EXPLOSIVENESS OF HYDROCARBON VAPOURS IN INDUSTRIAL INSTALLATIONS UNDER VARIOUS CONDITIONS
The result's identifiers
Result code in IS VaVaI
<a href="https://www.isvavai.cz/riv?ss=detail&h=RIV%2F00007064%3AK02__%2F20%3AN0000079" target="_blank" >RIV/00007064:K02__/20:N0000079 - isvavai.cz</a>
Result on the web
<a href="https://www.witpress.com/elibrary/wit-transactions-on-engineering-sciences/129/37660" target="_blank" >https://www.witpress.com/elibrary/wit-transactions-on-engineering-sciences/129/37660</a>
DOI - Digital Object Identifier
<a href="http://dx.doi.org/10.2495/RISK200081" target="_blank" >10.2495/RISK200081</a>
Alternative languages
Result language
angličtina
Original language name
EXPLOSIVENESS OF HYDROCARBON VAPOURS IN INDUSTRIAL INSTALLATIONS UNDER VARIOUS CONDITIONS
Original language description
Cleaning, maintenance and repair works in the petroleum transport and storage equipment are activities connected with an increased risk of explosion. After the pipes and vessels have been emptied, residual amounts of flammable liquids can spontaneously evaporate into the equipment vapour space. To appraise the risk of explosion, it is necessary to assess the formation of an explosive mixture of hydrocarbons with air under various operating conditions. A device was designed that simulates the described system at a reduced scale under stationary conditions for which a vapour-liquid equilibrium is reached. The equilibrium gas phase was analysed to determine the influence of temperature, pressure, and initial liquid phase volume proportion on the lower explosion limit percentage value. The results of the experiments were compared with numerical calculations. Aspen Hysys software was used for theoretical calculations of vapour liquid equilibrium and estimation of the lower explosive limit percentage value. It has been confirmed that the concentration of flammable substances in the mixture increases with temperature. As expected, the concentration of flammable substances at a certain temperature decreased with increasing pressure, as the partial pressure of flammable substances remained approximately the same at elevated partial pressures of air. The prediction of the vapour phase composition based on equilibrium calculations in the process simulator provided a pessimistic estimate of the results with a higher hydrocarbon concentration than the experimental measurements. Since the theoretical estimate of the composition of the hydrocarbon-containing atmosphere was always on the "safe side", it seems to be suitable for predicting the risk of explosion in industrial facilities under known conditions - temperature, pressure, composition and amount of flammable substance.
Czech name
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Czech description
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Classification
Type
D - Article in proceedings
CEP classification
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OECD FORD branch
20402 - Chemical process engineering
Result continuities
Project
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Continuities
I - Institucionalni podpora na dlouhodoby koncepcni rozvoj vyzkumne organizace
Others
Publication year
2020
Confidentiality
S - Úplné a pravdivé údaje o projektu nepodléhají ochraně podle zvláštních právních předpisů
Data specific for result type
Article name in the collection
Risk Analysis XII
ISBN
978-1-78466-401-5
ISSN
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e-ISSN
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Number of pages
11
Pages from-to
89-99
Publisher name
WIT Transactions on Engineering Sciences
Place of publication
UK
Event location
Lisabon
Event date
Jun 22, 2020
Type of event by nationality
WRD - Celosvětová akce
UT code for WoS article
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