Oisd STD 164
Oisd STD 164
Oisd STD 164
Number:OISD/DOC/2013/158
Page No. I
OISD - STD-164
Second edition: July, 2012
OISD - STD-164
First edition: July, 1998
Second edition: July, 2012
FOR RESTRICTED
CIRCULATION ONLY
Prepared by:
FUNCTIONAL COMMITTEE ON
FIRE PROOFING OF STEEL SUPPORTING STRUCTURES IN OIL & GAS INDUSTRY
Preamble
Indian petroleum industry is the energy lifeline of the nation and its continuous performance is essential
for sovereignty and prosperity of the country. As the industry essentially deals with inherently inflammable
substances throughout its value chain – upstream, midstream and downstream – Safety is of paramount
importance to this industry as only safe performance at all times can ensure optimum ROI of these
national assets and resources including sustainability.
While statutory organizations were in place all along to oversee safety aspects of Indian petroleum
industry, Oil Industry Safety Directorate (OISD) was set up in 1986 Ministry of Petroleum and Natural
Gas, Government of India as a knowledge centre for formulation of constantly updated world-scale
standards for design, layout and operation of various equipment, facility and activities involved in this
industry. Moreover, OISD was also given responsibility of monitoring implementation status of these
standards through safety audits.
In more than 25 years of its existence, OISD has developed a rigorous, multi-layer, iterative and
participative process of development of standards – starting with research by in-house experts and
iterating through seeking & validating inputs from all stake-holders – operators, designers, national level
knowledge authorities and public at large – with a feedback loop of constant updation based on ground
level experience obtained through audits, incident analysis and environment scanning.
The participative process followed in standard formulation has resulted in excellent level of compliance
by the industry culminating in a safer environment in the industry. OISD – except in the Upstream
Petroleum Sector – is still a regulatory (and not a statutory) body but that has not affected implementation
of the OISD standards. It also goes to prove the old adage that self-regulation is the best regulation. The
quality and relevance of OISD standards had been further endorsed by their adoption in various statutory
rules of the land.
Petroleum industry in India is significantly globalized at present in terms of technology content requiring
its operation to keep pace with the relevant world scale standards & practices. This matches the OISD
philosophy of continuous improvement keeping pace with the global developments in its target
environment. To this end, OISD keeps track of changes through participation as member in large number
of International and national level Knowledge Organizations – both in the field of standard development
and implementation & monitoring in addition to updation of internal knowledge base through continuous
research and application surveillance, thereby ensuring that this OISD Standard, along with all other
extant ones, remains relevant, updated and effective on a real time basis in the applicable areas.
Together we strive to achieve NIL incidents in the entire Hydrocarbon Value Chain. This, besides other
issues, calls for total engagement from all levels of the stake holder organizations, which we, at OISD,
fervently look forward to.
Jai Hind!!!
Executive Director
FOREWORD
Oil Industry in India is more than 100 years old. Over the years a variety of
practices have been in vogue because of collaboration/ association with different
foreign companies and governments. Standardisation in design, operating and
maintenance practices was hardly in existence at a national level. This lack of
uniformity, coupled with feed back from some serious accidents that occurred in
the recent past in India and abroad, emphasised the need for the industry to
review the existing state of art in designing, operating and maintaining oil and
gas installations.
With this in view, the Ministry of Petroleum and Natural Gas in 1986
constituted a Safety Council assisted by the Oil Industry Safety Directorate (OISD)
staffed from within the industry in formulating and implementing a series of self
regulatory measures aimed at removing obsolescence, standardising and upgrading
the existing standards to ensure safer operations. Accordingly, OISD constituted a
number of functional committees comprising of experts nominated from the
industry to draw up standards and guidelines on various subjects.
The Coordinator,
Functional Committee on
‘Fire Proofing of Steel Supporting Structures in Oil & Gas Industry.’
Oil Industry Safety Directorate
8th FLOOR, OIDB Bhavan, Plot No 2
Sector-73, Noida - 201301 (Uttar Pradesh)
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Page No. V
NOTE
Though every effort has been made to assure the accuracy and reliability
of the data contained in these documents OISD hereby expressly disclaims any
liability or responsibility for loss or damage resulting from their use.
LEADER
MEMBERS
MEMBER COORDINATOR
===================================================================
In addition to the above, several other experts from Industry contributed in the
preparation, review and finalisation of this document.
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Page No. VII
FUNCTIONAL COMMITTEE OF SECOND EDITION
ON
FIRE PROOFING OF STEEL SUPPORTING STRUCTURES IN OIL & GAS INDUSTRY
NAME ORGANISATION
LEADER
MEMBERS
MEMBER COORDINATOR
===================================================================
In addition to the above, several other experts from Industry contributed in the
preparation, review and finalisation of this document.
