FP 50-4
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INTERNATIONAL MARITIME ORGANIZATION
IMO
E
SUB-COMMITTEE ON FIRE PROTECTION
50th session
Agenda item 4
FP 50/4
12 October 2005
Original: ENGLISH
PERFORMANCE TESTING AND APPROVAL STANDARDS
FOR FIRE SAFETY SYSTEMS
Report of the correspondence group
Submitted by the United States
SUMMARY
Executive summary: This document reports the work of the Correspondence Group on
Performance Testing and Approval Standards for Fire Safety Systems
established at FP 49
Action to be taken: Paragraph 21
Related documents: FP 46/16; FP 47/WP.9; FP 47/16; FP 48/19; FP 49/17; FP 49/WP.2;
FP 49/4; FP 49/4/2; FP 49/4/4 and FP 49 INF.4
INTRODUCTION
1 The Sub-Committee, at its forty-ninth session, established a correspondence group, under
the coordination of the United States, to progress work intersessionally on performance testing
and approval standards for fire safety systems.
2 The following Member Governments participated in the work of the group:
ARGENTINA NETHERLANDSCANADA NORWAY
CHINA POLANDDENMARK REPUBLIC OF KOREAFINLAND ROMANIAGERMANY SWEDENITALY UNITED KINGDOMJAPAN UNITED STATES
and the following non-governmental organizations:
INTERNATIONAL ORGANIZATION FOR STANDARDIZATION (ISO)
INTERNATIONAL COUNCIL OF CRUISE LINES (ICCL)
3 The group was given the following terms of reference (FP 49/17, paragraph 4.26):
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.1 further consider matters related to water-mist fire-extinguishing systems for
accommodation, service and control spaces, taking into account document
FP 49/4;
.2 consider matters related to fixed high-expansion foam systems using inside air,
taking into account documents FP 49/4/2, FP 49/4/4 and FP 49/INF.4 and makerecommendations as appropriate;
.3 prepare relevant amendments for the following short-term priority category of
topics relating to the following machinery space and cargo pump-room
fire-extinguishing arrangements:
.1 fixed pressure water-spraying systems;
.2 fixed low-expansion foam fire-extinguishing systems; and
.3 portable foam applicator units;
.4 prepare relevant amendments for water-mist fire-extinguishing systems and fixed
pressure water-spraying fire-extinguishing systems for vehicle space, ro-ro space
and special category space extinguishing systems;
.5 consider further matters related to the revision of MSC/Circ.848;
.6 continue consideration of the use of total flooding carbon dioxide
fire-extinguishing systems in normally occupied areas in response to actions taken
by various governmental agencies;
.7 consider matters related to the revision of the proposed functional objectives and
requirements for class III engine-room water-mist fire protection protocol, as set
out in annex 2 to document FP 49/4, and make recommendations as appropriate;
.8 consider matters related to the development of the scientific methods on scaling of
the test volume to a larger shipboard protected volume and make
recommendations as appropriate;
.9 further consider the draft guidelines for inspection and maintenance of fixed
carbon dioxide systems, as set out in annex 3 to document FP 49/WP.2; and
.10 submit a report to FP 50.
MAINTENANCE AND INSPECTIONS OF FIXEDCO2 FIRE-EXTINGUISHING SYSTEMS
4 The group further considered the proposed draft carbon dioxide system inspection
guidance contained in document FP 49/WP.2, annex 3, taking into account comments made by
ICCL and ICS at FP 49 (FP 49/17, paragraphs 4.17 and 4.18). The draft guidelines were
subsequently revised to better define which inspection activities should be conducted by the
ship’s crew and which should be conducted by trained specialists. The majority of the group
previously held the view that carbon dioxide systems on all ships should be inspected by trainedspecialists at least biennially. However, since FP 49 additional members of the group now
support an inspection schedule coincident with the periodic and renewal survey procedures
established by resolution A.948(23). The Sub-Committee is invited to provide further direction
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in regard to recommended inspection intervals for fixed carbon dioxide systems. The revised
draft guidelines are set out in annex 1.
APPROVAL OF EQUIVALENT FIXED-GAS FIRE-EXTINGUISHING SYSTEMS FOR MACHINERY
SPACES AND CARGO PUMP ROOMS (MSC/CIRC.848)
5 As requested by the Sub-Committee (FP 48/19, paragraph 4.19), the group further
considered the proposed safe personnel exposure limits for halocarbon and inert gas
fire-extinguishing agents in paragraph 6 of the annex to MSC/Circ.848. Several members of the
group proposed using the personnel safety standards adopted by the National Fire Protection
Association’s (NFPA) 2001 Technical Committee in the 2004 edition of that standard. Other
members considered that the existing guidelines taken from the 2001 edition of the
NFPA standard should be retained. A draft of proposed paragraph 6 that incorporates
the 2004 guidelines has been developed to more clearly state the allowable exposure limits;
however, due to time constraints, unanimous agreement on the final wording was not reached and
should be further considered at FP 50.
6 The group also discussed the possible storage of halocarbon and inert gas agent
containers within the protected space, noting that IACS had recently approved a unified
interpretation to that effect (FP 48/19, paragraph 4.21). Paragraph 11 of the annex to
MSC/Circ.848 permits this practice if the provisions of regulation II-2/5.3.3 are met. However,
this regulation was deleted by the 2000 SOLAS amendments and is no longer a valid reference.
The group agreed that this practice should continue to be permitted. It was also noted that
MSC/Circ.848 contains references to other 1997 SOLAS amendments regulations. To resolve
these inconsistencies, MSC/Circ.848 was revised with updated references to the appropriate
SOLAS 2000 regulations, and the text of the deleted regulation II-2/5.3.3 was placed directly into
paragraph 11 of the circular.
7 The draft revised MSC/Circ.848 is set out in annex 2 and should be considered for
finalization by the ad hoc working group to be established at FP 50.
APPROVAL OF EQUIVALENT SPRINKLER SYSTEMS(RESOLUTION A.800(19))
8 The Sub-Committee is invited to recall that draft amendments to resolution A.800(19)
had been proposed in annex 6 of document FP 49/4. The working group established at FP 49,
having had a preliminary discussion of the proposed amendments, was unable, due to the time
available, to make substantial progress and agreed that further consideration of this matter should
be given by the intersessional correspondence group. The group has since agreed on the majorityof the revised draft guidelines as set out in annex 3, with a view to finalization at FP 50.
9 The proposed amendments changed a number of the technical requirements in the test
procedure and have added several alternatives in the system design criteria to allow more
flexibility. For example, the standard now permits the use of a battery consisting of water and
nitrogen cylinders in lieu of a pressure tank connected to a pressurized air source as an
emergency back-up, and also accepts the use of diesel engine driven water supply pumps in
addition to electric motor driven pumps.
10 The test procedure has also been amended to more realistically simulate operation of
automatic discharge nozzles during the approval tests. Actual ship installations are normally heldat a low standby pressure until a discharge nozzle operates, at which point the main supply
pumps are started and the system is brought up to full pressure. The configuration and total
length of the discharge piping between the pumps and the nozzles can influence the time
necessary for the arrival of full system pressure at the nozzles. The existing test procedure
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permits the laboratory test nozzles to be arranged to immediately operate at full discharge
pressure. The group was concerned that the use of this arrangement does not replicate actual
installations and could lessen the anticipated factor of safety. To account for this time delay in
system operation, the test procedure has been amended to require the nozzles to either be charged
at the minimum operating pressure throughout the tests, or be initially charged at standby
pressure and then brought up to full discharge pressure 15 seconds after operation of the firstnozzle. Correspondingly, the system design criteria have been amended to require piping
configurations to be limited such that full system pressure will be available at the most remote
nozzle within 60 seconds.
11 Another significant amendment is a revision of the text of paragraph 3.22 of the annex,
regarding the sizing of the water supply pumps, which the group deemed to be unclear. The
paragraph previously indicated that the supply pumps should be sized so as to be capable of
maintaining the required flow to the “hydraulically most demanding area of not less than
280 m2”. On many ships there are storage areas of less than 280 m2 that require higher flow rates
than public areas that exceed 280 m2, due to the higher nozzle flow rate requirements for the
protection of storage areas. The paragraph has been reworded to clearly indicate that the pumpsshould be sized to supply the hydraulically most demanding area on the ship, without
consideration of a minimum deck area. However, the group needs to further consider the
requirements for the fire integrity of the bulkheads and decks that separate the hydraulically most
demanding area from adjacent areas. The final issue remaining is for the group to decide if the
calculation of manually activated atrium systems should be included in the determination of the
water supply requirements. These issues should be further considered at FP 50.
FIXED HIGH EXPANSION FOAM FIRE-EXTINGUISHING SYSTEMS
12 The group further considered the proposals made in FP 49/4/2, FP 49/4/4 and
FP 49/INF.4, as well as comments made by Japan and Republic of Korea at FP 49. A preliminary draft testing and approval standard has been prepared and is included as set out in
annex 4. Due to the time available, the group was unable to finalize this document, and
recommends that the ad hoc working group further consider its technical content at FP 50.
FIXED PRESSURE WATER -SPRAYING FIRE-EXTINGUISHING SYSTEMS
13 SOLAS chapter II-2 refers to the use of fixed pressure water-spraying fire-extinguishing
systems for the protection of machinery spaces of category A and cargo pump-rooms. There is
no performance testing criteria in chapter 7 of the FSS Code for such systems. The
correspondence group considered whether to develop a new test procedure for such systems or toinclude them in an existing test procedure. A majority of the group deemed that the
characteristics of fixed pressure water-spraying nozzles were similar enough to those of water
mist nozzles and could therefore be subjected to the same performance criteria. Several
members, however, felt that water spray nozzles should not be subject to these testing criteria and
that requirements for increased flow rates and provisions for using foam additives would suffice.
A proposed draft amendment to chapter 7 of the FSS Code has been prepared that includes both
of these options. The revised chapter 7 is provided at annex 5 and should be further discussed at
FP 50 to resolve these divergent views.
R EVISION OF CHAPTER 6 OF THE FSS CODE
14 The group was assigned a short term priority item to consider possible improvements in
the criteria for fixed low-expansion foam systems. Such systems were previously considered
under the provisions of regulation II-2/8 as a non-mandatory form of protection to supplement
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required machinery space fire-extinguishing systems. The 2000 SOLAS amendments do not
require or reference low expansion foam systems. In view of the limited application of these
systems, the group considers that the information presently in chapter 6 of the FSS Code is
adequate and that no further actions should be taken in this regard.
R EVISION OF REGULATION 3.2 OF CHAPTER 4 OF THE FSS CODE
15 The group considered possible improvements in the criteria for portable foam applicators,
and agreed that it was not necessary to develop a separate testing standard for these portable
devices. Instead the prescriptive requirements listed in chapter 4 of the FSS Code were amended
to include fundamental engineering design standards. The text of revised chapter 4 is set out in
annex 6.
APPROVAL OF FIXED AEROSOL FIRE-EXTINGUISHING SYSTEMS (MSC/CIRC.1007)
16 The group revised MSC/Circ.1007 to include the correct references to the appropriate
paragraphs of SOLAS 1974, as amended by the 2000 amendments. The personnel exposureguidelines were also harmonized with the proposed new text decided for MSC/Circ.848.
Changes were also proposed to the test protocol to link the agent discharge to a fixed discharge
time rather than relying on the end of agent discharge. Experience with the test procedure has
shown that it is difficult to accurately determine when the end of agent discharge occurs due to
the obscured visibility caused by aerosol agents. The draft revised MSC/Circ.1007 is set out in
annex 7.
FIXED PRESSURE WATER -SPRAYING FIRE-EXTINGUISHING SYSTEMS AND WATER MIST
FIRE-EXTINGUISHING SYSTEMS FOR VEHICLE DECKS, RO-RO SPACES AND SPECIAL CATEGORY
SPACES
17 Preliminary discussion of possible revisions to MSC/Circ.914 and resolution A.123(V)
were held during the intersessional period. The group agreed that MSC/Circ.914 should be
replaced with a revised fire test procedure. The primary concerns with the existing test procedure
center on the lack of test data to substantiate the required fuel package and associated acceptance
criteria. Work was begun on a new test procedure by first attempting to define the design fire
scenarios that should be used to replicate the fire hazard posed by typical cargoes stowed on
vehicle decks. Because of time constraints, the group did not complete the proposed new test
procedure, and recommends that further consideration of the issue should be given by the ad hoc
working group at FP 50. The group also considered whether resolution A.123(V) should be
replaced by a new test procedure or whether the revised MSC/Circ.914 could be developed toaccommodate both water mist fire-extinguishing systems and fixed pressure water-spraying
fire-extinguishing systems. This matter should be further discussed at FP 50.
APPROVAL OF FIXED WATER -BASED LOCAL APPLICATION FIRE-FIGHTING SYSTEMS
(MSC/CIRC.913)
18 Minor revisions are proposed to MSC/Circ.913 to include interpretations from
MSC/Circ.1120 with respect to the definition of “protected areas”, and to clarify the meaning of
detection and suppression sections. The group also noted that a decision taken at FP 49
regarding the fire detection system criteria in paragraph 3.16 (FP 49/WP.2, annex 2) conflicted
with a decision previously taken at FP 48 (FP 48/WP.4, annex 2). This issue should be further discussed at FP 50 to resolve the conflict. The proposed revisions are set out in annex 8.
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FUNCTIONAL OBJECTIVES AND REQUIREMENTS FOR CLASS III ENGINE-ROOM WATER -MIST FIRE
PROTECTION PROTOCOL
19 Preliminary research results related to the proposed functional objectives and
requirements for class III engine-room water-mist fire protection protocol, as set out in annex 2
to document FP 49/4 were presented at FP 49. The data concerned measurement of theefficiency of water spray or water mist systems in large spaces, i.e. spaces where enclosure
effects are not the pre-dominant extinguishment effect. Additional results will be presented
at FP 50 together with plans for the final phase of the research project. It is anticipated that a
suggested test protocol will be available for FP 51, along with preliminary suggestions on scaling
of the test volume to a larger shipboard protected volume.
USE OF TOTAL FLOODING CARBON DIOXIDE FIRE-EXTINGUISHING SYSTEMS IN NORMALLY
OCCUPIED AREAS IN RESPONSE TO ACTIONS TAKEN BY VARIOUS GOVERNMENTAL AGENCIES
20 Since FP 49, several agencies have initiated actions that could affect the use of total
flooding carbon dioxide fire-extinguishing systems for the protection of occupied areas on ships.The U.S. Environmental Protection Agency (EPA) has begun a rulemaking to prohibit the use of
carbon dioxide total flooding fire-extinguishing systems in normally occupied spaces. The
International Organization for Standardization (ISO) has formed a working group to rewrite
ISO Standard 6183, with special emphasis on the advisability of the use of total flooding systems
in normally occupied spaces. The NFPA Technical Committee on Gaseous Fire-Extinguishing
Systems has drafted a committee proposal to prohibit the use of new carbon dioxide total
flooding systems in normally occupied spaces with very limited exceptions. Because of these
ongoing activities, continued consideration of this issue by the Sub-Committee is recommended.
SUMMARY
21 A summary of the working group deliberations thus far is given below:
SHORT-TERM PRIORITY CATEGORIES
Topic Applicable Documents Status
Machinery space and cargo
pump-room extinguishing
systems
Water mist fire-extinguishing
systems (MSC/Circ.668/728)
1. FP 48/WP.4 Rev 1,
annex 1
2. FP 49/WP.2, annex 1
Complete - Issued as MSC/Circ.1165
Fixed local applicationfire-extinguishing systems for
machinery spaces of category A
(MSC/Circ.913)
1. FP 48/WP.4 Rev 1,annex 2
2. FP 49/WP.2
3. FP 50/4, annex 4
Minor additional amendments areincluded in annex 8 to be finalized at
FP 50.
Fixed pressure water-spraying
fire-extinguishing systems
Annex 5 Draft amendments to chapter 7 of the
FSS Code are provided in annex 5 for
finalization at FP 50.
Fixed gas fire-extinguishing
systems (MSC/Circ.848)
1. FP 48/WP.4 Rev 1,
annex 3
2. FP 49/WP.2,
paragraph 19
3. FP 50/4, annexes 1
and 2
Annex 1 contains the revised draft
guidelines for CO2 system inspections
and maintenance. Annex 2 contains
revised MSC/Circ.848. The ad hoc
working group should finalize at this
session.
