Development of Boiling Liquid ExpandingVapor Explosion (BLEVE) Model for Process Plant Design
Boiling Liquid Expanding Vapor Explosion (BLEVE) was dangerous and can cause humongous loss for the process plant. Reid (1976) defined BLEVEs as the sudden loss of containment of a liquid that is at a superheated temperature for atmospheric conditions. There are a lot of commercialized tools in e...
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my-utp-utpedia.76222017-01-25T09:46:40Z http://utpedia.utp.edu.my/7622/ Development of Boiling Liquid ExpandingVapor Explosion (BLEVE) Model for Process Plant Design Abdul, Mohamad Irwan TP Chemical technology Boiling Liquid Expanding Vapor Explosion (BLEVE) was dangerous and can cause humongous loss for the process plant. Reid (1976) defined BLEVEs as the sudden loss of containment of a liquid that is at a superheated temperature for atmospheric conditions. There are a lot of commercialized tools in estimating the effects of BLEVE but very complicated and not user friendly. Development of model from Microsoft Excel in estimating the BLEVE effects was a main objective inthis project. In this project, a process in MLNG Malaysia was utilized as one of the case study. Stabilizer C-2502 was utilized as case study in this project. The feed to Stabilizer- 2502, consist of the bottom form the Demethanizer and any propane, which is being re-processed from the liquefaction unit. In this project, HYSYS simulator acted as "live" thermodynamic database to beextracted to Microsoft Excel for effect estimation. The first effect is overpressure or blast effect. In this case study the maximum overpressure due to distance is 0.87 psi which the damage is partial demolition of houses. The second effect is thermal radiation. The result that obtained is in term radiation dose. The maximum radiation dose is 721.171 kJ/m2. Thiswill cause third -degree burns (99%fatal). In this Final Year Project, the result from this BLEVE model is compared to the result from SAFETI Software. The SAFETI Software has being established for many years and well known in the process industries. This is to validate the result the obtained from BLEVE model. The main objectives were accomplished. The desired data from HYSYS is extracted toME interface to performs the calculation and effect estimation. Further development of this project is commercially advisable. Universiti Teknologi Petronas 2005-02 Final Year Project NonPeerReviewed application/pdf en http://utpedia.utp.edu.my/7622/1/2005%20-%20Development%20of%20Boiling%20Liquid%20ExpandingVapor%20Explosion%20%28BLEVE%29%20Model%20for%20Process%20Plant%20Des.pdf Abdul, Mohamad Irwan (2005) Development of Boiling Liquid ExpandingVapor Explosion (BLEVE) Model for Process Plant Design. Universiti Teknologi Petronas. (Unpublished) |
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TP Chemical technology Abdul, Mohamad Irwan Development of Boiling Liquid ExpandingVapor Explosion (BLEVE) Model for Process Plant Design |
description |
Boiling Liquid Expanding Vapor Explosion (BLEVE) was dangerous and can cause
humongous loss for the process plant. Reid (1976) defined BLEVEs as the sudden loss of
containment of a liquid that is at a superheated temperature for atmospheric conditions.
There are a lot of commercialized tools in estimating the effects of BLEVE but very
complicated and not user friendly. Development of model from Microsoft Excel in
estimating the BLEVE effects was a main objective inthis project.
In this project, a process in MLNG Malaysia was utilized as one of the case study.
Stabilizer C-2502 was utilized as case study in this project. The feed to Stabilizer- 2502,
consist of the bottom form the Demethanizer and any propane, which is being re-processed
from the liquefaction unit. In this project, HYSYS simulator acted as "live"
thermodynamic database to beextracted to Microsoft Excel for effect estimation.
The first effect is overpressure or blast effect. In this case study the maximum overpressure
due to distance is 0.87 psi which the damage is partial demolition of houses. The second
effect is thermal radiation. The result that obtained is in term radiation dose. The maximum
radiation dose is 721.171 kJ/m2. Thiswill cause third -degree burns (99%fatal).
In this Final Year Project, the result from this BLEVE model is compared to the result
from SAFETI Software. The SAFETI Software has being established for many years and
well known in the process industries. This is to validate the result the obtained from
BLEVE model.
The main objectives were accomplished. The desired data from HYSYS is extracted toME
interface to performs the calculation and effect estimation. Further development of this
project is commercially advisable. |
format |
Final Year Project |
author |
Abdul, Mohamad Irwan |
author_facet |
Abdul, Mohamad Irwan |
author_sort |
Abdul, Mohamad Irwan |
title |
Development of Boiling Liquid ExpandingVapor Explosion (BLEVE)
Model for Process Plant Design |
title_short |
Development of Boiling Liquid ExpandingVapor Explosion (BLEVE)
Model for Process Plant Design |
title_full |
Development of Boiling Liquid ExpandingVapor Explosion (BLEVE)
Model for Process Plant Design |
title_fullStr |
Development of Boiling Liquid ExpandingVapor Explosion (BLEVE)
Model for Process Plant Design |
title_full_unstemmed |
Development of Boiling Liquid ExpandingVapor Explosion (BLEVE)
Model for Process Plant Design |
title_sort |
development of boiling liquid expandingvapor explosion (bleve)
model for process plant design |
publisher |
Universiti Teknologi Petronas |
publishDate |
2005 |
url |
http://utpedia.utp.edu.my/7622/1/2005%20-%20Development%20of%20Boiling%20Liquid%20ExpandingVapor%20Explosion%20%28BLEVE%29%20Model%20for%20Process%20Plant%20Des.pdf http://utpedia.utp.edu.my/7622/ |
_version_ |
1739831487972245504 |
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13.214268 |