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Page No. VIII
CONTENTS
1.0 INTRODUCTION 01
2.0 SCOPE 01
3.0 DEFINITION 01
11.0 REFERENCES 15
1.0 INTRODUCTION
This standard provides technical details, including inspection and maintenance requirements, for
selection and application of fire proofing in Oil and Gas Industry.
Only passive fire proofing systems have been covered in this standard and details of active systems
such as automatic water deluge, which are used to protect pressure vessels, processing structures,
equipment etc., are excluded. Passive fire protection shall be used along with active fire protection
systems like water deluge sprinkler systems etc.
2.0 SCOPE
This standard provides minimum requirements of passive fire proofing for steel supporting
structures of on-shore installations for exploration & production, refineries, petrochemicals and
marketing installations.
This standard is not applicable to offshore installations.
The standard also covers technical details of materials used for fire proofing, fire rating, selection
and application methods for different areas, methods of application of fire proofing materials, quality
control measures and inspection during application of materials, including periodic inspection and
maintenance of fire proofing. Active fire protection system and its effects are beyond the scope of
this standard.
3.0 DEFINITIONS
i) Fire Proofing: Fire proofing is an insulation that provides a degree of fire resistance to protect
substrates of vessels, piping and structures for a predetermined time period against fire.
ii) Fire-Exposed Envelope: A fire-exposed envelope is the three-dimensional space into which fire
potential equipment can release flammable or combustible fluids that are capable of burning long
enough and with enough intensity to cause substantial property damage.
iii) Fire Rating is the duration of fire test exposure to which a component or construction assembly
is exposed and for which it meets all the acceptable criteria as determined by relevant standard.
iv) Flammable (or inflammable) product: Any product which when tested in a specified manner will
ignite when mixed with air on contact with a flame and will support combustion.
v) Shall indicate that the provision is mandatory.
vi) Should indicate that the provision is recommendatory as per good engineering practices.
vii) Substrate is the underlying layer being protected by a fireproofing barrier layer.
“OISD hereby expressly disclaims any liability or responsibility for loss or damage resulting
from the use of OISD Standards/Guidelines.”
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outside the industry premises due to release of large quantities of flammable products and/or toxic
materials.
Application of fireproofing will delay an eventual collapse of steel structures and allow it to happen in
gradually controlled manner with visible signs. This helps in timely isolation of the affected equipment
and carrying out safe fire fighting and rescue operations.
Refrigerated or cryogenic liquefied gases exert an intense cooling effect when escaping to
atmosphere, which may expose unprotected steelwork to severe embrittlement and failure due to
fracture. One of the most effective and well proven means of protection against such hazards is
fireproofing.
4.2 General application criteria
4.2.1 Fire protection
Fireproofing shall be applied to the steel supporting structures, whose sudden failure would lead to
endangering the lives of operating personnel, escalation of the incident or unacceptable
environmental pollution. Only the steel structures located within the fire exposed envelope shall be
considered for fireproofing.
Fire proofing is normally not provided for the following:
i) Top surfaces of the beams, which support floor plates, gratings or equipment.
ii) All the stairways, walkways and platforms etc which are designed for live loads.
For all the steel stanchion or supports requiring resistance against mechanical damage at the lower
end, fire proofing should preferably be made of reinforced cement concrete or otherwise suitable
means should be provided to protect the fire proofing from mechanical damage. The height of such
fire proofing shall be a minimum of 1.8 M from the grade level. However, at higher levels, alternative
fireproofing materials can be used.
4.2.2 Cold splash protection
Steel structure members which are under the danger of embrittlement due to cooling effect of the
product released through potential sources of leaks should be protected against cold splash.
The length of time during which a steel structure needs to maintain its integrity depends on local
circumstances such as type of plant, availability of fire-fighting services, and risk of escalation.
Due to high severity of hydrocarbon fire in comparison to cellulose type fire, all the fireproofing
systems for hydrocarbon fires shall meet the high rise hydrocarbon fire curve criteria mentioned
under UL1709 fire resistance tests for the duration of predicted fire exposure. (A brief write up about
testing of fireproofing materials is attached as ANNEXURE-II to this document.)
50 mm thick cement concrete cover of grade or proportion as specified at clause no 8.8.1 of this
document, meets the above hydrocarbon fire requirement. Systems based on other types of
fireproofing materials shall be referred as ‘other than cement concrete fireproofing systems’ as per
the scope of this standard. To establish fire rating of alternative materials appropriate tests or
calculations can be done. Results of the tests performed on new materials shall be as good as
those of the cement concrete.
“OISD hereby expressly disclaims any liability or responsibility for loss or damage resulting
from the use of OISD Standards/Guidelines.”
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The extent of the fireproofing around equipment and structures shall be based strictly on the detailed
fire assessment study and the same should be clearly indicated on layout and construction drawings.
