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GP 03-02-03 Fire Water Systems December 2004
Refining/Chemicals, Downstream Imperial Oil
For ExxonMobil Use Only Version 2.0.0
Page 1 of 27 ExxonMobil Development Company
Fire Water Systems
GP 03-02-03
Scope
[I] This Global Practice (GP) covers the design and installation of fire water systems.
[I] An asterisk (*) indicates that additional information is required. If a job is contracted, this additional
information is furnished in the Job Specification.
GP 03-02-03 Fire Water Systems December 2004
RFCH, DIOL For ExxonMobil Use Only Version 2.0.0
Page 2 of 27 ExxonMobil Development Company
Table of Contents
Table of Figures............................................................................................................. 4
1. Required References ............................................................................................ 5
1.1. Global Practices–ExxonMobil Engineering Practices ................................... 5
1.2. AWWA–American Water Works Association ................................................ 5
1.3. NFPA–National Fire Protection Association ................................................. 5
1.4. NSF International (National Sanitation Foundation) ..................................... 5
2. Additional Requirements ...................................................................................... 5
3. System Design ...................................................................................................... 6
3.1. Design Basis ................................................................................................ 6
3.2. Water Supply ................................................................................................ 7
3.3. Pumps and Drivers ....................................................................................... 7
3.4. Booster Pumps ............................................................................................. 8
3.5. Piping Layout ................................................................................................ 9
3.6. Hydrants Location and Spacing .................................................................. 10
3.7. Monitor Location ......................................................................................... 11
3.8. Hose Reel Location .................................................................................... 12
4. Hydrant Selection and Installation .................................................................... 12
5. Monitor Selection and Installation ..................................................................... 13
6. Hose Reel Selection and Installation ................................................................. 15
7. Valve Selection .................................................................................................... 16
8. Spray System Design and Installation .............................................................. 16
9. Deluge and Spray System Installation for Pressurized and Refrigerated Storage ................................................................................................................. 19
9.1. Common Requirements .............................................................................. 19
9.2. Pressurized Storage ................................................................................... 22
9.3. Refrigerated Storage .................................................................................. 22
10. Spray Systems for Air Preheaters ..................................................................... 23
10.1. Regenerative (Rotary) Air Preheaters ........................................................ 23
GP 03-02-03 Fire Water Systems December 2004
RFCH, DIOL For ExxonMobil Use Only Version 2.0.0
Page 3 of 27 ExxonMobil Development Company
10.2. Recuperative (Static) Air Preheaters that Receive Flue Gas from More than One Fired Heater/Boiler.............................................................................. 23
11. Inspection and Testing ....................................................................................... 24
Record of Change ....................................................................................................... 25
Attachment: Purpose Codes Definitions .................................................................. 27
GP 03-02-03 Fire Water Systems December 2004
RFCH, DIOL For ExxonMobil Use Only Version 2.0.0
Page 4 of 27 ExxonMobil Development Company
Table of Figures
Figure 1: Monitor Installations .................................................................................. 14
Figure 2: Monitor Feeder Line ................................................................................... 15
Figure 3: General Spray System Layout .................................................................. 17
Figure 4: Sample Spray Head .................................................................................... 18
Figure 5: Typical Piping Requirements for Top Mounted Cooling Water Deluge Systems (1)(2) ............................................................................................... 21
GP 03-02-03 Fire Water Systems December 2004
RFCH, DIOL For ExxonMobil Use Only Version 2.0.0
Page 5 of 27 ExxonMobil Development Company
1. Required References
[I] This Section lists Practices and Standards that are generically referenced and assumed to be a part of
this document. Unless otherwise specified herein, use the latest edition.
1.1. Global Practices–ExxonMobil Engineering Practices
GP 03-09-01 Winterizing and Protection Against Ambient Temperatures
GP 03-10-01 Piping Selection and Design Criteria
GP 03-10-03 Cement Lined Pipe and Fittings
1.2. AWWA–American Water Works Association
AWWA C502 Dry-Barrel Fire Hydrants
1.3. NFPA–National Fire Protection Association
NFPA 12 Standard on Carbon Dioxide Extinguishing Systems (National Fire
Codes, vol. 1)
NFPA 15 Standard for Water Spray Fixed Systems for Fire Protection
NFPA 22 Standard for Water Tanks for Private Fire Protection (National Fire
Codes, vol. 1)
1.4. NSF International (National Sanitation Foundation)
NSF 61E Drinking Water System Components - Health Effects
2. Additional Requirements
1) [I] The standards specified for use with this GP, as well as equipment descriptions given herein, apply
to equipment and installation in the U.S. and in countries with no comparable standards. Where
compliance with any code or standard by a local jurisdiction is mandatory, the requirements
prescribed therein shall also be met.
2) * [S] Fire hose couplings selected for a particular plant location shall be compatible with mutual aid
and local fire protection facilities. All fire protection equipment hydrants, monitors, hose reels, fire
main block valves, etc., shall be consistent with other plant fire protection facilities and shall be
approved by the plant Fire Chief.
GP 03-02-03 Fire Water Systems December 2004
RFCH, DIOL For ExxonMobil Use Only Version 2.0.0
Page 6 of 27 ExxonMobil Development Company
3. System Design
3.1. Design Basis
1) * [S] Design conditions, water supply and rates, piping sizes, materials of construction, and type of
hydrant couplings shall be specified. The fire water system design pressure and design temperature
shall comply with the requirements in GP 03-10-01.
2) * [S] The system layout shall be specified, including the general location and number of pumps,
hydrants, monitors, hose reels, deluge sprays, block and flushing valves. The final layout and
location of equipment and facilities shall be approved by the Owner's Engineer.
3) [S] Connections for permanent use of fire water other than for fire protection are not permitted,
except for supply of water to flare seal drums.
4) *[S] Underground carbon steel piping and above ground portions of carbon steel piping that pass
through a dike or dike sleeve shall be protected against external corrosion using a Single Coat Single
Wrap or Double Coat Double Wrap protective coating system as specified.
5) * [S] Fire main materials shall be suitable for plant fire water, and shall be designed to reduce
sediment buildup. Piping approved for underground fire water piping systems identified in the
General ExxonMobil Materials Specification (GEMS) Class Index are listed in Table 1. The
selection and use of underground fire water piping materials in this table, or the use of reinforced
plastic pipe (RTRP Grades) or Fiber Reinforced Plastic (FRP) for underground fire water systems,
shall require the approval of the Owner's Engineer and the plant Fire Chief.
