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The thematic network S2S is a European Community Project carried out in the "Competitive and Sustainable Growth" programme and funded in part by contract number G1RT-CT-2002-05092.
 

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Training

2 entries found!

Safety valve sizing for highly viscous flow according to EN ISO 4126-4 and industrial practice

Screening Tests: type of crucibles


65 entries found!

01 - Accident caused by an inexact P&I connected also to a fatality

02 - Fire on a hot oil furnace

04 - Accident involving contractors' injury during the operation of opening of a vessel for standard maintenance

A primary consistency test for saturated liquid and vapour property data for use in the integral multiphysics modelling of chemical reactor venting

Accuracy of safety valve two-phase mass flow capacity sizing in case of single-component steam/water, resp., refrigerant R 134a flow service

Activity 4

Application of Safety Measures

ATEX Directives - 9. Risk Assessment and Hazard Identification- II

Batch Reactor (BR)

Brief explanation of the methodology to know if your company is affected or not by SEVESO II

Building 2

Capabilities of the method

Case study 1: Crystallization Kettle - Questions

Characteristic Numbers

Consequence Evaluation Approaches for LOPA

Desk screening - Public Literature

Desktop methods - CHETAH

Desktop methods - reactive groups

Determining in which level your company is affected

Diagram cases

HarsMeth

Hazardous substances and processes

Hazards to assess

How to apply the ?Addition rule?

Introduction

LOPA - Layer of Protection analysis (first draft)

LOPA Model

Overview

Plug Flow Tube Reactor (PFTR)

Reproductive accuracy of safety valve two-phase mass flow capacity models in case of air/water, resp., viscous liquid flow duty

Safety measures

Scenario selection

Screening Methods

Screening Tests: atmosphere inside the crucible

Screening Tests: scanning rate

Semi-Batch Reactor (SBR)

Seveso II

STEP 10: Safety Instrumented System (SIS)

STEP 1: Identify the consequence

STEP 4: Initiating Event Frequency

STEP 7: Independent Protection Layers

Stoessel Diagram

Tests

Tests - Burning Rate

Tests - Burning Test For Solids

Tests - Steel Cartridge Test

Thermal Explosion Theory

Thermal unstable substances


Resources / Downloads

5 entries found!

An Introduction to Fire Dynamics

HarsNet

Low pressure and vacuum hazards

Process Safety and Environmental Protection (PSEP)

Reproductive accuracy of generic Omega Parameter safety valve two phase critical mass flow models based on water and refrigerant R134a data


Research projects

15 entries found!

CHAF
Serious explosion accidents have occurred in EU countries that have involved the bulk storage of display fireworks. Currently, there is no means of estimating the hazards posed by such storage and the UN transport classification scheme is all that ca

Development of Fine Chemical?s advanced processes. (Desarrollo de procesos avanzados de Qu?mica Fina) (DPAQ)? Doctoral Thesis
The objective of the present project is to solve the safety problems existing in the main fine chemicals discontinuous processes. In the approved projects PB98-0410 and PPQ2002-01806, the main target of the work was to obtain macrocyclic lactones as

EXPRO
This experimental/ theoretical/numerical project aims at revealing the physical-chemical mechanisms of explosion, and at deriving innovative methods for explosion protection. Both LES and VLES modelling strategies, with appropriate models for combust

FIREDETEX
The development of a new large passenger aircraft with two or even three deck configuration requires new ways in defining passenger safety. As one major goal, f ire safety has to be improved to enhance today's level of safety. A next generation fire

FLAMERET
The extensive use of polymers increases fire hazard. Harmful gases may also evolve at burning causing environmental damage. The integrated activity of universities, research institute, regulatory body, SMEs and user, from two EU countries plus two as

FLIE
The project aim to improve the understanding of the processes that occur in accidental flashing releases of liquids at high pressure, and to enhance the predictive capabilities of engineering tools used in hazard assessment. Flammable atmospheres con

HEMIND
Design, Prototype and Manufacture a helmet system for Fire-fighters, equipped with a high resolution, miniature, viewer and an autonomous, portable, computer system capable of presenting, overlapped to the normal viewing field of the user, images fro

Improvement of an industrial process for the production of cyclic macrolactones (MLC) ? Doctoral Thesis
The aim of this work is basically centred in the improvement and industrialization of the production of macrocyclic lactones (C11 and C16) through the Story synthesis useful as raw materials for high performance linear polyesters. As a starting point

