OPTIMISING FIRE PROTECTION FOR AN OFFSHORE PLATFORM
20190209882 · 2019-07-11
Inventors
Cpc classification
B63B35/4413
PERFORMING OPERATIONS; TRANSPORTING
A62C2/04
HUMAN NECESSITIES
B63B43/00
PERFORMING OPERATIONS; TRANSPORTING
B63B2043/003
PERFORMING OPERATIONS; TRANSPORTING
International classification
A62C2/04
HUMAN NECESSITIES
E02B17/00
FIXED CONSTRUCTIONS
Abstract
An offshore oil and gas platform 14, 16 has equipment and piping associated with an oil and gas installation. A method for optimising fire protection for the platform 14, 16 comprises: arranging the platform 14, 16 to have an evacuation time of at most 15 minutes or less using one or more evacuation route(s) via a gangway or bridge 136 allowing personnel to escape to a vessel or to another platform 14, 16; determining a maximum evacuation time for the platform 14, 16; assessing the risk to personnel using the evacuation route(s) in accordance with the determined maximum evacuation time in the event of a fire; and providing passive fire protection to equipment and/or piping on the platform 14, 16 in order to prevent escalation of the fire that would create a risk to personnel on the evacuation route(s) during the determined evacuation time.
Claims
1. A method for optimising fire protection for an offshore oil and gas platform, the platform having equipment and piping associated with an oil and gas installation, the method comprising: arranging the platform to have an evacuation time of at most 15 minutes or less using one or more evacuation route(s) via a gangway or bridge allowing personnel to escape to a vessel or to another platform; determining a maximum evacuation time for the platform; assessing the risk to personnel using the evacuation route(s) in accordance with the determined maximum evacuation time in the event of a fire; and providing passive fire protection to equipment and/or piping on the platform in order to prevent escalation of the fire that would create a risk to personnel on the evacuation route(s) during the determined maximum evacuation time.
2. A method as claimed in claim 1, wherein the passive fire protection is provided only to the extent required to prevent escalation of the fire that would create a risk to personnel on the evacuation route(s) during the determined maximum evacuation time.
3. A method as claimed in claim 2, wherein there is no further passive fire protection on the platform.
4. A method as claimed in claim 1, 2 or 3, wherein there is no active fire protection on the platform.
5. A method as claimed in any preceding claim, wherein the platform is an unmanned platform with no permanent personnel.
6. A method as claimed in any preceding claim, wherein the platform is an unmanned platform and has no provision of facilities for personnel to stay on the platform, for example there may be no shelters for personnel, no toilet facilities, no drinking water, no personnel operated communications equipment, no heli-deck and/or no lifeboat.
7. A method as claimed in any preceding claim, wherein the platform is an unmanned platform and requires personnel to be present for fewer than 10,000 maintenance hours per year.
8. A method as claimed in any preceding claim, wherein the evacuation route(s) make use of a Walk to Work system.
9. A method as claimed in any preceding claim, wherein the evacuation route(s) include different routes from different locations on the platform to an escape point via the gangway or bridge and the method includes identifying multiple possible evacuation routes for the different locations for personnel on the platform in order to find the maximum evacuation time.
10. A method as claimed in any preceding claim, comprising arranging the platform to have a maximum evacuation time of 10 minutes or below, optionally about 7 minutes or below.
11. A method as claimed in claim 10, wherein the maximum evacuation time is reduced by reducing the size of the decks of the platform, minimising the height between decks, reducing the number of decks, and/or arranging the decks for direct access to exit each deck toward the escape route.
12. A method as claimed in any preceding claim, wherein the maximum evacuation time is calculated based on assessing the nature of each part of the longest evacuation route, allocating a time required for a person to traverse each part of the evacuation route, and summing the times; and wherein the time required for a person to traverse each part of a route may be based on the length/distance for the route and on set speeds for different types of route based on evacuation of an injured person.
13. A method as claimed in claim 12, wherein in addition to the time required to move from a location to a safe distance from the platform via an evacuation route the method includes adding a time allowance for personnel to evaluate and understand the situation before a decision to escape the platform is made and/or a time allowance for personnel to evaluate and address injuries to other personnel before evacuating along with the injured personnel.
