Trichloro-S-Triazinertrione chlorine rather than gas chlorine to sanitize its pools. We will have all of the pools converted by May 1993. At Siemon, Jastro, Saunders, Planz, Central and Wayside Pools we will use a Daily Maximum of 10 lbs, a Daily Average of 5 lbs, and an Annual Amount of 300 lbs. At Beale, Martin Luther King, and Jefferson we will use a Daily Maximum of 20 lbs, a Daily Average of 10 lbs, and an Annual Amount of 600 lbs. We would store no more than 250 lbs at any site. We would also use Soda Ash at each of the sites. We would use a Daily Maximum of 20 lbs, a Daily Average of 10 lbs and an Annual amount of 600 lbs at each of the pool sites. cc: Scott Manzer Risk Management Division Aqultr:chlorine CITY of BAKERSFIELD "WE CARE" FIRE DEPARTMENT 2101 H STREET S. O. JOHNSON December 27, 1991 BAKERSFIELD, 93301 FIRE CHIEF 326-3911 Jim Ledoux Superintendent City of Bakersfield Recreation Division 4101 Truxtun Ave. Bakersfield, CA 93301 Mr. Ledoux: Bakersfield Fire has completed review of the Risk Management and Prevention Program (RMPP) prepared for the following City of Bakersfield Park Pools: Jefferson, Jastro, Siemon, Beale, Martin Luther King, Saunders, Planz and Wayside. The RMPP supporting document is complete in scope and content. The programs outlined in the RMPP must be implemented according to the schedule provided in the RMPP. Bakersfield Fire will inspect the facilities periodically to verify compliance with the plan. Please let us know if we, at the Fire Department, can provide assistance toward the implementation of this Risk Management Plan. I appreciate all of the cooperation that Linda Robinson'and Jerry DeLaurie extended during preparation of this document. It has been a pleasure working with the Recreation Division. Sincerely, Barbara Brenner Hazardous Materials Planning Technician cc: Ralph Huey Scott Manzer Linda Robinson MEMORANDUM "WE CARE" October 17, 1991 TO: Leland Andersen, Community Services Manager Jim Ledoux, Recreation Superintendent Linda Robinson, Recreation Supervisor Scott Manzer,Risk Manager FROM: Ralph Huey, Hazardous Materials Coordinator SUBJECT: Meeting to discuss park pools risk management plan The Risk Management and prevention Plan (RMPP) for the Bakersfield park pools is in the final stages of development. During the week of November 4, 1991, the Hazardous Materials Division will send out a draft document for your review. On November 13 at 10 A.M., we will meet in the Convention Center meeting room to discuss the plan. It is important that we take this opportunity to clarify any questions regarding the RMPP. Community Services will make the final determinations regarding the method of risk minimization prior to completion of the plan. If you need any .additional information, please call me or Barbara Brenner at 326-3979. MEMORANDUM "WE CARE" September 26, 1991 TO: Linda Robinson, Recreation Division FROM: Barbara Brenner, Hazardous Materials Division REGARDING: Completion of RMPP for the park pools. We are currently working on a final draft.of the Risk Management and Prevention Plan for the chlorination of the park pools. The law requires that a detailed training program be included in the RMPP. I have summarized the practices of the Recreation Department regarding the training of maintenance staff. I am, however, left with one question which must be answered by Recreation staff. The question can be most easily stated and answered by having you complete the sentence below with.an amount of time. Pool maintenance trainees will receive closely supervised hands ojk training regarding the chlorination systems for at least '~ ~6~<~ before being required to perform any inspectEons or ~outine duties alone. Please call me as soon as possible (326-3979) to let me know the amount of time which you feel Would be needed to properly train a new employee. We will then finish the draft RMPP and send out copies for review.. cc: Ralph Huey CITY BAKERSFIELD' ~.~ · ~ ~. ~ FIRE DEPARTtvlENT 2101 H STREET D, S. NEEDHAM J~i~16,1991 BAKERSFIELD 93301 FIRE CHIEF 326-3911 Jim Ledoux Recreation Superintendent ~.4101 Truxtun Ave. Bakersfield, CA 93309 Dear Jim: The California Health and Safety Code requires Bakersfield Fire to request the handler of an acutely hazardous material (AHM) to complete a Risk Management and Prevention Program (RMPP) if the use of the AHM presents a significant risk of an accident. In February of 1991, we requested a RMPP for the use of gaseous chlorine at eight Bakersfield park pools. ~ Hazardous .Materials Division Staff have now.'c~mpleted the preliminary studies upon which a RMPP must be based. The attached document contains hazard, risk and consequence analyses for the poQ1 chlorination facilities. Please review the document and contact either Barbara Brenner or myself at 326-3979 by 8-9-91 regarding your questions, comments or concerns. We plan to prepare the draft RMPP during the later part of August. We appreciate the assistance and cooperation of the Recreation Department staff toward the completion of this Risk Management and Prevention Plan. Sincerely, alph E.~- Materials Coordinator cc: Leland Anderson Mike Kelly Scott Manzer Linda Robinson M E M O R A N D U M RECEIVED TO: Barbara Brenner, Hazardous Materials HAZ. MAT. DIV. FROM: Mike Quon,~ilding Department DATE: June 7, 1991 SUBJECT: Swimming Pool Utility Buildings at Various City Parks I have reviewed plans for construction of storage buildings at various City parks. These plans were provided by the Public Works Department. 1) Siemon Park The plan consists of sheets 4 and 6, dated February 1964. The size of the structure is about 48' by 13'. The building is designed with reinforced masonry block walls on concrete footings. The roof is of gravel on 3/8" plyscord supported with 2 x 8 rafters on 24" centers. 2) Jefferson Park The plan consists of 2 sheets dated April 1970. The size of the structure is about 12' by 18'. The building is designed with reinforced masonry block walls on continuous concrete footings. The roof is of cedar shake on 3/4" plywood supported with 2 x 6 rafters on 24" centers. 