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SHORT-TERM PRIORITY CATEGORIES (Cont’d)
Topic Applicable Documents Status
Aerosol fixed fire-extinguishing
systems
FP 50/4, annex 7 Minor editorial changes are
recommended as set out in annex 7 to
harmonize with the 2000 SOLAS
amendments, and to facilitate the
conduct of the fire tests.
Fixed high-expansion foam
fire-extinguishing systems using
inside air
FP 50/4, annex 4 A draft performance standard has been
prepared. Further agreement on key
technical issues is needed with
expected finalization at FP 51.
Fixed low-expansion foam
fire-extinguishing systems
Complete - Because of the limited
application, it is proposed that no
further action is necessary.
Portable foam applicator units FP 50/4, annex 6 Draft amendments to the FSS Code
chapter 4 are proposed in annex 6.
Fire-extinguishing arrangementsin control stations,
accommodation and service
spaces
Water mist fire-extinguishing
systems in accommodation and
service spaces
(resolution A.800(19))
FP 50/4, annex 3 Draft complete – The ad hoc working
group should finalize at this session.
Vehicle space, ro-ro space and
special category space
extinguishing systems
Water mist fire-extinguishing
systems for vehicle space, ro-ro
space and special category space
extinguishing systems
Work has been started on a new test
procedure for water mist systems.
Fixed pressure water-spraying
fire-extinguishing systems
The new test procedure for water mist
may be applied to water spray systems.
At this time, the Sub-Committee is invited to consider the above actions, in principle, bearing in
mind that when work is completed, the revised draft protocols will be submitted for approval as a
group, and will in due course be proposed as a single MSC circular for adoption (FP 47/16,
paragraphs 8.18-8.21).
Action requested of the Sub-Committee
22 The Sub-Committee is invited to approve the report in general and, in particular, to:
.1 agree, in principle, with the proposed amendments set out in annexes 1 through 8;
.2 note the divergent views of the group in regard to the inspection intervals for
maintenance and inspections of fixed carbon dioxide systems set out in annex 1
and provide further instruction as appropriate in this regard (paragraph 4 and
annex 1);
.3 agree that the ad hoc working group should further consider the revised guidelines
for the approval of equivalent fixed-gas fire-extinguishing systems, as referred to
in SOLAS 74, for machinery spaces and cargo pump rooms (MSC/Circ.848)
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attached at annex 2 with a view to finalization at this session (paragraphs 5 to 7
and annex 2);
.4 agree that the ad hoc working group should further consider the revised guidelines
for approval of sprinkler systems equivalent to that referred to in SOLAS
regulation II-2/12 (resolution A.800(19)) as set out in annex 3 with a view tofinalization at this session (paragraphs 8 to 11 and annex 3);
.5 agree that the ad hoc working group should further consider the proposed draft
test procedure for high expansion foam systems using inside air as set out in
annex 4 with a view to finalization at FP 51 (paragraph 12 and annex 4);
.6 agree that the ad hoc working group should further consider whether fixed
pressure water-spraying fire-extinguishing systems for the protection of
machinery spaces of category A and cargo pump-rooms should have a separate
performance standard, or should be tested in accordance with MSC/Circ.1165
(paragraph 13);
.7 agree with the decision of the group that the criteria for fixed low expansion foam
systems listed in chapter 6 of the FSS Code are adequate and that no further
actions should be taken in this regard (paragraph 14);
.8 agree that the ad hoc working group should further consider the proposed
revisions to the guidelines for the approval of fixed aerosol fire-extinguishing
systems equivalent to fixed gas fire-extinguishing systems, as referred to in
SOLAS 74, for machinery spaces (MSC/Circ.1007) with a view to finalization at
FP 51 (paragraph 16 and annex 7);
.9 agree that the ad hoc working group should further consider the development of a
test procedure for fixed pressure water-spraying fire-extinguishing systems and
water mist fire-extinguishing systems for vehicle decks, ro-ro spaces and special
category spaces with a view to finalization at FP 51 (paragraph 17);
.10 agree that the ad hoc working group should further consider the proposed
revisions to the guidelines for the approval of fixed water-based local application
fire-fighting systems (MSC/Circ.913) with a view towards finalization at FP 50
(paragraph 18 and annex 8);
.11 note the ongoing research being performed related to the revision of the proposed
functional objectives and requirements for class III engine-room water-mist fire
protection protocol with further results expected at FP 51 (paragraph 19); and
.12 note the actions taken by various governmental agencies concerning the use of
total flooding carbon dioxide fire-extinguishing systems in normally occupied
areas, and agree to continue consideration of this issue (paragraph 20).
***
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ANNEX 1
DRAFT GUIDELINES FOR THE MAINTENANCE AND INSPECTIONS
OF FIXED CARBON DIOXIDE SYSTEMS
1 General
These guidelines provide the minimum recommended level of maintenance and inspections for
fixed carbon dioxide systems on all ships, and are intended to demonstrate that the system is kept
in good working order as specified in SOLAS regulation II-2/14.2.1.2. These guidelines are
intended to supplement the extinguishing system manufacturer’s approved maintenance
instructions. Certain maintenance procedures and inspections may be performed by competent
crewmembers, while others should be performed by persons specially trained in the maintenance
of such systems. The on-board maintenance plan should indicate which parts of the
recommended inspections and maintenance are to be completed by trained personnel.
2 Safety
Whenever carbon dioxide systems are subjected to inspection or maintenance, strict safety
precautions should be followed to prevent the possibility that individuals performing or
witnessing the activities are placed at risk. Prior to performing any work, a safety plan should be
developed to account for all personnel and establish an effective communications system
between the inspection personnel and the on-duty crew. Measures to avoid accidental discharges
such as locking or removing the operating arms from directional valves, or shutting and locking
the system block valve should be taken as the initial procedure for the protection of personnel
performing any maintenance or inspections. All personnel should be notified of the impending
activities before work is begun.
3 Maintenance and inspection plan
Fixed carbon dioxide fire-extinguishing systems should be kept in good working order and
readily available for immediate use. Maintenance and inspections should be carried out in
accordance with the ship’s maintenance plan having due regard to ensuring the reliability of the
system. The on-board maintenance plan should be included in the ship’s safety management
system and should be based on the system manufacturer’s recommendations including:
.1 maintenance and inspection procedures and instructions;
.2 required schedules for periodic maintenance and inspections;
.3 listing of recommended spare parts; and
.4 records of inspections and maintenance, including corrective actions taken to
maintain the system in operable condition.
4 Monthly inspections
4.1 At least every 30 days a general visual inspection should be made of the overall systemcondition for obvious signs of damage, and should include verification that:
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.1 all stop valves are in the closed position;
.2 all releasing controls are in the proper position and readily accessible for
immediate use;
.3 all discharge piping and pneumatic tubing is intact and has not been damaged;
.4 all high pressure cylinders are in place and properly secured; and
.5 the alarm devices are in place and do not appear damaged.
4.2 In addition, on low pressure systems the inspections should verify that:
.1 the pressure gauge is reading in the normal range;
.2 the liquid level indicator is reading within the proper level;
.3 the manually operated storage tank main service valve is secured in the open
position; and
.4 the vapour supply line valve is secured in the open position.
5 Annual inspections
The following minimum level of maintenance and inspections should be carried out in
accordance with the system manufacturer’s instructions and safety precautions:
.1 the boundaries of the protected space should be visually inspected to confirm that
no modifications have been made to the enclosure that have created uncloseable
openings that would render the system ineffective;
.2 all storage containers should be visually inspected for any signs of damage, rust or
loose mounting hardware. Cylinders that are leaking, corroded, dented or bulging
should be hydrostatically retested or replaced;
.3 system piping should be visually inspected to check for damage, loose supportsand corrosion. Nozzles should be inspected to ensure they have not been
obstructed by the storage of spare parts or a new installation of structure or
machinery;
.4 the manifold should be inspected to verify that all flexible discharge hoses and
fittings are properly tightened; and
.5 all entrance doors to the protected space should close properly and should have
warning signs, which indicate that the space is protected by a fixed carbon dioxide
system and that personnel should evacuate immediately if the alarms sound. All
remote releasing controls should be checked for clear operating instructions andindication as to the space served.
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6 Minimum Recommended Maintenance
6.1 At least biennially (intervals of 2 years +/- 3 months) [in passenger ships or at each
intermediate and periodical survey*
in cargo ships], the following maintenance should be carriedout (to assist in carrying out the recommended maintenance, typical service charts are attached at
annex):
.1 all high pressure cylinders and pilot cylinders should be weighed or have their
liquid levels detected by other reliable means to confirm that the available charge
in each is above 90% of the nominal charge. Cylinders containing less than 90%
of the nominal charge should be refilled. The liquid level gauge of low pressure
storage tanks should be checked to verify that the required amount of carbon
dioxide to protect the largest hazard is available;
2. the hydrostatic test date of all storage containers should be checked. High pressure cylinders should be subjected to periodical tests at intervals not
exceeding 10 years. At the 10 year inspection, at least 10% of the total number
provided should be subjected to an internal inspection and hydrostatic test**. If
one or more cylinders fail, a total of 50% of the on-board cylinders should be
tested. If further cylinders fail, all cylinders should be tested. Flexible hoses
should be replaced at the intervals recommended by the manufacturer and not
exceeding every 10 years; and
.3 the discharge piping and nozzles should be tested to verify that they are not
blocked. The test should be performed by isolating the discharge piping from the
system and flowing dry air, nitrogen from test cylinders or suitable means throughthe piping.
6.2 At least biennially (intervals of 2 years +/- 3 months) [in passenger ships or at each
renewal survey* in cargo ships], the following maintenance should be carried out by service
technicians/specialists trained to standards accepted by the Administration:
.1 the system controls should be functionally tested by blanking off or disconnecting
the cylinder bank or storage tank from the manifold and using pressure from test
cylinders to simulate operation of the system. Operation should be simulated
from one or more remote release stations. If the remote release controls areoperated by manual pull cables, they should be checked to verify the cables and
corner pulleys freely move, and do not require an excessive amount of travel to
actuate the system;
.2 all cable components should be cleaned and adjusted as necessary, and the cable
connectors should be properly tightened. If the remote release controls are
operated by pneumatic pressure, the tubing should be checked for leakage, and the
proper charge of the remote releasing station pilot gas cylinders should be
* Refer to “ Revised Survey Guidelines Under the Harmonized System of Survey & Certification (resolution A.948(23))”.
**Refer to “ Periodic inspection and testing of seamless steel gas cylinders (ISO – 6406)”.
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verified. All controls and warning devices should function normally, and the time
delay should prevent the stop valve from opening for the required time period; and
.3 after completion of the work, the system should be returned to service. Allreleasing controls should be verified in the proper position and connected to the
correct control valves. All pressure switch interlocks should be reset and returned
to service. All stop valves should be in the closed position.
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SERVICE CHART
HIGH PRESSURE CO2 SYSTEM
Date: Name of ship/unit: IMO No.: Certificate No.:
Technical Description No. Text Value
1 Manufacturer
2 No. of cylinders
3 Cylinder capacity
4 No. of pilot cylinders
5 Pilot cylinder each of capacity
6 No. of distribution lines7 Oldest cylinder pressure test date
8 Protected space(s)
Description of Inspection/Tests
No
.
Description Carried
out
Not
carried
Not
applic.
Comment
1 Release controls and distribution valves secured
2 Contents in cylinders checked by weighing
3 Contents in cylinders checked by liquid level indicator
4 Contents of pilot cylinders checked5 All cylinder valves visually inspected
6 All cylinder frames and connections checked for
tightness
7 Manifold inspected
8 Manifold tested
9 Main valve and distribution valves inspected
10 Main valve and distribution valves tested
11 Total flooding release system inspected
12 Total flooding release system tested
13 Release stations inspected
14 Warning alarms tested15 Fan stop tested
16 Distribution lines and nozzles inspected
17 Distribution lines and nozzles tested
18 Distribution lines and nozzles blown through
19 Detection system tested
20 Pressure test of servo tubing and discharge lines
21 All doors, hinges and locks inspected
22 All instruction plates on installation inspected
23 System left in operational order. Insp. date tags
attached
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SERVICE CHART
LOW PRESSURE CO2 SYSTEM
Date: Name of ship/unit: IMO No.: Certificate No.:
Technical Description No. Text Value
1 Manufacturer
2 No. of tanks
3 Tanks capacity (tons)
4 No. of pilot cylinders
5 Pilot cylinder each of capacity
6 No. of distribution lines7 Protected space(s)
Description of Inspection/Tests
No
.
Description Carried
out
Not
carried
Not
applic.
Comment
1 Tank main service valve closed and secured
2 Distribution valves verified closed
3 Check correct function of level indicator
4 Contents of CO2 tank checked by tank level indicator
5 Contents of CO2 tank checked by riser tube reading6 Contents of CO2 tank checked by level control valve
7 Contents of pilot cylinders checked
8 Start/stop function of cooling compressors tested
9 All connected electrical alarms and indicators tested
0 Main manifold valve inspected
11 Main manifold valve tested
12 Distribution valves inspected
13 Distribution valves tested
14 Release stations inspected
15 Total flooding release mechanism inspected
16 Total flooding release mechanism tested17 Warning alarms tested
18 Fan stop tested
19 Distribution lines and nozzles inspected
20 Distribution lines and nozzles tested
21 Distribution lines and nozzles blown through
22 All doors, hinges, locks and instruction plates
inspected
23 Detection system tested
24 Tank main service valve reopened and secured open
25 System left in operational order. Insp. date tags
attached
***
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ANNEX 2
PROPOSED AMENDMENTS TO MSC/CIRC.848
REVISED GUIDELINES FOR THE APPROVAL OF EQUIVALENT FIXED GAS
FIRE-EXTINGUISHING SYSTEMS, AS REFERRED TO IN SOLAS 74, FOR MACHINERY SPACES AND CARGO PUMP-ROOMS
General
1 Fixed gas fire-extinguishing systems for use in machinery spaces of category A and cargo
pump-rooms equivalent to fire-extinguishing systems required by SOLAS regulations II-2/10.4
and II-2/10.9 should prove that they have the same reliability which has been identified as
significant for the performance of fixed gas fire-extinguishing systems approved under the
requirements of the FSS Code chapter 5. In addition, the system should be shown by test to have
the capability of extinguishing a variety of fires that can occur in a ship's engine-room.
Principal requirements
2 All requirements of the FSS Code chapter 5, regulation 2.1, except as modified by these
guidelines, should apply.
3 The minimum extinguishing concentration should be determined by a cup burner test
conducted in accordance with ISO Standard 14520-1, 2000, “Gaseous Fire-Extinguishing
Systems –Physical Properties and System Design – Part 1: General Requirements”. The design
concentration should be at least 30% above the minimum extinguishing concentration. These
concentrations should be verified by full-scale testing described in the test procedure, as set out
in the appendix.
4 For systems using halocarbon clean agents, 95% of the design concentration should be
discharged in 10 seconds or less. For inert gas systems, the discharge time should not exceed
120 seconds for 85% of the design concentration.
5 The quantity of extinguishing agent for the protected space should be calculated at the
minimum expected ambient temperature using the design concentration based on the net volume
of the protected space, including the casing.
5.1 The net volume of a protected space is that part of the gross volume of the space which isaccessible to the free extinguishing agent gas.
5.2 When calculating the net volume of a protected space, the net volume should include the
volume of the bilge, the volume of the casing and the volume of free air contained in air receivers
that in the event of a fire is released into the protected space.
5.3 The objects that occupy volume in the protected space should be subtracted from the
gross volume of the space. They include, but are not necessarily limited to:
.1 auxiliary machinery;
.2 boilers;
.3 condensers;
.4 evaporators;
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.5 main engines;
.6 reduction gears;
.7 tanks; and
.8 trunks.
5.4 Subsequent modifications to the protected space that alter the net volume of the space
shall require the quantity of extinguishing agent to be adjusted to meet the requirements of this
paragraph and paragraph 6.
6 [Exposure to extinguishing agents, even at concentrations below an adverse effect level,
should not exceed 5 minutes. Halocarbon agents may be used up to their NOAEL (No Observed
Adverse Effect Level) without additional safety measures. Means should be provided to limit
exposure to no longer than 5 minutes. Unprotected personnel should not enter a space during or
after agent discharge until the protected space has been well ventilated and cleared of residue.