Table 1: Underground Fire Water Piping Materials
NPS SCH/RTG Description Notes
4–24 350 Ductile Iron, Cement
Lined, Restrained Joint,
CL-350
Pipe is supplied externally coated. In addition, pipe is
placed in loose polyethylene sleeve at installation to
retard graphitic corrosion.
1/2–2 80 Carbon Steel,
Galvanized, Seamless
All underground steel components shall be coated.
Coating requirements shall be specified on design
drawings.
Corrosion allowance for carbon steel pipe is 0.063 in.
(1.6 mm)
1/2–2 80 Carbon Steel,
Galvanized, Welded
2–24 CL 200 High Density
Polyethylene, FM
Approved, Seamless,
Extruded
With approval of the Owner's Engineer, class (or SDR)
requirements may be modified for specific applications.
3–24 Std Carbon Steel, Welded,
ERW, Cement Lined
Cement lining shall be per GP 03-10-03 for
underground pipe and components, excluding valves.
GP 03-02-03 Fire Water Systems December 2004
RFCH, DIOL For ExxonMobil Use Only Version 2.0.0
Page 7 of 27 ExxonMobil Development Company
3–24 Std Carbon Steel,
Seamless, Cement
Lined
6) [S] For pipe, tube, or fittings in fire water spray systems, use materials consistent with GP 03-10-01
and NFPA 15. Deviations shall require approval by the Owner's Engineer and the plant Fire Chief.
3.2. Water Supply
1) [S] When the fire water source can provide an unlimited supply of water (i.e., seawater, lake water, or
river water) and the system is designed to directly provide fire water to the grid, there are no
requirements for fire water storage.
Where the fire water supply from a given source is limited:
a) Fire water storage shall be furnished, with a capacity equal to 6 hrs supply at specified design
flow rates, independent of other plant process water usage; and
b) The fire water source shall be sufficient to supply water at half the specified maximum demand
on a continuous basis.
c) For lube plants, terminals, and warehouses, the fire water system supply and design shall conform
to the requirements of NFPA 22.
2) [S] A backflow preventer is required where fire water is supplied from a potable water source or any
municipal source. A break tank shall be used when required by local regulation as the means of
positively preventing contamination. This tank will be provided with an internal coating in
accordance with NSF 61E.
3) *[S] Provision shall be made for the addition of approved biological additives to the fire water system
where biological fouling may occur.
4) [S] Multiple fire water sources shall be provided to the fire water system for:
a) Onshore process facilities with a maximum flow demand greater than 6000 U.S. gpm (22.7
m3/min). In this situation, the different fire water sources shall be located to minimize the
potential that more than one fire water source can be affected by a single fire or explosion event.
b) Onshore facilities where environmental conditions (tides, seasonal water level fluctuations, etc.)
affect the availability or quality of the primary natural water source (e.g., loss of water to a pump
suction, fouling from water in the fire water source piping)
3.3. Pumps and Drivers
1) [S] A minimum of two fire water pumps, each sized for at least 50 percent of the system design
capacity, shall be required for all installations except those with a maximum flow demand of 1500
U.S. gpm (5.68 m3/min) or less. Design shall include the following:
a) Each pump shall be designed for at least 125 psig (860 kPag) discharge pressure at rated capacity
and good for continuous service. The pressure rise at shutoff shall not exceed 20 percent, and at
150 percent of rated capacity the head shall not be less than 65 percent of rated head.
b) System pressure shall be controlled at the pump discharge by a pressure controller, bypassing
excess flow back to the source of supply.
GP 03-02-03 Fire Water Systems December 2004
RFCH, DIOL For ExxonMobil Use Only Version 2.0.0
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c) * An averaging-type Pitot tube installation shall be provided to permit testing of each fire water
pump's capacity. The instrument shall be located in the bypass piping (pump discharge to source
of supply), or, if specified, in the main fire water grid piping. Alternative arrangements are
acceptable subject to approval by the Owner's Engineer.
d) If the fire water pump shutoff pressure exceeds the fire water system design pressure, a pressure
relief valve discharging to the fire water source shall be provided.
e) For installations having three or more fire water pumps, each pump shall be sized for not less than
the system design capacity divided by the number of pumps, unless the Owner's Engineer
otherwise specifies or approves.
2) * [S] Drivers—where only one pump is installed as permitted by Section 3.3, Item (1), it shall be
electric motor driven unless otherwise specified, or the Owner's Engineer otherwise approves. When
two or more pumps are installed:
a) At least one fire water pump shall be electric motor driven.
b) At least one fire water pump shall be diesel engine driven. A fuel tank with capacity for 6 hrs of
continuous operation at full load shall be provided for the diesel engine driven pump. A steam
turbine driven pump may be used in lieu of a diesel engine driven pump with the approval of the
Owner's Engineer and the plant Fire Chief.
c) Additional pumps, if any, may be electric motor diesel engine or steam turbine driven. Choice of
driver for additional pumps shall be based on overall reliability considerations.
d) A remote start button for at least one main fire water pump shall be located in the main control
house.
3) [S] Continuous positive pump suction shall be provided. Priming devices are not acceptable. Deep
well pumps shall be used where positive pump suction is not available.
4) [S] Suction screens shall be provided where foreign material may be present that could plug the
suction line or pumps. Either traveling or double removable screens, cleanable with the pump in
service, shall be used.
5) * [S] The fire water system shall be continuously pressurized from a supply source having a
minimum capacity of 300 U.S. gpm (1.13 m3/min) at 100 psig (690 kPag) pressure (when the main
fire water pumps are not in use) by one of the following means, as specified:
a) A separate electric motor driven pressurizing pump, manifolded in parallel with the main fire
water pumps.
b) A jumpover connection from the plant cooling water or process water systems, provided that the
water is free of oil and emulsion breaking/anti-foaming compounds.
A low pressure cut-in with alarm shall be provided to start one of the main fire water pumps at a
specified pressure. Such alarm shall be located in the main control house.