3) Wayside Park The plan consists of 1 sheet dated January 1977. The size of the structure is about 16' x 9'. The building is designed with reinforced masonry block walls on continuous concrete footings. The roof is of 4 ply material on 1/2" plywood supported with 2 x 6 rafters on 16" centers. In general, this type of structure design would be classified as a reinforced masonry building and is in substantial conformance with City codes. This type of structure might sustain damage during a major earthquake, but should be feasible to repair afterwards. MQBB _ .. MEMORA'N'DUM · ~ "WE CARE" ~pril 1, 1991 TO: Mike Quon Building Department FROM: Barbara Brenner '~ Hazardous Materials Division~ Fire Department REGARDING: Seismic review of park pool utility buildings. State law requires that a Risk Management and Prevention Plan (RMPP) be developed for any operation which utilizes an acutely hazardous material and poses.a significant risk if the material is released. The use of gaseous chlorine at 7 park pools brings the City of Bakersfield under this requirement. The Hazardous Materials Division is currently working with the Recreation Department to complete these plans. The RMPP must consider the consequences of an earthquake. We must ask the Building Department's technical assistance in this part of the hazard analysis. I am requesting that the Building Department conduct a seismic evaluation inspection at each of the following pool facilities: Beale Park Planz Park Jefferson Park Jastrow Park · Saunders Park Siemon Park Martin Luther King Jr. Park We are interested to know if the pool utility buildings are reinforced with steel and what type of structural failures could be expected in an earthquake of Richter Scale magnitude 8.3. Please include any other information which is pertinent or ~routinely ~ncluded in seismic evaluations. All of the chlorine storage buildings are easily identified by the exterior chlorine hazard warnings. Linda Robinson of the Recreation Department (326-3701) can provide a master key to the utility rooms. I am available to accompany the inspector if you find it necessary. It would ~e very helpful if you could arrange to have these inspections completed as soon as possible. Please call me at 3979 if there are any questions. Thank you for your assistance. cc: Ralph Huey PREPARER QUALIFICATIONS Ralph Huey: Hazardous Materials Coordinator, City of Bakersfield. Bachelor of Science in Engineering from the University of Pennsylvania. Masters Degree in Business Administration from Duquesne University. State of California Registered Environmental Assessor # 02199. Chairman of California Region 5 Local Emergency Planning Committee (LEPC). Commissioner on the California Chemical Emergency Planning and Response Commission (CEPRC) and a member of the CEPRC Chemical Exposure Subcommittee. Barbara Brenner: Hazardous Materials Planning Technician, City of Bakersfield Fire Department. Bachelor of Arts in Public Administration from California State University. State of California Registered Grade II Water Treatment Plant Operator # 13815. American Water Works Association Water Distribution System Operator # 04304. Member of CEPRC Community Right to Know Subcommittee representing California agencies which administer Chapter 6.95 of the CA Health and Safety Code. Member of Region 5 LEPC Risk Analysis and Community Right to Know Subcommittees. Jerry Delaurie: Craftworker I, city of Bakersfield Recreation Department. National Swimming Pool Foundation Certified Swimming Pool Operator # 93- 08620. Five years experience operating and maintaining the Bakersfield park pool chlorinators. ..._ .. CITY of BAKERSFIELD FIRE ~EPARTMENT 2101 H STREET D. S. NEEDHAM BAKERSFIELD, 93301 FIRE CHIEF 326-3911 ~eb~ua~y 8, ~99Z Ms. Linda Robinson Aquatics Director Bakersfield Recreation' Department Bakersfield, CA Dear Linda: The Bakersfield Recreation Department has been identified as a handler of gaseous chlorine an acutely hazardous material. It has been determined that the swimming pool operations may present an acutely hazardous materials accident risk, Therefore, pursuant to section 25534 of the California Health and Safety Code, a Risk Management and Prevention Program (RMPP) will be required for the use and handling of chlorine at Wayside, Jefferson, Saunders, Planz, Siemon, Martin Luther King, Jastro and Beale ParKs. The RMPP shall be based upon a risk assessment which shall consider all of the following:. THE RESULTS OF A HAZARD ANALYSIS .WHICH IDENTIFIES THE HAZARDS ASSOCIATED' WITH THE HANDLING OF AN ACUTELY HAZARDOUS MATERIAL DUE TO OPERATING ERROR, EQUIPMENT FAILURE AND EXTERNAL EVENTS WHICH MAY PRESENT AN ACUTELY HAZARDOUS MATERIALS ACCIDENT RISK. FOR THE HAZARDS IDENTIFIED IN THE HAZARD ANALYSIS, AN OFFSITE CONSEQUENCE ANALYSIS WHICH ASSUMES ,PESSIMISTIC AIR DISPERSION AND OTHER ADVERSE ENVIRONMENTAL CONDITIONS. -The RMPP shall include the following elements: A DESCRIPTION OF EACH ACCIDENT INVOLVING ACUTELY HAZARDOUS MATERIALS WHICH HAS OCCURRED AT THE FACILITY WITHIN THREE YEARS FROM THE DATE OF THIS RMPP REQUEST. THIS DESCRIPTION SHALL INCLUDE THE UNDERLYING CAUSES OF THE ACCIDENT AND THE MEASURES TAKEN, IF ANY, TO AVOID A RECURRENCE OF A SIMILAR ACCIDENT. A REPORT SPECIFYING THE NATURE, AGE AND CONDITION OF THE EQUIPMENT USED TO HANDLE ACUTELY HAZARDOUS MATERIALS AT THE FACILITY. INCLUDE SCHEDULES FOR TESTING AND MAINTENANCE OF THIS EQUIPMENT. DESIGN, OPERATING AND MAINTENANCE CONTROLS WHICH MINIMIZE THE RISK OF AN ACCIDENT INVOLVING ACUTELY HAZARDOUS MATERIALS. DETECTION, MONITORING OR AUTOMATIC CONTROL SYSTEMS WHICH MINIMIZE THE POTENTIAL RISKS POSED BY ACUTELY HAZARDOUS MATERIALS ACCIDENTS. IN RESPONSE TO THE FINDINGS OF THE RISK ANALYSIS, ADDITIONAL STEPS TO BE TAKEN BY THE BUSINESS IN ORDER TO REDUCE THE RISK OF AN ACCIDENT INVOLVING ACUTELY HAZARDOUS MATERIALS. THESE ACTIONS MAY INCLUDE ANY OF THE FOLLOWING: INSTALLATION OF ALARM, DETECTION, MONITORING OR AUTOMATIC CONTROL DEVICES. EQUIPMENT MODIFICATIONS, REPAIRS OR ADDITIONS. CHANGES IN THE OPERATIONS, PROCEDURES, MAINTENANCE SCHEDULES OR FACILITY DESIGN. THE RISK MANAGEMENT AND PREVENTION