14. A method as claimed in any preceding claim, including determining the maximum evacuation time using one or more of: a speed for a person crossing a deck, for example a speed in the range of 0.3 to 0.7 m/s for an injured person being evacuated across a flat deck; a speed for an injured person evacuating via ascending or descending stairs, for example a speed in the range of 0.1 to 0.3 m/s; a speed for an injured person evacuating via ascending or descending ladders, for example a speed in the range of 0.05 to 0.2 m/s; and/or a set time for particular actions during the evacuation, such as opening a barrier, boarding a vessel and/or detaching the vessel from the platform.
15. A method as claimed in any preceding claim, including isolation of a hydrocarbon inventory on the platform during a fire.
16. A method as claimed in any preceding claim, wherein the platform has five decks or fewer.
17. A method as claimed in any preceding claim, wherein the vertical extent between the uppermost deck and the deck from which personnel may exit the platform is at most 40 m.
18. A method as claimed in any preceding claim, wherein all decks of the platform have a maximum length and/or width of less than 30 m.
19. A method as claimed in any preceding claim, wherein the platform has no mechanism for depressurisation of its hydrocarbon inventory in the event of a fire and the equipment and piping on the platform is hence left at operating pressure in the event of a fire.
20. A platform for an offshore oil and gas installation, the platform comprising: equipment and piping associated with the oil and gas installation; a gangway and/or a bridge for connecting the platform to a vessel and/or another platform; and passive fire protection for at least some of the equipment and/or piping; wherein the platform is arranged to have an evacuation time of at most 15 minutes or less using one or more evacuation route(s) via the gangway or bridge allowing personnel to escape to a vessel or to another platform; and wherein the passive fire protection is installed on the equipment and/or piping in order to prevent escalation of the fire that would create a risk to personnel on the evacuation route(s) during a determined maximum evacuation time.
21. A platform as claimed in claim 20, being arranged as defined in any of claims 1 to 19.
22. A platform as claimed in claim 20 or 21, wherein passive fire protection is provided only to the extent required to prevent escalation of the fire that would create a risk to personnel on the evacuation route(s) during the determined maximum evacuation time and there is no further passive fire protection on the platform.
23. A platform as claimed in claim 20, 21 or 22 wherein there is no active fire protection on the platform.
24. A platform as claimed in any of claims 19 to 23, wherein the platform has five decks or fewer.
25. A platform as claimed in any of claims 19 to 24, wherein the vertical extent between the uppermost deck and the deck from which personnel may exit the platform is at most 40 m.
26. A platform as claimed in any of claims 19 to 25, wherein all decks of the platform have a maximum length and/or width of less than 30 m.
27. A platform as claimed in any of claims 19 to 26, wherein the platform is an unmanned platform with no permanent personnel, wherein the unmanned platform has no provision of facilities for personnel to stay on the platform, for example there may be no shelters for personnel, no toilet facilities, no drinking water, no personnel operated communications equipment, no heli-deck and/or no lifeboat; and/or wherein the unmanned platform is arranged such that personnel are required to be present for fewer than 10,000 maintenance hours per year.
28. A platform as claimed in any of claims 19 to 27, comprising isolation valves arranged to isolate the hydrocarbon inventory of the platform from external hydrocarbons in the event of a fire.
29. A platform as claimed in any of claims 19 to 28, wherein the platform has no mechanism for depressurisation of its hydrocarbon inventory in the event of a fire and the equipment and piping on the platform is hence left at operating pressure in the event of a fire.
Description
[0036] Certain embodiments of the present invention will now be described in greater detail by way of example only and with reference to the accompanying drawings in which:
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[0045]
[0046] The following is described in the context of a possible field development 10. A 6-slots subsea production system (SPS) 12 is proposed at a first remote site, A. Approximately 12 km away, within a second remote site, B, is proposed an Unmanned Wellhead Platform (UWP) 14 and an Unmanned Processing Platform (UPP) 16.
[0047] The distance between remote site A and remote site B is approximately 12 km, while the distance from remote site B to the tie-in point at a host pipeline is approximately 34 km. A schematic illustration of the pipeline systems is shown in
[0048] Oil, gas and water from the reservoir of remote site A are produced to the SPS 12. The well fluid is transported through an insulated and heat traced pipe-in-pipe pipeline 18 to remote site B. The UPP subsea and topside facility 16 at remote site B is protected from the high well shut-in pressure by a subsea high-integrity pressure protection system (HIPPS) system 20.