3.4. Booster Pumps
1) [S] Booster pumps (used to augment fire water system pressure for special fire protection systems
such as spray systems, as required) shall take suction from the fire water system. Where the
downstream pressure buildup may exceed the system design rating, a pressure relief valve that
discharges to a safe location shall be provided.
Conditions requiring booster pumps are:
GP 03-02-03 Fire Water Systems December 2004
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a) Extended fire water systems, where hydrant pressure may be insufficient to provide required
flow.
b) Elevated structures within process unit areas where fire water system pressure may be insufficient
to provide required flow.
2) * [S] Drivers for booster pumps shall be either electric motors or diesel engines. Use of steam
turbines shall be with approval of the Owner's Engineer and the plant Fire Chief.
3.5. Piping Layout
1) [S]The fire water system shall be looped around process units and other areas to be protected, except
for installations with a maximum flow demand of 1500 U.S. gpm (5.68 m3/min) or less, for which a
single feed distribution system is acceptable. The Owner's Engineer and the plant Fire Chief shall
approve the layout of the fire water system. Block valves shall be provided so that in the event of any
piping failure:
a) No more than 1000 ft (300 m) of pipe containing hydrants, hose reels, monitors or sprays can be
lost.
b) The piping to not more than two adjacent sides of any process block can be lost.
2) * [S] Fire water mains in freezing climates (Climatic Zones B, C, and D, as defined per GP 03-09-01)
shall be installed a minimum of 1 ft (300 mm) below the frost line. Fire water connections to
monitors, hose reels, sprays, etc., in freezing climates shall be designed to eliminate water from
freezing in the connections and incorporate winterization features by design.
3) [S] Fire water piping within process unit areas, except for branches to hose reels and to elevated
monitors, shall be underground and buried sufficiently deep to protect against mechanical damage.
Any aboveground section within process units shall be minimized in length.
4) [S] Fire water piping within process unit areas that feed any combination of more than two monitors,
hose reels, hydrants, or sprays, shall be connected to two separate sections of the fire main, and shall
be separated by a valve in the main. Lines to hose reels and monitors shall be valved at each end
where they connect to the main.
Branches to aboveground systems (elevated monitors, spray systems, etc.) located in exposed areas
(such as within a process block) shall be valved at the fire main. Such branches shall be capable of
being opened and isolated from a safe location.
However, short sections of aboveground pipe [less than 50 ft (15 m) long and not more than 4 in. (100
mm) size] that feed a single hose reel or monitor need not be valved at the fire water main takeoff.
5) * [S] Fire water piping to marine terminals shall be protected from direct exposure to a fire on the
water by installing the lines above the pier deck. Where it is necessary to locate the lines below deck,
they shall be fireproofed.
In freezing climates (Climatic Zones B, C, and D, as defined per GP 03-09-01) marine terminal fire
water lines shall be heat traced and insulated. A minimum of four valved hose connections
(international hose connections) shall be provided to permit fireboats to pump into the main fire water
system, at an Owner specified location.
GP 03-02-03 Fire Water Systems December 2004
RFCH, DIOL For ExxonMobil Use Only Version 2.0.0
Page 10 of 27 ExxonMobil Development Company
6) * [S] As specified, the fire water system shall extend to plant buildings used for operations and
storage.
3.6. Hydrants Location and Spacing
1) * [S] Maximum hydrant spacing shall be 300 ft (90 m) as measured along roadways or accessways
between the hydrants in offsite areas and 150 ft (45 m) between hydrants in onsite areas. The
Owner's Engineer may specify other spacing.
2) * [S] Hydrants shall be located on the street or roadside of all pipelines or drainage ditches. Hydrants
shall not be located within diked areas for tanks. The length of large diameter suction hose (4 in. [100
mm] size or larger as defined by the plant Fire Chief) required between the hydrants and fire truck
shall not exceed 25 ft (7.5 m). Where large pipe bands or drainage ditches may hinder access from
hydrants to process areas or tank fields, hydrants shall be located near accessways or walkways across
such obstructions.
3) * [S] Additional area requirements governing the spacing and location of hydrants are given in Table
2.
GP 03-02-03 Fire Water Systems December 2004
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Page 11 of 27 ExxonMobil Development Company
Table 2: Hydrant Location Requirements
Area Specific Requirements
Process Unit Sufficient number of hydrants shall be provided around the
periphery of the process unit to supply the design fire water
capacity for the process unit through hose runs of not more than
100 ft (30 m). Hydrants shall be arranged such that only about
one-half will be lost in case two sides of the loop around the
process unit is damaged (and needs to be isolated). Valves and
hydrants shall be so spaced that in the event of any line failure,
flow shall be provided to two adjacent sides of a process unit at
half the design capacity through hose runs not to exceed 400 ft
(120 m) to reach all the equipment. Other spacing may be
specified by the Owner's Engineer.
Atmospheric Tank Storage:
All tanks Sufficient number of hydrants shall be provided around the
storage tanks to supply the design fire water capacity for the
tank in question. Valves and hydrants shall be located so that
at least one hydrant is within 400 ft (120 m) of any tank in the
event of a line failure. Other spacing may be specified by the
Owner's Engineer.
Where fixed foam
connections are installed in
any tank: fixed roof, floating
roof, and fixed roof with
internal floating cover.
Hydrants shall be located in relation to foam connections so
that the total length of hose from hydrant to fire truck does not
exceed 25 ft (7.5 m) and from fire truck to foam connection
does not exceed 50 ft (15 m). Connections should be located at
least a distance of one tank diameter from the tank but in no
case less than 50 ft (15 m) from the tank.
Floating roof tank Hydrants shall be located such that the tank stairway is facing a
hydrant.
Pressurized and refrigerated storage:
All vessels Hydrants shall be located on at least two sides of each vessel,
so that the vessel can be reached by not less than 3 streams of
water from hoses, each hose length not to exceed 300 ft (90 m).
Vessels arranged two rows deep Hydrants shall be located along roads or accessways around the
vessels.
Cooling Tower At least two hydrants shall be located between 100 to 200 ft (30
to 60 m) of the cooling tower.
3.7. Monitor Location
1) * [S] Monitors shall be provided for fire protection of process units. These shall be located as
follows:
a) Monitor coverage shall extend to the complete process unit area and any other major hydrocarbon
containing equipment. The Plant Fire Chief shall approve the monitor coverage.
