- •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?
Defining three flammable releases
There is a propane sphere at the far north of the site. The propane sphere has the same dimensions as the chlorine sphere and the same design of pipework, and is also operating under saturation conditions at atmospheric temperature.
Setting the input data for the propane Equipment item
You can define the propane sphere Equipment item and all of the Scenarios by copying the chlorine Equipment item and its Scenarios and simply changing the selection of discharge material and the geographical co-ordinates for the vessel.
Copying the Equipment item
Select the Chlorine Pressure Vessel, copy and paste it, and name the copy Propane, Saturated 10 degC.
Changing the Material selection
Open the input dialog for the propane Pressure Vessel, and change the selection for the Material field from CHLORINE to PROPANE. After you make the selection there will be a brief pause while the program calculates the saturation pressure at 10oC and the mass for the inventory, and then displays the changed values in the dialog.
Changing the coordinates
In the Geometry tab, set the new location as shown in the illustration. After changing each value you should press [Enter] to
“commit” the changed value.
This completes the work on the input data, and you can OK the dialog.
You do not need to make any changes to the input data for the Scenarios, as the values that are set in the Scenario dialogs are appropriate for the propane vessel. However, you can delete the Time varying Scenario, as you will not be performing the investigation of the time-varying behaviour for the propane vessel.
Running the consequence calculations and viewing the results
Select the Propane Equipment node and run the calculations for all three Scenarios.
You can view the results for all three Scenarios at the same time, as long as you view the results for the same single Weather for all Scenarios. To do this, move to the Weathers tab of the Study Tree, select the Category 1.5/D Weather, and then click on the Graphs option in the Home tab of the Ribbon Bar.
In the Results selection dialog that appears, check the box next to the propane Equipment item to select all of the propane Scenarios for plotting, click on the right arrow to move the items to the Selected items list, and then click Finish to view the Graphs.
The Graph View will contains tab sections for Concentration graphs, as with the toxic Models, but it will contain Jet fire, Fireball, Pool Fire, Explosions and Flash Fire tab sections instead of the Toxic tab section.
The main features of the graphs are described below.
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Jet Fire Graphs
The Jet Fire tab section contains three graphs, which are presenting results for the two pipework failures. The first graph shows radiation level versus distance, the second shows Intensity Radii to the lowest of the three default radiation levels set in the input data (4 kW/m2), and the third graph shows Lethality Radii to a lethality level of 1%. The maximum downwind effect distance shown in these graphs is around 33 m, which is the distance for 4 kW/m2 for the liquid line rupture release.
If a given Fire Radii graph is showing results for more than one Scenario or more than one Weather, then it will initially only be displaying results for a single level, which will be the lowest level set for that type of result (e.g. the lowest intensity level, or the lowest lethality level). This is different from a graph for a single Scenario and Weather, which will initially always display results for all available levels.
To see results for additional Fire Radii levels, click on Series… in the Configuration tab of the Ribbon Bar to open the Edit Series Properties dialog as shown. This dialog lists each of the available level-results for each Scenario, and you can check the boxes for additional levels to include them in the graph.
Pool Fire Graphs
There are two sets of Pool Fire Graphs: a set for the early pool fire, which is modelled for a continuous release only and occurs at the beginning of the release, at the time when the spill rate into the pool equals the fire burn rate, and a set for the late pool fire, which occurs at a time when the pool has reached its maximum radius. Each set contains three graphs, as with the jet fire graphs.
The early pool fire graphs are showing results the liquid line rupture release, as this is the only continuous Scenario that gives rainout, and this means that the two Radii graphs will initially be showing the results for more than one level. The maximum downwind effect distance is about 16 m, to a radiation level of 4 kW/m2 for late pool fire, and the distance to a.lethality level of 1% is about 13 m. The late pool fire graphs show results for both the liquid line rupture and the catastrophic rupture, so they initially show results for only one level.
Fireball Graphs
The Fireball tab section contains five graphs, with graphs of the time-dependent geometry and surface emissive power in addition to the three graphs of radiation results. The graphs show results only for the rupture, and this means that the two Radii graphs will initially be showing the results for more than one level. The maximum downwind effect distance is about 660 m, to a radiation level of 4 kW/m2, and the distance to a .lethality level of 1% is about 260 m.
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