Methodologies for thermal risk analysis of discontinuous chemical processes (Metodologies per l?an?lisi del risc t?rmic de processos qu?mics discontinus) ? Doctoral Thesis
The objective of the present project is to solve the safety problems existing in the main fine chemicals discontinous processes. In the approved projects PB98-0410 and PPQ2002-01806, the main target of the work was is obtaining of macrocyclic lactone

PRESAFE
Main goal of PRESAFE is to create a strong centre providing services for the parties interested in pressure equipment safety. Second goal is to construct a network, which will be an extension of existing EPERC network. This will be achieved through a

SAFEKINEX
Process industry is challenged to produce higher product yields at lower costs and less waste while maintaining safety. Sustainable growth requires more partialoxidation of hydrocarbons and biomass. Such developments will increase explosion risk. Ris

SAFERELNET
Thematic Network concerned with providing safe and cost effective solutions to industrial products, systems, facilities and structures across different industries. The scope of the project is the integrated treatment of the important aspects of desig

Technological and natural risks
To manage the EPERC network and maintain the EPERC website on a day-to-day basis under the guidance of the Steering Committee in order to: 1. provide technical expertise to DG ENTR in support of the PED and of the harmonised standards required for

Thematic network on hazard assesment of highly reactive systems. Preliminary phase

TRANSFIRE
Fire engineering is a discipline which brings together professional engineers from a variety of academic backgrounds. The increasing use of high technology and the complexity of modern building design increases the importance of a common language and


Legislation & Standardisation

15 entries found!

1999/36/EC, transportable pressure equipment
Council Directive 1999/36/EC of 29 April 1999 on transportable pressure equipment

393/2001 - Decree of the Ministry of Transport and Communications on transportable pressure equipment
Liikenne- ja viestint?ministeri?n asetus kuljetettavista painelaitteista (393/2001)

87/404/EEC, simple pressure vessels
Council Directive 87/404/EEC of 25 June 1987 on the harmonization of the laws of the Member States relating to simple pressure vessels

90/488/EEC, simple pressure vessels
Council Directive 90/488/EEC of 17 September 1990 amending Directive 87/404/EEC on the harmonization of the laws of the Member States relating to simple pressure vessels

93/68/EEC, individual protection equipment
Council Directive 93/68/EEC of 22 July 1993 amending Directives 87/404/EEC (simple pressure vessels), 88/378/EEC (safety of toys), 89/106/EEC (construction products), 89/336/EEC (electromagnetic compatibility), 89/392/EEC (machinery), 89/686/EEC (per

97/23/EC, pressure equipment
Directive 97/23/EC of the European Parliament and of the Council of 29 May 1997 on the approximation of the laws of the Member States concerning pressure equipment

EN 13673-1:2003, explosive atmosphere
Determination of the maximum explosion pressure and the maximum rate of pressure rise of gases and vapours - Part 1: Determination of the maximum explosion pressure

EN 13673-2:2005, explosive atmosphere
Determination of maximum explosion pressure and the maximum rate of pressure rise of gases and vapours - Part 2: Determination of the maximum rate of explosion pressure rise

EN 14034-1:2004, explosion protection
Determination of explosion characteristics of dust clouds - Part 1: Determination of the maximum explosion pressure pmax of dust clouds

EN 14034-2:2006, explosion protection
Determination of explosion characteristics of dust clouds - Part 2: Determination of the maximum rate of explosion pressure rise (dp/dt)max of dust clouds

Note addendum to Pressure Systems Regulations 2000
Pressure Systems Safety Regulations 2000

Pressure Equipment Safety Regulations 2000
Pressure Equipment Safety Regulations 2000

Statutory Instrument 2004/568 (94/55/EC)
Statutory Instrument 2004/568 (ISBN 0110490630) - "The Carriage of Dangerous Goods and Use of Transportable Pressure Equipment Regulations 2004". This is consolidated legislation for road and rail for Great Britain (Northern Ireland are finalising si

Statutory Instrument 2004/568 (96/35/EC, 99/36/EC)
Statutory Instrument 2004/568 (ISBN 0110490630) "The Carriage of Dangerous Goods and Use of Transportable Pressure Equipment Regulations 2004". This is consolidated legislation for road and rail for Great Britain including radioactive materials by ra

Statutory Instrument 2004/568 (96/49/EC)
Statutory Instrument 2004/568 (ISBN 0110490630) "The Carriage of Dangerous Goods and Use of Transportable Pressure Equipment Regulations 2004". This is consolidated legislation for road and rail for Great Britain including radioactive materials by ra


Web Links

5 entries found!

