010bijl 1.7 tb6_M2019066805R001v3 Externe veiligheid (mrt 2021).pdf
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fraction
Horizontal jet only
Reduce risks for No mounded / underground tanks Non-ignition probabilities
Specify probability Calculate nonof non-ignition ignition probability Non-ignition probability
fraction
Immediate ignition Probability of Transport - Road probabilities immediate ignition tanker Immediate ignition probability Scenario
Pipe dimensions
Pipe length
10
m
Release location
Elevation
1
m
Tank head
2
m
Outdoor release direction
Horizontal
Outdoor release angle
0
deg
Pipe characteristics Pipe roughness
0,045
mm
Frequencies
Frequency of bends in pipe
0
/m
Frequency of couplings in pipe
0
/m
Frequency of junctions in pipe
0
/m
Frequency of 0 excess flow valves
/m
Frequency of non- 0 return valves
/m
Direction
Short pipe
fraction
Frequencies of valves
Audit Number: 2716767 Date: 23-11-2020 Time: 16:58 Page 22 of 130
Frequency of shut- 0 off valves Velocity head losses
/m
Excess flow valve velocity head losses
0
Non-return valve velocity head losses
0
Shut-off valve velocity head losses
0
Vacuum relief valve
Operating
Vacuum relief valve set point
0
bar
Inventory data for Tank volume time-varying releases
28
m3
Tank vapour volume
0
m3
Tank liquid volume 28
m3
Tank liquid level
m
Time varying Modelling of timereleases varying leaks and line ruptures
0
Maximum vapour release height
Dispersion
Dispersion scope
m
Minimum mass inventory
0
kg
Maximum mass inventory
1E+09
kg
Concentration of interest
ppm
Averaging time for concentration of interest Specify userNo defined averaging time
Audit Number: 2716767 Date: 23-11-2020 Time: 16:58 Page 23 of 130
User defined averaging time Distances of interest
Bund, building and terrain
s
Distances of interest
600
Averaging time for NLIV [1 hr] reports
No
Terrain and bund definition
IDLH [30 mins]
No
STEL [15 mins]
No
Type of terrain for Upgraded Terrain dispersion from RunRowSet Type of pool substrate and bunds
Building definition
m
LT2_Tkl bund
Release building In-building release?
Outdoor
Building wake effect
Roof/lee
Wind or release angle from North
0
Handling of droplets
Trapped
deg
Indoor mass 3 modification factor
LT2_Tkl leak Leak Venlo_barge_Terminal\Study\overslag\Handelingen\LT2_Tkl 5 containers*1E-6 Tab
Group
Field
Value
Units
Scenario
Hole
Orifice diameter
20
mm
Use specified discharge coefficient?
No
Discharge coefficient
fraction Audit Number: 2716767 Date: 23-11-2020 Time: 16:58 Page 24 of 130
Release location Elevation
1
m
Tank head
2
m
Outdoor release direction
Horizontal
Outdoor release angle
0
deg
5E-06
fraction
Direction
Risk
Event probability Event probability (probability of this event compared with others in this group)
Type of risk Reduce risks for No effects to model mounded / underground tanks Non-ignition probabilities
Specify probability of non-ignition
Calculate nonignition probability
Non-ignition probability Immediate ignition probabilities
Probability of immediate ignition
fraction Transport - Road tanker
Immediate ignition probability Material
Material
fraction
Material characteristics
Toxic and flammable
Material to track
ALLYLAMINE
Type of risk effects Toxic only to model Phase Dispersion
Phase to be released
Dispersion scope Concentration of interest
Liquid ppm
Averaging time for concentration of interest
Audit Number: 2716767 Date: 23-11-2020 Time: 16:58 Page 25 of 130
Specify userdefined averaging time
No
User defined averaging time
s
Distances of interest
Distances of interest
600
Averaging time for reports
NLIV [1 hr]
No
IDLH [30 mins]
No
STEL [15 mins]
No
m
LT2_Box Atmospheric storage tank Venlo_barge_Terminal\Study\overslag\Handelingen 20 boxcontainers, basiskans 1E-6 Tab
Group
Field
Value
Material
Material
Material
ALLYLAMINE
Specify volume inventory?
Yes
Mass inventory
770,90083
Volume inventory 1
Phase
Risk
Units
kg m3
Material to track
ALLYLAMINE
Type of risk effects to model
Toxic only
Specified condition Temperature and atmospheric pressure Temperature
9,85
degC
Pressure (gauge)
1E-10
bar
Fluid state
Liquid
Liquid mole fraction
1
Type of risk effects Jet fire modelling to model for horizontal releases
fraction
Horizontal jet only
Audit Number: 2716767 Date: 23-11-2020 Time: 16:58 Page 26 of 130
Reduce risks for No mounded / underground tanks Non-ignition probabilities
Specify probability Calculate nonof non-ignition ignition probability Non-ignition probability
fraction
Immediate ignition Probability of Transport - Road probabilities immediate ignition tanker Immediate ignition probability Scenario
Pipe dimensions
Pipe length
10
m
Release location
Elevation
1
m
Tank head
1
m
Outdoor release direction
Horizontal
Outdoor release angle
0
deg
Pipe characteristics Pipe roughness
0,045
mm
Frequencies
Frequency of bends in pipe
0
/m
Frequency of couplings in pipe
0
/m
Frequency of junctions in pipe
0
/m
Frequency of 0 excess flow valves
/m
Frequency of non- 0 return valves
/m
Frequency of shut- 0 off valves
/m
Direction
Short pipe
fraction
Frequencies of valves
Velocity head losses
Excess flow valve velocity head losses
0
Non-return valve velocity head losses
0
Audit Number: 2716767 Date: 23-11-2020 Time: 16:58 Page 27 of 130
Shut-off valve velocity head losses
0
Vacuum relief valve
Operating
Vacuum relief valve set point
0
bar
Inventory data for Tank volume time-varying releases
1
m3
Tank vapour volume
0
m3
Tank liquid volume 1
m3
Tank liquid level
m
Time varying Modelling of timereleases varying leaks and line ruptures
0
Maximum vapour release height
Dispersion
Dispersion scope
m
Minimum mass inventory
0
kg
Maximum mass inventory
1E+09
kg
Concentration of interest
ppm
Averaging time for concentration of interest Specify userNo defined averaging time User defined averaging time Distances of interest
s
Distances of interest
600
Averaging time for NLIV [1 hr] reports
No
IDLH [30 mins]
No
STEL [15 mins]
No
m
Audit Number: 2716767 Date: 23-11-2020 Time: 16:58 Page 28 of 130
Bund, building and terrain
Terrain and bund definition
Type of terrain for Upgraded Terrain dispersion from RunRowSet Type of pool substrate and bunds
Building definition
LT2_Box bund
Release building In-building release?
