Document dYyV31d9rNE1ZdJy9gKR3BN45

CHG 01606 c champlin ~ *. -i .v. ^ J". Kr ` i ^ V or. INTER-OFFICE CORRESPONDENCE TO: R. A. Arthur OFFICE: FW 2804 FROM: M. A. Hawkinson DATE: 12/02/86 SUBJECT: M&M Protection Consultants Inspection Reports November 10, 11, 1986 Enclosed please find copies of subject reports. This office would appreciate management comments concerning Mr. Frisbie's recommendations within about 30 days. Mark A. Hawkinson MAH/pah/77 cc: R. E. Schneck R. A. Loveless CH/W-002517 M&M PC M&M Protection Consultants A Resource of Marsh & McLennan PROPERTY LOSS PREVENTION REPORT CHAMPLIN PETROLEUM COMPANY REFINERY AND CRUDE TERMINAL Corpus Christi, TX 78400 INSPECTED BY: C. V. Frisbie DATE: November 10-12, 1986 RPJ CH/W-002518 M&M Protection Consultants PROPERTY LOSS PREVENTION REPORT CHAMPLIN PETROLEUM COMPANY REFINERY AND CRUDE TERMINAL Corpus Christi, TX 78400 INSPECTED BY: C. V. Frisbie DATE: November 10-12, 1986 CONFERRED WITH: Mr. Mr. Mr. Mr. R. A. Arthur, Superintendent Operations J. W. Bryant, Manager Employee Relations Robert Loveless, Manager of Safety L. E. Rolando, Safety Engineer DESCRIPTION OF OPERATIONS: This is a 170,000 barrel per day petroleum refinery. The refi nery operations are separated into four areas. These are the East Plant No. 1 and East Plant No. 2, the West Plant, Area 90 Tank Farm, and Area 91 Tank Farm. In addition, docks on the Industrial Canal are separated from exposure by operating facili ties. The refinery operates continuously with process areas constantly attended. A total of 585 employees work three 8-hour shifts, 7 days per week. There are 59 employees at East Plant No. 1 and No. 2 and 15 employees at the West Plant reporting on a minimum shift. CONSTRUCTION: Buildings are predominantly one story without basement of noncom bustible construction. Frame construction is generally limited to cooling towers. Process equipment is located in the open. In East Plant No. 2 and the West Plant, fire proofing material has been provided on the inside and outside of tower skirts as well as along the pipeways. In East Plant No. 1, there are some unprotected supports, or supports having insulation only, installed in these areas. Tanks are located for the most part within standard individual and common dykes. Horizontal bullet- type tanks and pressure storage service such as propane, etc. are not generally provided with dykes, however these are adequately separated from most process areas. EXPOSURES: East Plant No. 1 is exposed on the south by an adjacent refinery. East Plant No. 2 has no exposure to the north and west with expo sure to the south and east being East Plant No. 1 and Tank Farms. West Plant is surrounded by open fields. Process Units in East -1- RP2 CH/W-002519 M&M Protection Consultants Plant No. 2 and the West Plant are well spaced with little conjestion. Conjestion in the older process areas of East Plant No. 1 is considered severe. A truck loading terminal is located well away from process areas at the intersection of Buddy Lawrence Drive and Oak Park Avenue. PROCESSES AND SPECIAL HAZARDS: Crude oil and gas condensate are received via pipeline and tankers. It is processed in conventional refining units including crude topping with associated vacuum operation, cataly tic cracking, alkylation, reforming together with associated treating units. In addition, aromatic operations are conducted in the East plant as well as coke and sulfur production at the West Plant facilities. Products and crude oil storage is pro vided in various tanks contained within standard, and individual dykes, excluding pressure storage in isolated incidents. Tanks, for the most part, are gas tight. Products are shipped by pipe line, tanker, truck, and rail. All products, with the exception of coke and sulfur, are shipped to East Plant facilities while coke and sulfur are shipped by truck and rail at the West Plant. Process equipment is of modern design and incorporates basic safety features. COMMON HAZARDS: Electricity is received from public utility through a double feed to the East and West Plants. A manual tiebreaker is provided. The largest single users of electricity is the 4,000 horsepower motor on the blower at No. 1 Cat in East Plant No. 1 and the Recycle Gas Compressor in No. 4 Platformer in East Plant No. 1. In East Plant No. 2, the largest single user is a 6,000 hor sepower motor on the blower at No. 2 Cat. In the West Plant, the largest user is a 3,500 horsepower motor on the Recycle Gas Compressor of No. 5 Platformer. Emergency generators for some lights and critical instruments are provided at the West Plant, East Plant No. 2, No. 4 Platforming Unit, No. 1 Crude Unit and No. 1 FCCU. The generators are driven by diesel engines and rated as follows: West Plant East Plant No. 2 No. 4 Platforming No. 1 Crude Unit No. 1 FCCU Unit 388 300 50 25 25 KVA KW KW KW KW Electrical installations at