Vapour cloud assessment for overfilling incidents - …ukelg.ps.ic.ac.uk/48GA.pdf · Vapour cloud...
Transcript of Vapour cloud assessment for overfilling incidents - …ukelg.ps.ic.ac.uk/48GA.pdf · Vapour cloud...
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www.hsl.gov.ukAn Agency of the Health and Safety Executive
www.hsl.gov.ukAn Agency of the Health and Safety Executive
Vapour cloud assessment for overfilling incidents
Graham Atkinson (Health and Safety Laboratory)
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Jaipur October 29th 2009
12 dead, >50 injuries, Mass evacuation
Cloud diameter approx 1000m
Upward spray from a pipe under tank pressure (<1 bar)
Duration of leak ~75 minutes
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Caribbean Petroleum Corporation (Puerto Rico)
23rd October 2009Cloud diameter approximately 500m
Substance: Gasoline
Cause: Tank overfilling (Ship to Shore transfer)
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Buncefield and other incidents have shown that very large vapour clouds can be caused by liquid leaks
(Especially tank overfilling, releases of volatile liquids at elevation or upward facing sprays)
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05:34:38 AM
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05:48:07 AM
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05:56:11 AM
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05:36:28 AM
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05:44:28 AM
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05:45:28 AM
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05:56:28 AM
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How is the liquid released?
How does it break up as it falls?
How much air is drawn into the cascade?
How much liquid vaporises?
Calculating vaporisation in the casacde
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Droplet size in the cascadeGasoline
•Small, even sized drops
•Diameter approximately 2mm.
Water
•Wide range of droplet sizes
•Up to 6mm diameter
Surface tension (N/m)
Density (kg/m3)
Water 0.0727 998
Hexane 0.0184 667
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Air flow driven by gravity driven liquid cascade
Spray origin
Control surface
This is a straightforward mechanics problem (much easier than a turbulent gas jet)
There are no empirical constants
Hazards XX Conference (2007): “Liquid dispersal and vapour production during overfilling incidents”
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Droplet dynamics in cascade of varying mass density
0
2
4
6
8
10
12
14
16
18
20
0 5 10 15 20
Distance below origin (m)
drop
let v
eloc
ity (m
/s)
Free fall
100 kg/s/m2
10 kg/s/m2
1 kg/s/m2
0.1 kg/s/m2
0.01 kg/s/m2
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Air flow driven by sprays of varying mass density
0
2
4
6
8
10
12
14
16
18
20
0 5 10 15 20
Distance below origin (m)
Vapo
ur v
eloc
ity (m
/s)
100 kg/s/m2
10 kg/s/m2
1 kg/s/m2
0.1 kg/s/m2
0.01 kg/s/m2
free fall
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This analysis gives the amount of air drawn into the liquid cascade
If we assume thermodynamic equilibrium is reached, we can calculate the vapour
concentration at the foot of tank
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A given tank is overfilled at a specified rate with a specified liquid.
Can a significant flammable vapour cloud be formed?
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0
0.05
0.1
0.15
0.2
0.25
0.1 1 10
Mass release per metre of (total) tank perimeter (kg/s/m)
Tota
l hyd
roca
rbon
con
cent
ratio
n (w
/w)
F3 Condensate
Brent (RVP 13.9 psi)Cook (RVP 10.1 psi
Arabian (RVP 8.0 psi)
LFL
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Solvent concentration
0
0.01
0.02
0.03
0.04
0.05
0.06
0.07
0.08
0.1 1 10
Mass release per metre of (total) tank perimeter
Solv
ent c
once
ntra
tion
(w/w
)
MethanolMethanol LFL
TolueneToluene LFL
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Key areas addressed in the new experimental and modelling work:
•Heat and mass transfer – how good is the equilibrium assumption?
•Near field dispersion
•Far field dispersion
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Sometimes the cloud is visible
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Sometimes thermal imaging is required
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Measurements of liquid and vapour temperatures in full scale experimental cascades.
How effective is the vaporisation process?
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Deep layer observed outside
bund
Contaminated air entrained by vapour
current
Tank
Liquid cascade
Near field dispersion: Is entrainment of air suppressed by the deep accumulating vapour cloud ?
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Even when a deep layer accumulates around the tank the vapour flow entrains some fresh air
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Computational domain
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Test cases
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5m vertical
10m vertical
5m sloping
15m vertical
Effect of bund design on concentration in the cloud
(concentration at the tank foot ~0.05 mol/mol)
Temperatures
Concentrations
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Barrier height
(m)
Cloud depth (m)
Distance to barrier
(m)
Dilution factor
(conc. in cascade/conc. in
cloud)
4 5 30 1.5 2.5 3.6 30 2.1 2 - 5 1.8 2 - 10 2.0 2 - 15 2.0
What is the relationship between the concentration in the cascade and that in the vapour cloud?
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Conclusions from the experimental and modelling work
•Overfilling can be a well-defined source term and can be analysed with some confidence – compared other hazard modelling methods.
•Distribution of liquid discharge is the main uncertainty (especially for floating roof tanks)
•Long range dispersion in very light or zero winds is a major outstanding difficulty – site specific data can improve the value of modelling.
•These problems are worth the trouble - operators at gasoline depots should have an understanding of the way a vapour cloud is likely to develop in the event of an overfill.