PROGRAM SHALL IDENTIFY, BY TITLE, ALL PERSONNEL AT THE BUSINESS WHO ARE RESPONSIBLE FOR CARRYING OUT THE SPECIFIC ELEMENTS OF THE RMPP AND A DESCRIPTION OF THEIR RESPECTIVE RESPONSIBILITIES. THE RMPP SHALL INCLUDE A DETAILED TRAINING PROGRAM TO INSURE THAT THOSE PERSONS ARE ABLE TO IMPLEMENT THE RM~P. AUDITING AND INSPECTION PROGRAMS DESIGNED TO ALLOW THE HANDLER TO CONFIRM THAT THE RISK' MANAGEMENT AND PREVENTION PROGRAM IS EFFECTIVELY CARRIED OUT. RECORD KEEPING PROCEDURES FOR THE RISK MANAGEMENT AND PREVENTION PROGRAM. THE ACUTELY HAZARDOUS MATERIALS HANDLER SHALL REVIEW THE RISK MANAGEMENT AND PREVENTION PROGRAM'AND SHALL MAKE NECESSARY REVISIONS TO THE RMPP AT LEAST EVERY THREE YEARS. REVISIONS SHALL BE MADE WITHIN 60'DAYS FOLLOWING A MODIFICATION WHICH WOULD MATERIALLY AFFECT THE HANDLING OF AN ACUTELY HAZARDOUS MATERIAL. Bakersfield Fire Department Hazardous Materials Division is the administering agency for this state mandated risk management program. As I indicated during our phone conversations, Haz-Mat will do the analysis and complete the RMPP reports for City of Bakersfield depar~tments which are required to comply. I have made hazard analysis inspections with Jerry Delaurie and expect to have some draft RMPP documents'.for your review in early March. We can cover most of the Haz-Mat training requirements when we meet on February 21. Please call me at 326-3979 if you have any questions or concerns regarding the preparation of these Risk Management Plans. Sincerely, bara Brenner Hazardous Materials Planning Technician cc: Ralph Huey RISK RBNK'IN6 - Bakersfield Park Pools, Chlor'!~ne FBCILITY RISK INDEX 4]5 X ; INSPECTION HISTORY 0 POPULATION EXPOSED 7 X 2 MOP 5 X 1 T'OX F~O'TOR 8 X TOTAL. FaCZL. ITY RISK INDEX RaTIN6 W = 6ci. ivi%ie5 or* condiiions ihs{. increase %he likelihood o¢ are. ieas~, 8 x ,5 = ~ (NO, OF YES ANSWERS ON THE QUESTtO!\N61RE 1-13, Add '1 ;/es to each facility for '-+ ¢ .,. ~orag_ and minima]. X = 'This fac'for r'e¢lects a company's claim (safety) history, (WORKER p.m.~p F~O~OR HgXIHUM E~xPECTED Iq ~ 5) Y = .Self reported acciden't / safe~y record. 0 (RES~SONASLE=(3, IN~OEQJC~TE=0,25 6ROSSLY IN~DE~U2TE=e ~) Z = A discre'tionary ca~agory u~ed ~o account, for factors no'f, direcf, iy addressed .i.n ~he ques+,ionnaire, 0.5 (~e of equipment) (OTHER COMPLIC6TIN6 F~CTORS MiNIH~L=¢, CONSIDER~]BLE=O.S, 5UBST~NTI~L=i,O) FACILITY RISK INDEX = 4,5 R~.T.!,'NG FI ~= W + X + Y + Z RATING RATIONALE: Risk incpeaSes with increasing process comp .... ,.i~y and potent.iai for POPULrfiTZON EXPOSEO - RATING 1. IS TOXIC MRTERt¢',.L hPT TO BECOME &IRBORN RAPIDLY ~..e. ~ ~'~,5.~, FINE DUST HIGHLY UOL~T!LE L.~QUID NO=t YES= 2 IF ANSWER TO :~1 IS NO, PROCEED TO ~S IF hNS~JER 1'0 :~t iS YES,_ESTtMF~TE THE EUhCUhT!ON RADIUS, USING THE B~KER~FIELD FIRE DEPT, 6RhPH MODEL, F~t'4D .,~NS~ER"-' ~UESTIONS .4-5. IS 'THERE: 6 SCHOOL WiTH tN I"HE EbOE, UhlION RADIUS T IS .HER~ h NURSING HOME OR HOSPITAL. ~JITH IN THE EUhCUATION R~DZUS ? NO=~, YES=I ZS THERE r..ESZDENI~L HOUSZN6 ~Z'THZN THE ~V~.,u~FION R~DIUS ? !xlO=~ YES='I ZS THE POPULATION DENSITY OF THIS ~RE~ HZSHER TH~N THE ¢WERA6E DUE TO~LOT OF MULTISTORY BUILDINGS NO=O; YES=~ bJH~T ZS THE 00CUP~NCY OF THE BUILDING THRT f4HM IS STORED OR H~NDLED tN ? LESS TH~N 5 PEOPLE=~ 6 - 25 PEOPLE =2 26 -- S0 PEOPLE =3 HORE 'FH~N 5¢ PEOPLE =4 T'OI'F~L.. POPULATION EXPOSED R~TING FAC,~Li'FY I!';FORNAiZON Please answer each o.f_...the foilowin~ quessions by cicciihg ¥ (yes) or N no). 1. Is any acutely hazardous material (AHM) manufactured or used in a chemical reaction ~ '~)/ N 2. Is any other.flammable gas, flammable liquid or explosive material manufactured or used in a chemfcal reaction ? ~fogo~j,~ I~e~_~ y~. N 3. Is any reaction in question 1 or 2 a moderately or highly exothermic reaction ( e.g. alkylation esterfication, oxidation, nitration, polymerization or condensation) or one involving electrolysis 4. Can any unplanned release of a AHM to the atmosphere result from. the malfunction of any scrubbing, treatment or neutralization system or the discharge of a pressure relief system ~ ~/ N 5. Does any physical or chemical process in which an AHM is produced or used involve a batch process ? Y 6. Does any physical or chemical process involve the production or use of any AHM at a pressure in 7. In excess of 275 psig ~ Y / N~ 8. Does any physical or chemical process involve the production or use of an AHM at a temperature above 125 degrees F ? 9. In excess of 250 degrees ~ Y 10. Can any explosive dust be present in any closed container within I00 feet of an AH~ or otherwise be present in the same building as an AHM ~ Y /(~x~ 11. Is there any ignition source or open flame within 100 ft. of any process, storage or transfer area where a flammab~ie, or explosive AHM is present , except 'where there is a firewail providing protection ~ Y 12.Is any lined or non-metallic pipe used in the transfer of any AHM o 1U. Is any equipment or piping handlin~ any AHM more 10 years cid o /~-)/ N PLEAS£ PROVIDE THE FOLLOWING INFOR}]ATIO~;{ · Attach additional pa~es it' necessary) 1. Your company's current workers eompensanion j~ experience modification'factor. ~ 2. How many people occupy the building in which AHM's are used or stored ? O ~ ~ 3. Give details of all accidents which involved any hazardous material and all other instances when the fire department has been summoned in an emergency. 4. Briefly described the Operations process at your plant and the specific processes utilizing AHM's, inCluding storage proceedures. -2- 5. Briefly describe ti~e ~enui:3ment being used in tile processes involving AHMs. Report quantity of AHM(s), referenced in the cover letter, that this business handles. a) Maximum amount on hand at any One time ~' b) Please attach a Material Safety'Data Sheet for an~ material that is a mixture. Do not include MSDS for pure substances. DEMOGRAPHIC DATA: State the straight line distance in feet between the business property line and each of the following. 1. Nearest school. 2. Nearest daycare Center, hospital, nursing home or similar facility. 