The type of fireproofing material and its construction/application method should be clearly specified.
If necessary, heat transfer calculations should be made to determine the fireproofing thickness for
different Hp/ANote1 ratios of sections to be protected, the need for reinforcement and the need for
insulation. Reinforced and/or precast cement concrete can also be considered as an alternative to
fireproofed structural steel.
Note 1: Hp is the exposed perimeter and A is the cross sectional area of the substrates.
Structural members or bracings within a fire exposed envelope which are required for reducing the
effective buckling length of the stanchions shall be fireproofed. Structural members serving only a
windbracing function shall not be fireproofed.
Determination of fire proofing needs involves a three step procedure that establishes:
a) Fired heaters that charge liquid or mixed phase hydrocarbons, under the following conditions:
i. Operation at temperatures and flow rates that are capable of causing coking within the tubes.
ii. Operation at pressure and flow rates those are high enough to cause large spills before the
heater can be shut in.
iii. Charging of potentially corrosive fluids.
iv. Incorporation of a high level of automation and complex peripheral equipment such as
combustion air preheater.
“OISD hereby expressly disclaims any liability or responsibility for loss or damage resulting
from the use of OISD Standards/Guidelines.”
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b) Pumps that handle flammable and combustible liquids at or above their flash point or
autoignition temperatures, at high pressure, or at high flows. In some cases, maintaining
seals without serious leaks may be difficult because of the liquid being pumped.
c) Reactors that operate at high pressure or are apt to produce exothermic or runaway
reactions.
d) Compressors along with related lube-oil system. Compressors do not have a high liquid - fire
potential; however, they can generate a fire-exposed envelope if the likelihood exists that
there will be a prolonged release of gas and intense fire in the vicinity of important structural
supports.
e) Heat exchangers handling high temperature fluids at high pressure.
f) Pressure vessels handling light hydrocarbons e.g. C2, C3 and C4 (Reflux).
5.1.2 Medium Fire Potential Equipment :
a) Accumulators, feed drums, and other vessels that may leak as a result of broken
instrumentation, ruptured gaskets, or other apparatus.
b) Tower that may leak as a result of broken gauge columns or gasket failure on connected piping
and bottom reboilers.
5.1.3 Low Fire-Potential Equipment :
Note-2
a) Pumps that handle excluded class liquids below their flash points.
b) Piping that is within battery limits and has a concentration of valves, fittings, and flanges.
c) Heat exchangers that may develop flange leaks.
0
Note-2: Liquids having flash point of 93 C and above
A frequently used frame of reference for a fire-exposed envelope is one that extend 20-30 feet (6.1-
9.1 meters) horizontally and 30-40 feet (9.1-12.2 meters) vertically from a source of liquid fuel.
The following conditions within the fire-exposed envelope can either limit or extend the envelope’s
reference dimensions:
“OISD hereby expressly disclaims any liability or responsibility for loss or damage resulting
from the use of OISD Standards/Guidelines.”
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d) Fireproofing shall be used for knee and diagonal bracing that contributes to the support of
vertical loads or to the horizontal stability of columns if it is located within the fire-exposed
envelope. Knee and diagonal bracing that is used only for wind, earthquake, or surge loading
need not be fireproofed (see Figure 5.1).
e) When reactors, towers, or similar vessels are installed on protected steel or reinforced concrete
structures, fireproofing materials shall be used for protection of supporting steel brackets, lugs,
or skirts (see Figure 5.1). The insulating effect of the fireproofing material must be considered
in the design of supports for vessels that operate at high temperatures.
Because of the size and importance of large vessels such as reactors, regenerators and
vacuum towers that are mounted on high support structures, fireproofing should be provided for
the entire exposed support system regardless of its height.
f) Except for the upper surface of the top flange, fireproofing shall be provided for beams that
support equipment in fire-exposed areas.
f) A fireproofed catch beam or bracket shall be given beneath larger piping (greater than 6
inches) that is supported by exposed steel spring hangers or rods. Sufficient clearance should
be provided between the bracket or beam and the pipe to permit free movement.
a) Supports of grade level air fin-fan coolers handling liquid hydrocarbons shall be fireproofed.
b) Fireproofing shall be provided for the structural supports of all air-cooled exchangers handling
flammable or combustible liquids at an inlet temperature above their auto ignition or above
o
315 C, whichever is lower.
c) In case of the air-cooled exchangers located above vessels or equipment containing flammable
materials; all the supports located within a 6m – 12 m radius of such vessels or equipment
regardless of their height, shall be fireproofed. (See figure 5.5)
5.3.4 Tower & Vessel Skirts :
“OISD hereby expressly disclaims any liability or responsibility for loss or damage resulting
from the use of OISD Standards/Guidelines.”