[0049] Oil, gas and water from the reservoir of remote site B are produced to the UWP 14. The UPP subsea and topside facility 16 is protected from the high well shut-in pressure by a topside HIPPS system 22 on the UWP 14.
[0050] Injection of water for pressure support is planned for the reservoirs of both remote site A and remote site B via respective water injection pipelines 24, 26.
[0051] Produced fluid from remote site A and remote site B is mixed upstream of a subsea separator 30. The subsea separator 30 is a three phase separator operating at approximately 40 bar initially. The temperature in the separator 30 is high (90 C.) and good separation is expected.
[0052] Oil and water leaving the separator 30 is metered by a multiphase flow meter 32 and exported to a host 34. The receiving pressure at the host 34 will be kept at the same pressure as the subsea separator 30 to avoid flashing and multiphase flow in the export pipeline or inlet heater at the host 34. The oil is only partly stabilized in the subsea separator 30, and further stabilization to pipeline export specification is assumed at the host 34.
[0053] The subsea separator 30 and pumps (not shown) are provided as a subsea separator and booster station (SSBS) 29, which is located as close to the UPP 16 as possible to minimize condensation and liquid traps in the gas piping from the separator 30 to the UPP 16.
[0054] An umbilical 50 connects the UPP 16 to the host 34. The umbilical provides remote control of the operations of the UPP 16, as well as of the operations of the SPS 12, UWP 14 and SSBS 29 via secondary umbilicals 52, 54, 56. The secondary umbilicals 52, 54, 56 also supply any required power and chemicals required from the UPP 16 to the SPS 12, UWP 14 and SSBS 29.
[0055] Gas at 40 bar is delivered from the separator 30 to the UPP 16 topside inlet cooler 36 through a dedicated riser 38. The inlet cooler 36 comprises a seawater-cooled shell and tube heat exchanger. TEG is injected into the gas for hydrate inhibition before cooling the gas to 20 C. in the seawater-cooled shell and tube inter stage cooler 36. Condensed water and hydrocarbons are removed in a downstream scrubber 37.
[0056] Liquid from the scrubber 37 flows by gravitation back down to the subsea separator 30 through a dedicated riser 40.
[0057] The gas from the scrubber 37 is then compressed to around 80 bar in a first stage compressor with a discharge temperature of around 80 C. The temperature should ideally be as low as possible to reduce the amount of glycol required for dehydration.
[0058] The maximum cricondenbar pressure of the export gas is 110 barg. The cricondenbar is the pressure below which no liquid will be formed regardless of temperature. The cricondenbar is a property of the gas. The cricondenbar is determined by the conditions in the inlet scrubber 37.
[0059] The pressure in the scrubber 37 is determined by the pressure in the subsea separator 30. A low pressure in the separator 30 will reduce the flash gas in the export oil and is at some point in time required to realize the production profiles. The required compression work and power consumption will however increase with a lower pressure. The separator 30 will operate at about 40 bar initially and the pressure will be reduced to 30 bar or even lower towards the end of the lifetime.
[0060] The temperature in the scrubber 37 is determined by the inlet cooler discharge temperature. A lower temperature corresponds to a lower cricondenbar. The hydrate formation temperature is about 15 C. and a 5 C. margin gives a minimum cooler discharge temperature of 20 C.
[0061] The gas from the scrubber 37 is then dehydrated using the glycol dehydration to meet the appropriate export specification. For example, the maximum water content is 40 mg/Sm.sup.3 for gas exported to Statpipe.
[0062] The gas is compressed to the required export pressure after dehydration. For example, the maximum operating pressure of the Statpipe Rich Gas pipeline is 167 barg. The required export pressure will be a function of allocated gas volumes and selected operational pressure in the pipeline and could be lower than the maximum pressure specified.
[0063] The gas is metered and measured according to requirements in a dedicated metering package, before entering the export riser and gas export pipeline 44.
[0064] In one example, the discharge temperature from the compressor is about 80 C. at 167 barg. However, the gas will be cooled in the 45 km long, un-insulated gas export pipeline 44 and the gas temperature is well below the maximum operating temperature for Statpipe when it reaches the tie-in point.
[0065] The selected UPP 16 design facilitates the unmanned processing of oil and gas in remote site B. A combination of subsea processing and topside processing on the UPP 16 can maximise operability and minimise capital and operational expenditure.