3. Nearest residence/motel etc. 4. Nearest occupied building. Business Name: I certify that the foregoing information is true and correct to the best of myknowledge. Signature: --~-- RISK MANAGEMENT AND PREVENTION PROGRAM RISK REDUCTION MEASURES Based on the consequence analyses and the review of operations, the City Recreation Division will convert the City pools from gaseous chlorine to liquid chlorine. We are currently examining several liquid chlorination systems and are in the process of deciding which will be the most cost effective and safest to use. We will not be able to convert all the pools at once due to budget restraints. At the sites noted, residences are particularly close or in the predominate .downwind path. The school year overlaps with pOol schedules slightly during early June and late August. The schools open for summer session vary every year, however the special schools fOr the handicapped usually conduct a summer session. 1. Wayside: R'estrooms, exits and phone areas all expected impacted by chlorine plume. A school for handicapped children is adjacent to this location in the predominant downwind location. 2. Jefferson: Location of chlorination equipment in subterranean equipment room dangerous to maintenance workers. Escape may be difficult due to heavy nature of chlorine which will cause it to linger in a low area. Position of relief vent on pool deck. Child care facility directly across'the street. 3. M.L.K: Pool area is enclosed by walls deterring dispersion of ' chlorine. Community center is immediately adjacent to pool. Rest- rooms, exits and phone likely to be affected by chlorine release. Relief vent is only eight feet off the ground in a sheltered location. School adjacent. 4. Siemon: Restrooms, phones and'exits in close proximity to the chlorination room. 5. Jastro: Proximity of restrooms to chlorine room. Residences located immediately to south and east. 6. Saunders: ReStrooms, phones and exits in close proximity to the chlorination room. 7. Planz: Restrooms, phones and exits in close proximity to the chlorination room. 8. Beale~ Phones and enclosed spaces further from chlorine than at other pools. RISK MANAGEMENT AND PREVENTION PROGRAM IMPLEMENTATION FALL 1991 Evaluate the various alternative liquid chlorination systems regarding cost and effectiveness. Begin documentation of training and maintenance as outlined in the RMPP. FEBRUARY 1992 Recreation Division to notify BakerSfield Fire, Hazardous Materials Division regarding their choice of liquid chlorination systems. SPRING 1992' Conversion of the first two pool sites to conform with risk reduction plan. We have selected Wayside and M.L.K pools as the first locations to convert. SUMMER 1992 Evaluate the pilot projects for cost effectiveness and safety. FALL 1992 Convert more pools over to liquid chlorination, as the budget allows. RISK MANAGEMENT AND PREVENTION PROGRAM RISK REDUCTION MEASURES Based on the consequence analyses and the review of operations, the City Recreation Division will convert the City pools from gaseous chlorine to liquid chlorine. We are currently examining several liquid chlorination systems and are in the process of deciding which will be the most cost effective and safest to use. We will not be able to' convert all the pools at once due to budget restraints. At the sites noted, residences are particularly close or in the predominate downwind path. The school year overlaps with pool schedules slightly during early June and late August. The schools open for summer session vary every year, however the special schools for the handicapped usually conduct a summer session. 1. Wayside: Restrooms, exits and phone areas all-expected impacted.by chlorine plume. A school for handicapped children is adjacent to this location in the predominant downwind location. 2. Jefferson: Location of chlorination equipment in subterranean equipment room dangerous to maintenance workers. Escape may be difficult due to heavy'nature of chlorine which will cause it to linger in a iow area. Position of relief vent om pool deck. Child care facility directly.across the street. 3. M.L.K: Pool area is enclosed by Walls deterring dispersion of chlorine. Community center is immediately adjacent to pool. Rest- rooms, exits and phone likely to be affected by chlorine release. Relief vent is only eight feet off the ground in a sheltered location. School adjacent. 4. Siemon: Restrooms, phones and exits in close proximity to the chlorination room. 5. Jastro: Proximity of restrooms to chlorine room. Residences located immediately to south and east. 6. Saunders: Restrooms, phones and exits in close proximity to the chlorination room. 7. Plan~: Restrooms, phones and'ex/ts in close proximity to the chlorination room. .8. Beale: Phones and enclosed spaces further from chlorine than at other pools. RISK MANAGEMENT AND PREVENTION PROGRAM IMPLEMENTATION FALL 1991 Evaluate the various alternative liquid chlorination systems regarding cost and effectiveness. Begin documentation of training and maintenance as outlined in the RMPP. FEBRUARY 1992 Recreation Division to notify Bakersfield Fire, Hazardous Materials Division regarding their choice of liquid chlorination systems. ~PRING 1992~ Conversion of the first two pool sites to 'conform with risk reduction plan. We have selected Wayside and M.L.K pools as the first locations to convert. SUMMER 1992 Evaluate the pilot.projects for cost. effectiveness and safety. FALL 1992 Convert more pools over to liquid chlorination as the budget allows. HAZARD ANALYSIS CHECKLIST ChemiCal Storage: 1. Amount of C12 stored, in season? Amount of C12 stored, off season? 2. How are cylinders secured? C~~ ~'~3~ ~0~ld~'r~ S. Other Chemicals on site and location of storage? ~o~_ g%%~.. Reactive with C127 ~O~3 (~, 4. C12 consumption rate lbs/day? ~ -%0 I~¢O~b/~ 'ks% 5. Number of cylinders on line at one time? ~ 6. How is storage area ventilated? ~ ~(~3~ 7. Is storage area of combustible construction? 8. Is storage area dry and orderly?~ 9. what else is stored in the 012 storage room and does this area have multiple use? 10. Is hazard labeling adequate? 11. Is storage area secure?,/OtlC~~ Who has access? 