GP 03-02-03 Fire Water Systems December 2004
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b) Monitors shall be located such that pipebands and other equipment shall not obstruct the fire
water trajectory to the protected equipment.
c) Monitors may be elevated, as necessary, to achieve the required level of protection.
d) Where the monitor is at a fixed location, at grade—locate approximately 50 ft (15 m) from the
equipment being protected. Where closer spacing is specified, the actuating valve shall be
located at least 50 ft (15 m) from the protected equipment.
e) Where the monitor is at a fixed location, elevated—locate approximately 50 ft (15 m)
horizontally from equipment being protected, and at an elevation to cover the equipment. The
actuating valve shall be located at grade below the monitor.
f) Where closer monitor spacing is specified, the actuating valve shall be located at least 50 ft (15
m) horizontally, from the protected equipment.
g) Where remote control of elevated monitors is specified, final designs shall be approved by the
Owner's Engineer.
h) Location of trailer mounted monitors shall be specified.
2) [S] Cooling towers constructed of combustible materials shall be protected by fixed location
monitors, at-grade. The number of monitors shall be sufficient to provide fire water coverage to all
sides.
3) [S] Pressurized (horizontal) storage vessels handling flammable materials shall be protected by
providing fixed fire water monitors. These monitors shall cover and protect the areas of the vessels
containing nozzles or valves, and those areas of the vessel within 10 ft (3 m) of any valve in the
piping.
4) [S] Fixed fire water monitors shall be provided on at least two sides of each sphere or spheroid, so
that the entire underside of the vessel may be reached by these monitors.
3.8. Hose Reel Location
* [S] Hose reels shall be located per the following:
1) Within process unit areas—hose reels shall not be the primary means of fire protection in process
units. The minimum number of hose reels in a process unit shall be two, located in opposite sides of
the unit. Additional hose reels shall provide coverage to the entire plot area with spacing at
approximately 200-ft (60 m) centers.
2) Outside process unit areas—hose reels as required to protect equipment and facilities that are likely to
be a source of hydrocarbon release. These may include pump areas, tank car or tank truck loading
stations, and other areas with similar fire risk.
3) On cooling towers constructed of combustible materials, hose reels on the fan deck shall be sufficient
to provide total deck area coverage, unless the Owner's Engineer otherwise specifies.
4. Hydrant Selection and Installation
1) [S] Hydrant connections should be compatible with local community and mutual aid mobile
firefighting equipment that may be used in an incident.
GP 03-02-03 Fire Water Systems December 2004
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2) * [S] Self-draining hydrants shall be used in freezing climates (Climatic Zones B, C, and D, as
defined in GP 03-09-01). Hydrants with self-draining feature shall not be used on aboveground fire
line installations.
3) * [S] Hydrant connections. Hydrants shall be able to deliver a nominal 1000 gpm (3.78 m3/min) at 80
psig (550 kPag) grid pressure. Each hydrant shall be provided with three valved and capped
connections for 21/2 in. (65 mm) size hose. Unless otherwise specified, one pumper connection for 4
in. (100 mm) minimum size hose shall be provided as defined by the plant Fire Chief.
Threaded pumper connections shall be fitted with a pressure-tight cap suitable for the system design
pressure. Quick coupling pumper connections shall be valved. All caps shall be secured to the
hydrant with chains.
4) [S] Where commercial hydrants are furnished, they shall be per AWWA C502 or equivalent for
hydrants with 5 in. (125 mm) hydrant valve openings. A minimum 5 in. (125 mm) valve is required.
The branch feeding the hydrant from the fire main shall be a minimum of 6 in. (150 mm). Each
hydrant shall be provided with a hydrant wrench.
5) [S] Hydrant installation and orientation of connections:
a) The minimum vertical clearance between finished grade and the bottom of the hose connection
caps shall be as follows:
Connection Size Clearance
21/2 in. (65 mm) 20 in. (500 mm)
4 in. (100 mm) 10 in. (250 mm)
The maximum vertical clearance between finished grade and the bottom of the hose connection
caps shall be 36 in. (1000 mm).
b) The NPS 4 (100 mm) pumper connection shall be oriented to face the street or roadway.
c) There shall be no obstructions in front of these connections to hinder hose handling.
d) Hydrant guards are required to protect hydrants located within 3 ft (1 m) of roadways or
accessways in areas of high vehicular traffic, to avoid mechanical damage to hydrants. Guards
shall be NPS 4 (100 mm) Sch. 40 pipe, filled with concrete and set in a concrete foundation.
5. Monitor Selection and Installation
1) * [S] All monitors shall be capable of delivering not less than 500 gpm (1.89 m3/min) and shall have
an effective nozzle range of at least 150 ft (45 m) at 75 psig (515 kPag) discharge pressure. Monitors
shall be brass or bronze construction, double swivel, ball bearing, universal motion. The monitor
shall have a locking device suitable for unattended operation. The monitor shall be the deck pipe
type, lever operated, such as Akron Brass Style 3426, Stang Monitor BB0309-21 or equivalent, and
shall be approved by the plant Fire Chief.
A constant flow, combination straight stream fog nozzle, similar to the 21/2 in. (65 mm) size Akron
Brass Style 4450, shall be furnished instead of the normal tip and tube. The nozzle shall be consistent
with other fire protection equipment at the site and shall be approved by the plant Fire Chief. Note:
Akron Brass Company, 1450 Spruce Street, Wooster, Ohio, U.S.A.
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Construction features for elevated monitors shall be approved by the Owner's Engineer and the plant
Fire Chief. The elevated monitor shall include a feature to adjust the water spray pattern if the
movement of the monitor is controlled from grade, unless straight tips are specified by the Owner's
Engineer and the plant Fire Chief.
2) [S] Fixed location monitor installations shall be as shown in Figure 1.
Figure 1: Monitor Installations
Firewater
GearOperatedBall Valve
Grade
FrostLine
Min.
4 in. NPS (100 mm)
B
4 in. NPS (100 mm)
MONITOR ELEVATED
Min.
4 in. NPS (100 mm)
B
4 in. NPS (100 mm)
MONITOR AT GRADE
HC 2-1/2 in.(2)
Note (2)
Note (1)
Notes:(1) Caution Sign:
(2) In freezing climates (Climatic Zones B, C, and D per GP 03-09-01), self-draining or manually operated valvesare required for aboveground piping, and for underground piping above the frost line.