this plant are fairly well maintained and explosion-proof equipment is installed with conduits properly sealed where required. -2RP2 CH/W-002520 M&M Protection Consultants In East Plant No. 1 and No. 2 there are two air systems, one for plant air at 100 psi and one for instrument air at 85 psi. In East Plant No. 1, the system is supplied by two motor driven air compressors, one a centrifugal unit and one a reciprocating type unit. In East Plant No. 2, there are two "Centax" compressors, one driven by an electric motor and the other by a steam turbine. All units are equipped with their own dryers. In the West Plant, there are three centrifugal air compressors, two driven by electric motors and one by a steam turbine. Both plant and instrument air systems in the West Plant are rated at 100 psi. At East Plant No. 1, there are four steam systems rated at 600 psi, 250 psi, 100 psi and 40 psi. Steam is produced at two 67,000 pound per hour @ 250 psi gas fired boilers with water level control. In addition, there are two 35,000 pounds per hour @ 250 psi gas fired manually operated boilers. Waste heat is produced at No. 1 Catalytic Cracking Unit in the amount of 10,000 pounds per hour @ 250 psi. A CO Boiler rated at 100,000 pounds per hour @ 250 psi is operated in connection with Catalytic Cracking Unit No. 1. In East Plant No. 2, there are three steam systems rated at 450 psi, 175 psi and 65 psi. The fired boilers consist of a 220,000 pounds per hour @ 600 psi, a 130,000 pounds per hour @ 600 psi, and a 145,000 pound per hour @ 600 psi boiler. These units are gas/oil fired and are equipped with complete burner management systems. In addition, waste heat generation is produced at the following units: Unibon Crude Unit No. 4 FCC No. 2, Flue Gas FCC No. 2, Bottoms Cooler FCC No. 2, Slurry Generator Sulfur Units A & B 25.000 pounds perhour at 250 psi 85.000 pounds perhour at 100 psi 37.000 pounds perhour at 600 psi 50.000 pounds perhour at 100 psi 220,000 pounds perhour at 250 psi 30 ,000 pounds per hour each at 50 psi In the West Plant, the three steam systems rated at 450 psi, 175 psi and 65 psi are supplied from three 75,000 pounds per hour @ 450 psi gas fired boilers with complete burner management systems. Steam is generated utilizing waste heat according to the following table. Mixed Distillate Hydrotreater Coker Gas Oil Cooler Coker Convection Section Sulfur Plant 30.000 35.000 20.000 65.000 pounds pounds pounds pounds per hour at 175 psi per hour at 450 psi per hour at 175 psi per hour at 65 psi In all plants produced steam is let down to the lower rated systems utilizing rotating equipment or specifically designed letdown stations. -3- RP2 CH/W-002521 M&M Protection Consultants Steam produced in waste heat generators at East Plant No. 2 and West Plant in the Sulfur Units is used in the Sulfur Units and associated processes. Water for cooling and boiler feed comes through a connection to the city water system. The water is received at an average pressure of 32 psi. Make-up for the demineralizer in East Plant 2 comes through Tank No. 65. This is a 40,000 barrel tank is used as a suction source for two fire water pumps No's. 29 and 30. Only 10,000 barrels are used for the demineralizer feed with the remaining capacity reserved for the fire pumps. The East Plants (1 and 2) use 3.8 million gallons/day and the West Plant uses 0.8 million galls/day. Cooling water is recirculated uti lizing cooling towers with fans equipped with vibration shut downs . MANAGEMENT PLANNING AND CONTROL: (a) Housekeeping, Maintenance: Housekeeping is considered gen erally very good. Maintenance practices are satisfactory for refineries of this size. (b) Smoking Control: Smoking regulations are enforced and smoking is restricted to designated areas only. (c) Self-Inspection Programs: Fire Equipment: All fire extinguishers and other fire pro tection equipment receive regular inspection and records are kept indicating the status of the equipment along with corrective action taken. Hydrostatic tests are being con ducted at required intervals. Process Equipment: An equipment inspection program con sisting of the use of outside services, together with plant personnel, is in force and records are kept concerning these inspections. This program involves periodic tur narounds of the process areas with some on-stream inspec tions and analysis being conducted by plant personnel. (d) Fire Brigades: The plant has organized an Emergency Response Team setting up specific individuals with specific duties to be performed in case of emergency. Individuals chosen for the fire brigade have received training at industrial fire schools or locally at locations of the com pany. All employees receive some training in connection with the use of hand extinguishers and hose streams annually. (e) Cutting and Welding: When these operations are conducted outside of the shop area, combustible