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Sec.2: Design Principles and Accidental Loads [Table of Contents] Sec.4: Hazardous Area Classification

DNV-OS-A101 Safety Principles and Arrangements

[-] Sec.3: Arrangement

SECTION 3
Arrangement

Sec.3
A. General

Sec.3
A 100   Objective

Sec.3 A
101
   The provisions of this section aim to avoid or reduce the effects of hazards on the unit or installation, by means of safe general arrangement of structures, plants and facilities.

Sec.3
A 200   Application

Sec.3 A
201
   The requirements of this section shall be applied to all units and installations. Additional, specific requirements for arrangement of different unit types are given as indicated in Table A1.

Sec.3 A
Table A1 Additional requirements 
Reference Unit type 
Sec.7 Special provisions for floating production and/or storage units 
Sec.8 Special provisions for drilling units 
Sec.9 Special Provisions for LNG Import and Export Terminals (and LNG Production Units) 

Sec.3
B. Segregation of Areas

Sec.3
B 100   General

Sec.3 B
101
   The unit or installation shall be divided into different areas according to the type of activities that will be carried out and the associated hazard potential.

Sec.3 B
102
   Areas of high risk potential shall be segregated from areas of low risk potential, and from areas containing important safety functions. Incident escalation between areas shall be avoided.

Sec.3 B
103
   Accommodation and other areas important for safety, such as control stations, shall be located in areas classified as non-hazardous by location, and as far as practicable away from hazardous areas for hydrocarbon processing, hydrocarbon storage, wellheads, risers and drilling. The effect of prevailing winds and potential for segregation by less hazardous areas shall also be considered for area protection.

Sec.3 B
104
   Use of firewalls, blast walls, cofferdams etc. shall be considered in cases where segregation by physical distance is not sufficient.

Sec.3 B
105
   Where control stations or control functions are located in LER/LIRs outside the accommodation block/safe area special precautions against gas ignition related to gas detection, ventilation and shutdown will need to be provided.

Sec.3
C. General Arrangement

Sec.3
C 100   General

Sec.3 C
101
   Where practicable, the orientation of the unit or installation, with respect to wind direction, shall aim to avoid smoke or gas impairment of escape, muster and evacuation areas.

Sec.3 C
102
   Equipment shall be arranged with a view to providing:
safe escape from working areas
efficient ventilation of hazardous areas
minimal explosion overpressure in case of ignited gas release
access for fire fighting and emergency response
prevention of serious consequences from dropped objects
facilitation of well operations and control in normal and emergency situations
minimal possibility for escalation of fires and other failures or accidents
safe containment of accidental release of hazardous liquids
planned simultaneous operations.

Sec.3
D. Location of Plants and Equipment

Sec.3
D 100   Location of safety systems

Sec.3 D
101
   Important safety systems and controls shall be located such that they can remain operational during the defined accidental events. Controls for safety systems shall be located where they are accessible and available for safe, simultaneous use during an emergency.

Sec.3 D
102
   Where redundant safety equipment is used in meeting 101, this shall not be vulnerable to the same accidental events as the main system.

Sec.3 D
103
   The emergency and UPS systems and associated controls etc. shall be self-contained, and located such that they are not vulnerable to events that affect main power supply.

Sec.3 D
104
   The bridge of mobile installations intended for self propelled transit shall be located and arranged to provide sufficient field of vision for safe navigation and manoeuvring. The requirements in SOLAS Regulation V/22 or MODU Code 14.7 apply.

Sec.3 D
105
   Field control panels and energy or actuation sources for well control equipment, pipeline and riser ESD valves shall be protected from dimensioning accidental events such as fire, explosion and mechanical impact, to ensure emergency operation of the barrier as necessary.

Sec.3
D 200   Location of risers and ESD valves

Sec.3 D
201
   Risers shall be located to avoid damage e.g. by fire, explosion or impact from dropped objects.

Sec.3 D
202
   Riser ESD valves shall be located in easily accessible, open, well-ventilated areas, to avoid damage from wave impact and dimensioning accidental events such as fire, explosion and mechanical impact.

Sec.3
D 300   Location of air intakes and other openings

Sec.3 D
301
   Intakes for ventilation and combustion air shall be located to avoid ingress of hazardous substances. Such intakes shall be outside hazardous area.

Sec.3 D
302
   Exhausts from combustion equipment and ventilation systems shall be located to avoid cross contamination of air inlets.

