- •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?
Inserting a Short pipe Scenario and set up the equivalent input data
The Short pipe Scenario models the same type of hazardous event as the Time-varying short pipe release Scenario, but it calculates the initial discharge rate, without performing any time-varying discharge modelling. Inserting this Scenario involves repeating some of the data-input, but this is the approach taken in this tutorial as it will make the analysis clearer and easier to maintain: if you need to change some aspect of the input data you can edit the Scenario and rerun the calculations, whereas if you used a User-defined release Scenario you would have to edit and rerun the Time-varying Scenario first, then create a new User-defined release Scenario, and delete the previous User-defined release Scenario.
Before you insert the Short pipe Scenario, rename the Time varying Scenario to add “- time-varying not needed” at the end of the name.
Next, insert a Short pipe Scenario, name it Line rupture, liquid, and then edit it and set the values as follows:
Tab section |
Input field |
Value |
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|
Scenario |
Scenario type |
Line rupture |
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|
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|
Pipe internal diameter |
25.4 mm |
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|
|
|
Pipe length |
9 m |
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|
Elevation |
0.1 m |
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|
Tank head |
4.6 m |
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|
Material |
Phase to be released |
Liquid |
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|
|
Short pipe |
Frequency of bends in pipe |
0.11 per m |
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|
|
The Release height from vessel bottom field is not included in the input data for a Short pipe Scenario, which means that the program is not able to calculate the release phase, and you must use the Phase to be released field to specify whether you want to model a release from the liquid side or the vapour side.
You will see that there is no Risk tab in the dialog. This is because the Mode is set to Discharge instead of Risk. When the Mode is set to either Discharge or Consequence, the input dialogs only include the fields that are used in the consequence calculations, and the fields that are specific to the risk calculations do not appear.
To complete the full data for the Scenario, change the Mode to Risk, and then open the dialog again, move to the Risk tab, and set the Event frequency to 1E-5 /AvgeYear.
Run the consequence calculations for the Short pipe and view the results
Select the short pipe Scenario and select Run. When the calculations are complete, view the graphs for all of the Weathers.
You will see that there is a Pool Vaporisation tab in the Graphs View, which means that the liquid in the release did rain out. If you view the reports and look at the Commentary Report, you will see that rainout fraction is about 0.7 for all three Weathers, and the formation and behaviour of the pool will have an effect on the dispersion and on the toxic effects.
| SAFETI | April 2018 | www.dnvgl.com/software |
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