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a) Fire-proofing shall be used for the exterior surfaces of skirts that support tower and vertical
vessels. Consideration should also be given for fireproofing interior surfaces of skirts if there
are flanges or valves inside the skirt. Interior surfaces of skirts need not be fireproofed if there
is only one manway opening through the skirt and its diameter is not greater than 2 feet (0.6
meter). Openings other than the single manway can be closed with removable steel plate at
least 1/4 inch (6.4 millimetres) thick. The effect of draft through vent openings and space that
surrounds pipe penetrations in the skirt should be minimised.
b) Fireproofing shall be used for brackets or lugs that are used to attach vertical reboilers or heat
exchangers to towers or tower skirts.
c)
5.3.5 Leg Supports For Towers & Vessels :
If the towers or vessels are elevated on exposed steel legs; fireproofing the leg supports to their full
load-bearing height shall be used.
5.3.6 Supports for Horizontal Exchangers, Coolers, Condensers, Drums, Receivers and
Accumulators :
Fireproofing should be given for steel saddles that support horizontal heat exchangers, coolers,
condensers, drums, receivers, and accumulators that have a diameter greater than 30 inches (0.76
meter) if the vertical distance between the concrete pier and the shell of the vessel exceeds 18
inches (0.46 meter).
5.3.7 Fired Heaters :
a) Fireproofing shall be used for all supports for fired heaters in hydrocarbon service. Heaters are
often supplied with short, steel legs that are set on reinforced concrete piers. These legs shall
be fireproofed from the concrete piers upto the point where the steel columns are welded to the
steel floor plate of the firebox.
b) If structural supports are provided by horizontal steel beams beneath the firebox of an elevated
heater, fireproofing shall be used for the beams unless at least one flange face is in continuos
contact with the elevated firebox.
c) For common chimneys or stacks handling flue gas from several heaters; structural support for
ducts or breeching between heaters and stacks shall also be fireproofed.
d) When fired heaters in other than hydrocarbon service, such as steam superheaters or catalytic
cracking-unit air heaters, are located within a fire-exposed envelope, fireproofing shall be
provided for their support members if a collapse would result in damage to adjacent
hydrocarbon-processing equipment or piping.
5.3.8 Electrical power and Instrument cables
a) Cables in trays, racks or ducts which are critical (e.g. cables feeding emergency shutdown and
emergency depressuring valves) shall be protected from fire damage, unless they are
designed to fail safe during a fire exposure. Fire proofing requirements of such cables shall be
as per API-2218.
b) The need to protect other electrical, instrument or control systems not associated with control
or mitigation of fire should be based on the risk assessment.
5.3.9 Pneumatic and hydraulic instrument tubing
Pneumatic and hydraulic instrument lines which are critical (e.g. tubing for emergency shutdown
and emergency depressuring valves) shall be protected from fire damage, unless they are
designed to fail safe during a fire exposure. Fire proofing requirements of such lines shall be as per
API-2218.
5.3.10 Emergency valves within a fire exposed envelope
Emergency valves and valve actuators located in a fire exposed envelope meeting the following
criterion shall be fireproofed:
a) The valve is important to shutting down the unit safely.
“OISD hereby expressly disclaims any liability or responsibility for loss or damage resulting
from the use of OISD Standards/Guidelines.”
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Examples of these valves are isolation valves in piping to pumps that are fed from large towers,
accumulators or feed surge drums.
Fireproofing of such valves shall be done as specified in API-2218.
5.4 FIREPROOFING OUTSIDE PROCESSING UNITS:
5.4.1 Pipe Racks :
a) Fireproofing shall be provided for pipe rack supports outside processing units if they are
located within a fire-exposed envelope. Bracing for earthquakes, wind or surge protection and
stringer beams that run parallel to piping need not be fireproofed.
b) If important pipe racks run within 20-30 feet of open drainage ditches or channels that may
contain oil waste or receive accidental spills, either fireproofing should be considered for the
pipe rack supports as described in (5.3.2 (b)) as above or the ditch should be covered.
5.4.2 Storage Spheres/ Vessels & its Supports :
Fire proofing protects the LPG vessel by reducing the heat input to the vessel and also by controlling
the rate of rise of vessel wall temperature. Fireproofing provides protection in case water supply is
interrupted.
a) Fire proofing of all LPG vessels, their supports and connected/ nearby pipelines shall conform
to the requirements stipulated in OISD-STD-144.
b) Fireproofing shall be provided on the aboveground portion of the vessel’s supporting
structures. The fireproofing shall cover all support members required to support static load of
the full vessel. Fireproofing shall not encase the points at which the supports are welded to the
vessel.
Horizontal pressurised storage tanks should preferably be installed on reinforced concrete saddles.