6.1 If a halocarbon agent is to be used above its NOAEL, means should be provided to limit
exposure to no longer than the time specified according to a scientifically accepted PBPK
(physiologically based pharmacokinetic*) model or its equivalent which clearly establishes safe
exposure limits both in terms of extinguishing media concentration and human exposure time.
Halocarbon agents should not be used at a gas concentration above that determined safe for
human exposure for 5 minutes. That concentration should be calculated on the net volume of the
protected space at the maximum expected temperature.
6.2 For inert gas systems, means should be provided to limit exposure to no longer than
5 minutes for inert gas systems designed to concentrations below 43% (corresponding to an
oxygen concentration of 12%, sea level equivalent of oxygen) or to limit exposure to no longer than 3 minutes for inert gas systems designed to concentrations between 43% and 52%
(corresponding to between 12% and 10% oxygen, sea level equivalent of oxygen).
6.3 In no case should a halocarbon agent be used above the LOAEL (Lowest Observed
Adverse Effect Level) nor the ALC (Approximate Lethal Concentration) nor should an inert gas
be used at gas concentrations above 52% calculated on the net volume of the protected space at
the maximum expected ambient temperature, without the use of controls as provided in the
International Code for Fire Safety Systems (FSS Code), chapter 5, regulation 2.2.2, and the agent
storage containers should be located outside the protected spaces in accordance with
regulation II-2/10.4.3 of the Convention.]
7 The system and its components should be suitably designed to withstand ambient
temperature changes, vibration, humidity, shock, impact, clogging, and corrosion normally
encountered in machinery spaces or cargo pump-rooms in ships.
8 The system and its components should be designed and installed in accordance with
international standards acceptable to the Organization1 and manufactured and tested to the
satisfaction of the Administration. As a minimum, the design and installation standards should
cover the following elements:
1 Until international standards are developed, national standards acceptable to the Administration should be used.Available national standards include, e.g., Standards of Australia, the United Kingdom and NFPA 2001.
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.1 safety:
.1 toxicity;
.2 noise, nozzle discharge; and
.3 decomposition products;
.2 storage container design and arrangement:
.1 strength requirements;
.2 maximum/minimum fill density, operating temperature range;
.3 pressure and weight indication;
.4 pressure relief; and
.5 agent identification and lethal requirements;
.3 agent supply, quantity, quality standards;
.4 pipe and fittings:
.1 strength, material, properties, fire resistance; and
.2 cleaning requirements;
.5 valves:
.1 testing requirements;
.2 corrosion resistance; and
.3 elastomer compatibility;
.6 nozzles:
.1 height and area testing requirements; and
.2 corrosion and elevated temperature resistance;
.7 actuation and control systems:
.1 testing requirements; and
.2 backup power requirements;
.8 alarms and indicators:
.1 predischarge alarm, agent discharge alarms as time delays;
.2 abort switches;
.3 supervisory circuit requirements; and
.4 warning signs and audible and visual alarms should be located outside
each entry to the relevant space as appropriate;
.9 agent flow calculation:
.1 approval and testing of design calculation method; and
.2 fitting losses and/or equivalent length;
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.10 enclosure integrity and leakage requirements:
.1 enclosure leakage;
.2 openings; and
.3 mechanical ventilation interlocks;
.11 design concentration requirements, total flooding quantity;
.12 discharge time; and
.13 inspection, maintenance, and testing requirements.
9 The nozzle type, maximum nozzle spacing, maximum height and minimum nozzle
pressure should be within limits tested to provide fire extinction per the proposed test method.
10 Provisions should be made to ensure that escape routes which are exposed to leakage
from the protected space are not rendered hazardous during or after discharge of the agent.
Control stations and other locations that require manning during a fire situation should have
provisions to keep HF and HCl below 5 ppm at that location. The concentrations of other
products should be kept below concentrations considered hazardous for the required duration of
exposure.
11 Agent containers may be stored within a protected space if the containers are distributed
throughout the space and meet the following provisions:
.1 a manually initiated power release, located outside the protected space, should be provided. Duplicate sources of power should be provided for this release and
should be located outside the protected space and be immediately available.
.2 electric power circuits connecting the containers should be monitored for fault
conditions and loss of power. Visual and audible alarms should be provided to
indicate this.
.3 pneumatic, electric or hydraulic power circuits connecting the containers should
be duplicated. The sources of pneumatic or hydraulic pressure should be
monitored for loss of pressure. Visual and audible alarms should be provided toindicate this.
.4 within the protected space, electrical circuits essential for the release of the system
should be fire resistant according to IEC 60331 or other equivalent standards.
Piping systems essential for the release of systems designed to be operated
hydraulically or pneumatically should be of steel or other equivalent heat-resisting
material to the satisfaction of the Administration.
.5 each pressure container should be fitted with an automatic overpressure release
device which, in the event of the container being exposed to the effects of fire and
the system not being operated, will safely vent the contents of the container intothe protected space.
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.6 the arrangement of containers and the electrical circuits and piping essential for
the release of any system should be such that in the event of damage to any one
power release line through fire or explosion in a protected space, i.e., a single fault
concept, at least five sixths of the fire-extinguishing charge required by paragraph 5 of this annex can still be discharged having regard to the requirement
for uniform distribution of medium throughout the space.
.7 the containers should be monitored for decrease in pressure due to leakage and
discharge. Visual and audible alarms in the protected area and on the navigation
bridge or in the space where the fire control equipment is centralized should be
provided to indicate this condition.
12 A minimum agent hold time of 15 minutes should be provided.
13 The release of an extinguishing agent may produce significant over and under pressurization in the protected space. Measures to limit the induced pressures to acceptable
limits should be provided.
14 For all ships, the fire-extinguishing system design manual should address recommended
procedures for the control of products of agent decomposition. The performance of
fire-extinguishing arrangements on passenger ships should not present health hazards from
decomposed extinguishing agents, for example on passenger ships, the decomposition products
should not be discharged in the vicinity of muster (assembly) stations.
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APPENDIX
TEST METHOD FOR FIRE TESTING OF FIXED
GAS FIRE-EXTINGUISHING SYSTEMS
1 Scope
1.1 This test method is intended for evaluating the extinguishing effectiveness of fixed gas
fire-extinguishing systems for the protection of machinery spaces of category A and cargo
pump-rooms.
1.2 Fire-extinguishing systems presently covered in SOLAS regulation II-2/5, as amended,
are excluded.
1.3 The test method covers the minimum requirements for fire-extinguishing.
1.4 This test method is applicable to gases, liquefied gases and mixtures of gases. The test
method is not valid for extinguishing gases mixed with compounds in solid or liquid state at
ambient conditions.
1.5 The test programme has two objectives: (1) establishing the extinguishing effectiveness
of a given agent at its tested concentration, and (2) establishing that the particular agent
distribution system puts the agent into the enclosure in such a way as to fully flood the volume to
achieve an extinguishing concentration at all points.
2 Sampling
The components to be tested should be supplied by the manufacturer together with design and
installation criteria, operational instructions, drawings and technical data sufficient for the
identification of the components.
3 Method of test
3.1 Principle
This test procedure enables the determination of the effectiveness of different gaseous agentextinguishing systems against spray fires, pool fires and class A fires.
3.2 Apparatus
3.2.1 Test room
The tests should be performed in 100 m2 room, with no horizontal dimension less than 8 m, with
a ceiling height of 5 m. The test room should be provided with a closable access door measuring
approximately 4 m2 in area. In addition, closable ventilation hatches measuring at least 6 m2 in
total area should be located in the ceiling.
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3.2.2 Integrity of test enclosure
The test enclosure is to be nominally leak tight when doors and hatches are closed. The integrity
of seals on doors, hatches, and other penetrations (for example, instrumentation access ports)must be verified before each test.
3.2.3 Engine mock-up:
.1 an engine mock-up of size (width x length x height) 1 m x 3 m x 3 m should be
constructed of sheet steel with a nominal thickness of 5 mm. The mock-up should
be fitted with two steel tubes diameter 0.3 m and 3 m length that simulate exhaust
manifolds and a solid steel plate. At the top of the mock-up a 3 m2 tray should be
arranged. See below figures 1, 2 and 3; and
.2 a floor plate system 4 m x 6 m x 0.75 m high shall surround the mock-up.Provision shall be made for placement of the fuel trays, described in table 1, and
located as described in table 2.
3.2.4 Instrumentation
Instrumentation for the continuous measurement and recording of test conditions should be
employed. The following measurements should be made:
.1 temperature at three vertical positions (for example., 1, 2.5, and 4.5 m);
.2 enclosure pressure;
.3 gas sampling and analysis, at mid-room height, for oxygen, carbon dioxide,
carbon monoxide, and relevant halogen acid products, for example,
hydrogen iodide, hydrofluoric acid, hydrochloric acid;
.4 means of determining flame-out indicators;
.5 fuel nozzle pressure in the case of spray fire;
.6 fuel flow rate in the case of spray fires; and
.7 discharge nozzle pressure.
3.2.5 Nozzles
3.2.5.1 For test purposes, nozzles should be located within 1 m of the ceiling.
3.2.5.2 If more than one nozzle is used they should be symmetrically located.
3.2.6 Enclosure temperature
The ambient temperature of the test enclosure at the start of the test should be noted and serve as
the basis for calculating the concentration that the agent would be expected to achieve at that
temperature and with that agent weight applied in the test volume.
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3.3 Test fires and programme
3.3.1 Fire types
The test programme, as described in table 3, should employ test fires as described in table 1.
Table 1
Parameters of Test Fires
Fire Type Fuel Fire Size, MW Remarks
A 76 - 100 mm ID
Can
Heptane 0.0012 to 0.002 Tell tale
B 0.25 m2
Tray Heptane 0.35
C 2 m2
Tray Diesel /Fuel Oil 3
D 4 m2
Tray Diesel /Fuel Oil 6
E Low pressurespray
Heptane0.16 ± 0.01 kg/s
5.8
F Low pressure, lowflow spray
Heptane0.03 ± 0.005 kg/s
1.1
G High pressure
spray
Diesel /Fuel Oil
0.05 ± 0.002 kg/s
1.8
H Wood Crib Spruce or Fir 0.3 See Note 2
I 0.10 m2
tray Heptane 0.14
Notes to table 1:
1 Diesel/fuel oil means light diesel or commercial fuel oil.
2 The wood crib should be substantially the same as described in ISO/TC 21/SC5/WG 8
ISO Draft International Standard, Gaseous fire extinguishing systems, Part 1: General
Requirements. The crib should consist of six, trade size 50 mm x 50 mm by 450 mm long,
kiln dried spruce or fir lumber having a moisture content between 9% and 13%. The
members should be placed in 4 alternate layers at right angles to one another. Members
should be evenly spaced forming a square structure.
Achieve ignition of the crib by burning commercial grade heptane in a square steel tray
0.25 m2 in area. During the pre-burn period the crib should be placed centrally above the
top of the tray a distance of 300 to 600 mm.
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Table 2
Spray fire test parameters
Fire type Low pressure(E) Low pressure,
Low flow(F)
High pressure(G)
Spray nozzle Wide spray angle (120
to 125°)
full cone type
Wide spray angle
(80°)
full cone type
Standard angle(at 6 Bar)
full cone type
Nominal fuel pressure 8 Bar 8.5 Bar 150 Bar
Fuel flow 0.16 + 0.01 kg/s 0.03 + 0.005 kg/s 0.050 + 0.002 kg/s
Fuel temperature 20 + 5°C 20 + 5°C 20 + 5°C
Nominal heat release rate 5.8 + 0.6 MW 1.1 + 0.1 MW 1.8 + 0.2 MW
3.3.2 Test programme
The fire test programme should employ test fires singly or in combination, as outlined in table 3.
Table 3
Test Programme
Test No. Fire Combinations (See Table 1)
1 A: Tell tales, 8 corners. See note 1.
2-a
See Note 2
B: 0.25 m2 heptane tray under engine mock-up
E: Horizontal LP spray directed at 15-25 mm rod 0.5 m awayG: HP diesel/fuel oil spray on top of engine mock-up
Total Fire Load: 7.95 MW
2-b
See Note 2
B: 0.25 m2 heptane tray under mock-upI: 0.10 m2 heptane tray on deck plate located below solid steel obstruction plate
Total Fire Load: 0.49 MW
3 C: 2 m2
diesel/fuel oil tray on deck plate located below solid steelobstruction plate
H: Wood crib positioned as in Figure 1F: Low pressure, low flow horizontal spray - concealed - with
impingement on inside of engine mock-up wall
Total Fire Load: 4.4 MW
4 D: 4 m2
diesel tray under engine mock-up
Total Fire Load: 6 MW
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Note to table 3:
1 Tell-tale fire cans should be located as follows:
.1 in upper corners of enclosure 150 mm below ceiling and 50 mm from each
wall; and
.2 in corners on floors 50 mm from walls.
2 Test 2-a is for use in evaluating extinguishing systems having discharge times of
10 seconds or less.
3 Test 2-b is for use in evaluating extinguishing systems having discharge times
greater than 10 seconds.
3.3.2.1 All applicable tests of table 3 should be conducted for every new fire extinguishant gas,or mixture of gases.
3.3.2.2 Only Test 1 is required to evaluate new nozzles and related distribution system
equipment (hardware) for systems employing fire extinguishants that have successfully completed
the requirements of 3.3.2.1. Test 1 should be conducted to establish and verify the manufacturer's
minimum nozzle design pressure.
3.4 Extinguishing system
3.4.1 System installation
The extinguishing system should be installed according to the manufacturer's design and
installation instructions. The maximum vertical distance should be limited to 5 m.
3.4.2 Agent
3.4.2.1 Design concentration
The agent design concentration is that concentration (in volume per cent) required by the system
designer for the fire protection application.
3.4.2.2 Test concentration
The concentration of agent to be used in the fire extinguishing tests should be the design
concentration specified by the extinguishing system manufacturer, except for test 1 which should
be conducted at 77% of the manufacturer’s recommended design concentration but in no case at
less than the cup burner extinguishing concentration.
3.4.2.3 Quantity of agent
The quantity of agent to be used should be determined as follows:
3.4.2.3.1 Halogenated agents
W = (V/S) C/(100 - C)
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where:
W = agent mass, kg
V = volume of test enclosure, m3
S = agent vapour specific volume at temperature and pressure of the test
enclosure, kg/m3
C = gaseous agent concentration, volume per cent.
3.4.2.3.2 Inert gas agents
Q = V [294/(273 + T)] (P/1.013) ln[100/(100 - C)]
where:
Q = volume of inert gas, measured at 294 K and 1.013 bar, discharged, m3
V = volume of test enclosure, m3 T = test enclosure temperature, Celsius
P = test enclosure pressure, bar
C = gaseous agent concentration, volume per cent.
3.5 Procedure
3.5.1 Fuel levels in trays
The trays used in the test should be filled with at least 30 mm fuel on a water base. Freeboard
should be 150 ± 10 mm.
3.5.2 Fuel flow and pressure measurements
For spray fires, the fuel flow and pressure should be measured before and during each test.
3.5.3 Ventilation
3.5.3.1 Pre-burn period
During the pre-burn period the test enclosure should be well ventilated. The oxygen
concentration, as measured at mid-room height, shall not be less than 20 volume per cent at thetime of system discharge.
3.5.3.2 End of pre-burn period
Doors, ceiling hatches, and other ventilation openings should be closed at the end of the pre-burn
period.
3.5.4 Duration of test
3.5.4.1 Pre-burn time
Fires should be ignited such that the following burning times occur before the start of agent
discharge:
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.1 sprays - 5 to 15 seconds;
.2 trays - 2 minutes; and
.3 crib - 6 minutes.
3.5.4.2 Discharge time:
.1 halogenated agents should be discharged at a rate sufficient to achieve delivery
of 95% of the minimum design quantity in 10 s or less; and
.2 inert gas agents should be discharged at a rate sufficient to achieve 85% of the
minimum design quantity in 120 s or less.
3.5.4.3 Soak time
After the end of agent discharge the test enclosure should be kept closed for 15 minutes.
3.5.5 Measurements and observations
3.5.5.1 Before test:
.1 temperature of test enclosure, fuel and engine mock-up;
.2 initial weights of agent containers;
.3 verification of integrity agent distribution system and nozzles; and
.4 initial weight of wood crib.