Sec.3 D
303
   Openings, such as windows, doors, and ventilation ducts, shall normally be avoided in boundaries between main areas. In particular this applies to openings in accommodation spaces, control stations and other areas important for safety which face areas for hydrocarbon processing, hydrocarbon storage, wellheads, risers or drilling.

Sec.3 D
304
   External entrances to areas important for safety shall be provided with air locks if located where smoke or gas ingress is possible during an emergency.

Sec.3 D
305
   Requirements for freeboard to prevent uncontrolled flooding through openings in watertight barriers are given in DNV-OS-C301.

Sec.3
D 400   Fired heaters, combustion engines and hot surfaces

Sec.3 D
401
   Fired heaters and combustion engines shall normally be located at a safe distance from hazardous areas. Special precautions shall be taken where such items could cause ignition of accidental gas or liquid release. This could include use of gas tight enclosures, overpressure ventilation, gas detection and automatic isolation, insulation or cooling of hot surfaces etc.

Sec.3 D
402
   Other requirements for protection of hot surfaces are presented in DNV-OS-D101.

Sec.3 D
403
   Where fired heaters and combustion engines are located in the vicinity of hazardous areas, the potential for an incident to escalate from such equipment to the hazardous area shall be minimised, e.g. through use of segregation and/or fire barriers.

Sec.3 D
404
   The potential consequences of high-energy missiles from gas turbines shall be considered in relation to location of equipment. Damage to safety functions and associated controls shall be avoided.

Sec.3
D 500   Location of flares and vents

Sec.3 D
501
   Flares, burner booms, engine exhausts and other similar ignition sources shall be located to avoid ignition of normal or accidental gas releases. Use of dispersion calculations should be considered.

Sec.3 D
502
   The flare and vent systems shall comply with API RP 521 or equivalent. The radiant heat intensities or emissions from flares and vent systems shall not exceed the following limits:
6.3 kW/m2 (2000 Btu/hr/ft2) in areas where emergency actions lasting up to one minute may be required by personnel without shielding but with appropriate clothing
4.7 kW/m2 (1500 Btu/hr/ft2 in areas where emergency actions lasting several minutes may be required by personnel without shielding but with appropriate clothing
1.6 kW/m2 (500 Btu/hr/ft2) at any location where personnel are continuously exposed
temperature rating of electrical and mechanical equipment
50% LEL at any point on the installation where the gas plume from a vent could be ignited or personnel could get into contact with the gas. The most unfavourable weather and process conditions have to be taken into consideration when calculating heat radiation and dispersion.

The limits above also apply to abnormal conditions (e.g. flame out of flare system and accidental ignition of vent).

Sec.3
E. Storage of Hazardous Substances and Cryogenic Liquids

Sec.3
E 100   General

Sec.3 E
101
   Stores for hazardous substances shall be segregated from, and located at a safe distance from accommodation spaces and control stations. Indoor storage areas are to have access from open deck and have efficient ventilation.

Sec.3 E
102
   Equipment for storage and handling of cryogenic liquids (e.g. liquid nitrogen) shall be located in open areas with efficient natural ventilation. Equipment with potential for significant leakage shall be located in a bunded area, which is constructed of materials suitable for sustaining low temperatures. Reference also Sec.9 dealing with LNG terminals

Sec.3
F. Cranes and Lay Down Areas

Sec.3
F 100   General

Sec.3 F
101
   Cranes and lay down areas shall be located so as to minimise the risk of load handling or dropped object damage to systems and structures.

Sec.3 F
102
   The need for load handling above pressurised hydrocarbon equipment, hazardous inventories, and equipment important for safety shall be avoided as far as possible. Suitable impact protection shall be provided where such lifting cannot be avoided.

Sec.3 F
103
   Lay down areas shall normally be located in non-hazardous areas and provided with heavy-duty barriers to prevent damage to adjacent equipment. On floating installations, necessary points for securing of deck loading shall be provided.

Sec.3
G. Other Requirements

Sec.3
G 100   General

Sec.3 G
101
   The helicopter deck shall be located with a view to minimising hazards from obstructions, turbulence, gas vents or exhaust plumes, whilst providing a good approach path during prevailing weather conditions. The helicopter shall not be required to cross the unit or installation during such approaches.

Sec.3 G
102
   Major hydrocarbon inventory areas, e.g. wellhead, drill floor, riser and tank deck areas shall be arranged to allow efficient external fire fighting assistance.
Sec.2: Design Principles and Accidental Loads [Table of Contents] Sec.4: Hazardous Area Classification