Outdoor
Building wake effect
Roof/lee
Wind or release angle from North
0
Handling of droplets
Trapped
deg
Indoor mass 3 modification factor
LT2_Box fixed duration release Fixed duration release Venlo_barge_Terminal\Study\overslag\Handelingen\LT2_Box 20 boxcontainers, basiskans 1E-6 Tab
Group
Field
Value
Units
Scenario
Scenario
Duration for fixed duration release
30
s
Hole
Orifice diameter Use specified discharge coefficient?
mm No
Discharge coefficient
fraction
Release location Elevation
1
m
Tank head
1
m
Outdoor release direction
Horizontal
Outdoor release angle
0
Direction
deg Audit Number: 2716767 Date: 23-11-2020 Time: 16:58 Page 29 of 130
Risk
Event probability Event probability (probability of this event compared with others in this group)
2E-05
fraction
Type of risk Reduce risks for No effects to model mounded / underground tanks Non-ignition probabilities
Specify probability of non-ignition
Calculate nonignition probability
Non-ignition probability Immediate ignition probabilities
Probability of immediate ignition
fraction Transport - Road tanker
Immediate ignition probability Material
Material
fraction
Material characteristics
Toxic and flammable
Material to track
ALLYLAMINE
Type of risk effects Toxic only to model Phase Dispersion
Phase to be released
Liquid
Dispersion scope Concentration of interest
ppm
Averaging time for concentration of interest Specify userdefined averaging time
No
User defined averaging time Distances of interest
Distances of interest
s 600
m
Audit Number: 2716767 Date: 23-11-2020 Time: 16:58 Page 30 of 130
Averaging time for reports
NLIV [1 hr]
No
IDLH [30 mins]
No
STEL [15 mins]
No
GT3_Tgr Pressure vessel Venlo_barge_Terminal\Study\overslag\Handelingen 5 containers*1E-7 Tab
Group
Field
Value
Units
Material
Material
Material
AMMONIA
Specify volume inventory?
Yes
Mass inventory
12482,04
kg
Volume inventory
20
m3
Material to track AMMONIA Type of risk Toxic only effects to model Phase
Risk
Specified condition
Temperature/bubble point
Temperature
9,85
degC
Pressure (gauge)
5,0862016
bar
Fluid state
Liquid
Liquid mole fraction
1
Type of risk Jet fire effects to model modelling for horizontal releases
fraction
Horizontal jet only
Reduce risks for No mounded / underground tanks
Audit Number: 2716767 Date: 23-11-2020 Time: 16:58 Page 31 of 130
Non-ignition probabilities
Specify probability of non-ignition
Calculate non-ignition probability
Non-ignition probability Immediate ignition probabilities
Probability of immediate ignition
fraction Transport - Road tanker
Immediate ignition probability Scenario
Pipe dimensions Pipe length
10
m
Release location Elevation
1
m
Tank head
2
m
Direction
Short pipe
fraction
Outdoor release Horizontal direction Outdoor release 0 angle
deg
Pipe characteristics
Pipe roughness
0,045
mm
Frequencies
Frequency of bends in pipe
0
/m
Frequency of 0 couplings in pipe
/m
Frequency of 0 junctions in pipe
/m
Frequency of excess flow valves
0
/m
Frequency of non-return valves
0
/m
Frequency of shut-off valves
0
/m
Excess flow valve velocity head losses
0
Frequencies of valves
Velocity head losses
Audit Number: 2716767 Date: 23-11-2020 Time: 16:58 Page 32 of 130
Time varying releases
Non-return valve velocity head losses
0
Shut-off valve velocity head losses
0
Vacuum relief valve
Operating
Vacuum relief valve set point
0
bar
Inventory data Tank volume for time-varying releases
20
m3
Tank vapour volume
0
m3
Tank liquid volume
20
m3
Tank liquid level 0
m
Maximum vapour release height
m
Modelling of time-varying leaks and line ruptures
Minimum mass inventory
0
Maximum mass 1E+09 inventory Safety system modelling for time-varying releases Dispersion
Safety system modelling (isolation and blowdown)
Dispersion scope Concentration of interest
kg kg
No
ppm
Averaging time for concentration of interest
Audit Number: 2716767 Date: 23-11-2020 Time: 16:58 Page 33 of 130
Specify userdefined averaging time
No
User defined averaging time
s
Distances of interest
Distances of interest
600
Averaging time for reports
NLIV [1 hr]
No
m
IDLH [30 mins] No STEL [15 mins] No Bund, Terrain and bund Type of terrain building and definition for dispersion terrain
Upgraded Terrain from RunRowSet
Type of pool substrate and bunds
Type of pool substrate and bund
Building definition
Release building In-building release?