3.5.5.2 During test:
.1 start of the ignition procedure;
.2 start of the test (ignition);
.3 time when ventilating openings are closed;
.4 time when the extinguishing system is activated;
.5 time from end of agent discharge;
.6 time when the fuel flow for the spray fire is shut off;
.7 time when all fires are extinguished;
.8 time of re-ignition, if any, during soak period;
.9 time at end of soak period; and.10 at the start of test initiate continuous monitoring as per 3.2.4.
3.5.6 Tolerances
Unless otherwise stated, the following tolerances should apply:
.1 length ±2% of value;
.2 volume ±5% of value;
.3 pressure ±3% of value;
.4 temperature ±5% of value;
.5 concentration ±5% of value.
These tolerances are in accordance with ISO Standard 6182/1, February 1994 edition [4].
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4 Classification criteria
4.1 Class B fires must be extinguished within 30 seconds of the end of agent discharge. At the
end of the soak period there should be no re-ignition upon opening the enclosure.
4.2 The fuel spray should be shut off 15 seconds after extinguishment. At the end of the soak
time, the fuel spray should be restarted for 15 seconds prior to reopening the door and there
should be no re-ignition.
4.3 At the end of the test fuel trays must contain sufficient fuel to cover the bottom of the tray.
4.4 Wood crib weight loss must be no more than 60%.
5 Test report
The test report should include the following information:
.1 name and address of the test laboratory;
.2 date and identification number of the test report;
.3 name and address of client;
.4 purpose of the test;
.5 method of sampling system components;
.6 name and address of manufacturer or supplier of the product;
.7 name or other identification marks of the product;
.8 description of the tested product:
.1 drawings;
.2 descriptions;
.3 assembly instructions;
.4 specification of included materials; and
.5 detailed drawing of test set-up;
.9 date of supply of the product;
.10 date of test;
.11 test method;
.12 drawing of each test configuration;
.13 identification of the test equipment and used instruments;
.14 conclusions;
.15 deviations from the test method, if any;
.16 test results including measurements and observations during and after the test; and
.17 date and signature.
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***
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ANNEX 3
PROPOSED AMENDMENTS TO REVISED GUIDELINES FOR APPROVAL OF
SPRINKLER SYSTEMS EQUIVALENT TO THAT REFERRED TO IN
SOLAS REGULATION II-2/12
Resolution A.800(19)
3 Principle requirements for the system
Revise paragraph 3.3 as follows:
“3.3 The sprinkler system should be capable of continuously supplying the water-based
extinguishing medium for a minimum of 30 minutes. A pressure tank or other means
should be provided to meet the functional requirement stipulated in FSS Code, chapter 8,
regulation 2.3.2.1. The design of the system should ensure that full system pressure isavailable at the most remote nozzle in each section within 60 seconds of system
activation.”
Revise paragraph 3.8 as follows:
“3.8 There shall be not less than two sources of power for the system. Where the
sources of power for the pump are electrical, these shall be a main generator and an
emergency source of power. One supply for the pump shall be taken from the main
switchboard, and one from the emergency switchboard by separate feeders reserved solely
for that purpose. The feeders shall be so arranged as to avoid galleys, machinery spaces
and other enclosed spaces of high fire risk except in so far as it is necessary to reach theappropriate switchboards, and shall be run to an automatic changeover switch situated near
the sprinkler pump. This switch shall permit the supply of power from the main
switchboard so long as a supply is available there from, and be so designed that upon
failure of that supply it will automatically change over to the supply from the emergency
switchboard. The switches on the main switchboard and the emergency switchboard shall
be clearly labelled and normally kept closed. No other switch shall be permitted in the
feeders concerned. One of the sources of power supply for the alarm and detection system
shall be an emergency source. Where one of the sources of power for the pump is an
internal combustion engine it shall, in addition to complying with the provisions of
FSS Code, paragraph 2.4.3.1, be so situated that a fire in any protected space will notaffect the air supply to the machinery. Pump sets consisting of two diesel engines each
supplying at least 50% of the required water capacity are considered acceptable if the fuel
supply is adequate to operate the pumps at full capacity for a period of 36 hours on
passenger ships and 18 hours on cargo ships.”
Add to paragraph 3.9:
“The capacity of the redundant means should be sufficient to compensate for the loss of
any single supply pump or alternative source. Failure of any one component in the power
and control system should not result in a reduction of the automatic release capability or
reduction of sprinkler pump capacity by more than 50%.”
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Revise paragraph 3.13 as follows:
“3.13 Each section of sprinklers should be capable of being isolated by one stop valve
only. The stop-valve in each section should be readily accessible in a location outside of the associated section or in cabinets within stairway enclosures. The valve’s location
should be clearly and permanently indicated. Means should be provided to prevent the
operation of the stop-valves by any unauthorized person. Isolation valves used for service,
maintenance or for refilling of antifreeze solutions may be installed in the sprinkler piping
in addition to the section stop valves, if provided with a means for giving a visual and
audible alarm as required by paragraph 3.17. Valves on the pump unit may be accepted
without such alarms if they are locked in the correct position.”
Revise paragraph 3.15 as follows:
“3.15 The sprinkler system water supply components should be outside category Amachinery spaces and should not be situated in any space required to be protected by the
sprinkler system.”
Add to the end of paragraph 3.19
“The maintenance instructions should include provisions for a flow test of each section at
least annually to check for possible clogging or deterioration in the discharge piping.”
Modify paragraph 3.22 as follows:
“3.22 Pumps and alternative supply components should be capable of supplying the flowrate and pressure needed for the space with the greatest hydraulic demand. For the
purposes of this calculation, the design area used to calculate the required flow and
pressure should be the deck area of the most hydraulically demanding space, separated
from adjacent spaces by A-class [B-class] divisions, up to a maximum of 280 m2. The
quantity of water needed for the atrium deluge system, if provided should [should not] be
included in the calculation. For application to a small ship, the Administration may
specify the appropriate area for sizing of pumps and alternate supply components.”
Add a new paragraph 3.23 as follows:
“3.23 The nozzle location, type of nozzle, and nozzle characteristics should be within the
tested limits determined by the fire test procedures in appendix 2 to provide fire control or
suppression as referred to in paragraph 3.2.”
Add a new paragraph 3.24 as follows:
“3.24 For atria, theatres, restaurants and similar public spaces with ceiling heights greater
than 5 m, a manually activated deluge system should be installed at the ceiling using open
nozzles equivalent to those tested to the requirements of section 6 of annex 2, at a 5 m
ceiling height. The deluge system should be divided into sections not exceeding 280 m2.
The manually operated section valves should comply with the criteria in paragraph 3.13,and the criteria for visual and audible alarms in paragraph 3.17. All enclosed spaces and
any spaces beneath balconies or overhangs within the space should have automatic ceiling
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mounted nozzles. Spacing of nozzles within the atrium should be in accordance with the
public space test requirements.”
Add a new paragraph 3.25 as follows:
(Note – this addition is pending the final outcome of the Passenger Ship Working Group’s
deliberations)
“3.25 The system should be designed in such a way that during a fire occurrence, the
level of protection provided to those spaces unaffected by fire is not reduced.”
Add a new paragraph 3.26 as follows:
“3.26 A quantity of spare water mist nozzles shall be carried for all types and ratings
installed on the ship as follows:
Total number of nozzles Required number of spares
< 300 6
300 to 1000 12
> 1000 24
The number of spare nozzles of any type need not exceed the total number of nozzles
installed of that type.”
Add a new paragraph 3.27 as follows:
“3.27 Any parts of the system which may be subjected to freezing temperatures in
service should be suitably protected against freezing.”
Add a new paragraph 5.21.4 to appendix 1:
“5.21.4 Alternative supply arrangements to the apparatus shown in figure 3 may be used
where damage to the pump is possible. Restrictions to piping defined by note 2 of table 5
should apply to such systems.”
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APPENDIX 2
FIRE TEST PROCEDURES FOR WATER MIST SYSTEMS IN ACCOMMODATION,
PUBLIC SPACES AND SERVICE AREAS ON PASSENGER SHIPS
1 Scope
1.1 These test procedures describe a fire test method for evaluating the effectiveness of water
mist systems equivalent to systems covered by chapter 8 of the FSS Code in accommodation and
service areas on board ships. It should be noted that the test method is limited to the systems’
effectiveness against fire and is not intended for testing of the quality and design parameters of
the individual components of the system.
1.2 In order to fulfil the requirements of paragraph 3.5 of the guidelines, the system must be
capable of fire control or suppression in a wide variety of fire loading, fuel arrangement, room
geometry and ventilation conditions.
1.3 Products employing materials or having forms of construction differing from the
requirements contained herein may be examined and tested in accordance with the intent of the
requirements and, if found to be substantially equivalent, may be judged to comply with the
document.
1.4 Products complying with the text of this document will not necessarily be judged to
comply, if, when examined and tested, they are found to have other features which impair thelevel of safety contemplated by this document.
2 Hazard and occupancy classification
For the purposes of identifying the different fire risk classifications, table 1 is given, which
correlates the fire tests with the classification of occupancy defined in SOLAS regulations
II-2/9.2.2.3 and II-2/9.2.2.4:
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Table 1 – Correlation between fire tests with the classification of
of occupancy defined in SOLAS regulations II-2/9.2.2.3
and II-2/9.2.2.4
Corresponding fire test
Occupancy classification Section
5
cabin
Section
5
corridor
Section
6
public
spaces
Section
8
storage
(1) Control stations X
(2) Stairways X1
(3) Corridors X1
(6) Accommodation spaces of minor fire risk X2 X3
(7) Accommodation spaces of moderate fire risk X2
X3, 4
(8) Accommodation spaces of greater fire risk X3, 4
(9) Sanitary & similar spaces X2 X 3
(11) Refrigerated chambers X
(12) Main galleys and annexes X
(13) Store rooms, workshops, pantries, etc. X
(14) Other spaces in which flammable liquids are
stowed
X
Notes:
1 For corridors and stairways wider than 1.5 m, use section 6 public space fire test instead of the corridor fire test
2 For spaces up to the area of the cabin applied in tests of section 5
3 For spaces over the area of the cabin applied in tests of section 5
4 Refer to annex, item 3.24
3 Definitions
3.1 Fire suppression: sharply reducing the heat release rate of a fire and preventing itsre-growth by means of a direct and sufficient application of water through the fire plume to the
burning fuel surface.
3.2 Fire control: limiting the size of a fire by distribution of water so as to decrease the heat
release rate and pre-wet adjacent combustibles, while controlling ceiling gas temperatures to
avoid structural damage.
3.3 Fire source: fire source is defined as the combustible material in which the fire is set and
the combustible material covering walls and ceiling.
3.4 Igniter: the device used to ignite the fire source.
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4 General requirements
4.1 Nozzle positioning
These test procedures are applicable to either overhead nozzles installed on the ceiling, or
sidewall nozzles installed on bulkheads below the ceiling. Separate approval tests should be
conducted for each nozzle type. The testing organization should be responsible for assuring that
the nozzles for each fire test are installed in accordance with the manufacturer’s design and
installation instructions. The tests should be performed at the maximum specified spacings,
installation height and distances below the ceiling. In addition, if the testing organization finds it
necessary, selected fire tests should also be conducted at minimum specified spacings,
installation height and distances below the ceiling. Where two types of nozzles are installed in
the same area, an overlap of the different nozzle spray patterns should be provided equal to at
least one half of the maximum approved nozzle spacing.
4.2 Water pressure and flow rates
The testing organization should be responsible for assuring that all fire tests are conducted at the
operating pressure and flow rates specified by the manufacturer.
For all tests, the system should either be:
.1 pressurised to the minimum operating pressure specified by the manufacturer.
Upon activation of the first nozzle, the flowing water pressure should be
maintained at the minimum system operating pressure; or
.2 pressurised to the minimum stand-by pressure specified by the manufacturer.
Upon activation of the first nozzle, the flowing water pressure should be gradually
increased to the minimum system operating pressure, specified by the
manufacturer. The delay time until the minimum system operating pressure is
reached should be at least 15 seconds. The delay time recorded during the tests
should be documented and included in the approval of the system.
4.3 Temperature measurements
Temperatures should be measured as described in detail under each chapter. Chromelalumelthermocouple wires not exceeding 0.5 mm in diameter welded together should be used. The
temperatures should be measured continuously, at least every two seconds, throughout the tests.
4.4 Environmental conditions
The test hall should have an ambient temperature of between 10ºC and 30ºC at the start of each
test.
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4.5 Tolerances
Unless otherwise stated, the following tolerances should apply:
.1 Length ± 2 % of value
.2 Volume ± 5 % of value
.3 Pressure ± 3 % of value
.4 Temperature ± 5 % of value
These tolerances are in accordance with ISO Standard 6182-1. February 1994 edition.
4.6 Observations
The following observations should be made during and after each test:
.1 time of ignition;
.2 activation time of each nozzle;
.3 time when water flow is shut off;
.4 damage to the fire source;
.5 temperature recordings;
.6 system flow rate and pressure; and
.7 total number of operating nozzles.
4.7 Fire sources
If the requirements for fire sources specified in the following sections of this test method cannot
be fulfilled, it is the responsibility of the test laboratory to show that alternative materials usedhave burning characteristics similar to those of specified materials.
4.8 Product and documentation requirements
The fire test report should identify the critical parameters to be incorporated into the design,
installation and operating instruction manual.
The instruction manual should reference the limitations of each device and should include at least
the following items:
.1 description and operating details of each device and all accessory equipment,including identification of extinguishing system components or accessory
equipment by part or model number;
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.2 nozzle design recommendation and limitations for each fire type;
.3 type and pressure rating of pipe, tubing and fittings to be used;
.4 equivalent length values of all fittings and all system components through which
water flows;
.5 discharge nozzle limitations, including maximum dimensional and area coverage,
minimum mad maximum installation height limitations, and nozzle permitted
location in the protected volume;
.6 range of filling capacities for each size storage container;
.7 details for the proper installation of each device, including all component
equipment;
.8 reference to the specific types of detection and control panels (if applicable) to be
connected to the equipment;
.9 operating pressure ranges of the system;
.10 method of sizing pipe or tubing;
.11 recommended orientation of tee fittings and the splitting of flows through tees;
and
.12 maximum difference in operating (flowing) pressure between the hydraulically
closest and most remote nozzle.
5 Cabin and corridor tests
5.1 Test arrangement
5.1.1 The fire tests should be conducted in a 3 m x 4 m, 2.5 m high cabin connected to the
centre of a 1.5 m x 12 m long corridor, 2.5 m high with both ends open. The cabin area may be
increased up to the maximum size to be protected with one nozzle. The disabled nozzle testshould be conducted in a 3 m x 4 m cabin.
5.1.2 The cabin should be fitted with one doorway opening, 0.8 m wide and 2.2 m high, which
provides for a 0.2 m lintel above the opening
5.1.3 The walls of the cabin should be constructed from an inner layer of nominally 12 mm
thick non-combustible wall board with a nominally 45 mm thick mineral wool liner. The walls
and ceiling of the corridor and ceiling of the cabin should be constructed of nominally 12 mm
thick non-combustible wall boards. The cabin may be provided with a window in the wall
opposite the corridor for observation purposes during the fire tests.
5.1.4 The cabin and corridor ceiling should be covered with cellulosic acoustical panels. The
acoustical panels should be nominally 12 mm to 15 mm thick and should not ignite when tested
in accordance with IMO resolution A.653(16).
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5.1.5 Plywood panels should be placed on the cabin and corridor walls. The panels should be
approximately 3 mm thick. The ignition time of the panel should be not more than 35 seconds
and the flame spread time at 350 mm position should not be more than 100 seconds as measured
in accordance with IMO resolution A.653(16).
5.2 Instrumentation
During each fire test, the following temperatures should be measured using thermocouples of
diameter not exceeding 0.5 mm:
.1 the ceiling surface temperature above the ignition source in the cabin should be
measured with a thermocouple embedded in the ceiling material from above such
that the thermocouple bead is flush with the ceiling;
.2 the ceiling gas temperature should be measured with a thermocouple 75+1 mm below the ceiling in the centre of the cabin;
.3 the ceiling surface temperature in the centre of the corridor, directly opposite the
cabin doorway, should be measured with a thermocouple embedded in the ceiling
material such that the thermocouple bead is flush with the ceiling (figure 1); and
.4 the ceiling surface temperature directly above the corridor test fire source (if used)
described in paragraph 5.4.2 should be measured with a thermocouple embedded
in the ceiling material such that the thermocouple bead is flush with the ceiling
surface.