THIS VALVE SHALL BENORMALLY KEPT OPEN
HC
3) * [S] Trailer mounted type monitors shall have the nozzle assemblies mounted on a light weight two-
wheeled inflated tire trailer, suitable for handling by one person. The monitor-trailer assembly shall
be designed to resist the nozzle reaction forces and shall be stable during operation.
The monitor shall be furnished with two hose connections and two 50 ft (15 m) lengths of 21/2 in. (65
mm) size hose. Each inlet requires a check valve to protect against a hose burst. The hose shall be
stored on the trailer, and arranged to play out readily when the trailer is put into service. Hoses to the
monitor shall be permanently connected to valved outlets from the fire water system, unless the
Owner's Engineer otherwise specifies. This feeder line shall be as shown in Figure 2.
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Figure 2: Monitor Feeder Line
Firewater
Gear OperatedBall Valve
Grade
FrostLine
Min.
4 in. NPS (100 mm)
B
4 in. NPS (100 mm)
Min. 20 in. (500 mm)
HC
HOSE FEED LINE FOR TRAILER MOUNTED MONITOR
Note (1)
Note:
(1) In freezing climates (Climatic Zones B, C, and D per GP 03-09-01), self-draining or manually operated valves are required for above-ground piping, and for underground piping above the frost line.
4) [S] Hoses for trailer-mounted monitors shall be trade size 21/2 in. (65 mm) supplied in 50 ft (15 m)
lengths, with expansion ring type couplings. Hose shall be neoprene lined, and covered with an oil
and abrasive resistant neoprene or plastic coating which shall also protect the body of the hose against
deterioration from solar radiation and mildew attack. The hose shall be rated for 400 psig (2800
kPag) test pressure.
6. Hose Reel Selection and Installation
1) * [S] Fixed hose reels connected to the fire water system shall be sized to hold and handle 100 ft (30
m) of 11/4 in. (32 mm) or 1
1/2 in. (40 mm) size firm type hose, as specified by the plant Fire Chief,
without kinking or collapsing. The arrangement shall permit the hose to be placed in service without
completely unwinding the hose from the reel.
2) * [S] Hose, hose reel, and nozzles shall be in accordance with the following:
a) Hose: Trade size 11/4 in. (32 mm) or 1
1/2 in. (40 mm), as specified by the plant Fire Chief, 100 ft
(30 m) length, firm type, covered and lined with natural or synthetic rubber, and rated for 400
psig (2800 kPag) test pressure. Hose shall be furnished with 11/2 in. (40 mm) size hose couplings.
b) Hose reels shall be Wirt and Knox Model FD-47-11/2 -100, or equivalent:
Note: Wirt and Knox reels available from: National Foam System Inc., 150 Gordon Drive,
Lionsville, PA 19353
c) Fog nozzles provided for these hose reels shall be similar to Akron Brass Style 1717. The
nozzles shall be consistent with other fire protection equipment at the site and shall be approved
by the plant Fire Chief.
3) [S] Hose reels shall be installed so that the hose can be pulled off in a clear accessway, parallel to the
equipment being protected (i.e., along a pump row). In freezing climates (Climatic Zones B, C, and
D, as defined in GP 03-09-01) self-draining or manually operated valves are required for
aboveground piping and underground piping above the frost line.
GP 03-02-03 Fire Water Systems December 2004
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Page 16 of 27 ExxonMobil Development Company
7. Valve Selection
1) [S] Block valves in underground fire water piping shall be as follows:
a) Installed such that they are accessible for maintenance (for example, in masonry or reinforced
concrete boxes). When installed in valve boxes, the boxes shall have a suitable lockable cover.
b) Operable from grade with the valve stem and packing permanently protected from contact with
earth, rocks, etc. Valve handwheel extensions are permitted.
c) Provided with a valve position indicator at grade to indicate full open and closed positions.
d) Aboveground portions of the box, valve handwheel, and handwheel extension shall be painted a
distinctive color, consistent with other fire water piping, and shall be identified with a sign
indicating the area served.
e) Valve guards are required to protect valves located within 3 ft (1 m) of roadways or accessways
in areas of high vehicular traffic to avoid mechanical damage to valves. Guards shall be NPS 4
(100 mm) Sch. 40 pipe filled with concrete and set in a concrete foundation.
2) [S] Butterfly valves are not permitted in fire water service where such service normally requires the
valves to be in the open position. Butterfly valves, in the fire water piping to monitors, shall be
provided with manual gear operators to restrict closure time to not less than 10 to 15 seconds.
3) [S] Gate valves installed in aboveground fire water mains shall be OS&Y.
4) [S] Except for manual ball valves NPS 21/2 (65 mm) and smaller, all ball valves in the fire water
piping to monitors shall be provided with manual gear operators to restrict closure time to not less
than 10 to 15 seconds.
5) [S] Post indicator valves should be set so that the top of the post is 36 in. (914 mm) above the final
grade.
8. Spray System Design and Installation
1) * [S] Spray systems: Use of spray systems shall be approved by the plant Fire Chief. When a spray
system is specified for high-risk fire areas, it shall be designed in conformance with NFPA 15 and the
following paragraphs.
a) The spray system shall be a self-draining, normally dry, open head type system, with either a
remotely or a manually operated main actuating valve. See Figure 3.
GP 03-02-03 Fire Water Systems December 2004
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Page 17 of 27 ExxonMobil Development Company
Figure 3: General Spray System Layout
Water
Supply
Strainer
Spray Heads
Slope to Drain
Flushout Connections
Flushout Connection
Drain
b) The location of the manual main actuating valve shall be at least 50 ft (15 m) horizontally from
the area under protection. A sign shall identify the valve.
c) Remotely operated main actuating valves, if specified, shall be fail-open pneumatic type. They
shall be operable from a safe location at least 50 ft (15 m) horizontally from the area under
protection. In addition, the actuator shall incorporate a manual release mechanism, or another
means of actuation shall be provided adjacent to the valve. All valves shall be identified by signs
indicating the location of the system served.