gas tests are con ducted and a written hot work permit issued. A fire watch is provided during all operations of this type. RP2 -4- CH/W-002522 M&M Protection Consultants (f) Emergency Planning: An emergency plan has been developed and is posted at several locations throughout the refinery. Employees have been instructed as to their specific duties. This plan is reviewed annually and updated as required. PRIVATE PROTECTION: (a) Water Supplies: There are two 1,500 gpm @ 150 psi diesel driven fire pumps located near the east gate taking suction from a 16-inch city water main in Nueces Bay Boulevard. Two 1,500 gpm @ 150 psi diesel driven fire pumps are located on the west side of the plant and take suction from a 16-inch water main in Oak Park Avenue or from a 40,000 barrel fire water tank. The pumps are manual start and require attendance to be placed in operation. Two 2,000 gpm @ 150 psi diesel driven fire pumps take suction from the 40,000 barrel fire water storage tank. These pumps are equipped with automatic controllers and will start on pressure drop in the fire system. The fire water storage tank is supplied through a 16-inch main from the city water system in Poth Lane. Three 3,000 gpm @ 150 psi diesel driven fire pumps located at Area 90, take suction from a 3 million gallon resevoir. These pumps provide protection for the Crude Oil Terminal (Area 90) and the West Plant. These pumps are equipped with automatic controllers and designed so that on pressure drop, one pump comes on immediately with the other two pumps set on timers. Two 3,000 gpm @ 150 psi diesel driven fire pumps provide protection for the Tank Farm Area 91. These pumps take suction from a 5 million gallon resevoir and are manual in operation. One 3,000 gpm @ 150 psi diesel driven fire pump is provided at Dock No. 3 and provides protection for this dock and Dock No. 6. The pump is manual start or may be remotely started from Dock No. 6. This pump takes suction from the Navigational Channel and has an unlimited supply. (b) Yard Mains And Hydrants: The fire main system in East Plant No. 1 and No. 2 consists of a good network of looped 6, 8, 10, 12, and 16-inch buried mains. The 12 and 16-inch size mains are located in the East Plant No. 2 area. A dead-end 8-inch line from the plant to Dock No. 1 and No. 2 feeds hydrants, monitor nozzles and hose stations in the dock areas . -5RP2 CH/W-002523 M&M Protection Consultants (c) (d) (e) (f) The fire main system in Area 90, consists of looped 16-inch mains. This system has been extended to provide protection in the West Plant utilizing 6, 8, 10, 14, and 16-inch looped mains. These mains supply numerous fire hydrants, monitor nozzles, and hose stations together with water spray systems. Area 91 has a looped main consisting of 16-inch buried line supplying hydrants well distributed around the tank farm. All systems have good sectional control provided and relief valves are provided on the fire pumps. Automatic Sprinklers: In East Plant No. 1, an automatic pilot head operated deluge system protection is provided over the weigh tank at the Inline Blending Facility. Manual water spray systems are provided over pumps in the BTX Unit, over pumps and under air coolers at No. 4 Platformer and Unifiner. This protection is also provided for the pumps in the Alkylation Unit. At the Cumene Unit remote operated water spray protection is provided over pumps, cabletrays and under air coolers. The pumps in No. 3 Vacuum Unit are provided with manual water spray system. In East Plant No. 2, manual water spray systems have been provided under fin fans and over pumps in all areas with the exception of area 50, the Sulfur Plant, and Area 60, the Utility Section. A manual water deluge system is pro vided for the Butane Surge Drum located south of Dock. No. 1. A pilot head operated automatic water spray system is installed over pumps and under the air cooler in the MTBE Unit. In the West Plant, there are 19 individual pilot operated deluge systems located in the Mixed Distillate Hydrotreater, No. 5 Platformer and Coker. In additon, the cooling tower is equipped with an automatic deluge system. Detection And Alarm Systems: Smoke Detection System: A Smoke Detection System of the ionization type is installed in selected areas of the laboratory. Extinguishers, Standpipes and Hose: There is a good supply of portable and wheeled extinguishers for plant protection, well distributed throughout each area. Other Protection: Foam hose stream protection, together with snuffing steam for Process Units, is provided. Fixed foam chambers and laterals with risers are provided on Light Oil Storage Tanks at the refinery, in Area 90 and 91. Manual water spray protection is provided for three -6- RP2 CH/W-002524 M&M Protection Consultants spheres located north of the Vacuum Unit and old boiler area. In addition, water weir spray protection is provided