5.3 Nozzle positioning
The nozzles should be installed to protect the cabin and corridor in accordance with the
manufacturer’s design and installation instructions subject to the following:
.1 if only one ceiling nozzle is installed in the cabin, it may not be placed in the
shaded area in figure 2;
.2 if two or more ceiling nozzles are installed in the cabin the nominal water flux
density should be homogeneously distributed throughout the cabin;
.3 corridor nozzles should not be placed closer to the centreline of the cabin doorway
than one half the maximum spacing recommended by the manufacturer. An
exception is systems where nozzles are required to be placed outside each
doorway; and
.4 cabin mounted sidewall nozzles should be installed on the centreline of the front
wall of the cabin adjacent to the doorway, aimed towards the rear of the cabin.
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5.4 Fire sources
5.4.1 Cabin test fire source
Two pullman-type bunk beds having an upper and lower berth should be installed along the
opposite side walls of the cabin (figure 1). Each bunk bed should be fitted with 2.0 m by 0.8 m
by 0.1 m polyether mattresses having a cotton fabric cover. Pillows measuring 0.5 m by 0.8 m
by 0.1 m should be cut from the mattresses. The cut edge should be positioned towards the
doorway. A third mattress should form a backrest for the lower bunk bed. The backrest should
be attached in an upright position in a way that prevents it from falling over (figure 3).
The mattresses should be made of non-fire retardant polyether and they should have a density of
approximately 33 kg/m3. the cotton fabric should not be fire retardant treated and it should have
an area weight of 140 g/m2 to 180 g/m2. when tested according to ISO Standard 5660-1
(astm e-1354), the polyether foam should give results as given in the table below. the frame of the bunk beds should be of steel nominally 2 mm thick.
ISO STANDARD 5660, CONE CALORIMETER TEST
Test Conditions: Irradiance 35 kW/m2. Horizontal position.
Sample thickness 50 mm. No frame retainer should be used
Test results Foam
Time to ignition (s) 2-63 minute average HRR, q180 (kW/m2) 270650
Minimum heat of combustion (MJ/kg) 27
Total heat release (MJ/m2) 50612
5.4.1 Corridor test fire source
The corridor fire tests should be conducted using eight piled polyether mattress pieces measuring
0.4 m x 0.4 m x 0.1 m, as specified in paragraph 5.4.1, without fabric covers. The pile should be
placed on a stand, 0.25 m high, and in a steel test basket to prevent the pile from falling over
(figure 4).
5.5 Test method
The following series of fire tests should be performed with automatic activation of the nozzle(s)
installed in the cabin and/or corridor as indicated. Each fire should be ignited using an igniter
made of some porous material, e.g. pieces of insulating fibreboard. The igniter may be either
square or cylindrical, 60 mm square or 75 mm in diameter. The length should be 75 mm. Prior
to the test the igniter should be soaked in 120 ml of heptane and positioned as indicated for each
cabin fire test. For the corridor fire tests, the igniter should be located in the centre at the base of
the pile of the mattress pieces, and on one side of the test stand at the base of the pile of mattress
pieces:
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.1 lower bunk bed test. Fire arranged in one lower bunk bed and ignited with the
igniter located at the front (towards door) centreline of the pillow;
.2 upper bunk bed test. Fire arranged in one upper bunk bed with the igniter locatedat the front (towards door) centreline of the pillow;
.3 arsonist test;
.4 disabled nozzle test. The nozzle(s) in the cabin should be disabled. Fire arranged
in one lower bunk bed and ignited with the igniter located at the front (towards
door) centreline of the pillow. If nozzle(s) in the cabin are linked with nozzle(s)
in the corridor such that a malfunction would affect them all, all cabin and
corridor nozzles linked should be disabled;
.5 corridor test. Fire source located against the wall of the corridor under onenozzle; and
.6 corridor test. Fire source located against the wall of the corridor between two
nozzles;
the fire tests should be conducted for 10 minutes after the activation of the first nozzle, and any
remaining fire should be extinguished manually.
5.6 Acceptance criteria
Based on the measurements, a maximum 30 seconds average value should be calculated for eachmeasuring point which forms the temperature acceptance criteria.
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Acceptance criteria for the cabin and corridor tests
Maximumacceptable
damage on
mattresses (%)
Maximum30 s
average
ceiling
surface
temperature
in the cabin
(ºC)
Maximum30 s
average
ceiling
gas
temperature
in the cabin
(ºC)
Maximum30 s
average
ceiling
surface
temperature
in the
corridor
(ºC)
Lower
bunk
Upper
bunk
Other criteria
Lower
bunk
bed
40 10
Upper
bunk bed
360 320 120
N.A. 40
No nozzlesin corridor allowed tooperate3
Cabin
tests
Arsonist N.A. N.A. 120 N.A. N.A. N.A.
Corridor
tests
N.A. N.A. 1201 N.A. Only twoIndependent and
adjacent
nozzles incorridor
allowed tooperate4
Disabled nozzle N.A. N.A. 4002 N.A. N.A.
1 In each test, the temperature should be measured above the fire source.
2 The fire is not allowed to propagate along the corridor beyond the nozzles closest to the door
opening.
3 Not applicable, if cabin nozzle(s) are linked to corridor nozzle(s).
4 Not applicable, if corridor nozzle(s) are linked together.
N.A. Not applicable
Note: After the test, the fire sources should be examined visually to determine compliance with
the required maximum damage. The damages should be estimated using the following formula:
Damage to lower bunk bed = (damage to horizontal mattress (%) + 0.25 x damage to
pillow (%) + damage to backrest (%))/2.25
Damage to upper bunk bed = (damage to horizontal mattress (%) + 0.25 x damage to
pillow (%))/1.25
If it is not clearly obvious by visual examination whether the criteria are fulfilled or not,
the test should be repeated.
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6 Public space fire tests
6.1 Test arrangements
The fire tests should be conducted in a well-vented building under a ceiling of at least 80 m2 in
area with no dimension less than 8 m. There should be at least a 1 m space between the
perimeters of the ceiling and any wall of the test building. The ceiling height should be set
at 2.5 m and 5.0 m respectively.
Two different tests should be conducted as per paragraphs 6.1.1 and 6.1.2.
6.1.1 Open public space test
The fire source should be positioned under the centre of the open ceiling so that there is an
unobstructed flow of gases across the ceiling. The ceiling should be constructed from anon-combustible material. At least 1 m2 of the ceiling just above ignition should be covered with
acoustical panels. The acoustical panels should be nominally 12 mm to 15 mm thick, and should
not ignite when tested in accordance with IMO resolution A.653(16).
6.1.2 Corner public space test
The test should be conducted in a corner constructed by two at least 3.6 m wide, nominally
12 mm thick, non-combustible wall boards.
Plywood panels should be placed on the walls. The panels should be approximately 3 mm thick.
The ignition time of the panel should not be more than 35 seconds and the flame spread timeat 350 mm position should not be more than 100 seconds measured in accordance with
IMO resolution A.653(16).
The ceiling should be covered, 3.6 m out from the corner, with cellulosic acoustical panels. The
acoustical panels should be nominally 12 mm to 15 mm thick, and should not ignite when tested
in accordance with IMO resolution A.653(16).
6.2 Instrumentation
During each fire test, the following temperatures should be measured using thermocouples withdiameter not exceeding 0.5 mm.
6.2.1 Open public space test
.1 the ceiling surface temperature above the ignition source should be measured
using a thermocouple embedded in the ceiling material such that the thermocouple
bead is flush with the ceiling surface; and
.2 The ceiling gas temperature should be measured using a thermocouple located
75+1 mm below the ceiling 1.8 m from ignition.
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6.2.2 Corner public space test
.1 The ceiling surface temperature above the ignition source should be measured
using a thermocouple embedded in the ceiling material such that the thermocouple bead is flush with the ceiling surface.
.2 The ceiling gas temperature should be measured using a thermocouple located
75+1 mm below the ceiling within 0.2 m horizontally from the closest nozzle to
the corner.
6.3 Nozzle positioning
For nozzles with frame arms, tests should be conducted with the frame arms positioned both
perpendicular and parallel with the edges of the ceiling or corner walls. For nozzles without
framed arms, the nozzles should be oriented so that the lightest discharge density will be directedtowards the fire area.
6.4 Fire sources
6.4.1 Open public space
The fire source should consist of four sofas made of mattresses as specified in item 5.4.1 installed
in steel frame sofas. The steel frames for the sofas should consist of rectangular bottom and
backrest frames constructed of steel angles, channels or rectangular stock of at least 3 mm
thickness. The frame dimensions should be 2.0 m x 0.65 m. The seat and backrest cushions
should be supported on each frame by three steel bars 20-30 mm wide x 0.65 m long spacedevery 0.5 m and welded to the frames. Steel plates should not be used to support the cushions.
The assembled frames should be supported by four legs constructed of similar steel stock. The
two rear legs should be 500 mm in height and the front legs should be 580 mm in height. Each
sofa should have a rectangular armrest on each end. The armrest should be constructed of similar
steel stock and should be 0.2 m in height and 0.5 m in length. The rear section of the armrest
should be attached to the bottom frame 50 mm from the backrest. The sofas should be positioned
as shown in figure 7 spaced 25 mm apart. One of the middle sofas should be ignited, centric and
at the bottom of the backrest, with an igniter as described in item 5.5.
6.4.2 Corner public space test
The fire source should consist of a sofa, as specified in 6.4.1, placed with the backrest 25 mm
from the right-hand wall and close up to the left-hand wall. A target sofa should be placed along
the right-hand wall with the seat cushion 0.1 m from the first sofa and another target sofa should
be placed 0.5 m from it on the left hand side. The sofa should be ignited using an igniter, as
described in 5.5, that should be placed at the far left of the corner sofa, at the base of the backrest,
near the left-hand wall (figure 8).
6.5 Test method
The fire tests should be conducted for 10 minutes after the activation of the first nozzle, and anyremaining fire should be extinguished manually.
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6.5.1 Open public space tests
Fire tests should be conducted with the ignition centred under one, between two and below four
nozzles. An additional test should be conducted with the ignition centred under a disablednozzle.
6.5.2 Corner public space test
The fire tests should be conducted with at least four nozzles arranged in a 2 x 2 matrix.
6.6 Acceptance criteria
Based on the measurements, a maximum 30 seconds average value should be calculated for each
measuring point which forms the temperature acceptance criteria.
6.6.1 Acceptance criteria for the public space tests
Maximum 30 s
average ceiling
surface temperature
(ºC)
Maximum 30 s
average ceiling
gas temperature
(ºC)
Maximum acceptable
Damage on mattresses
(%)
normal 360 2202
50/351
Open space
disabled
nozzle
N.A. N.A. 50 (target sofas)[70]
Corner360 220
50/35
1
(ignition sofa)no charring of target
sofas
1 50% is the upper limit for any single test. 35% is the upper limit for the average of the public
space tests required in 6 at each ceiling height (excluding the disabled sprinkler test).
2 The gas temperature should be measured at four different positions and the evaluation of the
results is based on the highest reading.
N.A. Not applicable.
7 Storage area fire tests
7.1 Test arrangements
As per 6.1 but with 2.5 m ceiling height only.
7.2 Instrumentation
No temperature measurements are required.
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7.3 Nozzle positioning
As per 6.3.
7.4 Fire source
The fire source should consist of two central, 1.5 m high, solid piled stacks of cardboard boxes
packed with polystyrene unexpanded plastic cups with a 0.3 m flue space. Each stack should be
approximately 1.6 m long and 1.1 m to 1.2 m wide.
A suitable plastic commodity is the FMRC standard plastic commodity [9]. Similar commodities
might be used if they are designed in a similar way and are proven to have the same burning
characteristics and suppressability.
The fire source should be surrounded by six 1.5 m high solid piled stacks of empty cardboard boxes forming a target array to determine if the fire will jump the aisle. The boxes should be
attached to each other, for example by staples, to prevent them from falling over (figure 9).
7.5 Test method
Fire tests should be conducted with the ignition centred under one, between two and below four
nozzles.
Each fire should be ignited using two igniters as described in 5.5. The igniters should be placed
on the floor, each against the base of one of the two central stacks and ignited simultaneously.
The fire tests should be conducted for 10 minutes after the activation of the first nozzle, and any
remaining fire should be extinguished manually.
7.6 Acceptance criteria
.1 No ignition or charring of the target cartons is allowed.
.2 No more than 50% of the cartons filled with plastic cups should be consumed.
***
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ANNEX 4
DRAFT GUIDELINES FOR HIGH EXPANSION FOAM
USING INSIDE AIR
Item Requirement Discussion Comments1
DRAFT GUIDELINES FOR THE
APPROVAL OF INSIDE AIR FOAM
SYSTEMS
1 General
SOLAS provides for and accepts the use of
high expansion foam systems inside machinery
spaces. The fixed high expansion foam fire-
extinguishing system providing foamgenerators inside the protected space should
demonstrate by a test to have the capability of
extinguishing a variety of fires, which may
occur in a ship’s engine room.
2 2 Definitions
2.1 Foam solution is a solution of foam
concentrate and water.
2.2 Foam concentrate is the liquid which,
when mixed with water in the appropriateconcentration forms a foam solution.
2.3 Foam generator is a discharge device
consisting of a nozzle or set of nozzles and a
casing. The casing is typically made of
perforated steel / stainless steel plates shaped
into a box that enclose the nozzle(s).
2.4 Inside air foam system is a fixed high
expansion foam fire extinguishing system with
foam generators located inside the protected
space.
2.5 Nominal flow rate is the foam solution
flow rate expressed in L/min.
2.6 Nominal application rate is the flow
rate per area, i.e. expressed in L/min/m2.
2.7 Nominal foam expansion ratio is the
ratio of the volume of foam to the volume of
foam solution from which it was made.
2.8 Nominal foam production is the
volume of foam produced per time unit, that is
nominal flow rate times nominal foam
expansion ratio, expressed in m3/min.
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2.9 Nominal filling rate is the ratio of
nominal foam production to the area, i.e.
expressed in m/min.
2.10 Nominal filling time is the ratio of the
height of the protected space to the nominal
filling rate, i.e. expressed in minutes.
3 3 Principal requirements for the
system
3.1 Principal performance:
.1 The system should be capable of
manual release. Automatic releaseof the system should not be
permitted, except as permitted by
the Administration.
4 .2 The system should be capable of
fire extinction, and tested in
accordance with appendix 2 to this
guideline.
5 .3 The expansion ratio and drainage
time of the foam concentrate
should be approved by theAdministration in accordance with
MSC/Circ.670. However, the fire
tests specified in paragraph 3.8 of
the annex to MSC/Circ.670 need
not be applied. [The foam
concentrate should be approved in
accordance with (small scale foam
quality test to be developed)]
Co-ord
Clarification.
Sweden
Need to have small scale testsspecific to inside air
applications. The tests should
include repeatable exposure to
heat and smoke
Japan
Japan considers the small scale
foam quality test is not
necessary, since the fire test
using the 500 m3
enclosure
sufficiently assesses the foam
quality. Small scales test seems
to require duplicate fire tests.
For member’s reference, vessels
gross tonnage having 500 m3
ER is around 2,000 tons.
6 .4 The foam generators should be
successfully tested in accordance
with appendix 1 to this guideline.
7 Deleted
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8 3.2 Requirements for the system:
.1 Electrical power for the system should be supplied from emergency power.
The system should be supplied by both
main and emergency sources of power
and should be provided with an
automatic change-over switch. The
emergency power supply should be
provided from outside the protected
machinery space
Germany
Harmonize with MSC/Circ.668
Japan
Where the system is applied to
machinery spaces of category A,
main source supply is not
necessary because main source
should be cut off in case of fire
in the machinery spaces.
Therefore, Japan proposes to
retain the original text as it is.
9 .2 The system and its components should be suitably designed to withstand
ambient temperature changes,
vibration, humidity, shock, clogging
and corrosion normally encountered in
machinery spaces or cargo pump room
in ships, and manufactured and tested
to the satisfaction of the
Administration in accordance with the
requirements given in appendix 1 to
these Guidelines. Components inside
the protected spaces should be
designed to withstand the elevatedtemperatures, which could occur
during a fire.