2) * [S] Spray heads shall have a minimum orifice opening of 3/8 in. (10 mm) and shall be either upright-
type (spray head designed in such a way that the water spray is directed upwards against a deflector)
or pendant-type (designed to be installed in such a way that the water spray is directed downwards
against a deflector). The plant Fire Chief shall approve spray head type. Piping to individual spray
heads shall be connected to the top half of the distribution piping. See Figure 4.
GP 03-02-03 Fire Water Systems December 2004
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Page 18 of 27 ExxonMobil Development Company
Figure 4: Sample Spray Head
UPRIGHT TYPE
DELUGE HEAD
3) [S] Flushout connections shall be installed to permit flushing all sections of the system with fresh
water. They shall be capped or flanged. A valve shall be installed upstream of the actuating valve to
permit periodic flushing of the fire main connection.
4) [S] A strainer with a valved blowoff connection shall be installed in the main feeder pipe to the
sprays. The maximum size openings of the strainer shall be 1/4 in. (6 mm) and the ratio of free screen
area to pipe cross-sectional area shall be 3 to 1. Blowoff valve size and connection shall be NPS 2
(50 mm).
5) [S] Spray system piping shall comply with the following:
a) Piping materials downstream of the strainer shall minimize scale build-up and corrosion.
b) The main spray header shall be designed to minimize fire/explosion damage.
c) Piping for branch lines to individual spray heads shall not be less than 1 in. (25 mm) diameter.
d) Take-off to all distribution piping shall be from the top of the headers.
e) All low points in the system shall have a drain valve and all system piping shall be self-draining
to the drain valves.
6) * [S] Fire water application rate shall not be less than 0.2 gpm per ft2 (0.0080 m
3/min per m
2) of area
to be sprayed, unless otherwise specified.
7) * [S] The spray system design shall be approved by the Owner's Engineer and the plant Fire Chief.
8) [S] All automatic water spray systems shall be provided with a local alarm.
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Page 19 of 27 ExxonMobil Development Company
9. Deluge and Spray System Installation for Pressurized and Refrigerated Storage
9.1. Common Requirements
1) [S] Deluge systems shall be as follows:
a) Deluge heads for the top system shall be as indicated in Figure 5, Detail A.
b) Spray nozzles for tank shells, horizontal drums, and the bottom half of spheres shall be the non-
clogging type, and shall have a minimum orifice opening of 3/8 in. (10 mm).
c) Baffles, diverters, notched weirs or auxiliary deluge heads shall be used if needed, to distribute an
even water film over the entire surface of the vessel and to ensure coverage in areas shielded from
direct water flow by appurtenances, platforms and toe plates.
d) * The Owner's Engineer and the plant Fire Chief shall approve the detailed design of all spray
systems.
e) The capacity of the fire water systems in these areas shall be capable of supplying the sum of the
fire water to the deluge system of the vessel involved in an emergency, plus the deluge system of
adjacent exposed vessels, and an additional 1000 gpm (3.78 m3/min) of fire water for monitors
and hose streams. Where these requirements exceed the specified fire water system capacity,
piping may be arranged to sectionalize the control of individual deluge systems or groups of
systems. For example, if more than one deluge head is required on a vessel, the system may be
segmented to cover only that half of the vessel exposed to an adjacent fire.
2) [S] Operating and drain valves shall be provided for the fire water deluge system of each vessel, as
indicated in Figure 5. The following requirements shall govern the installation:
a) Valves shall be installed in a valve box located outside the dike and shall be accessible in case of
fire.
b) * In freezing climates (Climatic Zones B, C, and D, as defined per GP 03-09-01), the valve box
shall be winterized.
c) Minimum spacing between the vessel and the valve box shall be one vessel diameter or 100 ft (30
m), whichever is greater.
d) The operating valve shall be identified by a sign, located at the valve.
e) Piping layout to the deluge system shall permit complete draining at the single drain valve.
f) A valve shall be installed upstream of the actuating valve to permit periodic flushing of the fire
main connection.
g) Where a remotely operated actuating valve is provided, it shall be fail-open pneumatic type and
shall be provided with a full size bypass operable from a safe location at least one vessel diameter
or 100 ft (30 m), whichever is greater, horizontally from the vessel being protected.
3) [S] Spheres and spheroids shall be provided with a top mounted fire water deluge system as shown in
Figure 5. The water deluge shall cover the upper hemisphere and shall be sized to deliver 0.15 gpm
per ft2 (0.0062m
3/min per m
2) to one-half of the sphere total surface area.
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In addition, fire water monitors or spray systems actuated from the same location as the deluge
system shall be provided to protect the lower hemisphere and shall be sized to deliver 0.15 gpm per
ft2 (0.0062 m3/min per m2) to one-half of the sphere total surface area.
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Page 21 of 27 ExxonMobil Development Company
Figure 5: Typical Piping Requirements for Top Mounted Cooling Water
Deluge Systems (1)(2)
See Detail A20 in. Approx. (3)
H
1/4 in.Plate
Washer
(Stop)
Welding Reducer(See Chart)
2d
3/4 in. Bolt
(Concentric)
1/2 in.
1/2 x 3/4 in. Bar
DETAIL A
DELUGE HEAD
D
ELEVATION
Dike
Slope
Feed Pipe
(See Chart)
DrainValve
Identification SignFor Operating
Valve
NOTICE
OperatingValve
Valve Box(If Required)
Firewater
Main
Acceptable Metric EquivalentsFigure 1 Detail A
ITEM IN. MM
Plate
Bar
Bolt
1/4
1/2 x 3/4
3/4
6
12 x 20
20
d (Feed Pipe Nominal Diam) d (NPS, in.) x 25 mm
SPHERE
DIAMETER (4)(5)
"d"Nominal
PipeDiameter
REDUCER SIZE DIMENSION"D"
DIMENSION"H"
Ft M in. mm in. mm in. mm in. mm
Up to 41.0 Up to 12.5 4 100 4 x 2 100 x 50 12 300 3 75
41.5 -49.0
12.7 -15.0
4 100 4 x 2-1/2 100 x 62 12 300 3 75
49.5 -57.5
15.0 -
17.56 150 6 x 2-1/2 150 x 62 18 450 4 100
58.0 -69.5
17.7 -21.2
6 150 6 x 3 150 x 75 18 450 4 100
70.0 -
85.021.3 - 26 8 200 8 x 4 200 x
10024 600 6 150
Dia ="d"
Notes:
(1) Figure illustrates arrangement and components for spheres but is applicable to dome roof and spheroid tank installations.(2) Where sectionalized spray coverage is required, multiple deluge heads and individual piping including control at the valve box shall be provided.
