- •Contents
- •1 An introduction to Safeti
- •What to Expect of this Tutorial
- •Starting the program running
- •The main window
- •Opening the Safeti examples file
- •The Risk Supertabs
- •The tabs in the Study Tree pane
- •The Models tab section
- •Level 1: the Workspace
- •Level 2: the Study
- •Level 3: the Equipment item
- •Level 4: the Scenario
- •The Weather tab section
- •The Parameters tab section
- •The Materials tab section
- •Pure Components
- •Mixtures
- •Warehouse Materials
- •The Map tab section
- •Bund types
- •Terrain types
- •Building types and Buildings
- •Raster Image Set
- •The Risk tab section
- •Categories
- •Ignitions
- •Populations
- •Vulnerabilities
- •Risk transects
- •Risk ranking points
- •Plant Boundaries
- •Viewing input data
- •The input dialog for the Propane Pressure Vessel Equipment item
- •The Grid View allows you to work on input data for multiple items
- •Running the consequence calculations and viewing the results
- •Running the calculations
- •Viewing the graphs for the Propane Scenarios
- •Viewing results on the GIS, against the background of map images
- •Viewing the Reports for the Catastrophic rupture Scenario
- •Summary group: Consequence Summary Report
- •Summary group: Flammable Hazards Report
- •Input group: Input Report
- •Equipment group: Discharge Report
- •Equipment group: Dispersion Report
- •Equipment group: Commentary Report
- •Equipment group: Averaging Times Report
- •Equipment group: Dynamic Fireball Report
- •Equipment group: Explosion Report
- •Running the risk calculations and viewing the results
- •Running the calculations
- •The list of available risk results
- •Viewing the risk results
- •Multi-Level risk contours for day and night combined
- •Multi-Row contours for a risk level of 1x10-6/AvgeYear
- •Category PLL societal risk results for day and night combined
- •2 Setting up your own analysis
- •The form of the analysis
- •The Equipment and Scenarios defined in the analysis
- •Creating a new workspace
- •Saving the workspace
- •The contents of a new workspace
- •Setting up the map image
- •Inserting the raster image
- •Ensure that there is a Raster Image Set in the Map tab section
- •Insert a Raster Image inside the Set
- •Placing the image in the GIS Input View
- •Setting the co-ordinates and size of the image
- •The location of the site on the map
- •Setting up Weather data for day and night
- •Creating a second Weather folder
- •Defining representative day-time weathers
- •Defining representative night-time weathers
- •Setting up the Run Rows
- •Creating a second Run Row
- •Setting the selection of Weather folders
- •Saving the changes to the workspace
- •3 Performing the consequence analysis
- •Defining the pressure vessel that contains a toxic material
- •Turn on the option to insert Equipment on the GIS
- •Insert a Pressure Vessel Equipment item
- •Setting the input data for the vessel
- •The Material tab section
- •The Geometry tab section
- •A Summary of the Input Data
- •Defining a catastrophic rupture scenario
- •Inserting the Scenario
- •Setting the input data
- •Elevation in Scenario tab section
- •Event frequency in Risk tab section
- •Run the calculations for the Scenario and view the results
- •Viewing the set of Graphs
- •Viewing outdoor toxic lethality results against the map
- •Defining the second Scenario: a liquid release from pipework
- •Insert a Time varying short pipe Scenario
- •Supplying the tank shape data for the Pressure Vessel
- •Setting the input data for the Scenario
- •Scenario tab section
- •Risk tab section
- •Material tab section
- •Short pipe tab section
- •Time varying releases tab section
- •Running the discharge calculations
- •Using the averaged discharge results to create a User-defined source Scenario
- •Inserting a Short pipe Scenario and set up the equivalent input data
- •Run the consequence calculations for the Short pipe and view the results
- •Defining the third scenario: toxic vapour from pipework
- •Defining three flammable releases
- •Setting the input data for the propane Equipment item
- •Copying the Equipment item
- •Changing the Material selection
- •Changing the coordinates
- •Running the consequence calculations and viewing the results
- •Jet Fire Graphs
- •Pool Fire Graphs
- •Fireball Graphs
- •Explosion Graphs
- •Flash Fire Graph
- •Defining toxic releases from a rail tank wagon
- •Inserting a Route Model
- •Defining the rupture and leak Scenarios
- •Copying the existing Chlorine Equipment item
- •Editing the Equipment item
- •Editing the Catastrophic rupture Scenario
- •Defining the liquid leak
- •Defining the vapour leak
- •Defining the rail route inside the site
- •Drawing the route on the GIS
- •Completing the input data for the route segment
- •Running the consequence calculations and viewing the results
- •Saving the workspace
- •4 Performing the risk calculations
- •Viewing the wind rose data for the Weather folders
- •Setting up the population data
- •Defining the night population data
- •Drawing the shapes
- •Using the Grid View to set the population values
- •Defining the day population data
- •Adding the shape for the school
- •Setting the population values
- •Setting up the ignition source data
- •Setting up the risk ranking point data
- •Defining the Models and Populations Playlists for the two Run Rows
- •Defining a Models Playlist for the Day Run Row
- •Defining a Models Playlist for the Night Run Row
- •Defining the Populations Playlists
- •Running the risk calculations and viewing the results
- •Comparing the Multi-Level Risk Contour Plots for Day and Night
- •Viewing the individual risk ranking results for the school
- •Viewing the societal risk results for day, night, and the whole year
- •Setting values for the Combination Factors
- •Viewing the FN Curve
- •Saving the workspace
- •What next?
In the Toxic Lethality graph, the greatest effect distances are for the 1.5 m/s D weather outdoors, with a distance of about 450 m to a lethality level of 10%, which is approximately a fifth of the distance reached by the catastrophic rupture. The least stable condition, 3 m/s, B, reaches only about 200 m for 10% lethality outdoors.
If you open a GIS Results View for all three Weathers and view the Toxic Outdoor Lethality Footprint, you will see that the effects for 0.1% lethality do not reach the village or the town.
Defining the third scenario: toxic vapour from pipework
The vapour release is the rupture of a two-inch pipe attached to the top of the sphere. The line runs 3.4 m horizontally, then vertically downwards, and the rupture is assumed to occur 1 m from the ground.
Create the Scenario as a copy of the Line rupture, liquid Scenario, rename the copy to Line rupture, vapour, and change the input data as follows:
Tab Section |
Input Field |
Value |
|
|
|
Scenario |
Pipe internal diameter |
50.8 mm |
|
|
|
|
Pipe length |
13 m |
|
|
|
|
Elevation |
1 m |
|
|
|
|
Outdoor release direction |
Down – impinging on the ground |
|
|
|
Risk |
Event frequency |
1E-5 /AvgeYear |
|
|
|
Material |
Phase to be released |
Vapour |
|
|
|
Short pipe |
Frequency of Bends |
0.08 per m |
|
|
|
The release rate from the two-inch vapour line is similar to that from the one-inch liquid line, and the two pipework releases give very similar effect distances.
| SAFETI | April 2018 | www.dnvgl.com/software |
Page 43 |