10 Deleted
11 .4 Foam generators and System piping,
components and pipe fittings in contact
with the foam concentrate should be
constructed of corrosion resistant
materials such as stainless steel, CuNi
alloy or equivalent. Other system
piping and foam generators should be
galvanized steel or equivalent. [If the
system components (such as foam
proportioner, foam concentrate pump,
etc.) should be constructed of copper
or copper alloy by practical reason, an
effective means of protection such as a
steel cover or “A-60” insulation should
be provided, unless the components are
not located in a high fire risk area]
Norway
Add requirements for corrosion
resistant.
Japan
Japan proposes to add “and
water constantly” after
concentrate, because the
corrosion should be considered
only in such cases.
Korea
Foam generators would not be in
contact with foam concentrate.
Also propose deleting CuNialloy due to low melting point.
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11
bis
.4bis Means to test the foam and water
pumps as well as means to realistically
test at least one foam generator should be provided. All sections of piping
should be provided with connections
for flushing, draining and purging with
air.
12 .5 The expansion ratio of the foam should
not exceed 1,000 to 1. The quantity of
foam concentrate available should be
sufficient to produce foam for the
minimum operation time specified by
the manufacturer, but not less than
30 minutes.
13 .6 Means should be provided for the crew
to safely check the quantity of foam
concentrate and take periodic control
samples for foam quality.
14 .7 Operating instructions for the system
should be displayed at each operating
position.
15 .8 Spare parts should be provided in
accordance with the manufacturer’s
instruction.
16 .9 Filling rate for the system should be
followed the results of the test to be
conducted in accordance with appendix
2. Where the volume of the machinery
space in question is more than that of
the class 3 test enclosure, the test data
of filling rate conducted in the class 3
test enclosure can be used for approval.
[The design filling rate for the system should be based on the nominal filling rate calculated on the
basis of the nominal foam expansion ratio and the
nominal application rate used during the approval
tests in accordance with appendix 2. The nominal
foam expansion ratio should be determined
according to EN 13565-1]
[The design filling rate for the system should be
adequate to completely fill the largest protected
space in [2][10] minutes or less.]
Sweden
The design filling rate should be based on the rate used in the
approval tests. Also the
maximum fill time should be 10
minutes
USA
We propose that instead of a
filling rate, a maximum filling
time of 2 minutes should bespecified for all applications
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Poland
Agree with USA
Japan
Japan considers that filling up
time should be determined,
taking the character/performance
of each fixed fire fighting
system into account. CO2
system should be filled up the
space for short time taking into
account the leakage from
dampers, etc. On the other
hand, high expansion foam andwater systems are not necessary
to fill up for shorter time, taking
into account the cooling effect
by water and fire extinguishing
scenario and that machinery
spaces are protected by “A-60”
insulation. Therefore, Japan
considers that filling rate not
less than 1 m/min is enough
requirement to the system.
Therefore Japan proposes to
retain the original text as it is.17 .10 If an internal combustion engine is
used as a prime mover for the seawater
pump for the system, the fuel oil tank
to the prime mover should contain
sufficient fuel to enable the pump to
run on full load for at least 3 hours and
sufficient reserves of fuel should be
available outside the machinery space
of category A to enable the pump to be
run on full load for an additional
15 hours. If the fuel tank serves other
internal combustion engines
simultaneously, the total fuel tank
capacity should be adequate for all
connected engines.
18 .11 Means should be provided for
automatically giving audible and visual
warning of the release of the system.
The alarms should operate for the
length of time needed to evacuate the
space, but in no case less than 20
seconds.
Norway
Propose to delete
Japan
Japan proposes to retain thisrequirement as it is, taking a risk
to the crew by foam including
combustion gases into account.
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Poland
Agree with Japan
19 .12 The arrangement of foam generatorsand piping in the protected space
should not interfere with access to the
installed machinery for routine
maintenance activities.
20 .13 The system source of power supply,
foam concentrate supply and means of
controlling the system should be
readily accessible and simple to
operate, and should be arranged at
positions outside the protected space
not likely to be cut off by a fire in the protected space.
21 Deleted
22 .14 Arrangements of foam generators
should in general be designed based on
the approval test results. The number
of generators may be different, but the
minimum filling rate determined
during approval testing should be
provided by the system.
23 .15 Foam generators should be uniformly
distributed under the uppermost ceiling
in the protected spaces including the
engine casing. Extra foam generators
may be required in obstructed
locations. The foam generators should
be arranged with at least 1 m free space
in front of the foam outlets, unless
tested with less clearance.
24 Deleted
25 .7 The piping system should be sized in
accordance with a hydraulic
calculation technique*
to ensure
availability of flows and pressures
required for correct performance of the
system.
26 .8 The control system of ventilation
fans**
, discharge alarm and oil pumps**
should be available at the position(s)where this extinguishing system is
controlled.
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27 APPENDIX 1
COMPONENT MANUFACTURING
STANDARDS FOR INSIDE AIR FOAM
SYSTEMS
Foam generators nozzles installed in the protected
space should be tested in accordance with the
following items stipulated in appendix A to
MSC/Circ.668 and generators should be tested in
accordance with the following items 1 and 6:
.1 dimension;
.2 flow constant: the value of the flow
constant K should be determined by
measuring the flow at the maximum
operational pressure, minimum
operational pressure and the middle
operational pressure;
.3 stress corrosion;
.4 sulphur dioxide corrosion: visual
inspection only may be carried out;
.5 salt spray corrosion: the test may be
carried out at NaCl concentration
of 5%. Paragraph 3.14.2 in appendix A
to MSC/Circ.668 need not to apply;
.6 resistance to heat: where the
components are made of steel, this test
need not be applied;
.7 impact test: only, the nozzles may need
to be tested; and
.8 clogging test: where the diameter of
the opening of the nozzle exceeds
[1.5 mm], this test need not apply.
[Foam generators should be tested in accordance
with the following items stipulated in EN
13565-1:
• Clause 4: General construction requirements
(4.1-connections, 4.5-corrosion resistance of
metal parts, 4.8-heat and fire resistance)
•
Clause 5: Discharge coefficients• Clause 6: Quality of foam (6.2-High-expansion
components)
Norway
This section should only apply
to foam nozzles and should be
based on revised MSC/Circ.913,
whereas a suitable set of design
requirements may be defined for
the casing.
Japan
Japan proposes that the tests
specified in paragraphs .3 and .4
should be applied to the nozzles
only, taking into account thenecessity of application of these
tests to casings and that it
is impossible to carry out
these tests for large objects such
as the casings. Additional tests
according to EN 13565-1 are not
familiar worldwide and the tests
mentioned in original ones
are enough to assess the
components. Therefore, Japan
proposes to delete “ and should
meet the requirements of clauses5 & 9 of EN 13656-1”
Sweden
Water mist nozzle component
tests are not appropriate.
Recommend using EN 13565-1
plus an added vibration test
taken from MSC/Circ.668
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• Clause 9: Components for medium and
high-expansion foam systems
Foam generators should also be able to withstand
the effects of vibration without deterioration of
their performance characteristics when tested in
accordance with (paragraph 4.16 of appendix A to
MSC/Circ.668) After the vibration test according
to (paragraph 4.16 of appendix A to
MSC/Circ.668) the generators should show no
visible deterioration and should meet the
requirements of (clauses 5 & 9 of EN13565-1)
28 APPENDIX 2
TEST METHOD FOR HIGH EXPANSION
FOAM FIRE-FIGHTING SYSTEM
1 Scope
The test method is intended for evaluating the
extinguishing performance of inside-air high-
expansion foam fire-fighting systems. System
design should be based on the conditions used
during the specified fire tests
2 Sampling
The components to be tested should be supplied
by the manufacturer together with design and
installation criteria, operational instructions,
drawings and technical data sufficient for the
identification of the components.
29 3 Fire tests
3.1 Test principles
This test procedure enables the determination of
design criteria and the effectiveness of high
expansion foam fire-extinguishing system against
spray and pool fires, which are obstructed by a
simulated engine.
3.2 Test description
3.2.1 Test enclosure
3.2.1.1 The fire extinguishing tests of the system
should be carried out using the following test
compartments:
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.1 test compartment 1: the test should be
performed in a 100 m2 room with 5 m
ceiling height and ventilation through a2 m x 2 m door opening according to
figure X (figure 2 in MSC/Circ.668).
The engine mock-up should be
designed according to figure Y
(figure 2-3 in MSC/Circ.668). The
door opening to the test compartment
may be covered during the test at the
same rate as the foam layer is building
up in the compartment to avoid foam
leakage through the door opening;
.2 test compartment 2: the test should be performed in a test compartment
having a volume of between 1,200
to 3,000 m3 and a height exceeding
7.5 m. The ventilation of the test
compartment should be as in test
compartment 1 but with four additional
1 m2
square ventilation openings
located at each corner of the ceiling.
The foam generators should not be
positioned near the ceiling openings;
and
.3 test compartment 3: the same
arrangement should be used as for test
compartment 2 but without any ceiling
in order to avoid any restrictions in air
supply. The height of the walls must be
high enough to avoid foam overflow
which will depend on the performance
of the system.
3.2.1.2 Any test enclosure should be provided
with natural or forced ventilation to ensure that
the oxygen concentration at the fire locationshould be a minimum of 20% (by volume) at the
start of the test. The ventilation should be
arranged so that fresh air from the ventilation
should not been taken into the foam generators
directly.
Sweden
Propose three different fire
scenarios to account for varyingshipboard ventilation and
configuration parameters
Japan
Japan considers that two fire
scenarios using small (500 m3)
and large (3,000-4,000 m3) test
enclosures are enough to assess
the performance of the system,
taking volume and ventilationcondition of the machinery
space, duration and cost of
approval test into account.
Furthermore, Japan considers
that the test using the
small test compartment should
be conducted to assess the affect
by smoke produced by the test
fire and the test using the
large compartment should be
conducted for confirmation of
the system performance.
Sweden
Delete the entire paragraph.
Covered by the vent conditions
in the 3 new fire test scenarios
30 3.2.2 Simulated engine
The fire test should be performed in a test
apparatus consisting of:
.1 A simulated engine of size (width x
length x height) 1 m x 3 m x 3 m
constructed of sheet steel with a
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nominal thickness of 5 mm. The
simulated engine is fitted with two
steel tubes of 0.3 m in diameter
and 3 m in length, which simulateexhaust manifolds and a grating. At the
top of the simulated engine a 3 m2
tray
is arranged (figure 1); and
.2 A floor plate system of 4 m x 6 m and
0.5 m in height surrounding the
simulated engine with a tray (4 m2
in
area), underneath (figure 1).
31 3.2.3 Test Program
The fire test should be carried out using followingfire scenarios.
.1 combination of the following fire
programs (test fuel: commercial fuel
oil or light diesel oil):
.1 low-pressure spray on top
of the simulated engine centred
with nozzle angled upward
at a 45-degree angle to strike a
12–15 mm diameter rod 1 m away;
and
.2 fire in trays under (4m2) and on top
(3m2) of the simulated engine.
.2 high-pressure horizontal spray fire on
top of the simulated engine. (Test fuel:
commercial fuel oil or light diesel oil);
.3 low pressure concealed horizontal
spray fire on the side of the simulated
engine with oil spray nozzle positioned
0.1 m in from the end of the simulated
engine and 0.1 m2
tray positioned 1.4
m in from the engine end at the inside
of floor plate. (Test fuel: commercial
fuel oil or light diesel oil); and
.4 flowing fire 0.25 kg/sec from top of
mock-up (test fuel: heptane)
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Fire type Low
pressure
High
pressure
Spray
nozzle
Wide spray
angle (120°to 125°)
full cone
type
Standard
angle(at 6 bar)
full cone
type
Nominal oil
pressure
8 bar 150 bar
Oil flow 0.16 ± 0.01
kg/s
0.050
±0.002 kg/s
Oil
temperature
20 ± 5°C 20 ± 5°C
Nominal
heat releaserate
5.8 ± 0.6
MW
1.8 ± 0.2
MW
32 3.2.4 Installation requirements for tests:
.1 foam generators should not be installed
above the simulated engine in such a
way that the foam flow directly hits the
test fires;
.2 foam generators should be installed at
the uppermost level of the space. Thedistance between the generators and
test ceiling and floor should be
recorded and reflected in the
manufacturer’s design manual; and
.3 the number and spacing of foam
generators should be in accordance
with the manufacturer’s system design
and installation manual.
33 4 Test procedure
4.1 Preparation
.1 the tray(s) used in the tests should be
filled with at least 50 mm fuel on a
water base. Freeboard should be
150±10 mm, except for the 3 m2
tray
on top of the simulated engine where
the freeboard should be 50±10 mm;
and
.2 Seawater or simulated seawater specified in paragraph 3.6.3 of
MSC/Circ.670 should be used for the
fire test, except the case where it is
Sweden
Propose alternate text
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shown that fresh water gives the same
level of performance as seawater.
Seawater or simulated seawater
specified in paragraph 3.6.3 of MSC/Circ.670 should be used for the
fire tests. However, fresh water may be
used for practical reasons if it is shown
that seawater provides the same level
of performance. This should be done
either by repeating the fresh water test
with the longest time to
extinguishment to ensure that the
minimum performance requirements is
still fulfilled or to use the small scale
test method for foam concentrates
intended for inside air systems(paragraph 3.1.3). If the system is
tested in more than one test
compartment, the seawater test should
be performed in test compartment 2
or 3.
Japan
Since paragraph 3.6.3 is widely
used as simulated seawater for foam concentration and
such seawater has been
demonstrated to produce foam
having the same level of
performance as foam produced
by seawater, additional tests
using seawater are not
necessary. Therefore, Japan
proposes to retain the original
text as it is.
34 4.2 Measurements
The following should be measured during the
test.:
.1 oil flow and pressure in the oil system;
.2 foam concentrate flow and pressure
and water flow and pressure in the
extinguishing system;
.3 oxygen concentration in the test
compartment. The sampling point
should be located 4.5 m from the
centre of the engine mock-up on the
exhaust pipe side and 2.5 m from floor
level (The measurement may be
terminated when the foam fills up to
the oxygen sampling point); and
.4 temperatures at the fire locations.
Thermocouples should be located 1 m
in front of the spray nozzles and 0.5 m
above the tray fuel surface to provide
additional information about time to
extinguishment.
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35 4.3 Pre-burn
After ignition of all fuel sources, a 2-minute pre-burn time for the tray fires and 10 to
15 seconds for the spray and heptane fires is
required before the extinguishing agent is
discharged.
Sweden
We propose a 2-minute pre-burnfor all test fires
USA
Agree with Sweden
Poland
Agree with Sweden. We also
propose a 20% design safety
factor when calculating the
required quantity of foam.
Japan
Since spray nozzles for spray
fire are located with certain
height, which is not less than
3 m, spray fire is continuously
burned until foam is filled up to
the position of the spray fire
(that is pre-burn time is
normally not less than
1.5 minutes). Therefore, Japanconsiders that pre-burn time of
10-15 seconds is enough
duration to confirm continuous
burning of spray fire.
Therefore, original text should
be retained as it is.
36 4.4 Duration of test
Extinguishing agent should be discharged for
50% of the discharge time recommended by the
manufacturer or 15 minutes whichever is less.
The oil spray, if used, should be shut of
15 seconds after the end of agent discharge. The
oil spray, if used should be shut off 30 seconds
after the fire has been judged extinguished. The
overall time to extinction may not exceed [15][5]
minutes (or 50% of the recommended discharge
time).
Sweden
Propose alternate text.
USA
Propose 5 minutes as the
maximum time to extinction.
Japan
The original text should be
retained due to the reasons
mentioned in item number 16.
37 4.5 Observations before the fire test
Temperature of the test room, fuel and thesimulated engine should be measured and
recorded.
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38 4.6 Observations during the fire test
The following observations should be recorded:
.1 start of ignition procedure;
.2 start of the test (ignition);
.3 time when the system is activated;
.4 time when the fire is extinguished;
.5 time when the system is shut off;
.6 time when the fire is re-ignited, if any;
.7 time when the oil flow for the spray
fire is shut off; and
.8 time when the test is finished.