for Sphere No's. 174, 175, and 176 located north of the MTBE Unit. Light oil tanks are equipped with high level alarms sounding in the Inline Blending Control Room. A 300 lb. Halon 1301 system is installed Blending Facility in the Engine Knock Room. acuated by products of combustion detectors, and flammable gas detectors. at the Inline The system is heat detectors A 1963 pumper rated at 1250 gpm 150 psi and carrying 500 gallons of foam concentrate is kept in the open near the control room in the West Plant. A 1980 "Telesquirt" with a 1000 gpm 150 psi pump and 1000 gallons of foam concentrate is stationed at the Safety Office in the East Plant. PUBLIC PROTECTION: Protection from 3rd class city of Corpus Christi is considered good. The fire department will respond if called. The refinery belongs to the Refinery Terminal Fire Company with a station located approximately lfz mile from the East Plants and 5 miles from the West Plant. REMARKS: During this visit to the refinery the fire equipment, maintenace records, together with management programs, were reviewed during the inspection. The plant was inspected physically and tests of the fire pumps were witnessed. Subsequent to the previous inspection a major turn-around has been conducted on the majority of the processing units at the refinery. During the maintenance procedures, modification to No. 4 Crude and Vacuum Unit was accomplished. This was to improve the liquid recovery from the vacuum towers. The vacuum heater was changed from a four pass heater to an eight pass heater with additional instrumentation provided. Two of the 35,000 pounds per hour, 250 psi gas fired manually operated boilers located in East Plant No. 1 have been retired. A new fin-fan cooler and associated equipment has been installed at the splitter near No. 4 Platformer with fire proofing material applied to the supporting members. In addition, two ready hose reels have been installed with 100 feet of ityz inch hose on each with a combination nozzle. -7RP2 CH/W-002525 M&M Protection Consultants The Demex Unit in East Plant No. 2 has not operated during 1986 and is still idle today. Tank No. 1005 has been razed and a new 80,000 barrel tank insu lated with fiberglass is being erected and will be placed in coker feed service. A circulating hot oil heater previously used with Tank No. 1005 will remain for use with the new tank. On completion of this construction. Tank No. 1004 is to be taken out of service. All fire pumps were tested during this inspection and the results are indicated on the attached fire pump test data sheets. A review of the results compared to those obtained previously on these pumps indicates satisfactory operating conditions. The tachometer on Pump No. 29 and Pump No. 31 were not functioning and results could not be corrected to the rated RPM. Pump No's. 33 and 34 located at the east gate to the plant indicated initial results below the rated capacity of the pumps, however when the results are corrected for head loss, satisfactory operations are indicated. Pump No's. 31 and 32 indicated improved results, however there was considerable blow by of oil on the exhaust manifold causing the units to smoke badly due to the exterior oil. It is understood that a work order has been issued and it has been reported that these two engines need to be overhauled. A review of the previous recommendations indicates that Recommendation 76-1 concerning redesign of the water spray systems in the No. 4 platformer has been accomplished with water spray of adequate capacity provided over the pumps under the finfans and over the lube oil console at the recycle gas compressors. A review of the oil handling and movement system (OHMS) was conduced and after discussions, it was determined that Recommendation 84-3 is no longer valid and this recommendation has been removed from the report. The remaining recommendations appearing on the previous report have partially been completed and are repeated at this time until the work is finished. Additional suggestions resulting from this inspection are included. RECOMMENDATIONS: 82-5 (Revised) In the Cumene Control Building, the Control Building at the West Plant and East Plant No. 2 Control Building, computer equipment provides the control for several units. It is suggested that smoke detection be installed under the raised floor in these buildings so that an alarm can be received and hand Halon type extinguishers be used to discharge under the floor space in event of fire in these areas. Experience has shown that it is the under floor areas where considerable cables are where most of the problems in respect to fire occurs in computer installations. -8- RP2 CH/W-002526 M&M Protection Consultants (Note: It was indicated that the computers were origi nally used to obtain optimum results and some changes have occurred whereby the computer equipment is actually doing some processing directions. A detection system in East Plant No. 2 Control Building has been taken out of service due to the extensive maintenance needed on the equipment. In compliance with this recommendation, the system should be replaced.) 