(3) The specified 20 in. (500 mm) dimension may be varied to permit the water to clear obstacles such as appurtenances and platforms.(4) For spheroids use diameter at equator
(5) For spheres and spheroids of diameter greater than 85 ft (26 m) the use of oversized lines or a booster pump shall be considered to compensatefor the increased static head.
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Page 22 of 27 ExxonMobil Development Company
4) [S] Pressurized (horizontal) storage vessels handling flammable materials shall be protected as
follows:
a) For three or more vessels located within 50 ft (15 m) from each other (shell-to-shell), each shall
be fireproofed.
b) * For single vessels or for two vessels located within 50 ft (15 m) of each other but with more
than 50 ft (15 m) spacing from other pressurized storage vessels, provisions for cooling with fire
water monitors, or remotely actuated fixed fire water spray systems, may be substituted for
fireproofing.
9.2. Pressurized Storage
1) [S] Provisions for water flooding. All pressurized storage vessels handling flammable materials not
in refrigerated service (including horizontal drums used for storage, spheres and spheroids) shall have
a connection installed to permit flooding of the vessel with fire water, as follows:
a) * The connection shall be to the product line at the bottom of the vessel.
Additional water flooding connections shall be specified.
b) The connection shall terminate outside the dike, and at least 100 ft (30 m) from the vessel.
c) When the connection is to a non-dedicated line (such as the normal fill line or pump suction line),
the connection shall be located between the vessel block valve and the manifold valve and shall
comply with the following additional criteria.
i) The connection shall be made in the top of the line, to prevent accumulation of water.
ii) The connection shall be minimum length and include (in the order listed) a block valve, a
check valve, and a 21/2 in. (65 mm) size hose connection fitted with a pressure tight cap and
a vent valve.
d) The termination point shall be located such that not more than 100 ft (30 m) of hose is required
for its use.
e) The termination shall be identified with a sign indicating the purpose and vessel served.
9.3. Refrigerated Storage
1) [S] In addition to a top-mounted fire water deluge system per Section 9.1 Item (3), double wall
spheres using a granular type insulation in the annular space shall be furnished with a bottom spray
system. Such system shall be sized to deliver water at a rate of 0.15 gpm per ft2 (0.0062 m
3/min per
m2) to the under portion of the vessel within the vessel support legs.
2) [S] Dome roof tanks shall be provided with a top mounted fire water deluge system. The system shall
be designed to deliver water at a rate of 0.15 gpm per ft2 (0.0062 m
3/min per m
2) of roof surface. A
deflector plate shall be installed continuously around the tank at the roof-to-shell joint to deflect roof
cooling water run-off back against the vertical shell.
3) [S] Dome roof tanks higher than 75 ft (23 m) shall be provided with additional water at a rate of 0.15
gpm per ft2 (0.0062 m
3/min per m
2) of total vertical shell area. This water shall be supplied through a
spray ring system located at the top shell course installed below the compression ring.
4) [S] Dome roof tanks less than 75 ft (23 m) high shall be provided with additional cooling water
capacity at a rate of 0.15 gpm per ft2 (0.0062 m3/min per m2) of total vertical shell area. The water
may be supplied through a spray ring located at the top shell course installed below the compression
ring or by fixed water monitor nozzles located at grade around the tank.
GP 03-02-03 Fire Water Systems December 2004
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Page 23 of 27 ExxonMobil Development Company
10. Spray Systems for Air Preheaters
10.1. Regenerative (Rotary) Air Preheaters
1) * [S] Regenerative air preheaters shall be provided with a fixed internal fire water spray system. Fire
water application rates shall be:
a) 1.3 gpm/ft2 (0.052 m
3/min per m
2) over the entire area of the upper face of a vertical axis air
preheater.
b) 1.3 gpm/ft2 (0.052 m
3/min per m
2) over the entire area of both faces of a horizontal axis air
preheater.
Lower application rates shall require approval by the Owner's Engineer.
Inert systems such as CO2 (see NFPA 12), nitrogen, and steam may be used instead of fire water to
minimize damage while extinguishing a fire. When required, details for such systems shall be
specified.
2) [S] Water spray nozzles shall be located in both air and flue gas ducts.
3) [S] Spray nozzles shall be suitable for the high temperature and corrosive environment in the flue gas
duct. The nozzles shall be equipped with a rupture disc or an equivalent seal to prevent flue gases
from condensing in the piping.
4) [S] Spray system shall conform to Section 8, Items 1-5, 7, and 8, except that:
a) The location of the main actuating valve shall be at a safe location at grade and at least 25 ft (7.6
m) from the air preheater.
b) The water supply shall have a double block and bleed.
c) In freezing climates, portions of the system that are continually filled with water shall be
winterized.
5) [S] An air preheater and duct drainage system shall be provided as follows:
a) The drainage system shall be designed to be self-opening (for example, by using water seals,
pressure-loaded panels, or rupture disks in the drainage system), or be operable from a safe
location 25 ft (7.6 m) from the air preheater.
b) Air preheater and duct drains with a minimum diameter of 4 in. (100 mm), or equivalent open
area, shall be located at all low points in sufficient number to provide adequate drainage during
the operation of the deluge system.
c) Any drain lines connected to the flue gas ducts shall be protected against acid dew-point
corrosion.
10.2. Recuperative (Static) Air Preheaters that Receive Flue Gas from More than One Fired Heater/Boiler
1) * [S] The water wash system installed for cleaning the preheater shall be modified to allow injection
of fire water at a rate equivalent to the water wash rate, approximately 4 gpm/ft2 (0.17 m
3/min per m
2)
over the cross sectional area of the air preheater.
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Page 24 of 27 ExxonMobil Development Company
Inert systems such as CO2 (see NFPA 12), nitrogen, and steam may be used instead of fire water to
minimize damage while extinguishing a fire. When required, details for such systems shall be
specified.