12. Who is responsible for receipt of deliveries? 13. How close is storage area to exit? ~ ~i~iC~C~'- Are there other exits? '~/ ~' Chlorination System: ~. , 1. Type of system? bO~ik~c4. .~-~G~o~ 2. Year installed? Was equipment new?' 3.Who designed and installed? '4. Have there been any changes made to system design? 5. Are there any PID's of system? 6. List all system components: 7. Is there visible corrosion or"damage?~o 8. Are there any excess flow controls on the system? 9. Does the system utilize electricity? 't~ ~0~ What are the results of power outage? ' 10. Are lines braced?'~.~a ',~g ~ ?00~ ~(~a 11. Are lines 'susceptible to physical damage? 12. Is s~stem char~ed with chlo=ine and/or in operation while pool is unattended? Maintenance: 1. Who is responsible fo~ system maintenance? ~'~rr% 2. How many peopi~interact with system in any way? 3. How often is system inspected? ~ ~c~~c~ By whom and against what criteria?~~C~/ ~ -~~~ ~ 4. Is maintenance logged? Training: 1. A~e lifegum~ds trmined regm~ding hazards of ClZ? 'Is there a hazard communication p~ogrmm? Are MSDS available? 3. Are lifeguards trained adequately if the~ change cylinders etc... 4. What t~ining have m~intensnoe personnel h~d? ~ Hr. 5. Are safet~ ~egulations established and adequate? Emergency Identification and Response: 1. Is there a leak detector in the-C12 room with exterior alarm? No 2. Has response plan been established and are emergency procedures posted? I.~_~ ~ ~60~- ~0~0~ 3. Would the phone be in the plume? ~¼~ ~ 6_~0~ ~ %.C-6oc~e~ 4. Are the exits in the plume?-- ~C°~-~n~ ~~ ~%%., O~'~ 5. Has evacuation plan been established, ie. toward upwind site? occo c- 0 Protective Equipment: .... - . 1. What is used while changing cylinders or otherwise working on system? 2. Is~ PE stored on site or in maintenance vehicle? ~Q~ 3. Is eyewash available? Operatin, Procedures: 1. Are there written operating procedures for work on or around system? ~a~. ~ Documented training of daily work staff - guards? History.' 1. AccidentS? Releases Injuries while around or working on System? 3. Equipment failures and system weaknesses? ~O 4. Observations and experiences of staff?fO §. Fire department inspection outcome? 6. OSHA Inspection outcome?~ COSTS. .... HAZARD ANALYSIS CHECKLIST Chemical Storage: 1. Amount of CiE stored, in season? Amount of C12 stored, off' season? 2. How are cylinders secured? 3. Other Chemicals on site and location of storage? . Reactive with C127 4. C12 consumption rate lbs/day? ~_~ 5. Number of cylinders on line at one time? 6. How is storage area ventilated? 7. Is storage area of combustible construction? S. Is storage area dry and orderly? 9. what else is stored in the C12 storage room and does this area have multiple use? 10. Is hazard labeling adequate? 11. Is storage area secure? Who. has access? 12. Who is responsible for receipt of deliveries? 13. How' close is storage area to exit? Are there other exits? Chlorination System: ...... ..=..,= _=~ ............... 10 Type of system? Year installed? Was equipment new? 3. Who designed and installed? 4. Have there been any changes made to system design? 5. Are there any PID's of system? 6. List all system components: 7. Is there visible corrosion or damage? 8. Are there any excess flow controls on the system? 9. Does the system utilize electricity? What are the results of power outage? 10. Are lines braced? 11. Are lines susceptible to physical damage? 12. Is system charged with chlorine and/or in operation while pool is unattended? Maintenance: i. Who is responsible, fo~ system maintenance? 2. Mow many people interact with system in any way? 3. How often is system inspected? By whom and against what criteria? 4. Is maintenance logged? Training: 1. Are lifeguards trained regarding hazards of C127 2. Is there a hazard communication program? Are MSDS available? 3. Are lifeguards trained adequately if they change cylinders etc... 4. What training have maintenahce personnel had? 5. Are safety regulations established and adequate? Emergency Identification and Response: . 1. Is there a leak detector in the C12 room with exterior alarm? 2. Has response plan been established and are emergency procedures posted? 3. Would the phone be in the plume? 4. Are the exits in the plume? 5. Has evacuation plan been established, ie. toward upwind site? - Protective Equipment: 1. What is used while changing cylinders or otherwise working on system? Z. Is PE stored on site or in main.tenance vehicle? 3. Is eyewash available?. Gas Masks, SCBA? Operating Procedures: 1. Are there written operating procedures for work on or around system? Documented training of daily work staff - guards? History: 1. Accidents? Releases .2. Injuries while around or working on.system? 3. Equipment failures and system weaknesses? 4. Observations and experiences .of staff? 5. Fire department inspection outcome? 6. OSHA Inspection outcome?. COSTS ..... HAZARD ANALYSIS CHECKLIST pool Site: Chemical Storage: 1. Amount of C12 stored, in season? ~ Amount of C12 stored, off season? 2. How are cylinders secured? 3. Other Chemicals on site and location of storage? Reactive with C127 4. C12 consumption rate lbs/day? 5. Number of cylinders on line at one time? 6. How is storage area ventilated? 7. Is storage area of combustible construction? 8. Is storage area dry and orderly? 9. What else is stored in the C12 storage'room and does this area have multiple use? 10. Is hazard labeling adequate? 11. Is storage area secure? Who has access? 12. Who is responsible for receipt of deliveries? 13. How close is storage area to exit? Are there other exits? Chlorination System: 1. Type of system? Year installed? Was equipment new? 3. Who designed and installed? 4. Have there been any changes made to system design? §. Are there any PID's of system? 6. List all System components: 7. Is there visible corrosion or damage? 8. Are there any excess flow controls on the system? 9. Does the system utilize electricity? What are the results of power outage? 10. Are lines braced? 11. Are lines susceptible to physical damage? 