82- 7 Fireproofing material had been installed on the legs of the spheres located north of the Alkylation Unit. In a number of instances it was noted that the fireproofing has been broken away and is deteriorating. It is suggested that the fireproofing material on these spheres be repaired and sealed to prevent the corrosion of the sup porting members of these spheres behind the fireproofing material. (Note: Some fireproofing has been corrected with some still left to do. This recommendation is repeated until the areas covered have had the work completed.) 83- 1 Extensive water spray systems have been provided throughout the West Plant. It was noted in the Coker that all, fin fans have not been protected nor have all pumps been protected. It is suggested that the water spray systems in the Coking Unit be extended to include all hydrocarbon pumps and all fin fans over the main pipeway. It is felt that the fin fans on the east west pipeway on the north side of the unit are not seriously exposed and would not require water spray protection. 84- 4 (Revised) The motor control centers and rack rooms in East Plant No. 2 and the West Plant are provided with pressurization systems to maintain the pressure at l/10th of an inch of water. During this inspection, it was noted that the majority of air pressurization systems were not fuctioning properly. In addition, the instrumentation indicating a lack of pressure was not functioning. All pressurization systems and motor control centers and rack rooms are important due to the ordinary classification of the wiring methods in these buildings and their proximity to areas where accidental release of flammable vapors is possible. It is suggested that the pressurization systems in these areas be returned to functional status. (Note: A review of the various pressurization systems in the motor control centers and rack rooms indicates that the systems are not maintaining one tenth of an inch of water. This is the pressure which should be maintained in these structures.) -9- CH/W-002527 M&M Protection Consultants 85-1 85-2 85-3 86-1 86-2 86-3 86-4 RP2 (Revised) In the warehouse buildings at the East and West Plants falammable liquids are stored on open shelves. Also at the East Plant Warehouse laboratory storage con sisting of MIBK, Tri methyl pentane, methanol, etc. was noted. Flammable and/or combustible liquids should be stored in a separate cut-off room so as not to become involved in a possible incident. An alternative would be to provide an outside building separate from the main warehouse and in the event of small containers such as aerosols, etc., a flammable liquid storage cabinet should be provided. The dyke surrounding Tank Nos. 53, 54, 52, 72, 70, and 71, which are in aeromatic service, has eroded to the point that an accidental rupture involvement of these tanks could spread throughout the area in the vicinity of the warehouse. It is suggested that dyking around these tanks be reviewed and erected so that the dykes will contain the capacity of the largest tank plus ten percent of the capa city of the remaining tanks. In the Alkyation Unit and No. 5 Platformer Rack Room, it was noted that considerable combustible storage is in the motor control centers. These motor control centers are designed with pressurization systems and all combustible storage should be eliminated from these areas. A positive pressurization system is provided in the BTX Control Room. The audible alarm does not function. It is suggested that the alarm situation be reviewed and that audible alarms be repaired. In East Plant No. 1 at the FCC No. 1, No. 1 Crude, and other older units on the plant, the fireproofing material is not designed for three hour protection. It is suggested that the supporting members of major towers, fin-fans, and pipeways, where pumps are located beneath the pipeway, be provided with fireproofing material capable of maintaining the steel at a temperature of 1000F under an exposing fire of 1800F for a period of three hours. A satellite laboratory operation is conducted in a plywood building near No. 4 platformer. The flare drum, balance drum and air compressor in this area seriously expose this laboratory. It is recommended that the laboratory building be removed and that a building of noncombustible construction be provided for these operations. The Hydrar heater is located at a higher grade than the balance of the Hydrar Unit. It is suggested that 6-inch curbs with drains be provided around the heater to prevent the accidental flow of oil throughout the unit. -10- CH/W-002528 M&M Protection Consultants 86-5 Manual water spray systems have been provided