39 4.7 Observations after fire test
The following should be recorded:
.1 damage to any system components;
.2 level of fuel in the tray(s) to make sure
that no limitation of fuel occurred
during the test; and
.3 temperatures of test room, fuel and the
simulated engine.
40 5 Classification criteria
At the end of discharge of foam and fuel at each
test, there should be no re-ignition or fire spread.
41 6 Test report
The test report should include the following
items:
.1 name and address of the test
laboratory;
.2 date and identification number of the
test report;
.3 name and address of client,
manufacturer and/or supplier of the
system;
.4 purpose of the test;
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.5 name or other identification marks of
the product;
.6 description of the test product;
.7 date of the test;
.8 test methods;
.9 drawing of each test configuration;
.10 identification of the test equipment and
instruments used (including type and
manufacturer of the foam
concentration);
.11 conclusions;
.12 deviations from the test method, if any;
.13 test results including observation and
measurement before, during and after
the test; and
.14 date and signature.
42 7 Application of Test Results
Systems that have been successfully tested to the
provisions of paragraph 3 may be installed in
different size spaces according to the following:
.1 the extinguishing system configuration
used for the test compartment 1 tests
may be applied to systems for the
protection of shipboard spaces of equal
or less volume and with restricted
airflow;
.2 the extinguishing system configurationused for the test compartment 2 tests
may be applied to systems for the
protection of shipboard spaces with
volumes and ventilation conditions
between test compartments 1 and 3
using linear interpolation; and
.3 the extinguishing system configuration
used for the test compartment 3 tests
may be applied to systems for the
protection of shipboard spaces of equal
or greater volumes and no restriction inventilation.
Sweden
Guidance is needed on
application of test results to
different size compartments.
Japan
This sentence should be deleted,
since it is impossible to apply to
ships, because it is impossible to
define the restricted airflow in
the machinery spaces.
***
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ANNEX 5
PROPOSED AMENDMENTS TO FSS CODE, CHAPTER 7
Option 1
Chapter 7 Fixed pressure water-spraying and water-mist fire-extinguishing systems
1 Application
This chapter details the specifications for fixed pressure water-spraying and water-mist
fire-extinguishing systems as required by chapter II-2 of the Convention.
2 Engineering specifications
2.1 Fixed pressure water-spraying fire-extinguishing systems
Fixed-pressure water-spraying fire-extinguishing systems for machinery spaces and cargo pump
rooms shall be approved by the Administration based on the guidelines developed by the
Organization*.
2.2 Equivalent water-mist fire-extinguishing systems
Water-mist fire-extinguishing systems for machinery spaces and cargo pump rooms shall be
approved by the Administration based on the guidelines developed by the Organization∗.
* Refer to “Revised guidelines for the approval of equivalent water-based fire-extinguishing systems for machinery spaces and cargo pump room” (MSC/Circ.1165).
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Option 2
Chapter 7 Fixed pressure water-spraying and water-mist fire-extinguishing systems
1 Application
This chapter details the specifications for fixed pressure water-spraying and water-mist
fire-extinguishing systems as required by chapter II-2 of the Convention.
2 Engineering specifications
2.1 Fixed pressure water-spraying fire-extinguishing systems
2.1.1 Nozzles and pumps
2.1.1.1 Any required fixed pressure water-spraying fire-extinguishing system in machinery
spaces shall be provided with spraying nozzles of an approved type. The system shall be
available for immediate use and capable of continuously supplying water for at least 20 minutes.
2.1.1.2 The system and its components shall be suitably designed to withstand ambient
temperature changes, vibration, humidity, shock, impact, clogging and corrosion normally
encountered in machinery spaces. Components within the protected spaces should be designed to
withstand the elevated temperatures which could occur during a fire. Components should be
tested in accordance with the listed sections of appendix A of MSC/Circ.1165, as modified
below:
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MSC/Circ.1165
appendix A, paragraph No.
Modifications
3.1 Dimensions Nozzles should be provided with a nominal 12 mm (1/2 inch) or larger inlet thread
3.4.1 Flow constant
3.4.2 Water distribution
3.4.3 Water drop size and
velocity
3.11.1 Stress corrosion
3.11.2 Sulphur dioxidecorrosion
Open nozzles should be subject to post test visual examination.The requirements of paragraph 3.14.2 are not applicable.
3.11.3 Salt spray corrosion The NaCl concentration used for the test should be [5,20%].
Following exposure, open nozzles should meet the flow constant
requirements of paragraph 3.4.1. The requirements of
paragraph 3.14.2 are not applicable.
3.12 Integrity of nozzle
coating
Applicable only if the nozzles have wax or bitumen coatings.
3.15 Resistance to heat
3.16 Resistance to vibration Open nozzles shall be subject to post test visual examination.
The requirements of paragraphs 3.5 and 3.8 are not applicable.
3.17 Impact test
3.22 Clogging test
2.1.1.2 The number and arrangement of the nozzles shall be to the satisfaction of the
Administration and shall be such as to ensure an effective average distribution of water of at
least 5 [X] l /m2
per minute in the spaces to be protected. Where increased application rates areconsidered necessary, these shall be to the satisfaction of the Administration. An indication of
areas for which increased application rates may be required is given below:
Protected area Application rate
Boiler fronts or roof, firing areas, oil fuel units,
centrifugal separators (not oily water separators),
oil purifiers and clarifiers 20 l /min
Hot oil fuel pipes near exhausts or similar heated
surfaces on main or auxiliary diesel engines 10 l /min
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2.1.1.3 Precautions shall be taken to prevent the nozzles from becoming clogged by
impurities in the water or corrosion of piping, nozzles, valves and pump.
2.1.1.4 The pump shall be capable of simultaneously supplying at the necessary pressure allsections of the system in any one compartment to be protected.
2.1.1.5 The pump may be driven by independent internal combustion machinery but, if it is
dependent upon power being supplied from the emergency generator fitted in compliance with
the provisions of regulation II-1/44 or regulation II-1/45, as appropriate, that generator shall be so
arranged as to start automatically in case of main power failure so that power for the pump
required by paragraph 2.1.1.4 is immediately available. The independent internal combustion
machinery for driving the pump shall be so situated that a fire in the protected space or spaces
will not affect the air supply to the machinery.
2.1.2 Installation requirements
2.1.2.1 Nozzles shall be fitted above bilges, tank tops and other areas over which oil fuel is
liable to spread and also above other specific fire hazards in the machinery spaces.
2.1.2.2 The system may be divided into sections, the distribution valves of which shall be
operated from easily accessible positions outside the spaces to be protected and will not be
readily cut off by a fire in the protected space.
2.1.2.3 The pump and its controls shall be installed outside the space or spaces to be
protected. It shall not be possible for a fire in the space or spaces protected by the water-spraying
system to put the system out of action.
2.1.2.4 The piping system should be sized in accordance with a hydraulic calculation
technique** to ensure availability of flows and pressures required for correct performance of the
system.
2.1.3 System control requirements
The system shall be kept charged at the necessary pressure and the pump supplying the water for
the system shall be put automatically into action by a pressure drop in the system.
** Where the Hazen-Williams Method is used, the following values of the friction factor "C" for different pipe
types which may be considered should apply:
Pipe type C
Black or galvanised mild steel 100Copper and copper alloys 150Stainless steel 150
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2.1.4 Additives
Foam concentrates suitable for extinguishing oil fires may be used to supplement the system
water supply. The quantity of foam provided shall be adequate to operate the system at fullcapacity for 20 minutes.
2.2 Equivalent water-mist fire-extinguishing systems
Water-mist fire-extinguishing systems for machinery spaces and cargo pump rooms shall be
approved by the Administration based on the guidelines developed by the Organization∗.
***
∗ Refer to the “Revised guidelines for the approval of equivalent water-based fire-extinguishing systems for machinery spaces and cargo pump rooms” (MSC/Circ.1165).
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ANNEX 6
PROPOSED AMENDMENTS TO CHAPTER 4 OF THE FSS CODE
3.2 Portable foam applicators
A portable foam applicator unit shall consist of a foam nozzle of an inductor type and
inductor capable of being connected to the fire main by a fire hose, together with a
portable tank containing at least 20 l of foam concentrate and one spare tank of foam
concentrate.
3.2.1 System Performance
3.2.1.1 The nozzle shall be capable of producing effective foam suitable for extinguishing an
oil fire, at a waterflow rate of at least 200 l pm [1.5 m3/min with the foam expansion ratio
determined in 3.2.1.2.]
3.2.1.2 The foam concentrate shall be approved by the Administration based on guidelines
developed by the Organization*.
3.2.1.3 The foam produced by the portable foam applicator unit shall have an expansion ratio
and drainage time within 10% of that determined in 3.2.1.2.
3.2.1.4 The portable foam applicator unit shall be designed to withstand ambient temperature
changes, vibration, humidity, shock, impact, clogging and corrosion normally encountered on
ships.
***
* Refer to the “Guidelines for the performance and testing criteria and surveys of low-expansion foam
concentrates for fixed fire-extinguishing systems” (MSC/Circ.582/Corr. 1).
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ANNEX 7
PROPOSED AMENDMENTS TO
GUIDELINES FOR THE APPROVAL OF FIXED AEROSOL FIRE-EXTINGUISHING
SYSTEMS EQUIVALENT TO FIXED GAS FIRE-EXTINGUISHING SYSTEMS, AS
REFERRED TO IN SOLAS 74, FOR MACHINERY SPACES (MSC/Circ.1007)
General
1 Fixed aerosol fire-extinguishing systems for use in machinery spaces of category A
equivalent to fire-extinguishing systems required by SOLAS regulation II-2/10.5 should prove
that they have the same reliability which has been identified as significant for the performance of
fixed gas fire-extinguishing systems approved under the requirements of the FSS Code,
chapter 5. In addition, the system should be shown by testing according to the appendix to have
the capability of extinguishing a variety of fires that can occur in machinery spaces.
2 Aerosol fire-extinguishing systems involve the release of a chemical agent to extinguish a
fire by interruption of the process of the fire. There are two methods considered for applying the
aerosol agent to the protected space:
.1 condensed aerosols are created in pyrotechnical generators through the
combustion of the agent charge; and
.2 dispersed aerosols that are not pyrotechnically generated and are stored in
containers with carrier agents (such as inert gases or halocarbon agents) with the
aerosol released in the space through valves, pipes and nozzles.
Definitions
3 Aerosol is a non ozone depleting fire-extinguishing medium consisting of finely divided
solid particles of chemicals released into a protected space as either condensed aerosol or
dispersed aerosol.
4 Generator is a device for creating a fire-extinguishing medium by pyrotechnical means.
5 Design application density (g/m³ ) is the mass of an aerosol forming composition per m³ of
the enclosure volume required to extinguish a specific type of fire, including a safety factor of 1.3 times the test density.
6 Agent – medium for the purpose of these guidelines, these words are interchangeable.
Principal requirements
7 The minimum agent density should be determined and verified by the full-scale testing
described in the test method, as set out in the appendix.
8 For aerosol systems, the discharge time should not exceed 120 seconds for 85% of the
design density. Systems may need to discharge in a shorter time for other reasons than for fire-extinguishing performance.
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9.1 The quantity of extinguishing agent for the protected space should be calculated at the
minimum expected ambient temperature using the design density based on the net volume of the
protected space, including the casing.
9.2 The net volume of a protected space is that part of the gross volume of the space, which is
accessible to the fire-extinguishing agent.
9.3 When calculating the net volume of a protected space, the net volume should include the
volume of the bilge, the volume of the casing and the volume of free air contained in air receivers
that in the event of a fire may be released into the protected space.
9.4 The objects that occupy volume in the protected space should be subtracted from the
gross volume of the space. They include, but are not necessarily limited to:
.1 auxiliary machinery;
.2 boilers;
.3 condensers;
.4 evaporators;
.5 main engines;
.6 reduction gears;
.7 tanks; and
.8 trunks.
9.5 Subsequent modifications to the protected space that alter the net volume of the space
should require the quantity of extinguishing agent to be adjusted to meet the requirements of this
paragraph and paragraphs 10.1, 10.2, 10.3, 10.4, 11.1, 11.2 and 11.3.
10.1 No fire suppression system should be used which is carcinogenic, mutagenic or
teratogenic at application densities expected during use. The discharge of aerosol systems toextinguish a fire could create a hazard to personnel from the natural form of the aerosol, or from
certain products of aerosol generation (including combustion products and trace gases from
condensed aerosols). Other potential hazards that should be considered for individual systems
are the following: noise from discharge, turbulence, cold temperature of vaporizing liquid,
reduced visibility, potential toxicity, thermal hazard and potential toxicity from the aerosol
generators, and eye irritation from direct contact with aerosol particles. Unnecessary exposure to
aerosol media, even at concentrations below an adverse effect level, and to their decomposition
products should be avoided.
10.2 All systems should employ two separate controls for releasing the extinguishing medium
into a protected space. Means should be provided for automatically giving visual and audiblewarning of the release of fire-extinguishing medium into any space in which personnel normally
work or to which they have access. The alarms should operate for the period of time necessary to
evacuate the space, but not less than 20 seconds before the medium is released.
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10.3 [Condensed aerosols: condensed aerosol systems for spaces that are normally occupied
should be permitted in concentrations where the aerosol particulate density does not exceed the
adverse effect level as determined by a scientifically accepted technique* and any combustion
products and trace gases produced by the aerosol generating reaction do not exceed theappropriate excursion limit for the critical toxic effect as determined in acute inhalation toxicity
tests.
10.4 Dispersed aerosols: dispersed aerosol systems for spaces that are normally occupied
should be permitted in concentrations where the aerosol particulate density does not exceed the
adverse effect level as determined by a scientifically accepted technique**. If the carrier gas is a
halocarbon, it may be used up to its NOAEL. Exposure to extinguishing agents, even at
concentrations below an adverse affect level, should not exceed 5 minutes. Unprotected
personnel should not enter a space during or after agent discharge until the protected space has
been well ventilated and cleared of residue. If a halocarbon carrier gas is to be used above its
NOAEL, means should be provided to limit exposure to no longer than the correspondingmaximum permitted human exposure time specified according to a scientifically accepted
physiologically based pharmacokinetic** (PBPK) model or its equivalent which clearly
establishes safe exposure limits both in terms of extinguishing media concentration and human
exposure time. Halocarbon agents should not be used at a gas concentration above that
determined safe for human exposure for 5 minutes. That concentration should be calculated on
the net volume of the protected space at the maximum expected temperature. If the carrier is an
inert gas, means should be provided to limit exposure to no longer than 5 minutes for inert gas
systems designed to concentrations below 43% (corresponding to an oxygen concentration
of 12%, sea level equivalent of oxygen) or to limit exposure to no longer than 3 minutes for inert
gas systems designed to concentrations between 43% and 52% (corresponding to between 12%
and 10% oxygen, sea level equivalent of oxygen).]
10.5 In no case should a dispersed aerosol system be used with halocarbon carrier gas
concentrations above the Lowest Observed Adverse Effect Level (LOAEL) nor the Approximate
Lethal Concentration (ALC) nor should a dispersed aerosol system be used with an inert gas
carrier at gas concentrations above 52% calculated on the net volume of the protected space at
the maximum expected ambient temperature, without the use of controls as provided in the
FSS Code, chapter 5, regulation 2.2.2. [and the agent storage containers should be located outside
the protected spaces in accordance with regulation II-2/10.4.3 of the Convention.]
11 The system and its components should be suitably designed to withstand ambienttemperature changes, vibration, humidity, shock, impact, clogging, electromagnetic compatibility
and corrosion normally encountered in machinery spaces. Generators in condensed aerosol
systems should be designed to prevent self-activation at a temperature below 250°C.
* Reference is made to the United States’ EPA’s Regional Deposited Dose Ratio Program in the “Methods of Derivation of Inhalation Reference Concentrations and Application of Inhalation Dosimetry”EPA/600/8-90/066F, October 1994.
** Refer to document FP 44/INF.2 – Physiologically based pharmacokinetic model to establish safe exposure
criteria for halocarbon fire extinguishing agents.