Fireproofing shall be given for exposed steel tank supports that are more than 18 inches (0.46 m)
high, measured at the lowest point of the tank shell.
Supports of flare lines shall be fireproofed if they are within a fire-exposed envelope or if they are
with in 20-30 ft distance from the open ditches/drainage channels, likely to receive large accidental
spills of hydrocarbons.
b) The fire protection should not fail at the end of this specified period, but should continue to offer a
reasonable measure of protection beyond this period.
c) It should have system integrity so that the protection remains in place during a fire, and can
withstand both the thermal stresses and impingement of fire water from hoses/monitors. Test
checks as necessary should be carried out.
d) The fire protection must be non-corrosive to the substrate and be compatible to environmental
conditions. It must not in itself become a hazard in a fire condition whether by spalling,
spreading flame, or producing toxic fumes.
“OISD hereby expressly disclaims any liability or responsibility for loss or damage resulting
from the use of OISD Standards/Guidelines.”
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e) Selection of the fire proofing system must take into account the weight limitations imposed on the
strength of steel supports to be fireproofed especially for existing installations.
f) The materials should have adequate adhesion, strength and durability.
g) The fire proofing system should be adequate for the desired fire rating.
h) The fire proofing material/coating should be resistant to weather effects such as chalking and
erosion. Top coat, wherever provided, must be resistant to solar ultra violet radiation.
6.2 Fire rating criteria for material selection
The following factors should be considered in selecting the fire rating of the material to be applied:
This concrete is made of light weight aggregates such as vermiculite, mica, perlite and cements. Dry
densities range from 640 to 960 kg/cum. Lightweight materials are normally sprayed on but they may
be troweled or formed in place using light reinforcing mesh.
“OISD hereby expressly disclaims any liability or responsibility for loss or damage resulting
from the use of OISD Standards/Guidelines.”
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Insulating concrete, fire proofing cements and plasters made with lightweight or special aggregates,
may be used when weight becomes a limiting factor in the design.
Finished lightweight concrete normally require top coat for weather protection when used in extreme
climates.
Irregular shapes such as flanges, valves, pipes, cable trays, etc., present difficulties in application
techniques and create conflict with the access requirements for routine maintenance. The problem is
suitably addressed with the availability of other than concrete fireproofing systems including
preformed and/or sculptured sections, designed boxes, etc. Applicability of these systems shall
conform to the necessary requirements mentioned in clause no 7.2.2 of this document.
6.3.5 Asbestos
Dense cement concrete shall be of grade M20 conforming to IS:456 or equivalent. Solid
encasement of the structural member is the usual method of application. (Refer to Annexure V)
In case of application of cement concrete in the operating units, only metallic shuttering shall be
used.
Other than concrete fireproofing systems should meet the following requirements:
b.) System provider should furnish test results carried out by independent laboratories
demonstrating that the system is adequate for the proposed application and its thickness shall
have the required resistance against hydrocarbon fires;
c.) It should be reliable in service and should provide desired life-span with reasonable
maintenance, taking into account all possible variations in ambient temperature and humidity;
d.) When exposed to damp conditions, the system should not initiate or sustain any long-term
pernicious effects, such as corrosion of the painted steel work.
e.) Installation of the system shall be carried out by specialists, strictly as per the approved
procedures of the manufacturer.
“OISD hereby expressly disclaims any liability or responsibility for loss or damage resulting
from the use of OISD Standards/Guidelines.”
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Fireproofing shall not be carried out when the ambient air temperature and/or the temperature of the
surface to be fireproofed is 10-Deg C or below.
Provision should be made for adequate ventilation during and after application, until the materials
are dry. However, in extremely dry and hot conditions, appropriate measures should be taken to
keep vermiculite-containing systems moist until set.
The fireproofing should be resistant to frost damage after its proper setting, wherever necessary.
Approved welding procedure by a competent authority should be followed if the fixing of such
systems to surfaces necessitates the welding of certain fixtures to the surfaces.
The application shall be performed by qualified applicator having training, equipment and
experience. Supervisory or lead personnel involved with the application shall be or have been
trained by the manufacturer of fire proof coating material and its application. Applicator shall submit
written verification of such training in case of proprietary products.
“OISD hereby expressly disclaims any liability or responsibility for loss or damage resulting
from the use of OISD Standards/Guidelines.”
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E) Water shedding
Where water-shedding cowls are not provided, top surfaces and all terminations of fire proof coating
against steel must be sloped and floated to shed water.
A `U' shape shall be cut at the concrete steel junction to receive mastic sealant.
F) Top Coating - Weather Barrier
After the concrete coating has been allowed to cure and dry for at least five days, suitable top coat
as recommended by manufacturer may be applied, if required.