over some LPG bullets in the area north of the Alkylation Unit. It is suggested that water spray systems be provided over bullet No's. 203 - 209 and 213 -214 as well as 131 - 136. The water spray systems should include ail horizontal pressure vessels in the refinery. The water spray systems should be designed for a density of 0.25 gpm/sq. ft. of surface area. 86-6 A positive displacement pump to transfer LPG from sphere 102 to sphere 101 has developed leaks at the cylinder. This pump was used to move liquids from one sphere to the other. Due to the difficulty of maintaining a good seal with a positive displacement pump, it is suggested that other type equipment be used in the future for this ser vice and that this positive displacement pump be removed from the area. 86-7 It was noted at the LPG bullet storage area that the plate and chain used to lock the block valves beneath relief valves has been removed in a number of instances. A chain and lock program should be provided on all block valves beneath relief valves and the locks and chains should be maintained in position so that the block valves cannot be closed without adequate notification. It is suggested that the block valves be checked since they are wrench operated to be sure they are in the open position and" the locking plates and chains be replaced. 86-8 There are a number of pump pads such as pad No. 1 and the LPG transfer pumps which are outside the range of monitor nozzle protection. It is suggested that at least two monitor nozzles be installed at all pump pads so that the stream from the monitor can cover the pump pad. The moni tor should be located approximately 50 feet from the nearest edge of the pump or transfer pit. 86-9 The fire truck at the West Plant is kept in the open. This results in exposure to the weather with accelerated corrosion and resulting additional maintenance required over a period of time. It is suggested that the fire truck be housed to reduce the damage due to this exposure to the weather and climatic elements. ITEMS OF INTEREST: Certain conditions do not comply with accepted standards, but may be considered impractical to correct under present conditions. These are valid recommendations and are listed here as a matter of record. Each recommendation should be reviewed periodically and considered when changes in construction or occupancy are con templated . -11- RP2 CH/W-002529 M&M Protection Consultants 1. A test of the water spray systems under the elevated fin fan coolers indicates that each system should be extended one head beyond the edge of the cooler to reduce the effect of wind on the discharge pattern of water under the fin fan coolers. 2. To provide protection of the splitter tower from the heater, the monitor nozzle at the northeast corner of the heater should have hydraulic controls installed. This will also provide protection for the horizontal vessels at the No. 4 Platformer. An alternative would be to install a water cur tain between the splitter tower and the heater. To be effec tive, the water curtain should be capable of delivering 0.25 gpm/square foot of wetted area. 3. Provide water weir protection for spheres located north of the Alkylation Unit. 4. Provide water spray under the fin-fans at the BTX Units. 5. Separation of the fire water system from the service water system. This would be particularly beneficial in East Plant No. 2. -12RP2 CH/W-002530 MS.M PC M&M Protection Consultants A Resource of Marsh & McLennan FIRE PUMP TEST REPORT - Client Champ 1 in Petrol etira r.n. ' ' PUMP . ' -- _::___________________ *0. " - 29 Near Tank So. 65' _____________ ~ ' - Location Corpus Christ! r TX Type Hnri r.. -Centrifugal Date __ November 11 f 1986 Rating. 2QQ0 gpm ISO psl By ____ C. V. Frishtp________ __ RPM 1900 VOLTS/ AMPS ' / PUMP RPM PUMP PRESSURE [________ PRT > DISCH. SUCT. NET NOZZLE SIZE & NUMBER * 188 18 - 170 PITOT PRESSURES < PSI ) ... .. DRIVER Mfg. _______________________ Type Diesel Engine__ Power ______________________ Engine Hours________________ Gear Ratio -Direct Drive . INDIVIDUAL ; FLOWS < GPM > TOTAL FLOW ( GPM > CORRECTED TO RATED RPM NET HEAD FLOW .... So Flow * 170 "18 152 1-1 3/4" 86 848 848 :k 156 18 138 2-13/4" . 80-78 ' y - 818-807 1625 * 140 18 122 3-1 3/4" 78-70-68 818-765-754 2337 * Tach jmeter n< >t fur ction Ing d iring te st PUMP CURVE: ':. ' ' " CH/W-002531 /UV'Jfk^PRESSURE ( P a I ) M&M PC M&M Protection Consultants A Resource of Marsh & McLennan FIRE PUMP TEST REPORT Client Champlin Petroleum Cn Near Tank No. 65___________ Location Corpus ChrlsM, TX Date Novemher 11, 1 qftfi By C. V. Frlstvlp___________ PUMP No----------------------- IQ____________ Mfg. ___________________________ Type Horl 7.. -Centrifugal Rating 2000 GPM ISO ps^ RPM ___________1 Qnn___________ VOLTS/ AMPS PUMP RPM PUMP PRESSURE ( PSI ) DISCH. SUCT. NET NOZZLE SIZE & NUMBER 1800 176 18 158 -- PITOT PRESSURES ( PSI ) -- DRIVER Mfg. Type ------ DieBe.lEngltiP Power - '' ; Engine Hours Gear Ratio Pi rep INDIVIDUAL FLOWS ( GPM > -- TOTAL v- ^CORRECTED,!; : FLOW ~ . RATED RPM ( GPM -NET-.:: t HEAD ` ' - 7j=.