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Outline of the Vapour Cloud Assessment method
•Calculate the volume production rate for the specific tank / flow rate
•Calculate the concentration of fuel vapour at the foot of the tank
•Allow for near field dilution (reduces concentrations and increases volumes)
•Analyse long range slumping of the vapour cloud.
http://www.hse.gov.uk/research/rrhtm/rr908.htm
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Tank diameter D 25 m Tank height H 15 m Fuel flow rate F (Gasoline) 115 kg/s Fuel temperature Tfuel 14°C Air temperature Tambient 0 °C Duration of release 1400 s
Example 1- A gasoline tank like Buncefield
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Tank diameter D 25 m Tank height H 15 m Fuel flow rate F (Gasoline) 115 kg/s Fuel temperature Tfuel 14°C Air temperature Tambient 0 °C Duration of release 1400 s
Example 1- Air mass entrained
Mass entrainment in cascade 25.045.075.0
/1151025/90 ⎟⎟
⎠
⎞⎜⎜⎝
⎛⎟⎠⎞
⎜⎝⎛
⎟⎠⎞
⎜⎝⎛=
skgF
mH
mDskgM air
108 kg/s
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The standard gasoline used (from Buncefield)
n-butane1 9.6% wt/wtn-pentane2 17.2 % wt/wtn-hexane3 16% wt/wtn-decane4 57.2% wt/wt
1 as a surrogate for all C4 hydrocarbons2 as a surrogate for all C53 as a surrogate for all C64 as a surrogate for all low volatility materials
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Concentration at the tank foot
Concentration at the tank foot
)10(0062.0)10(011.042.0
28.1)/%(17 −−−
⎟⎠⎞
⎜⎝⎛= ambientfuel TTair
fuel eeF
MwwC
= 17 % (w/w) ( 0.92 ) . 1.04 . 0.94
15.3% w/w
Tank diameter D 25 m Tank height H 15 m Fuel flow rate F (Gasoline) 115 kg/s Fuel temperature Tfuel 14°C Air temperature Tambient 0 °C Duration of release 1400 s
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Mass vaporised Mvaporised = Mair .. Cfuel / (100 -. Cfuel)
19.5 kg/s
Mass splashed Msplash (kg/s)= 0.02 F
2.2 kg/s
Total mass addition rate to cloud Mcloud = 2. (Mair +Mvaporised + Msplash)
259 kg/s
Volume addition rate to cloud
Vcloud = Mcloud/ρambient
199 m3/s
The rate at which the cloud volume is growing
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Concentration of fuel vapour in cloud Ccloud (kg/m3) =(Mvaporised + Msplash) / Vcloud
0.11 kg/m3
110 g/m3
Range (after 1400s) to which cloud may hinder escape Rescape = [ 1/ 2π Vcloud . T ]1/2
210 m
Range to which low level cloud might be ignited Rignition = [ 1/ π Vcloud . T ]1/2
297 m
Results
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Substance Mass concentration at the lower flammable limit at 0°C (g/m3)
Butane 48 Pentane 46 Hexane 47 Heptane 47 Benzene 47 Methanol 103 Ethanol 70
Propanol 60 Acetone 70
MEK 62
Lower explosion limits
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Substance Mass concentration for a stoichiometric
mixture at 0°C (g/m3) Butane 83 Pentane 84 Hexane 84 Heptane 84 Benzene 98 Methanol 187 Ethanol 140
Propanol 122 Acetone 134
MEK 120
Stoichiometric mixtures
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An Agency of the Health and Safety Executive
The gasoline cloud is slightly rich with an equivalence ratio of 110 / 84 = 1.3
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An Agency of the Health and Safety Executive
Range (after 1400s) to which cloud may hinder escape (2m high cloud) Rescape = [ 1/ 2π Vcloud . T ]1/2
210 m
Range to which low level cloud might be ignited (1m high cloud) Rignition = [ 1/ π Vcloud . T ]1/2
297 m
Results – Hazard ranges
These give an indication of the potential reach of the cloud at different heights. Note the cloud will not flow uphill from the tank foot by more than 3m.
The figure for the 2m high cloud matches the average radius and typical height of the Buncefield cloud quite well.
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An Agency of the Health and Safety Executive
After 5 minutes (300 s) the range to which the cloud might extend over head height and impede escape would be:
Rescape = [ 1/ 2π
Vcloud . 300 ]1/2 = 97 m
This kind of analysis shows the need for prompt and effective evacuation in the event of an overfill in calm conditions.
Early warning to allow escape before the cloud arrives can greatly reduce risk. Staying put (even in a toxic refuge) is very dangerous if the cloud is flammable.
Use of the method for simple risk assessment
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An Agency of the Health and Safety Executive
Tank diameter D 25 m
Tank height H 15 m
Fuel flow rate F (Methanol) 115 kg/s
Fuel temperature Tfuel 14°C
Air temperature Tambient 0 °C
Duration of release 1400 s
A similar tank and condition - but filled with methanol
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An Agency of the Health and Safety Executive
Concentration of fuel vapour in cloud Ccloud (kg/m3) =(Mvaporised + Msplash) / Vcloud
35 g/m3
(110 g/m3)
Equivalence ratio of mixture in cloud
0.19 (1.3)
Range (after 1400s) to which cloud may hinder escape Rescape = [ 1/ 2π Vcloud . T ]1/2
197 m (210 m)
Range to which low level cloud might be ignited Rignition = [ 1/ π Vcloud . T ]1/2
N/A (297 m)
Results for the methanol tank compared to gasoline (in brackets)
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An Agency of the Health and Safety Executive
There is no risk of a vapour explosion but there will be high concentrations of methanol to a range of around 200m after 1400 s.
Early warning would be of great benefit
Staying put in a toxic refuge would be the safest option in many cases.
Use of the method for simple risk assessment
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An Agency of the Health and Safety Executive
What does HSE expect from industry?
• An understanding of the consequences of tank overfilling incidents in calm conditions.
• Inclusion of large vapour cloud scenarios in risk assessments
• Consideration of appropriate risk reduction measures (overflow protection, ROSOVs, gas detection, OB modification, ignition source control etc) to make risks ALARP