Presented at: HAZARDS XX, Manchester, 23–25 November 2008Explosion venting is the most frequently used method for mitigating the effects from accidental dust explosions in the process industry. Optimal design of vent systems and credible execution of risk assessments in powder handling plants require practical and reliable ways of predicting the course and consequences of vented dust explosions. The main parameters of interest include flame propagation and pressure build-up inside the vented enclosure, the volume engulfed by the flame, and the magnitude of blast waves outside the enclosure. Extensive experimental work forms the empirical foundation for current standards on vent sizing, such as EN 14491 and NFPA 68, and various types of soft...
The purpose of the present paper is threefold. First, a brief review of modelling, main results, and...
Accidental gas explosions are a significant concern in process industries. In an explosion event, th...
A vented corn starch dust explosion in an 11.5 m3 vessel is studied by comparing experiments, simula...
Explosion venting is the most frequently used method for mitigating the effects from accidental dust...
Modelling of industrial dust explosions poses a formidable challenge to researchers and safety engin...
Presented at: HAZARDS XIX, Manchester, 28-30 March 2006The purpose of the present paper is threefold...
The use of explosion venting is a widely applied safety measure, mitigating the effects of an intern...
This dissertation describes the development and validation of a methodology for estimating the conse...
This study presents CFD simulations of biomass dust explosions in a newly developed experimental 1 m...
Dust explosions pose a serious hazard to both personnel and equipment in industries that handles com...
Dust explosion is a constant threat to industries which deal with combustible powders such as woodwo...
Protection against dust explosion hazards is often based on venting. Most design methods, whether co...
Dust explosions are among the most hazardous accidents affecting industrial facilities processing pa...
AbstractDespite a much greater awareness of dust explosion hazards, numerous accidents continue to h...
PresentationThe purpose of this study is to compare calculated sizes of explosion venting fireballs ...
The purpose of the present paper is threefold. First, a brief review of modelling, main results, and...
Accidental gas explosions are a significant concern in process industries. In an explosion event, th...
A vented corn starch dust explosion in an 11.5 m3 vessel is studied by comparing experiments, simula...
Explosion venting is the most frequently used method for mitigating the effects from accidental dust...
Modelling of industrial dust explosions poses a formidable challenge to researchers and safety engin...
Presented at: HAZARDS XIX, Manchester, 28-30 March 2006The purpose of the present paper is threefold...
The use of explosion venting is a widely applied safety measure, mitigating the effects of an intern...
This dissertation describes the development and validation of a methodology for estimating the conse...
This study presents CFD simulations of biomass dust explosions in a newly developed experimental 1 m...
Dust explosions pose a serious hazard to both personnel and equipment in industries that handles com...
Dust explosion is a constant threat to industries which deal with combustible powders such as woodwo...
Protection against dust explosion hazards is often based on venting. Most design methods, whether co...
Dust explosions are among the most hazardous accidents affecting industrial facilities processing pa...
AbstractDespite a much greater awareness of dust explosion hazards, numerous accidents continue to h...
PresentationThe purpose of this study is to compare calculated sizes of explosion venting fireballs ...
The purpose of the present paper is threefold. First, a brief review of modelling, main results, and...
Accidental gas explosions are a significant concern in process industries. In an explosion event, th...
A vented corn starch dust explosion in an 11.5 m3 vessel is studied by comparing experiments, simula...