Outdoor
Building wake effect
Roof/lee
Wind or release 0 angle from North
deg
Handling of droplets
Trapped
Indoor mass modification factor
3
GT3_Tgr leak Leak Venlo_barge_Terminal\Study\overslag\Handelingen\GT3_Tgr 5 containers*1E-7 Tab
Group
Field
Value
Units
Audit Number: 2716767 Date: 23-11-2020 Time: 16:58 Page 34 of 130
Scenario
Hole
Orifice diameter
50
Use specified discharge coefficient?
No
mm
Discharge coefficient Release location
Elevation
1
m
Tank head
2
m
Outdoor release direction
Horizontal
Outdoor release angle
0
deg
Event probability Event probability (probability of this event compared with others in this group)
5E-07
fraction
Type of risk effects to model
Reduce risks for mounded / underground tanks
No
Non-ignition probabilities
Specify probability of non-ignition
Calculate nonignition probability
Direction
Risk
fraction
Non-ignition probability Immediate ignition probabilities
Probability of immediate ignition
fraction Transport Road tanker
Immediate ignition probability Material
Material
Phase Dispersion
fraction
Material characteristics
Toxic only
Material to track
AMMONIA
Type of risk effects to model
Toxic only
Phase to be released Liquid
Dispersion scope Concentration of interest
ppm
Audit Number: 2716767 Date: 23-11-2020 Time: 16:58 Page 35 of 130
Averaging time for concentration of interest Specify user-defined No averaging time User defined averaging time
s
Distances of interest
Distances of interest 600
m
Averaging time for reports
NLIV [1 hr]
No
IDLH [30 mins]
No
STEL [15 mins]
No
GT3_Tkl Pressure vessel Venlo_barge_Terminal\Study\overslag\Handelingen 5 containers*1E-6 Tab
Group
Field
Value
Units
Material
Material
Material
AMMONIA
Specify volume inventory?
Yes
Mass inventory
12482,04
kg
Volume inventory
20
m3
Material to track AMMONIA Type of risk Toxic only effects to model Phase
Specified condition
Temperature/bubble point
Temperature
9,85
degC
Pressure (gauge)
5,0862016
bar
Fluid state
Liquid
Liquid mole fraction
1
fraction
Audit Number: 2716767 Date: 23-11-2020 Time: 16:58 Page 36 of 130
Risk
Type of risk Jet fire effects to model modelling for horizontal releases
Horizontal jet only
Reduce risks for No mounded / underground tanks Non-ignition probabilities
Specify probability of non-ignition
Calculate non-ignition probability
Non-ignition probability Immediate ignition probabilities
Probability of immediate ignition
fraction Transport - Road tanker
Immediate ignition probability Scenario
Pipe dimensions Pipe length
10
m
Release location Elevation
1
m
Tank head
2
m
Direction
Short pipe
fraction
Outdoor release Horizontal direction Outdoor release 0 angle
deg
Pipe characteristics
Pipe roughness
0,045
mm
Frequencies
Frequency of bends in pipe
0
/m
Frequency of 0 couplings in pipe
/m
Frequency of 0 junctions in pipe
/m
Frequency of excess flow valves
/m
Frequencies of valves
0
Audit Number: 2716767 Date: 23-11-2020 Time: 16:58 Page 37 of 130
Frequency of non-return valves
0
/m
Frequency of shut-off valves
0
/m
Excess flow valve velocity head losses
0
Non-return valve velocity head losses
0
Shut-off valve velocity head losses
0
Vacuum relief valve
Operating
Vacuum relief valve set point
0
bar
Inventory data Tank volume for time-varying releases
20
m3
Tank vapour volume
0
m3
Tank liquid volume
20
m3
Tank liquid level 0
m
Maximum vapour release height
m
Velocity head losses
Time varying releases
Modelling of time-varying leaks and line ruptures
Minimum mass inventory
0
Maximum mass 1E+09 inventory Safety system modelling for time-varying releases
Safety system modelling (isolation and blowdown)
kg kg
No
Audit Number: 2716767 Date: 23-11-2020 Time: 16:58 Page 38 of 130
Dispersion
Dispersion scope Concentration of interest
ppm
Averaging time for concentration of interest Specify userdefined averaging time
No
User defined averaging time
s
Distances of interest
Distances of interest
600
Averaging time for reports
NLIV [1 hr]
No
m
IDLH [30 mins] No STEL [15 mins] No Bund, Terrain and bund Type of terrain building and definition for dispersion terrain
Upgraded Terrain from RunRowSet
Type of pool substrate and bunds
Type of pool substrate and bund
Building definition
Release building In-building release?
Outdoor
Building wake effect
Roof/lee
Wind or release 0 angle from North Handling of droplets
Trapped
Indoor mass modification factor
3
deg
Audit Number: 2716767 Date: 23-11-2020 Time: 16:58 Page 39 of 130
GT3_Tkl leak Leak Venlo_barge_Terminal\Study\overslag\Handelingen\GT3_Tkl 5 containers*1E-6 Tab
Group
Field
Value
Units
Scenario
Hole
Orifice diameter
10
mm
Use specified discharge coefficient?
No
Discharge coefficient Release location
Elevation
1
m
Tank head
2
m
Outdoor release direction
Horizontal
Outdoor release angle
0
deg
Event probability Event probability (probability of this event compared with others in this group)
5E-06
fraction
Type of risk effects to model
Reduce risks for mounded / underground tanks
No
Non-ignition probabilities
Specify probability of non-ignition
Calculate nonignition probability
Direction
Risk
fraction
Non-ignition probability Immediate ignition probabilities
Probability of immediate ignition
fraction Transport Road tanker
Immediate ignition probability Material
Material
fraction
Material characteristics
Toxic only
Material to track
AMMONIA Audit Number: 2716767 Date: 23-11-2020 Time: 16:58 Page 40 of 130
Type of risk effects to model Phase Dispersion
Toxic only
Phase to be released Liquid
Dispersion scope Concentration of interest
ppm
Averaging time for concentration of interest Specify user-defined No averaging time User defined averaging time
s
Distances of interest
Distances of interest 600
m
Averaging time for reports
NLIV [1 hr]
No
IDLH [30 mins]
No
STEL [15 mins]
No
GT3_Box Pressure vessel Venlo_barge_Terminal\Study\overslag\Handelingen 80 boxcontainers*1E-6 Tab
Group
Field
Value
Units
Material
Material
Material
AMMONIA
Specify volume inventory?