G) Sealing of concrete Coating/Steel junctions
Suitable flexible sealant e.g. Polysulphide based or Silicone rubber based should be applied in the
groove.
“OISD hereby expressly disclaims any liability or responsibility for loss or damage resulting
from the use of OISD Standards/Guidelines.”
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All sealants must be suitable for use with a concrete mixture and be weather resistant and remain
flexible.
8.8.3 Mastics
A) Mesh retaining pins
Pin Installation wherever required, shall be done in accordance with the procedure outlined in the
Manufacturer's Application Manual. Embedded mesh reinforcement shall be used based on
manufacturers’ recommendation.
B) Substrate preparation
Substrate preparation shall be done in accordance with product requirements. The blast
finish/profile shall be accepted prior to priming.
C) Priming procedure
Priming of substrate shall be done in accordance with paint manufacturer’s application guideline.
The primers approved by material manufacturers only shall be used.
D) Mesh reinforcement
Meshing of substrate shall be done in accordance with the procedures outlined by mastic material
manufacturer’s application manual.
E) Masking
Any surfaces or equipment in the spraying areas which do not receive mastic must be masked off,
using polyethylene or equivalent. Regardless of the structural configuration being worked on,
overspray is always a concern.
F) Intumescent/Subliming coating
Solvent based or Solventless application of Intumescent / Subliming Materials shall be done in
accordance with the procedure outlined by the Intumescent/ Subliming Materials Manufacturers
Application Manual upto the required thickness.
G) Surface finish and inspection
Surface finish is a visual standard for sprayed Intumescent/Subliming Material, which includes
various structural configurations. Visual inspection should be performed to ensure that there is no
exposed mesh, debonding at terminations or bubbles below the finish surface layer.
Physical inspection would consist of drilling holes in the Intumescent/ Subliming Material to
determine actual thickness, tapping with a hammer to detect possible hollow areas or delamination
between sprayed layers of coating not visible.
Substrate surfaces must be cleaned so that they are free from oil, grease, liquid contaminants, rust,
scale and dust. If a primer is required, it must be compatible with the fire proofing material.
9.1.4 Application
It is to be ensured that the materials must be applied in accordance with the manufacturer’s
recommendations for dry thickness and use of reinforcing materials. Thickness of material must be
ensured as some of the mastic coating shrinks as much as 30 per cent when cured.
9.1.5 Curing
Some materials require a controlled curing period to develop full strength and prevent serious
cracking in the future. Hence, proper curing is to be ensured.
9.1.6 Random core sample check
Random core samples should be taken after application to verify coat thickness, proper bonding,
and voids. Defects, if any, should be rectified properly.
9.1.7 Supervision
Fire proofing shall be supervised by competent personnel having appropriate knowledge and
experience backed with test results. These persons shall inspect the process at its various stages
and maintain an inspection check list for stage wise approvals of the same. Following minimum
stages shall be included in the inspection check list
i) The condition of the steel surface to be fire proofed.
ii) The quality and placing of the reinforcement mesh.
iii) The quality and application of fire proofing material.
iv) The joints between fire proofing and the steel work which are exposed to weather.
v) Weatherproofing.
b) Selectively remove small sections of fireproofing to examine conditions at the face of the substrate
and the surface of reinforcing wire.
c) Visually check for the loss of fireproofing materials as a result of mechanical abuse.
d) When the fireproofing material is applied, coat and set aside several pieces of structural steel for
periodic fire testing over the expected life of the coating.
In the event of a fire, the affected area of coating should be thoroughly examined; including
substrate if required and necessary repairs should be carried out.
10.3 Maintenance
Maintenance of fire proof coatings should be done in as under:
a) When cracks are wider than hairline, the opening should be cleaned out and filled with new
material according to the manufacturer’s instructions.
b) If top coat is required to prevent moisture from penetrating, it must be renewed at intervals
recommended by the manufacturer.
c) Loss of bonding to the substrate may be noticed when the surface bulges or if an abnormal
sound is given off when the surface is tapped with a light hammer. In areas that have evidence
of bond failure, fireproofing should be removed, and the substrate should be thoroughly cleaned
and properly primed before new material is applied.
d) Whenever rust stains are observed on the external surface of fire proof coating, the integrity of
coating as well as the condition of substrate should be established by chipping the affected
area.
11.0 REFERENCES
ii) UL-Subject 1709 : Structural steel Protected for Resistance to Rapid Temperature rise fires
iii) ASTM E119 : Method for fire test of building construction and Material
iv) ASTM –E1529 : Standard test methods for determining effects of large Hydrocarbon pool fires
on Structural members and assemblies.
vii) API-2510A : Fire-Protection consideration for the design and operation of LPG storage
facilities
viii) OISD-STD-144 Vol. IV : Safety and Fire protection in LPG Bottling Plant operations
“OISD hereby expressly disclaims any liability or responsibility for loss or damage resulting
from the use of OISD Standards/Guidelines.”