-: `T NtirFldw 1800 160 18 142 1-1 3/4" 82 1750 150 18 132 >-l 3/4" 74-74 828 786-786 828 :ii5s;.; :874^ 'Tv~ ' "r . 15722^ 51707 1525 118 18 100 5-1 3/4" 56-60-70 684-708-765 2157A > HWi: 2687 PRESSURE ( P S I M&M PC M&M Protection Consultants A Resource of Marsh & McLennan FIRE PUMP TEST REPORT ; .V- uneni l.namp i in Merrmenm Ln. Npar r.nnl trig Tnupr Location f!n|-piic Oir-t cM , Tit Date NmrDmVtPr 1 1 J 1 By --C,--XL--Friable---------------------- PUMP No____________ 31_______________ Mfg. __________________________ Type HrvHz .-Centrifugal Rating _ 1 500 0PM 150 psi RPM __________1 7 f,n___________ VOLTS/ AMPS PUMP RPM PUMP PRESSURE < PSI > DISCH. SUCT. NET NOZZLE SIZE & NUMBER PITOT PRESSURES ( PSI ) * 142 18 124 -- -- * 136 14 122 1-1 3/4' 58 * 122 12 110 2-1 3/4' 60-50 * 104 10 94 3-1 3/4' 42-52-56 DRIVER M,g- -------------------' Type Diesel Englneg"T%: Engine Hours Gear Ratio Direct: '; .iiufech^ .r. ' INDIVIDUAL FLOWS ( GPM ) TOTAL'-; . CORRECTED TO FLOW - > "RATED-RPM. ( GPM 4 " NET-+IEAD 'FLOW ' \T^' -Jsr-v--:C KR- No Flbw >-?- .-1 ;-_V\ ; ' 696 --v 696 J ^ ; *'} ' ' ' ... 708-646 ..-r. 1354 r-;; - .77 t` * *. . * - - - .i.. - .r'TV - 'l"!. 592-659-684 1935 --f:- IT j" *: . * * Ta chometer Jot [unct: onint During Xe_____________ - ' ; i' - t: *!_ RE ( P - I l IOOO M&M PC M&M Protection Consultants A Resource of Marsh & McLennan FIRE PUMP TEST REPORT Client Champlin Petroleum Co. Near Cooling Tower________ Location Corpus Christi. TX Date November 11. 1986 By __ C._V. .Frisble_________ PUMP No___________ 22______________ Mffl. __________________________ Type Horiz.-Centrifugal Rating 1500 GPM ISO pai RPM ________ U6Q.____________ VOLTS/ AMPS PUMP RPM PUMP PRESSURE ( PS1 ) DISCH. SUCT. NET NOZZLE SIZE & NUMBER PITOT PRESSURES < PSI ) 1600 138 18 120 -- -- driver Mfg.'~ " ;;_ Type Diesel Engine ' } ; . Power _______ ' ? Engine Hours '' ' - ~~ ; *?7;r Gear Ratio Dlrert'^tJi-t-V-r.Tnt^'h : INDIVIDUAL FLOWS ( GPM ) TOTALS FLOWm- CORRECTED TO: : RATED RPM . V ( GPM NET -HEAD FLOW ; -- No Plow 1145 - 1600 132 14 118 1-1 3/4" 60 1550 118 12 106 2-1 3/4" 58-50 708 696-646 708':r 143; 779 ^37:* 1342"~' ' 1524 . ' 1550 100 10 90 3-1 3/4" 58-50-40 696-646-578 1920-" 116 - 2180 .. PRESSURE ( P S I (600 M&M PC M&M Protection Consultants A Resource ol Marsh & McLennan FIRE PUMP TEST REPORT Client Champlin Petroleum Co. _Near East Gate Location Corpus Christ!. TX Date November 11. 1986 By __ C. V. Frisbie_________ PUMP No----------------23________________ Mfg. __________________________ Type Horiz.-Centrifugal Rating 1500 gpm 1 SO psl RPM ___________ L26Q________ VOLTS/ AMPS PUMP RPM PUMP PRESSURE ( PSI ) DISCH. SUCT. NET NOZZLE SIZE & NUMBER PITOT PRESSURES ( PSI ) 1750 177 50 127 -- -- 1700 165 48 117 1-1. 3/4' 134 1650 150 44 106 2-1 3/4" 90-100 1600 130 34 96 3-1 3/4" 74-65-70 DRIVER ,,i-y . - Mfg. .............. Type .Diesel-Eri&lne Power Engine Hours - .:r`... Gear Ratio Direct Wi rh Cl - INDIVIDUAL FLOWS ( GPM ) 1058 867-914 786-736-765 total' FLOW ( GPM -) CORRECTS! TO: ' RATED RPM WET HEAD ! ifibw; So.-Flow J28; ":'i " 1 . r*". 1058 ? 125' 1095 . \?y:'-r->: - . 1781V- 121: 11900 ^' ' -r-* '-.>j 2287 : jll6 .2516' PSI ft PUMP CURVE: " ." . 1-* ; 7: CHAW-002535 M&M Protection Consultants______ A Resource of Marsh & McLennan FIRE PUMP TEST REPORT Client___ Champ 1 in Petrol pnm f.n. PUMP ------------------------------------------------------------ No---------------------- 34-----------------------Near East Gate Mfg. Location _ Corpus Christ!. TX__ Type Hnri 7., - Centrifugal Date -November 11,__L2S6________ Rating IS00 gpm 1 SO psi By ___C^.y.a Frisbie rpm 17fi0 rpm DRIVER Mfg. ' ; ' Type Diesel JSnglhe Power "' Engine Hours r'..^ f Gear Ratio Jti'rect ffiith ^Clutch VOLTS/ AMPS PUMP RPM PUMP PRESSURE ( PSI ) DISCH. SUCT. NET NOZZLE SIZE & NUMBER PITOT PRESSURES ( PSI ) INDIVIDUAL FLOWS ( GPM > TOtAL FLOW ( 6pm CORRECTED TO ' . flATED RPM : ' NET HEAD. - -FLOW - 1700 150 44 106 1-1 3/4" 134 1058 : 1058-s; .ii4j' 1095 1700 135 35 100 2-1 3/4" 84-95 838-890 1728 ,1789 1650 122 34 88 3-1 3/4" 74-60-65 786-708-736 2230 f- -100 i 2379 " ' PRESSURE ( P S I O' 1. " .____L_ \.. M.S.M PC M&M Protection Consultants A Resource of Marsh & McLennan FIRE PUMP TEST REPORT Client Champ!-fn Pprrnlpiim On --Axea~&0 Location -Corpus-Christ!, TX Date Novaabar 11,--19&6--------By --C^-V -- Er isb ia------------------ PUMP No-----------------------4_____________ Mfg. ___________________________ Type .iter tic a 1--Turbine-- Rating 3000 gpm-150 psi RPM ------------- 17JO____________ VOLTS/ AMPS PUMP RPM PUMP PRESSURE ( PSI DISCH. SUCT. NET NOZZLE SIZE & NUMBER PITOT PRESSURES < PSI > 1550 146 -2 148 1-1 3/4' 130 INDIVIDUAL FLOWS (GPM > 1042 ^OTAt^: 'CORRECTED TOe Cfldw ~ -c.HATED RPM Ogpm NET-HEAD - :%pw > Iti -:7.L. > 193" 119Q S 1525 126 -2 128 2-1 3/4' 108-108 950-950 X v l$Q0 :: 172' v 2205 v; . 