[0066] The UPP 16 has a steel jacket configuration. The jacket 46 is square with a spacing of 14 metres between the support columns 114. The jacket orientation is turned at 45 to the platform north to optimise weight versus size for the topside 48, so that the topside decks 48 are at 45 to the square of the jacket 46, as shown in
[0067] The UPP 16 uses a piled, four legged, symmetrically battered jacket 46 to support the topside 48. The topside 48 is 19.8 m19.8 m across the main structural span and its orientation is twisted compared to the jacket 46.
[0068] Umbilicals will be pulled into the platform 48 with a winch located on the weather deck 112 and a umbilical slot and reserved space are provided for this activity in centre of the platform 48. The slot and reserved space can be used for other purposes on the module deck areas once the pulling operation is completed.
[0069] The SSBS 29 is located on the seabed within the jacket 46. A subsea separator 30 is used instead of a topside solution on the UPP 16 because a topside solution would require an additional level on the UPP 16 due to the size and weight requirement.
[0070] The separator 30 is based on a symmetrical design with a central top inlet arrangement and top outlet arrangements at both ends combined with cyclones for gas polishing. Likewise oil and water outlets are at the bottom part inside and outside respective baffle-plates. Operation of the subsea separator 30 is performed using several distinct control loops.
[0071] The levels in the separator 30 are measured by a profiler level detector system. Water level control will adjust speed of the water injection pump and the level of oil will adjust speed of the export pump. The pressure in the subsea separator 30 is adjusted by the speed of the 1st stage compressor (suction pressure control). The control loops will be closed at the host 34 using fiber optic cables in an umbilicals 50, 56.
[0072] The platform 14, 16 would be oriented based on the prevailing wind direction. For example, with the prevailing wind defined as north to south and west to east, the process equipment should be located on the east and southeast side of the platform to allow for good natural ventilation.
[0073] As noted above, the platform layout advantageously uses a twisted topside 48 as shown in
[0074] The spider deck 102 is located at an elevation of 20 m above sea level. An example layout is shown in
[0075] For the personnel landing 122 on the north corner a muster area 126 is defined. The muster area can be located below the module and close to the north staircase to the decks above. A temporary escape chute 124 will be located on the combined north-east personnel landing 122.
[0076] It is likely that the preferred side for a SOV is the east side of UPP 16 due to the prevailing wind direction. For this reason a laydown area 128 for material handling is located on this side. The laydown area 128 is 85 m. From the laydown area 128 stairs are provided up to ESDV deck 104. Between the personnel landings 122 and the laydown area 128, access and escape routes are provided.
[0077] The hang off arrangement for pipeline and risers that need 3D or 5D bend will be located on the spider deck 102. In addition is it likely that the umbilical and power cables should be hanged off at this level and routed directly up to the termination panels.
[0078] The ESDV deck 104, which can have a layout as shown in
[0079] A temporary and removable open drain tank is located on the ESDV laydown area 130. The laydown area 130 is sized (52.5 m) to allow for material handling when the drain tank is on the laydown area 130. The crane operator will have direct view and good accessibility with the weather deck crane 132.
[0080] The TEG circulation pump (24P0002) is located on east side of the deck and below the 2nd stage scrubber to allow for sufficient pump suction height (6 m). Access to Cellar deck 106 above will be from north and south end of the ESDV deck 104 using the stair cases.
[0081] An example layout for the cellar deck 106 is shown in
[0082] On the north is a laydown area 134 (64 m) that will be designed to take the weight and size of the main power transformer located close to the laydown area 134. The transformers are the largest and heaviest equipment on this deck 106. Due to the large equipment maintenance handling route is dimensioned to take this large equipment. The high voltage transformers are located in a natural ventilated area that will be normally locked and only available for authorized personnel.
[0083] On the northwest side of the deck 106 is a mechanical ventilated Compressor VSD room. The access to the VSD room is from the process area and air lock in the centre of this deck 106 or from the north end of the room. Larger items that shall be removed from the room will be removed through the north access and skidded to the laydown 134.
[0084] A HVAC room is located on the south west side with access doors from east and south in addition will safe access be provided from the air lock used for access to the electrical VSD room. Larger items that need to be replaced could be handled through the east and follow the material handling route to the laydown area. The air intake for the HVAC room is proposed located on the cellar deck 106 west wall and the intake filter packing shall be designed <25 kg to enable manual handling.