12. Is system charged with'chl°rine and/or in operation while pool is unattended? Maintenance: 1. Who is responsible fo~ system maintenance? 2. How many people interact with system in any way? S. How often is system inspected? ~By whom and against what criteria? 4. Is maintenance logged? Training: 1. Are lifeguards trained regarding hazards of C127 2. Is there a hazard communication program? Are MSDS available? 3. Are lifeguards trained adequately if they change cylinders etc... 4. What training have maintenance personnel had? 5. Are safety regulations established and adequate? Emerge$cy Identification and Response: 1. Is there a leak detector in'the C12 room with exterior alarm? 2. Has response plan been established and are emergency procedures posted? 3. Would the phone be in the plume? 4. Are the exits in the plume? 5. Has evacuation plan been established, ie. toward upwind site? Protective,Equipment: 1. What is used while changing cylinders or otherwise working on system? 2. Is PE stored on site or in maintenance vehicle? 3. Is eyewash available? Gas Masks, SCBA? ODerating Procedures: 1. Are there written operating procedures for work on or around system? Documented training of daily work staff - guards? History: 1. Accidents? Releases 2. Injuries while around or working on 'system? S. Equipment failures and system weaknesses? 4. Observations and experiences of staff? 5. Fire department inspection outcome? 6. OSHA Inspec.tion outcome? COSTS ..... HAZARD ANALYSIS CHECKLIST Pool Site: Chemical Storage: 1. Amount of C12 stored, in season? Amount of C12 stored, off season? 2. How are 'cylinders secured? 3. Other Chemicals on site and location of storage? Reactive with C127 ~' 4. C12 consumption r.te lbs/da~?~ 5. Number of cylinders on line at one time? ~ 6. How is storage area ventilated? 7. Is storage area of combustible construction? 8. Is storage area dry and orderly? ~6~ 9. what else is stored in the C12 storage room and does this area have multiple use? ~~ a~~ gO0~,.. 10. 'Is hazard labeling adequate?~~~ ~OC ~ I~b ~OD~ Ne~_~ 11. Is storage area secure? Mt Who has access? 12. Who is responsible for receipt of deliveries? 13. How close is ~torage area to exit? Are there other exits? 1. Type of system? ~C~C 2. Year installed? Was equipment new? Who designed and installed? 4. Have there been any changes made to system design? 15. Are there any PID's of system? List all system components: 7. Is there visible corrosion or damage?~ 8. Are there any excess flow controls on the system? 9. Does the system utilize electricity? What are the results of power outage? 11. Are lines susceptible to physical damage? /h/~ %~/c~ ~_~ 12. Is system charged with chlorine and/or in operation while pool is unattended? ~L Maintenance: i. Who is responsible fo~ system maintenance? 2. How many people interact with system in any way? S. How often is system inspected? By whom and against what criteria? 4. Is maintenance logged? Training: 1. Are lifeguards trained regarding hazards of C127 2. Is there a hazard communication program? Are MSDS available? 3. Are lifeguards trained adequately if they change cylinders'etc... 4. What training have maintenance personnel had? 5. Are safety regulations established and adequate? Emergency Identification and Response: 1. Is there a leak detector in the C12 room with exterior alarm? 2. Has response plan been established and are emergency procedures posted? ~vl~ 3. Would the phone be in the plume? 4. Are the exits in the plume? 5. Has evacuation plan been established~ ie. toward upwind si.re? Protective Equipment: -.....-~ ._ ._._._.~_ ...... 1. What is used while changing cylinders or otherwise working on system? 2. Is PE stored on site or in maintenance vehicle? 3. Is eyewash available? Gas Masks, SCBA? Operating Procedures: 1. Are there written operating ~,roc~d~res for work on or around Documented training of daiAy w6rk staff - guards? Histor~z: 1. Accidents? Releases ~Q 2. Injuries while around or working on system? 3. Equipment failures and system weaknesses? 4. Observations and experiences of staff? Fire department inspection outcome? 6. OSHA Inspection outcome? Al0 ' COSTS ..... HAZARD ANALYSIS CHECKLIST Chemical Storage: 1. Amount of C12 stored, in season?~ Amount of C12 stored, off season?~ 2. How are cylinders secured?~k~,~. 3. Other Chemicals on site and location of storage? Reactive with 0127 4. C12 consumption rate lbs/day? 5. Number of cylinders on line at one time? ~_~ 6. How is storage area ventilated?-~ 7. Is storage area of combustible 8. Is storage area dry and orderly?~ 9. what else is stored in the C12 storage room and does this arem have multiple, use? ~'t~,4[~,~ ~_ 10 Is hazard labeling adequate? 11. Is storage area secure? ~f $ Who has access? 12. Who is responsible for receipt of deliveries? 13. How close is storage area to exit? Are there other exits? Chlorinatio'n System: 1. Type of system? 2. Year installed? Was equipment new? ' 3. Who designed and installed? 4. Have there been'any changes made to system design? 5. Are there any PID's of system? 6. List all system components: 7. Is there visible corrosion or damage?~O 8. Are there any excess flow controls on the system? 9. Does the system utilize electricity? What are the results of power outage? 11. Are lines susceptible to physical damage? ). 12. Is system charged with chlorine and/or in operation while pool .is unattended? Maintenance: 1. Who is responsibl'e fo~ system maintenance? 2. How many people interact with system in any way? 3. How often is system inspected? By whom and against what criteria? 4. Is maintenance logged? Training: 1. ~Are lifeguards trained regarding hazards of C127 2. Is there a hazard communication program? Are MSDS available? 3. Are lifeguards trained adequately if they change cylinders etc... 4. What training have ~aintenance personnel' had? 5. Are safety regulations established and adequate? Emergency Identification and Response: 1. Is there a leak detector in the C12 rooTM with exterior alarm? 2. Has response plan been established and are emergency procedures posted? S. Would the phone be in the plume? 