1675 140 -2 142 2-1 3/4' 120-116-114 1001-984-976 *W* - V :156 - 3129 160 -2 162 Relief Valve Setting V.- a ". . --;':c T.>S r.~/ i PUMP CURVE: := -r:' CH/W-002537 PRESSURE ( ? s t 2ooo 3ooo M&M M&M Protection Consultants M ]t 1 AResourceofTJareT&^cLennanTM U FIRE PUMP TEST REPORT v-V. -- i"rW.; VV-rfi Client__ Champlin Petroleum Co. Area 90 Location Corpus Christi. Date . November 11. 1986 By C. V. Frisbie TX__ . pump ----Mlg. Type Vertical Tnrhinp Rating 3000 ppm 130 psi RPM _____________ 1_L?2Q____'_________ DRIVER nrny. -------------- Typ TH pppI Power Engine Hours Gear Ratio v-:v ' VOLTS/ AMPS PUMP RPM PUMP PRESSURE < PST > DISCH. SUCT. NET NOZZLE SIZE & NUMBER PITOT PRESSURES ( PSI ) 1525 128 -2 130 1-1 3/4" 110 1775 156 -2 158 2-1 3/4" 130-130 INDIVIDUAL FLOWS ( GPM ) 959 1042-1042 TOTAL FLOW < GPM - '1 -% : T.-'r: CORRECTED TO - RATED RPM : rtlET HEAD FLOW . 959; i ;U75.. 3113 2084' 7 :- ,, 'V . * ' 157: .'2078 1750 130 -2 132 3-1 3/4" 110-110-110 959-959-959 287?/;; : 'i35' 2910 160 -2 162 PUMP CURVE: Relief Valvt Setting > W 1T . *; . * - c-' _V CH/W-002538 PRESSURE( PSI M&M PC M&M Protection Consultants A Resource of Marsh & McLennan FIRE PUMP TEST REPORT Client Champlin Petroleum Co. . Area 9Q Location Corpus ChrisM, TX Date November 11, 1 QR6 By ___ C_. ,y. -Frishie PUMP No. c Mfg. _ Type _ Vert11-al Turhfnp Rating _ 3nnn pinm ISO ns-1 RPM _ ....1Z70_____________ ... DRIVER. Tyne THesel F.njHrie Power r-" - Engine Hours --'-'r:- `'V.-v-\ ^f -- -: Gear Ratio" \ ' VOLTS/ AMPS PUMP RPM PUMP PRESSURE ( PSI ) DISCH. SUCT. NET NOZZLE SIZE & NUMBER PITOT PRESSURES < PSI > INDIVIDUAL FLOWS <GPM > TOTAL" FLOW <-GPM > CORRECTED TO 7 ;raTEORPM : - -NET , HEAD FLOW . 1525 120 -2 122 1-1 3/4' 106 941 941 - .164 1092 ' 1675 130 -2 132 2-1 3/4' 112-112 967-67 :- 1934 .7 147 2044 1775 pump CURVE: 142 -2 144 3-1 3/4' 120-120-120 1001-1001-1001 3003 :'H 143 72995 158 -2 160 Relief Valve Setting 7 ; *-J - r-- : ** . V *- - T-"'' ... V-- 7;7' CH/W-002539 PRESSURE{ PSI M&M PC M&M Protection Consultants A Resource of Marsh & McLennan FIRE PUMP TEST REPORT Client__ Champlin Petroleum Co. Area 91 Locationi Corpus Christ!r TX Date November 11r 1986 By C. V. Frishle_____________ PUMP No----------------lqq___________ Mfg. __________________________ Type Vertical Tnrhfne Rating **000 gpm 1 50 pgl RPM ________ 17.20____________ VOLTS/ AMPS PUMP RPM PUMP PRESSURE <EI__________ ! DISCH. SUCT. NET NOZZLE SIZE & NUMBER PITOT PRESSURES ( PSI ) 1200 85 -2 87 1-1 3/4" 60 - ? -v "v:y: '-in 2-y-~f f-r?* j'..- .. ' driver - y'y-yyytZ-r- ': 2-v-.w:' -? ? Mfg. .-rA.V' - Type Diesel .Engine ' -'-f :n Power _____ Engine Hours . Gear Ratio __ INDIVIDUAL FLOWS ( GPM ) 708 TOTAL plow. :5 < GPM ) CORRECTED TO vV RATED RPM j!" NET HEAD ;flow s 708 > , 189 ' 10442 1400 112 -2 114 2-1 3/4" 82-86 828-848 '-A * 1676 /: : 182 >. 2119 ' 1700 146 -2 148 3-1 3/4" 112-106-116 967-941-984 2892- vr. \. -160 3011'; Vi L- * W-'T'7, - ''4* '' . PRESSURE ( I'S I M&M PC M&M Protection Consultants A Resource of Marsh & McLennan FIRE PUMP TEST REPORT client Champlin Petroleum Co. Area 91_____________________ Location Corpus Christi. TX Date November 11. 1986 By __ C. V. Frisbie PUMP No___________ 101___________ Mfg. ___________________________ Type Vertical Turbine Rating 3000 gpm 150 psi RPM _________1770__________ VOLTS/ AMPS PUMP RPM PUMP PRESSURE < ESI > DISCH. SUCT. NET NOZZLE SIZE & NUMBER PITOT PRESSURES ( PSI ) 1100 80 -2 82 1-1 3/4' 60 1600 140 -2 142 2-1 3/4' 100-110 DRIVER Mfg. _ Type Diesel Engine - r ~- Power Engine Hours Gear Ratio " Itl .Xy-.-b'-l" : INDIVIDUAL FLOWS ( GPM ) . .. TOTAL FLOW - ( GPM ) CORRECTED TO ; RATED RPM V NET .HEAD - -'FLOW"'. 708 708 VJ 212^ . 1139 ; .1 - * ; 914-959 1873 `. 174 2072 1600 120 -2 122 3-1 3/4" 92-84-90 877-838-867 2582 ' ' 149 2856 .; \V`* ' v ^y ^ PRESSURE ( r i f MS.M M&M Protection Consultants______ I Ij '^ A Resource of Marsh & McLennan FIRE PUMP TEST REPORT . "i-r . ' : ^ Scr-r. - Client------ Champ! In Ppfrnlejim Hn. PUMP - * - -"* -ivc. No. 3 Dock ___________________ Location _.Corpus ChristJU.TX__ Date Novemher 11 f 1986________ By --C. V. Fr.isbie RPM 1 770 No_________________________________________M__fg_. Mfg. _ Type Type Vertical Turbine Power ` -' Rating 3000 GPM 1 SO pai Engine Hours Gear Ratio ~. ~ .. **V' 'v<--- ' - VOLTS/ AMPS PUMP RPM PUMP PRESSURE < PSI ) DISCH. SUCT. NET NOZZLE SIZE& NUMBER PITOT PRESSURES ( PSI > 1800 188 -3 191 1-1 3/4* 138 1800 160 -3 163 2-1 3/4' 114-116 1770 136 -3 139 3-1 3/4* 100-100-90 INDIVIDUAL FLOWS < GPM ) 1073 976-984 914-914-867 TOTAL- FLOW / < GPM > NET v HEAD' ; -H--' W. KV;: - 1073 J?185, 1055: I960 - * I; ` */ 2695 IT- -.V" 158 ; _"19.2v 7 139 : 2695 . ' --- 196 -3 199 Relief Valve Setting PUMP CURVE: CH/W-002542 RE ( PSI