Yes
Mass inventory
624,102
kg
Volume inventory
1
m3
Material to track
AMMONIA
Type of risk effects to model
Toxic only
Audit Number: 2716767 Date: 23-11-2020 Time: 16:58 Page 41 of 130
Phase
Risk
Type of risk effects to model
Specified condition
Temperature/bubble point
Temperature 9,85
degC
Pressure (gauge)
5,0862016
bar
Fluid state
Liquid
Liquid mole fraction
1
fraction
Jet fire Horizontal jet only modelling for horizontal releases Reduce risks No for mounded / underground tanks
Non-ignition probabilities
Specify Calculate non-ignition probability probability of non-ignition Non-ignition probability
Immediate ignition probabilities
fraction
Probability of Transport - Road tanker immediate ignition Immediate ignition probability
Scenario
fraction
Pipe dimensions
Pipe length
10
m
Release location
Elevation
1
m
Tank head
1
m
Outdoor release direction
Horizontal
Direction
Outdoor 0 release angle
deg
Audit Number: 2716767 Date: 23-11-2020 Time: 16:58 Page 42 of 130
Short pipe Pipe Pipe characteristics roughness Frequencies
Frequencies of valves
0,045
mm
Frequency of 0 bends in pipe
/m
Frequency of 0 couplings in pipe
/m
Frequency of 0 junctions in pipe
/m
Frequency of 0 excess flow valves
/m
Frequency of 0 non-return valves
/m
Frequency of 0 shut-off valves
/m
Velocity head Excess flow 0 losses valve velocity head losses Non-return 0 valve velocity head losses Shut-off 0 valve velocity head losses Time varying releases
Modelling of Vacuum relief Operating time-varying valve leaks and line ruptures Vacuum relief 0 valve set point
bar
Inventory Tank volume 1 data for timevarying releases
m3
Audit Number: 2716767 Date: 23-11-2020 Time: 16:58 Page 43 of 130
Tank vapour volume
0
m3
Tank liquid volume
1
m3
Tank liquid level
0
m
Maximum vapour release height
m
Minimum mass inventory
0
kg
Maximum mass inventory
1E+09
kg
Safety system Safety No modelling for system time-varying modelling releases (isolation and blowdown) Dispersion Dispersion scope
Concentration of interest
ppm
Averaging time for concentration of interest Specify user- No defined averaging time User defined averaging time
s
Distances of interest
Distances of interest
600
Averaging time for reports
NLIV [1 hr]
No
m
Audit Number: 2716767 Date: 23-11-2020 Time: 16:58 Page 44 of 130
Bund, building and terrain
Terrain and bund definition
IDLH [30 mins]
No
STEL [15 mins]
No
Type of terrain for dispersion
Upgraded Terrain from RunRowSet
Type of pool Type of pool substrate and bund substrate and bunds Building definition
Release building
Buildings\Container_GT3\Building
In-building release?
Inbuilding
Building wake Roof/lee effect Wind or 0 release angle from North Handling of droplets
Trapped
Indoor mass modification factor
3
deg
GT3_Box leak Leak Venlo_barge_Terminal\Study\overslag\Handelingen\GT3_Box 80 boxcontainers*1E-6 Tab
Group
Field
Value
Units
Scenario
Hole
Orifice diameter
15
mm
Use specified discharge coefficient?
No
Discharge coefficient Release location
Elevation
fraction 1
m Audit Number: 2716767 Date: 23-11-2020 Time: 16:58 Page 45 of 130
Tank head
1
Outdoor release direction
Horizontal
Outdoor release angle
0
deg
Event probability Event probability (probability of this event compared with others in this group)
8E-05
fraction
Type of risk effects to model
Reduce risks for mounded / underground tanks
No
Non-ignition probabilities
Specify probability of non-ignition
Calculate nonignition probability
Direction
Risk
m
Non-ignition probability Immediate ignition probabilities
Probability of immediate ignition
fraction Transport Road tanker
Immediate ignition probability Material
Material
Phase Dispersion
fraction
Material characteristics
Toxic only
Material to track
AMMONIA
Type of risk effects to model
Toxic only
Phase to be released Liquid
Dispersion scope Concentration of interest
ppm
Averaging time for concentration of interest Specify user-defined No averaging time
Audit Number: 2716767 Date: 23-11-2020 Time: 16:58 Page 46 of 130
User defined averaging time
s
Distances of interest
Distances of interest 600
m
Averaging time for reports
NLIV [1 hr]
No
IDLH [30 mins]
No
STEL [15 mins]
No
GF3_Tgr Pressure vessel Venlo_barge_Terminal\Study\overslag\Handelingen 60 containers*1E-7 Tab
Group
Field
Value
Units
Material
Material
Material
PROPANE
Specify volume inventory?