4. Are the exits in the plume? §. Has evacuation pla. n been. established,' ie. toward upwind site? -~Protective Equipment: 1. What is used while changing cylinders or otherwise working on system? 2. Is PE stored on site or in maintenance vehicle? 3. Is eyewash available? Gas Masks, SCBA? Operating Procedures: 1. Are there written operating procedures for work on or around system? Documented training of daily work staff - guards? History: 1. Accidents? Releases 2. Injuries while around or working on system? 3. Equipment failures and System weaknesses? 4. Observations and experiences of staff? 5. Fire department inspection outcome? 6. OSHA Inspection outcome? COSTS ..... HAZARD ANALYSIS CHECKLIST Chemical Storage: of C12 stored, in season? ~ 1. Amount Amount of C12 stored, off season? 2. How are'cylinders secured? 3. Other Chemicals on site and location of storage? Reactive with C127 4. C12 consumption rate lbs/day? ~-~ I~~ 5. Number of cylinders on line at one time? 6. How is storage area ventilated? 7. Is storage area of combustible construction? 8. Is storage area dry and orderly? 9. What else is stored in the C12 storage room and does this area have multiple use? 10. Is hazard labeling adequate? 11. Is storage area secure? Who has access? 12. Who is responsible for receipt of deliveries? 13. How close is storag'e area to exit? Are there other exits? Chlorination System: 1. Type of system? 2. Year installed? Was equipment new? 3. Who designed and installed? 4. Have there been any changes made to system design? Are there any PID's of system? List all system components: 7. Is there visible corrosion or damage? 8. Are there any excess flow controls on the system? 9. Does the system utilize electricity? What are the results of power outage? 10. Are lines braced? 11. Are lines susceptible to physical damage? 12. Is system charged with chlorine and/or in operation while pool i's unattended? Maintenance: i. Who is responsible fo~ system maintenance? 2. How many people interact with system in any way? 3. How often is system inspected? By whom and against what criteria? 4. Is maintenance logged? Training: 1. Are lifeguards trained regarding hazards of C127 2. Is there a hazard communication program? Are MSDS available? 3. Are lifeguards trained adequately if they change cylinders etc... 4. What training have maintenance personnel had? 5. Are safety regulations established and adequate? Emergency Identification and Response: 1. Is there a leak detector in the C12 room with exterior alarm? 2. Has response plan been established and are emergency procedures posted? 3. Would the phone be in the plume? 4. Are the exits in the plume? 5. Has evacuation plan been established, ie. toward upwind site? .Protective Equipment: 1. What is used while changing cylinders or otherwise working on system? 2. Is PE stored on site or in maintenance vehicle? 3. Is eyewash available? Gas Masks, SCBA? Operating Procedures: 1. Are there written operating procedures for work on or around system? Documented training of daily work staff - guards? History: 1. Accidents? Releases Injuries while around or working on system? 3. Equipment failures and system weaknesses? 4. Observations and experiences of staff? 5. Fire department inspection outcome? 6. OSHA Inspection outcome? COSTS ..... HAZARD ANALYSIS CHECKLIST Pool Site: t/~ Chemical Storage: 1. Amount of Ci~. stored, in season? Amount of ClX. stored, off season? 2. How are cylinders secured? 3. Other Chemicals on site and location of storage? Reactive with C127 4. C12 consumption rate lbs/day? ~-~ lb 5. Number of cylinders on line at one time? ~2~ 6. How is storage area ventilated? 7. Is storage area of combustible construction? 8. Is storage area dry and orderly? b~ 9. what else is stored in the C12 storage room and does this area have multiple use? 10. Is hazard labeling adequate? ~}~ 11. Is storage area s~ecure? Who has access? 12. Who is responsible for receipt of deliveries? 13. How close is storage area to exit? Are there other exits? .Chlorination System: 1. Type of system? 2. Year installed? Was equipment new? 3. Who designed, and installed? 4. Have there been any changes made to system design? 5. Are there any PID's of system? 6. List all system components: 7. Is there visible corrosion or damage? 8. Are there an~ excess flow controls on the system? 9. Does the system utilize electricity? What are the results of power outage? 10. Are lines braced? 11. Are lines susceptible to physical damage? 12. Is system charged with chlOrine and/or in operation while pool is unattended? Maintenance: 1. Who is responsible fo~ system maintenance? 2. How many people interact with system in any way? 3. How often is system inspected? By Whom and against what criteria? 4. Is maintenance logged? Training: 1. Are lifeguards trained regarding hazards of C127 2. Is there a hazard communication program? Are MSDS available? 3. Are lifeguards trained adequately if they change cylinders etc... 4. What training have maintenance personnel had? 5. Are safety regulations established and adequate? Emergency Identification and Response: 1. Is there a Ieak detector in the C12 room with exterior alarm? 2. Has response plan been established and are emergency procedures posted? 3. Would the phone be in the plume? 4, Are the exits in the plume? 5. Has evacuation plan been established, ie. toward upwind site? Protective Equipment: 1. What is used while changing Cylinders or otherwise working on system? 2. Is PE stored on site or in maintenance vehicle? 3. Is eyewash available? Gas Masks, SCBA? Operating Procedures: 1. Are there written operating procedures for work on or around system? Documented training of daily work staff - guards? History: 1. Accidents? Releases 2. Injuries while around or working on system? 3. Equipment failures and system weaknesses? 4. Observations and experiences of staff? 5. Fire department inspection outcome? 6. OSHA Inspection outcome? COSTS ..... HAZARD ANALYS~S CHECKLIST Pool Site: ~6m Chemical Storage: 1. Amount of C12 stored, in season? Amount of C12 stored, off season? '2. How are cylinders secured? / 3. Other Chemicals on site and location of storage? Reactive with Cl2?