[0085] Process equipment is located on east side of the module including scrubbers, pump and the fiscal metering package. A stair to a mezzanine deck 108 is provided in the centre of the module to avoid passage through the local instrument room when accessing to the local electrical equipment room. An example layout for the cellar mezzanine deck 108 is shown in
[0086] The cellar deck mezzanine deck 108 is 4.6 m above the cellar deck 106 in this example. Access to the deck below and the deck above is arranged for by the north and south staircase, in addition to the internal south stair. A local instrument room with natural ventilation is on the south part of this mezzanine deck 108. Access can be provided from a stair on the south end or through the stair on the north east corner of the room. Material handling may be provided with a monorail and hoist 138 through a panel and to a drop area on the south east side and down to the east side of the bridge landing.
[0087] The local equipment room is mechanical ventilated for non-Ex approved equipment and are provided with air lock when entered from the east stair close to the process equipment. On the north access is provided directly into the north staircase. No deck is provided over the process area and large equipment, however from the mezzanine deck 108 a platform is arranged for access to the elevated part of the scrubbers.
[0088] Above the cellar deck 106 and cellar deck mezzanine 108 is a process deck 110, which may be arranged as shown in
[0089] A laydown area 140 (64 m) with crane access is located on the north end of the process deck 110 with a short transport route for the 1st and 2nd stage compressor transformers. Each transformer will have a weight of approximately 25 ton and need to be handled by a heavy lift vessel during installation due to the SOV crane limitation of 8-10 ton. Gas to Pipe Mixer (G2P) and Inlet De-liquidizer's are located on the east side of the process deck 110.
[0090] The weather deck 112 is 8 m above the process deck 110 in this example and can have a layout as shown in
[0091] The vent stack 142 is located on the south-east corner due to the prevailing wind direction and to be close to process equipment for shortest possible pipe routing. Relief valves for the vent line will be located close to the vent stack 142. In this example the size of the stack is 1.51.510 m. The vent stack 142 is used for cold venting during certain procedures, and it is not used for depressurisation in the event of a fire. The vent stack 142 can be used for pressure relief of methane gas through cold vent 142 during barrier testing and maintenance operations that require pressure relief. It will be appreciated that there is no flare for this platform 16, which is a significant difference to the conventional arrangement. In the event of a fire there is no emergency depressurisation and instead the piping and equipment on the platform 16 is isolated from wells and larger volumes of hydrocarbons in connected external piping by valves, then left at operating pressure. As discussed above this generates an added risk in relation to escalation of the fire, but this risk can be managed by restricting the size of the platform 16 and hence minimising the evacuation time, and also by adding passive fire protection as described below.
[0092] The platform crane 132 is located on the north east corner for good access to all the laydown areas 128, 130, 134, 140 provided on the various decks below. This has an 18 m reach and the access to the laydown areas 128, 130, 134, 140 as well as to the SOV is aided by the twisted topside arrangement of the platform 16.
[0093] Goods lifted by the SOV to the spider deck laydown area 128 can be picked up by the platform crane 132 and moved to a local laydown area 130, 134, 140. In case of a breakdown of the platform crane 132, davits 144 are proposed installed between the two laydown areas 134, 140 on the north side and between the two laydown areas 128, 130 on the east side.
[0094] An area 146 on the weather deck 112 can be reserved for helicopter drop, although it will be appreciated that the platform design does not allow for a heli-deck.
[0095] Material from drop areas on cellar deck 106 could be moved to the north laydown area 134 with a trolley. Similarly, hand-liftable equipment on all decks can be transported by trolley to the local laydown area for further transportation.
[0096] The base case for equipment transfer from/to the UPP 16 is by mean of SOV crane used during normal scheduled visits in the operation phase. Cargo and equipment transport to and from the platform uses the SOV crane to the lowermost laydown area 128 on the spider deck 102. This is at a height of 20 m above sea level on both the UWP 14 and UPP 16. The maximum load for the SOU crane will typically be 10 tons at 20 m height and up to 3 m Hs. Loads below twenty five kilograms can be handled by the members of the crew through the W2W (SOV).
[0097] Loads up to three tons could alternatively be transferred by means of helicopter to a laydown area 146 on the weather deck 112. The weather deck 112 can contain a landing area 146 for cargo from helicopter and a personnel winch-up area for escape in a situation without access to the SOV.