Yes
Mass inventory
10285,848
kg
Volume inventory
20
m3
Material to track PROPANE Type of risk Flammable only effects to model Phase
Risk
Specified condition
Temperature/bubble point
Temperature
9,85
degC
Pressure (gauge)
5,3307354
bar
Fluid state
Liquid
Liquid mole fraction
1
Type of risk Jet fire effects to model modelling for horizontal releases
fraction
Horizontal jet only
Audit Number: 2716767 Date: 23-11-2020 Time: 16:58 Page 47 of 130
Reduce risks for No mounded / underground tanks Non-ignition probabilities
Specify probability of non-ignition
Calculate non-ignition probability
Non-ignition probability Immediate ignition probabilities
Probability of immediate ignition
fraction Transport - Road tanker
Immediate ignition probability Scenario
Pipe dimensions Pipe length
10
m
Release location Elevation
1
m
Tank head
2
m
Direction
Short pipe
fraction
Outdoor release Horizontal direction Outdoor release 0 angle
deg
Pipe characteristics
Pipe roughness
0,045
mm
Frequencies
Frequency of bends in pipe
0
/m
Frequency of 0 couplings in pipe
/m
Frequency of 0 junctions in pipe
/m
Frequency of excess flow valves
0
/m
Frequency of non-return valves
0
/m
Frequency of shut-off valves
0
/m
Frequencies of valves
Audit Number: 2716767 Date: 23-11-2020 Time: 16:58 Page 48 of 130
Velocity head losses
Time varying releases
Excess flow valve velocity head losses
0
Non-return valve velocity head losses
0
Shut-off valve velocity head losses
0
Vacuum relief valve
Operating
Vacuum relief valve set point
0
bar
Inventory data Tank volume for time-varying releases
20
m3
Tank vapour volume
0
m3
Tank liquid volume
20
m3
Tank liquid level 0
m
Maximum vapour release height
m
Modelling of time-varying leaks and line ruptures
Minimum mass inventory
0
Maximum mass 1E+09 inventory Safety system modelling for time-varying releases Dispersion
Safety system modelling (isolation and blowdown)
Dispersion scope Concentration of interest
kg kg
No
ppm
Averaging time for Audit Number: 2716767 Date: 23-11-2020 Time: 16:58 Page 49 of 130
concentration of interest Specify userdefined averaging time
No
User defined averaging time
s
Distances of interest
Distances of interest
600
Averaging time for reports
NLIV [1 hr]
No
m
IDLH [30 mins] No STEL [15 mins] No Bund, Terrain and bund Type of terrain building and definition for dispersion terrain
Upgraded Terrain from RunRowSet
Type of pool substrate and bunds
Type of pool substrate and bund
Building definition
Release building In-building release?
Outdoor
Building wake effect
Roof/lee
Wind or release 0 angle from North Handling of droplets
Trapped
Indoor mass modification factor
3
deg
GF3_Tgr leak Leak Venlo_barge_Terminal\Study\overslag\Handelingen\GF3_Tgr 60 containers*1E-7 Audit Number: 2716767 Date: 23-11-2020 Time: 16:58 Page 50 of 130
Tab
Group
Field
Value
Units
Scenario
Hole
Orifice diameter
50
mm
Use specified discharge coefficient?
No
Discharge coefficient Release location
Elevation
1
m
Tank head
2
m
Outdoor release direction
Horizontal
Outdoor release angle
0
deg
Event probability Event probability (probability of this event compared with others in this group)
6E-06
fraction
Type of risk effects to model
Reduce risks for mounded / underground tanks
No
Non-ignition probabilities
Specify probability of non-ignition
Calculate nonignition probability
Direction
Risk
fraction
Non-ignition probability Immediate ignition probabilities
Probability of immediate ignition
fraction Transport Road tanker
Immediate ignition probability Material
Material
Phase
fraction
Material characteristics
Flammable only
Material to track
PROPANE
Type of risk effects to model
Flammable only
Phase to be released Liquid
Audit Number: 2716767 Date: 23-11-2020 Time: 16:58 Page 51 of 130
Dispersion
Dispersion scope Concentration of interest
ppm
Averaging time for concentration of interest Specify user-defined No averaging time User defined averaging time
s
Distances of interest
Distances of interest 600
m
Averaging time for reports
NLIV [1 hr]
No
IDLH [30 mins]
No
STEL [15 mins]
No
GF3_Tkl Pressure vessel Venlo_barge_Terminal\Study\overslag\Handelingen 60 containers*1E-6 Tab
Group
Field
Value
Units
Material
Material
Material
PROPANE
Specify volume inventory?
Yes
Mass inventory
10285,848
kg
Volume inventory
20
m3
Material to track PROPANE Type of risk Flammable only effects to model Phase
Specified condition
Temperature/bubble point
Temperature
9,85
degC
Pressure (gauge)
5,3307354
bar
Fluid state
Liquid Audit Number: 2716767 Date: 23-11-2020 Time: 16:58 Page 52 of 130
Liquid mole fraction Risk
Type of risk Jet fire effects to model modelling for horizontal releases
1
fraction
Horizontal jet only
Reduce risks for No mounded / underground tanks Non-ignition probabilities
Specify probability of non-ignition
Calculate non-ignition probability
Non-ignition probability Immediate ignition probabilities
Probability of immediate ignition
fraction Transport - Road tanker
Immediate ignition probability Scenario
Pipe dimensions Pipe length
10
m
Release location Elevation
1
m
Tank head
2
m
Direction
Short pipe
fraction
Outdoor release Horizontal direction Outdoor release 0 angle
deg
Pipe characteristics
Pipe roughness
0,045
mm
Frequencies
Frequency of bends in pipe
0
/m
Frequency of 0 couplings in pipe
/m
Frequency of 0 junctions in pipe
/m
Audit Number: 2716767 Date: 23-11-2020 Time: 16:58 Page 53 of 130
Frequencies of valves
Frequency of excess flow valves
0
/m
Frequency of non-return valves
0
/m
Frequency of shut-off valves
0
/m
Excess flow valve velocity head losses
0
Non-return valve velocity head losses
0
Shut-off valve velocity head losses
0
Vacuum relief valve
Operating
Vacuum relief valve set point
0
bar
Inventory data Tank volume for time-varying releases
20
m3
Tank vapour volume
0
m3
Tank liquid volume
20
m3
Tank liquid level 0
m
Maximum vapour release height
m
Velocity head losses
Time varying releases
Modelling of time-varying leaks and line ruptures
Minimum mass inventory
0
Maximum mass 1E+09 inventory
kg kg
Audit Number: 2716767 Date: 23-11-2020 Time: 16:58 Page 54 of 130
Safety system modelling for time-varying releases Dispersion
Safety system modelling (isolation and blowdown)
No
Dispersion scope Concentration of interest
ppm
Averaging time for concentration of interest Specify userdefined averaging time
No
User defined averaging time
s
Distances of interest
Distances of interest
600
Averaging time for reports
NLIV [1 hr]
No
m
IDLH [30 mins] No STEL [15 mins] No Bund, Terrain and bund Type of terrain building and definition for dispersion terrain
Upgraded Terrain from RunRowSet
Type of pool substrate and bunds
Type of pool substrate and bund
Building definition
Release building In-building release?