~,~,~ / 4. C12 consumption rate lbs/day? ~-~ lb/~ 5. Number of cylinders on line at one time? storage area ventilated? ~ ~-~O~. //~'~ ~CrO'~,,' CO~.~ 6. How is 7. Is storage area of combustible construction? 8. Is storage area dry and orderly? 9. What .else is stored in the C12 storage room and does this area have 10. Is hazard labeling adequate?~ 11. Is storage area secure? Who has access? b~ 12. Who is responsible for receipt of deliveries? 13.Are How clo~ethere other is storage exits? area to exit? Chlorination System: 1. Type of system? 2. Year installed? Was equipment new? 3. Who designed and installed? 4. Have there been any changes made to system design? 5. Are there any PID's of system? ~6. List all system components: 7. Is there visible corrosion or damage? 8. Are there any excess flow controls on the system? 9. Does the system utilize electricity? What are the results of power outage? 10. Are lines braced? 11. Are lines susceptible to physical damage? 12. Is system charged with chlOrine and/or in operation while pool is unattended? Maintenance: 1. Who is responsible fo~ system maintenance? 2. How many people interact with system in any way? 3. How often is system inspected? By whom and against what criteria? 4. Is maintenance logged? Training: 1. Are lifeguards trained regarding hazards of C127 2. Is there a hazard communication program? Are MSDS available? 3. Are lifeguards trained adequately if they change cylinders etc... 4. What training have maintenance personnel had? 5. Are safety regulations established and adequate? Emergency Identification and Response: C~'~ ~,'+ N~ Lor~ ~ 1. Is there a leak detector in the Ct2 room with exterior alarm? 2. Has response plan been established and are emergency procedures posted? 3. Would the phone be in the plume? 4. Are the exits in the plume? 5. Has evacuation plan been established, ie. toward upwind site? Protective Equipment: ~.~-.- ........ ~ 1. What is used while changing cylinders or otherwise working on system? 2. Is PE stored on site or in maintenance vehicle? 3. Is eyewash available? Gas Masks, SCBA? Operating Procedures: 1. Are there written operating procedures for work on or around system? Documented training of daily work staff - guards? History: 1. Accidents? Releases 2. Injuries while around or working on system? '3. Equipment failures and system weaknesses? 4. Observations and experiences of staff? 5. Fire department inspection outcome? 6. OSHA Inspection outcome? COSTS ..... 1700 FI°wet Street Telephone (805) 861-3636 Environmental Health Department ~ ~ .~P. UBLIC SWIMMINGPOOL OPERATION AND MAINTENANCE INSPECTION REPORT ,me o, Poo, ._ .... : : ...... ......... ................................. .. ............. , ..: ,_. ..... ,...,. / ~,' .,_ _._ · Location of Pool:..Z_-:./.'>.~-:/' ..Y.L. ..... .~,~.-. ,:~..: ..... ~ ........... '~..L. .......... ,:~..JZz'z."..' ...................... City: ..... ~~ .......................................... ,'I / , ,-.,. / ~,~ / , o,,~,,.. . .~.?,." .'.: ::...,.:, ,'-~,:.:~, ~'- :-,:.--..~:...... ........................................ ,,,,,,, ,=....~.,:...,....:..~: ............................. · :_,.,.~:,.._ , ~,, fi ,, ,. · .. . 1.. , Owner's AddreSs's: /'./ ,' \..~',: / '-...'C, t. L ,',......,',' ::!././-~--- Phone #: ....................................................... Manager's Address: .......................................................................................................................... Phone #: · '~, / ~/ - / -/~ / ! POINTS TYPE OF INSPECTION: HEALTH & SAFETY 2.:. CODE & CALIFORNIA Routine .... Reinspection: ............... Complaint: .............. Survey: ............... ADMINISTRATIVE CODE (Title 17) ..... :~.../...(10) 1. Clarity of Water (to be closed if in violation) 65545 & 65527 ...... ~...(10) 2. D,s,nfectant Res,dual~.(1.0/1.5 ppm m,n,mu~ m...........opp (CI) 65529 Cyanuric Acid Concentrati~"(re£s-fri~n 100 ppm) ..?_-~/.....ppm ~..,..,.: ..~..::.....110) 3. Chemi~l Balance IpH 7.2 - 6.0) .............................. 65529 t~rnover time) ....... :....(10) 5. Disinfectant Equipment 2-9040, 2-9041, 65529 & 65547 ............ ( ) 6. Test Kits 655291b) ...'.:.:. ..... 15) ?. Operational Re~ords and'S~pervision 65523 ..... ~,:...(5) 9. W~ter Supply and Waste Disposal (backflo~ protection, source, nuisance) 2-9045 .... .'.~:....(5) '10. Sho~er and Toilet Facilities (soap, to~el dispensers, hot and cold ~ater) 65535 & 65551 .... :.~:.;..(10) 11. Lifesaving andSafety (fencing, signs, 12' pole or life ring, safety line, depth markers, 65539, 2-90~, 2-9024(b} lighting, chemical storage, drain cover, electrical receptacles) 2-9028, 2-9025, 3.680.0 ._~.~....(5) 12. Wading Pool - (disinfectant residual) ........ -~---/-/-'-~t ..... ppm 65543 Ichem,ca~,a~ance) pH.._/.~..&.~.: ............ ( ) 13. Replacement of Equipment or Appurtenances 65549 _~.~. ...... (5) 14. Health of Employees and Patrons , : 65541 ¥ .... ~'....,. ......TOTAL Score 10 pt. items - 10 for good, 7 for fair, 0 for poor Score 5 pt. items - 5 for good, 3 for fair, 0 for poor COMMENTS: ...................................................................................................................................................................................................... : ' ~S~nitarian ~ Time For Completion Signed, ~, Title cc: Bakersfield Office Facility Sanitarian Health 580 4110 259 (R er. 12-81 ) MARCH 1131 TUESDAY WEDNESD, 1990 72nd day -- 293 days follow .~.?~ 1 990 73rd day -- 292 days follow .J ..... , . ~f.~: ', ~ ~,. ~ _._ . ...................... ........................ ...... ~ ~': ~: ......................................... FIRST AID AND :~'- MEDICAL MANAGEMENT · .F_OF CH LOR! N E EXPOSU RES I_ I .. Edition 4 ~ February 1985 CHLORINE INSTITUTE PAMPHLET 63 CHLORINE INSTITUTE, IN(:.. 2001 L STREET. N.W.. WASHIN,CaTON. Q.C. 2003~ A~llJ~nal co~ee o~ tttm gamgnl~ -,re avalla~e &l nominal coal Chlorine and YourHealth. --__ THE CHLORINE INSTITUTE, INC. CLOTHING FOR CHLORINE Edition 2 July 1988 CHLORINE INSTITUTE PAMPHLET #65 The Chlorine Institute, Inc., 2001 L Street, NW, Washington, DC 20036