[0098] Internal lifting on the UPP 16 is performed by a slewing jib crane 132, which is mounted on the weather deck 112 as noted above. The jib crane 132 in this example has a SWL capacity of 10 tons at 18 m distance along the jib. A similar design can be used for the UWP 14. Transport to/from the laydown area 128 on the spider deck 102 to the platform decks 104, 106, 108, 110, 112 can be done via the platform crane 132 to laydown areas 130, 134, 140 outside of the decks 104, 106, 108, 110, 112. This crane 132 is for onboard lifting only and all laydown areas 128, 130, 134, 140, 146 are arranged to be within reach of the crane 132. Advantageously, this crane 132 is only required during favourable weather since in the case of adverse weather then personnel will not visit the platform 16. This means that there is a lesser requirement for the capability of the platform crane 132 to operate in bad weather. Similarly, the SOU crane need not be capable of operating in bad weather. For example, the cranes need not meet the requirements of BS EN 13852-1 in relation to operation offshore in significant wave heights, such as operating at wave heights as large as 5 to 6 m. Instead the platform crane and also the SOV crane may only be required to operate at wave heights of up to 2 m.
[0099] Lifts above 10 tons could be performed by a separate heavy lifting vessel, although equipment weighing only slightly above 10 tons might be handled by the SOV crane with more stringent restrictions to wave height, but this will depend on the actual capacity of the crane on the vessel utilized.
[0100] Heavier equipment items are placed such that it is possible to lift them out of position and transport them to an external laydown area where they can be picked up by a suitable lifting vessel. Internal transport can be by lifting beams or monorails and rail based trolleys capable of handling the relevant load. Lifting/transport devices can be brought onto the platform as required for the relevant operation.
[0101] All vertical transport between decks is done by the platform crane 132, at least for larger items. As an alternative lifting arrangement for smaller items there are two davits 144 on weather deck level, one serving the east side covering laydown areas on the spider deck 102 and ESDV deck 104, and the other on the north side covering laydown areas on the process deck 110 and the cellar deck 106.
[0102] Local handling for each item will involve the use of permanently installed pad eyes and monorails and temporary equipment. It shall be possible to install trolley/hoists without use of temporary scaffolding. The platform 16 is designed for internal horizontal transport handling from laydown areas to/from location where the items are needed.
[0103] The lifting equipment that is used is advantageously of modular and temporary design and is to be stored, maintained and inspected onshore to reduce the maintenance hours required offshore. This lifting equipment can be transported to the platform via the SOV (or over the bridge 136, if a bridge 136 is present). Only the weather deck jib crane 132, lifting lugs and monorails are permanently on the platform. Jib crane moving parts should as far as possible be modular based and removable so that they can be stored and maintained onshore. It is preferred for only the parts too heavy to be removed to be kept on the jib crane and these should be suitable for prolonged storage in harsh conditions with minimum maintenance.
[0104] The platform 16 will allow for various evacuation routes from differing locations. The evacuation routes need to be established with the slowest evacuations being used as the basis for a maximum evacuation time. This maximum evacuation time is then used in determining what fire protection should be included. The platform 16 is provided with passive fire protection (PFP) in order to ensure that a fire will not escalate until after personnel on the platform have been safely evacuated. It should be noted that the absence of a flare can increase the risk of a dangerous escalation of a fire, since there is no depressurisation. However, the absence of the flare contributes to allowing for the size of the platform 16 to be reduced and the evacuation time to be minimised. Moreover since the platform 16 is an unmanned platform then personnel will only be present with a connection via a bridge 136 or a gangway to a SOV being present as well, which means that the evacuation process can be very quick. It is evaluated that personnel can escape to the stair tower within 1 minute after the initial incident, and a conservative assumption is that personnel will be on the service ship within 10 minutes.