Outdoor
Building wake effect
Roof/lee
Wind or release 0 angle from North Handling of droplets
deg
Trapped
Audit Number: 2716767 Date: 23-11-2020 Time: 16:58 Page 55 of 130
Indoor mass modification factor
3
GF3_Tkl leak Leak Venlo_barge_Terminal\Study\overslag\Handelingen\GF3_Tkl 60 containers*1E-6 Tab
Group
Field
Value
Units
Scenario
Hole
Orifice diameter
10
mm
Use specified discharge coefficient?
No
Discharge coefficient Release location
Elevation
1
m
Tank head
2
m
Outdoor release direction
Horizontal
Outdoor release angle
0
deg
Event probability Event probability (probability of this event compared with others in this group)
6E-05
fraction
Type of risk effects to model
Reduce risks for mounded / underground tanks
No
Non-ignition probabilities
Specify probability of non-ignition
Calculate nonignition probability
Direction
Risk
fraction
Non-ignition probability Immediate ignition probabilities
Probability of immediate ignition
fraction Transport Road tanker
Audit Number: 2716767 Date: 23-11-2020 Time: 16:58 Page 56 of 130
Immediate ignition probability Material
Material
Phase Dispersion
fraction
Material characteristics
Flammable only
Material to track
PROPANE
Type of risk effects to model
Flammable only
Phase to be released Liquid
Dispersion scope Concentration of interest
ppm
Averaging time for concentration of interest Specify user-defined No averaging time User defined averaging time
s
Distances of interest
Distances of interest 600
m
Averaging time for reports
NLIV [1 hr]
No
IDLH [30 mins]
No
STEL [15 mins]
No
LF2_Tgr Atmospheric storage tank Venlo_barge_Terminal\Study\overslag\Handelingen 1000 containers * 1 E-7 Tab
Group
Field
Value
Material
Material
Material
N-HEXANE
Specify volume inventory?
Yes
Mass inventory
18744,663
Volume inventory 28 Material to track
Units
kg m3
N-HEXANE
Audit Number: 2716767 Date: 23-11-2020 Time: 16:58 Page 57 of 130
Type of risk effects to model Phase
Risk
Flammable only
Specified condition Temperature and atmospheric pressure Temperature
9,85
degC
Pressure (gauge)
1E-10
bar
Fluid state
Liquid
Liquid mole fraction
1
Type of risk effects Jet fire modelling to model for horizontal releases
fraction
Horizontal jet only
Reduce risks for No mounded / underground tanks Non-ignition probabilities
Specify probability Calculate nonof non-ignition ignition probability Non-ignition probability
fraction
Immediate ignition Probability of Transport - Road probabilities immediate ignition tanker Immediate ignition probability Scenario
Pipe dimensions
Pipe length
10
m
Release location
Elevation
1
m
Tank head
2
m
Outdoor release direction
Horizontal
Outdoor release angle
0
deg
Pipe characteristics Pipe roughness
0,045
mm
Frequencies
Frequency of bends in pipe
0
/m
Frequency of couplings in pipe
0
/m
Direction
Short pipe
fraction
Audit Number: 2716767 Date: 23-11-2020 Time: 16:58 Page 58 of 130
Frequency of junctions in pipe Frequencies of valves
Velocity head losses
0
/m
Frequency of 0 excess flow valves
/m
Frequency of non- 0 return valves
/m
Frequency of shut- 0 off valves
/m
Excess flow valve velocity head losses
0
Non-return valve velocity head losses
0
Shut-off valve velocity head losses
0
Vacuum relief valve
Operating
Vacuum relief valve set point
0
bar
Inventory data for Tank volume time-varying releases
28
m3
Tank vapour volume
0
m3
Tank liquid volume 28
m3
Tank liquid level
m
Time varying Modelling of timereleases varying leaks and line ruptures
0
Maximum vapour release height
Dispersion
Dispersion scope
m
Minimum mass inventory
0,1
kg
Maximum mass inventory
1E+09
kg
Concentration of interest
ppm
Audit Number: 2716767 Date: 23-11-2020 Time: 16:58 Page 59 of 130
Averaging time for concentration of interest Specify userNo defined averaging time User defined averaging time Distances of interest
Bund, building and terrain
s
Distances of interest
600
Averaging time for NLIV [1 hr] reports
No
Terrain and bund definition
IDLH [30 mins]
No
STEL [15 mins]
No
Type of terrain for Upgraded Terrain dispersion from RunRowSet Type of pool substrate and bunds
Building definition
m
LT1_Tgr bund
Release building In-building release?