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12 The system and its components should be designed, manufactured and installed in
accordance with standards acceptable to the Organization. As a minimum, the design and
installation standards should cover the following elements:
.1 safety:
.1 toxicity;
.2 noise, generator/nozzle discharge;
.3 decomposition products; and
.4 obscuration;
.2 storage container design and arrangement:
.1 strength requirements;
.2 maximum/minimum fill density, operating temperature range;
.3 pressure and weight indication;
.4 pressure relief; and
.5 agent identification, production date, installation date and hazard
classification;
.3 agent supply, quantity, quality standards, shelf life and service life of agent and
igniter;
.4 handling and disposal of generator after service life;
.5 pipes and fittings:
.1 strength, material properties, fire resistance; and
.2 cleaning requirements;
.6 valves:
.1 testing requirements; and
.2 elastomer compatibility;
.7 generators/nozzles:
.1 height and area testing requirements; and
.2 elevated temperature resistance;
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.8 actuation and control systems:
.1 testing requirements; and
.2 back-up power requirements;
.9 alarms and indicators:
.1 predischarge alarm, agent discharge alarms and time delays;
.2 supervisory circuit requirements;
.3 warning signs, audible and visual alarms; and
.4 annunciation of faults;
.10 enclosure integrity and leakage requirements:
.1 enclosure leakage;
.2 openings; and
.3 mechanical ventilation interlocks;
.11 design density requirements, total flooding quantity;
.12 agent flow calculation:
.1 verification and approval of design calculation method;
.2 fitting losses and/or equivalent length; and
.3 discharge time;
.13 inspection, maintenance, service and testing requirements; and
.14 handling and storage requirements for pyrotechnical components.
13 The generator/nozzle type, maximum generator/nozzle spacing, maximum
generator/nozzle installation height and minimum generator/nozzle pressure should be within
limits tested.
14 Installations should be limited to the maximum volume tested.
15 Agent containers may be stored within a protected machinery space if the containers are
distributed throughout the space and the provisions of MSC/Circ.848, paragraph 11, as
applicable, are met, except that the arrangement of generators, containers, electrical circuits and piping essential for the release of any system should be such that in the event of damage to any
one power release line through fire or explosion in the protected space (i.e. a single fault
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concept), at least the design density of the fire-extinguishing charge as required in paragraph 10
above can still be discharged having regard to the requirement for uniform distribution of
medium throughout the space.
16 The release of an extinguishing agent may produce significant over and under
pressurization in the protected space. Measures to limit the induced pressures to acceptable
limits may have to be provided.
17 For all ships, the fire-extinguishing system design manual should address recommended
procedures for the control of products of agent decomposition. The performance of
fire-extinguishing arrangements on passenger ships should not present health hazards from
decomposed extinguishing agents, (for example, on passenger ships, the decomposition products
should not be discharged in the vicinity of assembly stations).
18 Spare parts and operating and maintenance instructions for the system should be providedas recommended by the manufacturer.
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TEST METHOD FOR FIRE TESTING OF FIXED
AEROSOL FIRE-EXTINGUISHING SYSTEMS
1 Scope
1.1 This test method is intended for evaluating the extinguishing effectiveness of fixed
aerosol fire-extinguishing systems for the protection of machinery spaces of category A.
1.2 The test method is applicable to aerosols and covers the minimum requirements for
fire-extinguishing.
1.3 The test programme has two objectives:
.1 establishing the extinguishing effectiveness of a given agent at its tested
concentration; and
.2 establishing that the particular agent distribution system puts the agent into the
enclosure in such a way as to fully flood the volume to achieve an extinguishing
concentration at all points.
2 Sampling
The components to be tested should be supplied by the manufacturer together with design and
installation criteria, operational instructions, drawings and technical data sufficient for the
identification of the components.
3 Method of test
3.1 Principle
This test procedure is intended for the determination of the effectiveness of different aerosol
agent extinguishing systems against spray fires, pool fires and class A fires.
3.2 Apparatus
3.2.1 Test room
The tests should be performed in 100 m2 room, with no horizontal dimension less than 8 m, with
a ceiling height of 5 m. The test room should be provided with a closable access door measuring
approximately 4 m2 in area. In addition, closable ventilation hatches measuring at least 6 m2 in
total area should be located in the ceiling. Larger room may be employed if approvals are sought
for larger volumes.
3.2.2 Integrity of test enclosure
The test enclosure should be nominally leaktight when doors and hatches are closed. The
integrity of seals on doors, hatches and other penetrations (for example, instrumentation access ports) should be verified before each test.
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3.2.3 Engine mock-up:
.1 an engine mock-up of size (width x length x height) 1 m x 3 m x 3 m should be
constructed of sheet steel with a nominal thickness of 5 mm. The mock-up should be fitted with two steel tubes diameter 0.3 m and 3 m length that simulate exhaust
manifolds and a solid steel plate. At the top of the mock-up, a 3 m 2 tray should be
arranged (figures 1, 2 and 3); and
.2 a floor plate system 4 m x 6 m x 0.75 m high should surround the mock-up.
Provision should be made for placement of the fuel trays, as described in table 1,
and located as described in table 2.
3.2.4 Instrumentation
Instrumentation for the continuous measurement and recording of test conditions should beemployed. The following measurements should be made:
.1 temperature at three vertical positions (for example, 1 m, 2.5 m and 4.5 m);
.2 enclosure pressure;
.3 gas sampling and analysis, at mid-room height, for oxygen, carbon dioxide,
carbon monoxide and other relevant products;
.4 means of determining flame-out indicators;
.5 fuel nozzle pressure in the case of spray fires;
.6 fuel flow rate in the case of spray fires;
.7 discharge nozzle pressure; and
.8 means of determining generator discharge duration.
3.2.5 Generators/nozzles
3.2.5.1 For test purposes, generators/nozzles should be located within 1 m of the ceiling.
3.2.5.2 If more than one generator/nozzle is used, they should be symmetrically located.
3.2.6 Enclosure temperature
The ambient temperature of the test enclosure at the start of the test should be noted and serve as
the basis for calculating the concentration that the agent would be expected to achieve at that
temperature and with that agent weight applied in the test volume.
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3.3 Test fires and programme
3.3.1 Fire types
The test programme, as described in table 3, should employ test fires as described in table 1
below.
Table 1
Parameters of test fires
Fire Type Fuel Fire size, MW Remarks
A 76 - 100 mm ID can Heptane 0.0012 to 0.002 Tell tale
B 0.25 m2
tray Heptane 0.35
C 2 m2 tray Diesel /Fuel oil 3 (Note 1)
D 4 m2
tray Diesel /Fuel oil 6 (Note 1)
E Low pressure, low flow
spray
Heptane
0.03 ± 0.005 kg/s
1.1
F Wood crib Spruce or fir 0.3 (Note 2)
G 0.10 m2 tray Heptane 0.14
Notes:
1 Diesel/Fuel oil means light diesel or commercial fuel oil.
2 The wood crib should be substantially the same as described in ISO Standard 14520,
“Gaseous fire extinguishing systems, Part 1: General Requirements (2000)”. The crib shouldconsist of six, trade size 50 mm x 50 mm by 450 mm long, kiln dried spruce or fir lumber having
a moisture content between 9% and 13%. The members should be placed in 4 alternate layers at
right angles to one another. Members should be evenly spaced forming a square structure. Ignition of the crib should be achieved by burning commercial grade heptane in a square steel
tray 0.25 m2 in area. During the pre-burn period the crib should be placed centrally above the top
of the tray a distance of 300 to 600 mm.
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Table 2
Spray fire test parameters
Fire type Low pressure,
Low flow(E)
Spray nozzle Wide spray angle (80°)
full cone type
Nominal fuel pressure 8.5 Bar
Fuel flow 0.03 + 0.005 kg/s
Fuel temperature 20 + 5°C
Nominal heat release rate
1.1 + 0.1 MW
3.3.2 Test programme
3.3.2.1 The fire test programme should employ test fires singly or in combination, as
outlined in table 3 below.
Table 3
Test programme
Test No. Fire combinations (table 1)
1 A: Tell tales, 8 corners. (See note).
2 B: 0.25 m2
heptane tray under mock-up
G: 0.10 m2
heptane tray on deck plate located below solid steel
obstruction plate
Total fire load: 0.49 MW
3 C: 2 m2
diesel/fuel oil tray on deck plate located below solid steel
obstruction plate
F: Wood crib positioned as in figure 1
E: Low pressure, low flow horizontal spray - concealed - with
impingement on inside of engine mock-up wall.
Total fire load: 4.4 MW
4 D: 4 m2
diesel tray under engine mock-up
Total fire load: 6 MW
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Notes:
Tell-tale fire cans should be located as follows:
.1 in upper corners of enclosure 150 mm below ceiling and 50 mm from each wall;
and
.2 in corners on floors 50 mm from walls.
3.3.2.2 All applicable tests of table 3 should be conducted for every new fire-extinguishing
media.
3.3.2.3 Only test 1 is required to evaluate new nozzles and related distribution system
equipment (hardware) for systems employing fire-extinguishing media that have successfully
completed the requirements of paragraph 3.3.2.2. Test 1 should be conducted to establish andverify the manufacturer's minimum nozzle design pressure.
3.4 Extinguishing system
3.4.1 System installation
The extinguishing system should be installed according to the manufacturer's design and
installation instructions. The maximum vertical distance should be limited to 5 m.
3.4.2 Agent
3.4.2.1 Design density
The agent design density is the net mass of extinguishant per unit volume (g/m3) required by the
system designer for the fire protection application.
3.4.2.2 Test density
The test density of agent to be used in the fire-extinguishing tests should be the design density
specified by the manufacturer, except for test 1, which should be conducted at not more than 77%
of the manufacturer’s recommended design density.
3.4.2.3 Quantity of aerosol agent
The quantity of aerosol agent to be used should be determined as follows:
W = V x q (g),
where:
W = agent mass (g);
V = volume of test enclosure (m3);
q = fire-extinguishing aerosol density (g/m3).
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3.5 Procedure
3.5.1 Fuel levels in trays
The trays used in the test should be filled with at least 30 mm fuel on a water base. Freeboard
should be 150 ± 10 mm.
3.5.2 Fuel flow and pressure measurements
For spray fires, the fuel flow and pressure should be measured before and during each test.
3.5.3 Ventilation
3.5.3.1 Pre-burn period
During the pre-burn period the test enclosure should be well ventilated. The oxygen
concentration, as measured at mid-room height, should not be less than 20 volume per cent at the
time of system discharge.
3.5.3.2 End of pre-burn period
Doors, ceiling hatches and other ventilation openings should be closed at the end of the pre-burn
period.
3.5.4 Duration of test
3.5.4.1 Pre-burn time
Fires should be ignited such that the following burning times occur before the start of agent
discharge:
.1 sprays - 5 to 15 seconds;
.2 trays - 2 minutes; and
.3 crib - 6 minutes.
3.5.4.2 Discharge time
Aerosol agents should be discharged at a rate sufficient to achieve 85% 100% of the minimum
design density in 120 seconds or less.
3.5.4.3 Hold time
After the end of agent discharge the test enclosure should be kept closed for 15 minutes.
3.5.5 Measurements and observations
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3.5.5.1 Before test:
.1 temperature of test enclosure, fuel and engine mock-up;
.2 initial weights of agent containers;
.3 verification of integrity agent distribution system and nozzles; and
.4 initial weight of wood crib.
3.5.5.2 During test:
.1 start of the ignition procedure;
.2 start of the test (ignition);
.3 time when ventilating openings are closed;
.4 time when the extinguishing system is activated;
.5 time from end of agent discharge;
.6 time when the fuel flow for the spray fire is shut off;
.7 time when all fires are extinguished;
.8 time of re-ignition, if any, during hold time;
.9 time at end of hold time; and
.10 at the start of test initiate continuous monitoring as per 3.2.4.
3.5.6 Tolerances
Unless otherwise stated, the following tolerances should apply:
.1 length ±2% of value;
.2 volume ±5% of value;
.3 pressure ±3% of value;
.4 temperature ±5% of value; and
.5 concentration ±5% of value.
These tolerances are in accordance with ISO Standard 6182/1, February 1994 edition 4.
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4 Classification criteria
4.1 Class B fires should be extinguished within 30 seconds of the end of agent the 2-minute
discharge. At the end of the hold period there should be no re-ignition upon opening theenclosure.
4.2 The fuel spray should be shut off 15 seconds after extinguishments. At the end of the
hold time, the fuel spray should be restarted for 15 seconds prior to reopening the door and there
should be no re-ignition.
4.3 The ends of the test fuel trays should contain sufficient fuel to cover the bottom of the
tray.
4.4 Wood crib weight loss should be no more than 60%.
4.5 A re-ignition test should be conducted after the successful extinguishments of the tell-tale
fires in test 1 (Fire A) within 30 seconds after completion of agent the 2-minute discharge. The
test should involve the attempted ignition of two of the tell-tale fire containers. One container
should be at the floor level and the other at the ceiling level at the diagonally opposite corner. At
10 minutes after extinguishment of the fires, a remotely operated electrical ignition source should
be energized for at least 10 seconds at each container. The test should be repeated at one
two minutes intervals four two more times, the last at 14 minutes after extinguishment.
Sustained burning for 30 seconds or longer of any of these ignition attempts constitutes a re-
ignition test failure.
5 Test report
The test report should include the following information:
.1 name and address of the test laboratory;
.2 date and identification number of the test report;
.3 name and address of client;
.4 purpose of the test;
.5 method of sampling system components;
.6 name and address of manufacturer or supplier of the product;
.7 name or other identification marks of the product;
.8 description of the tested product:
.1 drawings;
.2 descriptions;
.3 assembly instructions;
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.4 specification of included materials; and
.5 detailed drawing of test set-up;
.9 date of supply of the product;
.10 date of test;
.11 test method;
.12 drawing of each test configuration;
.13 identification of the test equipment and used instruments;
.14 conclusions;
.15 deviations from the test method, if any;
.16 test results including measurements and observations during and after the test; and
.17 date and signature.
***
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ANNEX 8
PROPOSED AMENDMENTS TO REVISED GUIDELINES FOR THE APPROVAL OF
FIXED WATER-BASED LOCAL APPLICATION FIRE-FIGHTING SYSTEMS
(ANNEX TO MSC/CIRC.913)
1 Amend paragraph 2.3 of annex 2 of document FP 48/WP.4 as follows:
“2.3 Protected area: an area (an installation or part of an installation) within a
protected space which is required to be protected by the system.
For internal combustion machinery, typical protected areas are hot surfaces such as
exhaust pipes without insulation, or with insulation fitted in accordance with
SOLAS regulation II-2/4.2.2.6.1 that is likely to be removed frequently for maintenance,
and high-pressure fuel oil systems installed near hot surfaces. For typical diesel engines,
such areas would include the area on top of the engine, the fuel injection pumps and turbochargers, unless the fuel injection pumps are installed in a sheltered location beneath the
steel platform.
For boiler fronts and oil-fired inert gas generators, typical protected areas are hot surfaces
around the burners without insulation, or with insulation fitted in accordance with
SOLAS regulation II-2/4.2.2.6.1 that is likely to be removed frequently for maintenance.
For incinerators, typical protected areas are hot surfaces around the burners without
insulation, or with insulation fitted in accordance with SOLAS regulation II-2/4.2.2.6.1
that is likely to be removed frequently for maintenance.”
2 Amend paragraph 3.11 of annex 2 of document FP 48/WP.4 as follows:
“3.11 The system may be grouped into separate sections within a protected space. The
capacity and design of the system should be based on the zone section demanding the
greatest volume of water. In any case the minimum capacity should be adequate for a
single zone section protecting the largest single engine, diesel generator or piece of
machinery.”
3 Amend paragraph 3.15.2 of annex 2 of document FP 48/WP.4 as follows:
“.2 the system release should be controlled by [a combination of flame and smoke
detectors] [a detection system capable of reliably identifying the local sections].
Consideration should be given to prevent accidental release. The detection system should
provide an alarm upon activation of any single detector and discharge if two or more
detectors activate. The area of coverage of the detection system zones sections should
correspond to the area of coverage of the extinguishing system zones sections. Grouped
visual and audible alarms, as well as indication of the activated section, should be
provided in each protected space, in the engine control room and in the wheelhouse.
Audible alarms may use a single tone.”
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4 Amend paragraph 3.19 of annex 2 of document FP 48/WP.4 as follows:
“3.19 Appropriate operational measures or interlocks should be provided if the engine
room is fitted with a fixed high-expansion foam or aerosol fire fighting system, to preventthe local application system from interfering with the effectiveness of the foam these
systems.”
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