[0105] The evacuation route(s) can include different routes from different locations on the platform 16 to an escape point via the gangway or bridge 136. In the case of a vessel connecting to the platform 16 via a gangway then the evacuation route includes personnel boarding the vessel and moving away from the platform to a safe distance by using the vessel. In the case of a bridge 136, for example to another platform such as the UWP 14, then the evacuation route may include traversing some or all of the bridge 136 to get to a safe distance. Identifying the evacuation routes includes taking account of the routes required for traversing decks, climbing and/or descending stairs, climbing and/or descending ladders, descending escape chutes and/or moving around obstructions. The evacuation time and/or the length of the route is assessed for all evacuation routes, or at least for the longest routes, in order to identify the evacuation route with the longest evacuation time. The evacuation time is calculated based on assessing the nature of each part of the evacuation route, allocating a time required for a person to traverse each part of the evacuation route, and summing the times. The time required for a person to traverse each part of a route is based on the length/distance for the route and on a set speed for different types of route. Preferably the speed is based on evacuation of an injured person. Optionally the speed may be based on favourable weather conditions. In the case of an unmanned platform personnel would not board the platform during adverse weather and therefore it may not be necessary for the speed during evacuation to take account of adverse weather. The speeds can be based on past experience and/or empirical calculations for speed of movement of a person.
[0106] By way of example, the speed of movement may be set as follows:
[0107] Evacuation of uninjured person: 1.0 m/s for corridors (flat decks), 0.6 m/s for stairs and 0.3 m/s for ladders.
[0108] Evacuation of injured person: 0.5 m/s for corridors, 0.2 m/s for stairs and 0.3 m/s for ladders.
[0109] The example platform above is about 20 m by 20 m with three full decks 106, 110, 112 and one mezzanine deck 108, plus two decks 102,104 as a part of the jacket structure. The jacket 46 is about 18 m by 18 m. The longest evacuation route is determined to be from the weather deck 112 to the SOV. Conservatively, the distance diagonally across the deck is used. The escape route is hence as follows: walk diagonal across deck28 m, walk via stairs from weather deck 112 to bridge deck (spider deck 102)91 m (based on height of 27 m and stair pitch not to exceed 38), and walk from bridge deck to SOV30 m.
[0110] Using the speeds set out above, the evacuation time for non-injured and injured personnel can then be found. For a non-injured person the timings are: walk diagonal across deck28 s, walk via stairs from weather deck 112 to bridge deck (spider deck 102)152 s, and walk from bridge deck to SOV30 s, with a total time of 210 s. For evacuating an injured person the timings are: walk diagonal across deck56 s, walk via stairs from weather deck 112 to bridge deck (spider deck 102)456 s, and walk from bridge deck to SOV60 s, with a total time of 572 s.
[0111] In an alternative scenario the evacuation route could be via the bridge 136 to the neighbouring platform. By way of example, it is required that the personnel traverse the full length of the bridge 136 to be deemed safe, and in this instance the bridge 136 is located at the cellar deck 106. The escape route is hence as follows: walk diagonal across weather deck 11228 m, walk via stairs from weather deck 112 to cellar deck 10657 m, and walk from cellar deck 106 across bridge 13675 m.
[0112] Using the speeds set out above, the evacuation time for non-injured and injured personnel can then be found. For a non-injured person the timings are: walk diagonal across weather deck 11228 s, walk via stairs from weather deck 112 to cellar deck 10696 s, and walk across bridge 13675 s, with a total time of 199 s. For evacuating an injured person the timings are: walk diagonal across weather deck 11256 s, walk via stairs from weather deck 112 to cellar deck 106287 s, and walk across bridge 136150 s, with a total time of 493 s.
[0113] The evacuation time is used in assessing the risk and determining the required passive fire protection. Passive fire protection is provided to equipment and/or piping on the platform in order to prevent escalation of the fire that would create a risk to personnel on the evacuation route(s) during the determined evacuation time. For minimum fire protection this includes providing passive fire protection only to the extent required to remove the risk to personnel on the evacuation route(s) during evacuation. Thus, if there is a risk of escalation within the maximum evacuation time due to rupture of certain pipework in the vicinity of an escape route, or liable to affect an escape route then passive fire protection is provided to restrict the increase in temperature of the pipework during a fire and/or to increase the strength of the pipework to make it more resistant to rupturing. Alternatively or additionally, if there is a risk of escalation within the maximum evacuation time due to hydrocarbons present in certain equipment in the vicinity of an escape route, or liable to affect an escape route then passive fire protection is provided to restrict the increase in temperature of the equipment during a fire and/or to protect the equipment from to make it more resistant to ignition of the hydrocarbons and/or explosion of the equipment. Such equipment may include compressors, scrubbers, coolers, metering devices, valves and so on.
[0114] It will be appreciated that the above system for optimisation of fire protection could also be applied to the UWP 14 in a similar fashion. It will also be understood that the exact layout for the platform in terms of the decks that are present and the equipment that is used can vary.