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ANNEXURE- I
In a hydrocarbon industry the leaks from various potential sources of leakage (PSL) e.g. small bore
connections on piping and equipment, flange joints, pump mechanical seals, expansion joints etc
under different ambient conditions and the type of product handled; can form a liquid pool or be
dispersed as either an aerosol liquid cloud or as a vapour cloud. Ignition of these leaked products
shall either result in a pool fire or a torch fire. These fires continue to sustain till the source feeding
these leaks is completely stopped.
It is observed that liquid pools are normally formed by all hydrocarbon products containing Pentane
and also butanes/butenes at sub zero ambient temperatures. Further it is also seen that
refrigerated/cryogenic liquefied gases may form liquid pools in case of their accidental release while
they are handled at or near their atmospheric boiling points. Particularly this may happen during a
prolonged release of these gases, when the vapourization rate caused by heat pick-up from the
surroundings does not match the rate of release. Pool fires possibilities shall be taken into account
for above categories.
As the pressurized liquefied gases disperse in the form of an aerosol liquid jet or as a vapour jet
upon their accidental release, they shall not result in pool fires. Similarly vapour release shall also
disperse as a jet. Hence, ignition of an aerosol liquid jet or a vapour jet shall lead to a torch fire
which may cause impinging flames with high radiation intensities The length and width of jet flames
is dependent on factors like size of the hole, wind speed and direction and the pressure at the
upstream of the leakage point.
Maximum efforts should be made to protect the supporting steel structures from torch fires by
proper location selection and orientation of the supporting structure with regard to PSL and/or by
providing fire shields near the PSLs or the surfaces of the structures to avoid direct impingement. If
the supporting structures protection against torch fires is not possible or practicable then fire
proofing of these structures should be done as per the relevant fire exposed envelope.
For the most part, liquid and gaseous hydrocarbon fires are characterized by highly luminous flames
resulting from hot carbon particles (soot).Because of limited mixing with oxygen, combustion gases
are fuel-rich and produce nearly continuous radiation in the infrared region making the hot gas and
soot particles behave as a grey body radiator. Petrochemical fire temperatures reach as high as
130deg C (240Deg. F) but average 100deg C (185deg F) because of various factors including
radiational cooling of the fire ball, winds and geometry. Free burning fires normally do not achieve
the theoretical combustion temperatures for the fuels involved. During fires with high pressure fuel
sources, convection plays a larger role and can even be the primary mode of heat transfer. Jet fires
are characterized by high convective inputs.
“OISD hereby expressly disclaims any liability or responsibility for loss or damage resulting
from the use of OISD Standards/Guidelines.”
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Annexure II (Page1 of 2)
UL 1709 Rapid Rise Fire Tests of Protection Materials for Structural Steel and ASTM E1529
Standard Test Methods for Determining Effects of Large Hydrocarbon Pool Fires on Structural
Members and Assemblies were first issued in the early 90s. Both tests involve a test furnace which
develops an average temperature of 2000F (1093C) within the first 5 minutes of the test. The
principal difference is that UL 1709 involves a total heat flux of 65,000 BTU/ft2-hr (205 kW/m2),
whereas the ASTM E1529 heat flux is 50,000 BTU/ft2-hr (158 kW/m2). Temperature is an important
parameter but heat flux is considered as a better measure of the amount of heat stress being placed
on a material (how fast heat works on a material). Although the temperature is the same, the higher
heat flux of UL 1709 makes it a more severe test. A comparison of standardized fireproofing test
procedures is placed in tabular form as below
.
Heat flux in BTU/ft2-hr
After
Temperature after
* Heat flux is neither specified nor measured in ASTM E 119. Data listed above are from a
Major Test Methods E 11furnace as reported in the Appendix of ASTM E 1529-93, section XI. 2.2.
Annexure-II (Page 2 of 2)
There are a number of fire test laboratories in North America and Europe (For partial directory refer
Annexure III). These laboratories conduct fire tests according to defined standards and depending
upon performance, a rating is determined for the particular type of test run. A rating is given in time
units with temperature limits imposed on the protected part of the test assembly. Annexure - IV list
some of the important ratings used in the Hydrocarbon processing industries for structural and
personnel protection of stationary materials.
The oldest and most widely used independent testing organization is Underwriters Laboratories, Inc.
(ULI) in USA.ULI provides fire test and manufacturing follow-up services for many products on a
non-profit basis. ULI was the first testing organization to standardize the high rise fire test as UL
1709 and offer it as one of their services. Other testing laboratories now conduct similar tests.