2) [S] Water wash piping shall be extended to a safe location at grade and at least 25 ft (7.6 m) from the
air preheater. At this location, the piping shall be provided (in the order listed) with a block valve,
check valve, and 21/2 in. (65 mm) fire hose connections (with a pressure tight cap) in sufficient
number to allow application of the desired fire water rate.
3) [S] An air preheater and duct drainage system shall be provided as described in Section 10.1, Item
(5).
11. Inspection and Testing
* [S] Acceptance tests. Fire water systems covered by this Practice shall be tested in the presence and to
the satisfaction of the Owner's Representative, by demonstrating the capability to deliver the design fire
water rate prior to the system being placed in service.
GP 03-02-03 Fire Water Systems December 2004
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Page 25 of 27 ExxonMobil Development Company
Record of Change
Version 1.0.0 Date: 07/01
Location Action Description
Initial Publish.
Version 1.0.0 Date: 09/03
Global Practice version number and format updated to comply with new
process; however, original publish date remains, and no content was
modified.
Version 2.0.0 Date: 12/04
Section 1.1 Modified Added references to GP 03-10-01 and GP 03-10-03.
Section 1.3 Modified Added reference to NFPA 12 and removed references to NFPA 20 and
NFPA 24.
Section 1.4 Added Added new section to identify reference to NSF 61E.
Section 3.1,
Item (1)
Modified The pressure and temperature criteria were referenced to GP 03-10-01.
Section 3.1,
Item (2)
Modified Changed paragraph from [I] to [S].
Section 3.1,
Item (3)
Modified Rationale expanded to include potential contamination of the fire water
system as a reason for prohibiting permanent connections between fire
water and process systems.
Section 3.1,
Item (5)
Modified Added GEMS specifications for underground fire water piping (new
Table 1). Added requirement that all underground fire water piping
materials shall be approved by the Owner's Engineer and the plant Fire
Chief.
Section 3.1,
Item (6)
Added Added, "For pipe, tube or fittings in fire water spray systems, use
materials consistent with GP 03-10-01 and NFPA 15. Deviations shall
require approval by the Owner's Engineer and the plant Fire Chief."
Section 3.2,
Item (2)
Added Added requirement for a backflow preventer in potable water or
municipal water lines supplying fire water systems. Added requirement
for internal coating on dual service break tanks per NSF 61E.
Section 3.2,
Item (3)
Added Added that provision should made for the addition of approved biological
additives where the fire water supplies are liable to biological fouling.
Section 3.2,
Item (4)
Modified Clarified that this item provides criteria when the installation of more
than one fire water source is required.
Section 3.4,
Item (2)
Modified Use of steam drivers for booster pumps now requires approval of the
Owner's Engineer and the plant Fire Chief.
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Page 26 of 27 ExxonMobil Development Company
Section 3.5,
Item (2)
Modified
Modified the text to specify that the potential for water freezing, leading
to system damage, needs to be addressed in the system design.
Table 2
(formerly
Table 1)
Modified Under Atmospheric Tank Storage, Fixed Foam in Fixed Roof Tanks,
added the requirement that "connections should be located at least a
distance of one tank diameter from the tank but in no case less than 50 ft
(15 m) from the tank."
Section 3.7,
Item (2)
Modified Rationale expanded.
Section 3.7,
Item (3)
Modified Rationale expanded.
Section 4, Item
(1)
Added Added requirement that the hydrant connections should be compatible
with local community and mutual aid mobile firefighting equipment that
may be used in an incident. Subsequent items in Section 4 renumbered.
Section 4, Item
(5d)
Addition Rationale added.
Section 5, Item
(1)
Modified Amended the monitor criteria to 500 gpm with a range of 150 feet at 75
psig, to match the capability of referenced monitor models.
Modified constant flow, combination straight stream fog nozzle from
Akron Black Widow Style 2145 to Akron Brass Style 4450. The Black
Widow Style 2145 is no longer offered.
Section 7, Item
(5)
Added Added the requirement that Post Indicator valves should be set so that the
top of the post is 36 in (914 mm) above the final grade. Added rationale.
Section 8, Item
(1c)
Modified Deleted bypass on main actuating valves. Added, "In addition, the
actuator shall incorporate a manual release mechanism, or another means
of actuation shall be provided adjacent to the valve."
Section 8, Item
(8)
Added Added that all automatic water spray systems shall be provided with a
local alarm.
GP 03-02-03 Fire Water Systems December 2004
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Page 27 of 27 ExxonMobil Development Company
Attachment: Purpose Codes Definitions
Code Description
C Assigned to paragraphs containing specifications whose primary purpose is reduced costs.
Reduced cost in this context refers to initial investment cost and does not include Life-Cycle
cost considerations. Life-Cycle cost considerations are captured under reliability,
maintainability, or operability purpose codes.
E Assigned to paragraphs containing specifications whose primary purpose is driven by
environmental considerations. Environmental considerations typically include specifications
intended to protect against emissions/leakage to the air, water, and/or soil. Deviations from the
specifications contained in such paragraphs require formal review and approval according to
local environmental policy.
I Assigned to paragraphs that provide only clarifying information such as Scope statements,
definitions of terms, etc.
M Assigned to paragraphs containing specifications whose primary purpose is to provide for
maintainability of equipment or systems. Maintainability provisions are those that facilitate the
performance of maintenance on equipment/systems either during downtimes or during on-
stream operations.
O Assigned to paragraphs containing specifications whose primary purpose is to assure
operability of equipment or systems. Operability is the ability of the equipment/system to
perform satisfactorily even though conditions are off-design, such as during startups, process
swings, subcomponent malfunction, etc.
R Assigned to paragraphs containing specifications whose primary purpose is to improve or
assure the reliability of equipment or systems. Reliability is a measure of the ability of
equipment/systems to operate without malfunction or failure between planned maintenance
interventions.
S Assigned to paragraphs containing specifications whose primary purpose is avoidance of
personnel or operational safety incidents. Any deviation from the specifications contained in
such designated paragraphs requires formal review and approval according to local safety
policy.
Personnel Safety: Refers to the avoidance of recordable personnel injuries; i.e., burns, cuts,
abrasions, inhalation, or exposure to dangerous substances, etc., that
could result in medical treatment, restricted work, lost-time incidents, or
fatalities.
Operational
Safety:
Refers to the prevention and control of process releases, fires, explosions,
etc.