Outdoor
Building wake effect
Roof/lee
Wind or release angle from North
0
Handling of droplets
Trapped
deg
Indoor mass 3 modification factor
LF2_Tgr leak Leak Venlo_barge_Terminal\Study\overslag\Handelingen\LF2_Tgr 1000 containers * 1 E-7 Tab
Group
Field
Value
Units
Audit Number: 2716767 Date: 23-11-2020 Time: 16:58 Page 60 of 130
Scenario
Hole
Orifice diameter
50
Use specified discharge coefficient?
No
mm
Discharge coefficient Release location
Elevation
1
m
Tank head
2
m
Outdoor release direction
Horizontal
Outdoor release angle
0
deg
Event probability Event probability (probability of this event compared with others in this group)
0,0001
fraction
Type of risk effects to model
Reduce risks for mounded / underground tanks
No
Non-ignition probabilities
Specify probability of non-ignition
Calculate nonignition probability
Direction
Risk
fraction
Non-ignition probability Immediate ignition probabilities
Probability of immediate ignition
fraction Transport Road tanker
Immediate ignition probability Material
Material
Phase Dispersion
fraction
Material characteristics
Flammable only
Material to track
N-HEXANE
Type of risk effects to model
Flammable only
Phase to be released Liquid
Dispersion scope Concentration of interest
ppm
Audit Number: 2716767 Date: 23-11-2020 Time: 16:58 Page 61 of 130
Averaging time for concentration of interest Specify user-defined No averaging time User defined averaging time
s
Distances of interest
Distances of interest 600
m
Averaging time for reports
NLIV [1 hr]
No
IDLH [30 mins]
No
STEL [15 mins]
No
LF2_Tkl Atmospheric storage tank Venlo_barge_Terminal\Study\overslag\Handelingen 1000*1E-6 Tab
Group
Field
Value
Material
Material
Material
N-HEXANE
Specify volume inventory?
Yes
Mass inventory
18744,663
Volume inventory 28
Phase
Units
kg m3
Material to track
N-HEXANE
Type of risk effects to model
Flammable only
Specified condition Temperature and atmospheric pressure Temperature
9,85
degC
Pressure (gauge)
1E-10
bar
Fluid state
Liquid
Liquid mole fraction
1
fraction
Audit Number: 2716767 Date: 23-11-2020 Time: 16:58 Page 62 of 130
Risk
Type of risk effects Jet fire modelling to model for horizontal releases
Horizontal jet only
Reduce risks for No mounded / underground tanks Non-ignition probabilities
Specify probability Calculate nonof non-ignition ignition probability Non-ignition probability
fraction
Immediate ignition Probability of Transport - Road probabilities immediate ignition tanker Immediate ignition probability Scenario
Pipe dimensions
Pipe length
10
m
Release location
Elevation
1
m
Tank head
2
m
Outdoor release direction
Horizontal
Outdoor release angle
0
deg
Pipe characteristics Pipe roughness
0,045
mm
Frequencies
Frequency of bends in pipe
0
/m
Frequency of couplings in pipe
0
/m
Frequency of junctions in pipe
0
/m
Frequency of 0 excess flow valves
/m
Frequency of non- 0 return valves
/m
Frequency of shut- 0 off valves
/m
Direction
Short pipe
fraction
Frequencies of valves
Velocity head losses
Excess flow valve velocity head losses
0
Audit Number: 2716767 Date: 23-11-2020 Time: 16:58 Page 63 of 130
Non-return valve velocity head losses
0
Shut-off valve velocity head losses
0
Vacuum relief valve
Operating
Vacuum relief valve set point
0
bar
Inventory data for Tank volume time-varying releases
28
m3
Tank vapour volume
0
m3
Tank liquid volume 28
m3
Tank liquid level
m
Time varying Modelling of timereleases varying leaks and line ruptures
0
Maximum vapour release height
Dispersion
Dispersion scope
m
Minimum mass inventory
0
kg
Maximum mass inventory
1E+09
kg
Concentration of interest
ppm
Averaging time for concentration of interest Specify userNo defined averaging time User defined averaging time Distances of interest
s
Distances of interest
600
Averaging time for NLIV [1 hr] reports
No
m
Audit Number: 2716767 Date: 23-11-2020 Time: 16:58 Page 64 of 130
Bund, building and terrain
Terrain and bund definition
IDLH [30 mins]
No
STEL [15 mins]
No
Type of terrain for Upgraded Terrain dispersion from RunRowSet Type of pool substrate and bunds
Building definition
LT1_Tkl bund
Release building In-building release?
Outdoor
Building wake effect
Roof/lee
Wind or release angle from North
0
Handling of droplets
Trapped
deg
Indoor mass 3 modification factor
LF2_Tkl Leak Venlo_barge_Terminal\Study\overslag\Handelingen\LF2_Tkl 1000*1E-6 Tab
Group
Field
Value
Units
Scenario
Hole
Orifice diameter
20
mm
Use specified discharge coefficient?
No
Discharge coefficient Release location Direction
fraction
Elevation
1
m
Tank head
2
m
Outdoor release direction
Horizontal
Outdoor release angle
0
deg
Audit Number: 2716767 Date: 23-11-2020 Time: 16:58 Page 65 of 130
Risk
Event probability Event probability (probability of this event compared with others in this group)
0,001
Type of risk effects to model
Reduce risks for mounded / underground tanks
No
Non-ignition probabilities
Specify probability of non-ignition
Calculate nonignition probability
Non-ignition probability Immediate ignition probabilities
Probability of immediate ignition
fraction Transport Road tanker
Immediate ignition probability Material
Material
Phase Dispersion
fraction
fraction
Material characteristics
Flammable only
Material to track
N-HEXANE
Type of risk effects to model
Flammable only
Phase to be released Liquid
Dispersion scope Concentration of interest
ppm
Averaging time for concentration of interest Specify user-defined No averaging time User defined averaging time
s
Distances of interest
Distances of interest 600
m
Averaging time for reports
NLIV [1 hr]
No
Audit Number: 2716767 Date: 23-11-2020 Time: 16:58 Page 66 of 130
IDLH [30 mins]
No
STEL [15 mins]
No
LT1_Lgr Atmospheric storage tank Venlo_barge_Terminal\Study\overslag\Handelingen 300 containers * 1 E-7 Tab
Group
Field
Value
Units
Material
Material
Material
ACRYLONITRILE
Specify volume inventory?