HARSNET - Thematic network on hazard assessment of highly reactive systems
An extensive forum within which universities, research centres and industries collaborate to develop and disseminate fundamental knowledge that can be used for hazard assessment of reactive systems, in order to improve the global safety of the chemic

MSDS
A pyrophoric material can spontaneously ignite in air. The word is derived from Greek for "fire-bearing". Many pyrophoric materials are also water reactive, reacting vigorously with water or high humidity, often igniting upon contact

Physikalisch-Technische Bundesanstalt
The Physikalisch-Technische Bundesanstalt (PTB) is the national metrology institute providing scientific and technical services. PTB measures with the highest accuracy and reliability - metrology as the core competence.

Pressure relief - Training tool
Safety Engineering Technology Course Pressure Relief - Training tool

Society of Fire Protection Engineers
The purpose of the Society is to advance the science and practice of fire protection engineering and its allied fields, to maintain a high ethical standard among its members and to foster fire protection engineering education.


Glossary

23 entries found!

Emergency pressure relief design

Explosion pressure relief (venting)

High pressure crucibles

High Reliability Organisations (HROs)

Low and high temperature exposure

Maximum allowable pressure

Maximum explosion pressure (Pmax)

Maximum pressure rise rate

Maximum rate of pressure rise

Open crucibles

Overpressure

Peak pressure

Pressure at maximum rise rate

Pressure piling

Pressure production

Pressure Relief Systems

Pressure relief valves

Pressure shock

Pressure shock + resistant

Pressure vessels

Reduced explosion pressure

Set pressure

Vapour pressure


131 entries found!

Activation energy

Adiabatic

Adiabatic temperature rise

Arrhenius diagram

Arrhenius law

Autocatalytical

Basis of safety

Batch process

Batch reactor

Blow down lines

Body protection Garments

Boiling liquid expanding vapour explosion (BLEVE)

Boiling point

Breathing apparatus

Bursting discs (Chemical reactions)

Bursting discs (Explosions)

Calvet calorimetry

Carius tube

Category 1

Category 2

Computational fluid dynamics (CFD)

Concept and magnitudes that can be found in MSDS

Consequences

Constructional safety

Containment

Contamination of reactants

Crew Resource Management

Decomposition reactions

Decomposition temperature

Device

Dewar calorimetry

DIERS methodology

Differential scanning calorimetry (DSC)

Differential thermal analysis (DTA)

Dissipative materials

Dow indices

Dump or quench vessel

Electrical resistivity of a layer

Emergency relief system

Endothermic

Enthalpy of reaction

Error

Event tree analysis (ETA)

Explosion doors

Explosion protection

Explosions

Extruder

Fast acting shut off valves

Fault tree analysis (FTA)

Fire blanket

Flame proof

Flammability - Pyrophoric properties of solids and liquids(contact with water causing fire)

Flash fire

Frequency

Frequency factor

Fuel-air explosions

Full scale process

Gassy system

Goggles

Hard (safety) Hats

Hazard

Hazard and operability study (HAZOP)

Head protection

Header sizing

Hearing protection

Heat capacity

Heat of reaction

Hybrid system (reaction)

Ideal gas constant

Ideal gas law

Incompatibility / Reactive interactions

Inerting or purging

Ingress protection

Inherent safety

Isothermal

Isothermal calorimetry

KG-value

Learning Curve

Linearly increasing temperature method

Maximum temperature attainable by the synthesis reaction (MTSR)

Melting / freezing temperature

Metal dusts

Microcalorimetry

Minimum ignition energy (MIE)

Mistakes

Modelling, simulation and optimisation

Normal boiling point

Open cell experiment

Overpressurisation

Pressurisation

Probability

Protection/Mitigation of runaway reactions

Rate of reaction

Reaction calorimetry (RC)

Reaction type

Reactive distillation

Reactive material

Read-Backs

Reflux

Relative density

Release protection

Relief device

Relief valve

Risk

Risk assessment

Risk identification

Rotary valves

Runaway reactions

Safety culture

Semi-batch process

Semi-batch reactor

Sensitivity of reactions

SHE policy

Specific heat capacity

Sphere - 20-litre

Structural fire protections

Suppression

Systems Approach

Tempered system

Thermal inertia Φ

Thermal radiation (Modelling, simulation and optimisation)

Thermal reaction number B

Thermal stability measurement

TNT equivalent

Turbulence

Type of explosion

Vapour system

Vessel - 1 m?

Weak


 
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