In the case of the UL 1709 test, the furnace temperature is brought up to 1093deg C (2000deg F)
within 5 minutes and held within a tolerance of this level for the duration of the test. Tests are
usually run on a light column designated as a W10X49, but they can be run on lighter or heavier
sections. Less material is required to protect heavier members, so the user should be careful to
determine which member was tested. Steel temperatures are measured beneath the protective
material at 4 levels with 3 thermocouples per level. Failure criteria for columns are:
When the average of all thermocouples at any level reaches 538 deg C (1000deg F) or;
Environmentally exposed materials are tested against control material to determine the effect on
fireproofing performance. A loss in performance of 25% or more in any of these tests prevents a
material from receiving an external use rating. Even though these evaluations are helpful in
determining material suitability for industrial use, the aging tests are accelerated and small losses in
performance may turn into significantly larger ones over long periods of time. However, this test
program is an important tool in rating and monitoring potential fire protection materials for outdoor
use.
After successful completion of the test, a listing or rating is offered, which in the case of ULI, is
printed in an annual Fire Resistance Index under X or XR classifications for columns for the hourly
period tested. Listings in the X classification are for designs tested to the ASTM E-119 cellulosic fire
environment whereas those in the XR classification have been tested to the UL 1709 high intensity
fire environment. XR ratings (listings) include mandatory additional testing for environmental aging
such as freeze thaw cycling, salt fog, high humidity, and SO2 / CO2 exposures. For X
classifications, environmental testing is optional.
While, UL -1709 is the minimum requirement for a fire proofing material, materials being used for
pressurized storage vessels must have preferably undergone independent tests successfully on
such type of vessels.
“OISD hereby expressly disclaims any liability or responsibility for loss or damage resulting
from the use of OISD Standards/Guidelines.”
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ANNEXURE - III
U. S. Department of USA
Transportation (DOT)
“OISD hereby expressly disclaims any liability or responsibility for loss or damage resulting
from the use of OISD Standards/Guidelines.”
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ANNEXURE - IV
UL 1709 W 10 X49 1093 deg C (2000 Protected steel High intensity or high
Column 9” deg F) must not exceed rise fire curve. Gas
high 538 deg C (1000 fired furnace
deg F)
BAM 90 min. for Horizontal 600-900 deg C 250 deg C (482 Pressurised Propane
pressurised 485 M3 Tank (1112 - 1652 deg deg F) maximum jets in a series
LPG tanks with 6.4 mm F) wall temperature surrounding the tank.
(Germany) wall thickness measured in the
and 50% ullage space not
filled with adjacent to the
Propane liquid. maximum
internal pressure
of approximately
20 bars.
GESIP (France) Loaded 1000 deg C Protected steel Simulated
vessel + + must not exceed Pool fine furnace test
Flame 1100 deg C 427 deg C (800 H/C
impingement deg F)
and + Hose
Stream
H.S.E. Loaded Pool fire (H/S) 427 deg C Pool fire
(U.K.) vessel 1100 deg
C
“OISD hereby expressly disclaims any liability or responsibility for loss or damage resulting
from the use of OISD Standards/Guidelines.”
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ANNEXURE V
TYPICAL DETAILS - CONCRETE FIREPROOFING - SOLID ENCASEMENT
“OISD hereby expressly disclaims any liability or responsibility for loss or damage resulting
from the use of OISD Standards/Guidelines.”
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ANNEXURE VI
TYPICAL DETAILS - COVER PLATES FOR WEATHER PROTECTION
“OISD hereby expressly disclaims any liability or responsibility for loss or damage resulting
from the use of OISD Standards/Guidelines.”
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“OISD hereby expressly disclaims any liability or responsibility for loss or damage resulting
from the use of OISD Standards/Guidelines.”
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PIPES
“OISD hereby expressly disclaims any liability or responsibility for loss or damage resulting
from the use of OISD Standards/Guidelines.”
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Fire Exposed
Envelope
Hydrocarbon Pumps
Figure No. 5.4 : Pipe racks with large Fire-Potential Pumps installed below
“OISD hereby expressly disclaims any liability or responsibility for loss or damage resulting
from the use of OISD Standards/Guidelines.”
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Stinger beams
supporting vertical
No fireproofing on stinger loads to be
beams which do not fireproofed.
support vertical loads
Fireproofing
Figure 5.5 - Pipe rack supporting air fin-fan coolers in a fire exposed envelope.
“OISD hereby expressly disclaims any liability or responsibility for loss or damage resulting
from the use of OISD Standards/Guidelines.”
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Fireproofing
Fire potential
equipment
Floor on which
liquids can
accumulate.
Fire exposed
envelope
Figure 5.6 : Structures supporting fire potential and non fire potential equipment in a fire exposed envelope
“OISD hereby expressly disclaims any liability or responsibility for loss or damage resulting
from the use of OISD Standards/Guidelines.”