Yes
Mass inventory
818,17239
Volume inventory 1
Phase
m3
Material to track
ACRYLONITRILE
Type of risk effects to model
Toxic only
Specified condition
Temperature and atmospheric pressure
Temperature
9,85
degC
Pressure (gauge) 1E-10
Risk
Type of risk effects to model
Non-ignition probabilities
Fluid state
Liquid
Liquid mole fraction
1
kg
bar fraction
Jet fire modelling Horizontal jet only for horizontal releases Reduce risks for mounded / underground tanks
No
Specify probability of non-ignition
Calculate nonignition probability
Non-ignition probability
fraction
Audit Number: 2716767 Date: 23-11-2020 Time: 16:58 Page 67 of 130
Immediate ignition probabilities
Probability of immediate ignition
Transport - Road tanker
Immediate ignition probability Scenario
Pipe dimensions
Pipe length
10
m
Release location
Elevation
1
m
Tank head
0,2
m
Outdoor release direction
Horizontal
Outdoor release angle
0
deg
Pipe characteristics
Pipe roughness
0,045
mm
Frequencies
Frequency of bends in pipe
0
/m
Frequency of 0 couplings in pipe
/m
Frequency of junctions in pipe
0
/m
Frequency of excess flow valves
0
/m
Frequency of 0 non-return valves
/m
Frequency of shut-off valves
/m
Direction
Short pipe
fraction
Frequencies of valves
Velocity head losses
0
Excess flow valve 0 velocity head losses Non-return valve 0 velocity head losses Shut-off valve velocity head losses
0
Audit Number: 2716767 Date: 23-11-2020 Time: 16:58 Page 68 of 130
Time varying Modelling of time- Vacuum relief releases varying leaks and valve line ruptures Vacuum relief valve set point
Operating
0
bar
Inventory data for Tank volume time-varying releases
1
m3
Tank vapour volume
0
m3
Tank liquid volume
1
m3
Tank liquid level
0
m
Maximum vapour release height
Dispersion
Dispersion scope
m
Minimum mass inventory
0,1
kg
Maximum mass inventory
1E+09
kg
Concentration of interest
ppm
Averaging time for concentration of interest Specify userNo defined averaging time User defined averaging time
s
Distances of interest
Distances of interest
600
Averaging time for reports
NLIV [1 hr]
No
IDLH [30 mins]
No
STEL [15 mins]
No
Bund, Terrain and bund Type of terrain building and definition for dispersion terrain
m
Upgraded Terrain from RunRowSet
Audit Number: 2716767 Date: 23-11-2020 Time: 16:58 Page 69 of 130
Type of pool substrate and bunds
LT2_Lgr bund
Building definition Release building In-building release?
Outdoor
Building wake effect
Roof/lee
Wind or release 0 angle from North Handling of droplets
Trapped
Indoor mass modification factor
3
deg
LT1_Lgr leak Leak Venlo_barge_Terminal\Study\overslag\Handelingen\LT1_Lgr 300 containers * 1 E-7 Tab
Group
Field
Value
Units
Scenario
Hole
Orifice diameter
50
mm
Use specified discharge coefficient?
No
Discharge coefficient Release location Elevation Direction
Risk
Event probability (probability of this event
fraction 1
m
Tank head
0,2
m
Outdoor release direction
Horizontal
Outdoor release angle
0
deg
Event probability
3E-05
fraction
Audit Number: 2716767 Date: 23-11-2020 Time: 16:58 Page 70 of 130
compared with others in this group) Type of risk Reduce risks for No effects to model mounded / underground tanks Non-ignition probabilities
Specify probability Calculate nonof non-ignition ignition probability Non-ignition probability
Immediate ignition probabilities
fraction
Probability of Transport - Road immediate ignition tanker Immediate ignition probability
Material
Material
fraction
Material characteristics
Toxic and flammable
Material to track
ACRYLONITRILE
Type of risk effects Toxic only to model
Dispersion
Phase
Phase to be released
Dispersion scope
Concentration of interest
Liquid ppm
Averaging time for concentration of interest Specify userNo defined averaging time User defined averaging time Distances of interest
s
Distances of interest
600
Averaging time NLIV [1 hr] for reports
No
IDLH [30 mins]
No
STEL [15 mins]
No
m
Audit Number: 2716767 Date: 23-11-2020 Time: 16:58 Page 71 of 130
LT1_Lkl Atmospheric storage tank Venlo_barge_Terminal\Study\overslag\Handelingen 300*1E-6 Tab
Group
Field
Value
Units
Material
Material
Material
ACRYLONITRILE
Specify volume inventory?
Yes
Mass inventory
818,17239
Volume inventory 1
Phase
m3
Material to track
ACRYLONITRILE
Type of risk effects to model
Toxic only
Specified condition
Temperature and atmospheric pressure
Temperature
9,85
degC
Pressure (gauge) 1E-10
Risk
Type of risk effects to model
Non-ignition probabilities
Fluid state
Liquid
Liquid mole fraction
1
bar fraction
Jet fire modelling Horizontal jet only for horizontal releases Reduce risks for mounded / underground tanks
No
Specify probability of non-ignition
Calculate nonignition probability
Non-ignition probability Immediate ignition probabilities
kg
Probability of immediate ignition
fraction Transport - Road tanker Audit Number: 2716767 Date: 23-11-2020 Time: 16:58 Page 72 of 130