SAFETY INSTRUCTIONS, GAS, INSTALLATION  Maintain permanently a good ventilation of the building which might receive hydrogen plant.  The light fittings,

Slides:



Advertisements
Similar presentations
FHM TRAINING TOOLS This training presentation is part of FHM’s commitment to creating and keeping safe workplaces. Be sure to check out all the training.
Advertisements

Before starting actual arc welding the student should be fully aware of the dangers involved. The high temperature arc and hot metal can cause severe.
Regulations (Standards - 29 CFR) Flammable and Combustible liquids
Electrical Safety.
Compressed Gases Slide Show Notes
East Carolina University Compressed Gas Safety Training Program
Compressed Gas Cylinder Safety
Ag Metals I Using Gas Welding Equipment. Objectives Identify major part of oxyacteylene welding equipment Change oxygen and acetylene cylinders Turn on.
Forktruck LP Gas Safety
Inspection & Preventive maintenance of breakers
Fire Hazards of Oxygen Enriched Atmospheres
Complied by H S Dave DDISH Surat Health & Safety at Work Hazards from Aerosols.
CHEMICAL HYDROGEN GENERATOR TYPE GIP ™ 3 Training Module.
COMPRESSED GASES. Compressed Gases Chemicals include oxygen, argon, nitrogen, helium, acetylene, hydrogen, nitrous oxide, carbon dioxide, ammonia, chlorine,
1926 Subpart J Establishes the requirements for welding and cutting in the construction industry Establishes requirements for equipment, fire protection,
HAZARD STATEMENTS Extremely flammable gas Contains gas under pressure; may explode if heated Toxic if swallowed Toxic if inhaled Causes skin irritation.
Unit: Oxy-Acetylene; Welding, Brazing, Cutting & Heating
Oxygen/ Fuel Cutting and Welding By Ryan Saucier.
Asia Industrial Gases Association 3 HarbourFront Place, #09-04 HarbourFront Tower 2, S(099254) Internet: http// Oxygen Enrichment Risks.
Management of Hazardous Chemicals chlorine. Management of Haz.Chemicals Every day lot of chemicals are being handled Some chemicals are safe,some are.
HOW TO LIGHT AND TURN OFF THE OXY-ACETYLENE TORCH
OXY-ACETYLENE TORCHES Protect your head and eyes by wearing proper welding goggles or face shields equipped with a minimum shade 5 lens. Protect your.
Fires and Explosions In OR and ICU By Professor Dr. Mohammed Saeed Abd El Aziz.
Welding, Cutting, And Brazing
Standard 29 CFR Part Welding, Cutting and Brazing Training.
Oxygen/ Acetylene Cutting & Safety By Keith Dover.
1 Welding Module 10. 2Objectives After this module you should be able to – identify the most common welding hazards – take the necessary steps to avoid.
Welding, Cutting and Brazing 29 CFR 1910, Subpart Q
Safe Handling of Flammable and Combustible Liquids
Copyright  Business & Legal Reports, Inc. BLR’s Safety Training Presentations Welding, Cutting and Brazing 29 CFR 1910, Subpart Q.
Liquid Fuel Safety Cummins Southern Plains, Ltd..
General Industrial Battery Safety Changing and Charging Storage Batteries (g)  Battery charging installations shall be located in areas designated.
Fire Safety.
Health & Safety at Work Hazards from Aerosols.  To understand the hazards associated with aerosol products.  Understand how to control these hazards.
Flammable and Combustible Liquids
Flammable and Combustible Liquids Presented by Martina Schmeling Adapted From OSHA.
CXS490 Carbon Dioxide Systems
Safety Training Presentation
Fire Safety and Prevention Plan
Handling and Storage of Hazardous Chemicals direct.com/assets/ite ms/c126.jpg.
SAFETY AND TOOLS CHAPTER 2.
1 Welding Module DISCLAIMER This material was produced under grant number SH from the Occupational Safety and Health Administration, U.S.
Training Package 1 Fire Hazards of Oxygen and Oxygen enriched atmospheres Training Package TP 02/05 Oxygen Enrichment Risks Asia Industrial Gases Association.
Hazardous Materials Subpart H. Subpart H Standards Compressed Gases Acetylene Hydrogen Oxygen Nitrous Oxide Flammable.
HOUSTON, TEXAS1 Pipeline Repair ENGINEERING SERVICES LP HOUSTON, TEXAS Engineering Specification.
Basic Awareness Training for all Staff
Science Safety Rules! You must score 90 or above before you may participate in the laboratory science activities. If labs occur before your completion.
Dangerous Throughout Canada, standard symbols are used to identify ___________ materials. The ______________________ _____________________________ (________)
Flammable and Combustible Liquids. Introduction !The two primary hazards associated with flammable and combustible liquids are explosion and fire !Safe.
FIRE PREVENTION. Fire Of the many hazards on site or at work, fires are the worst kind. They do a great deal of damage every year.  All fires, however.
2 IMPACT - THE FIRE PERMIT = Hot Work Permit 3 Welcome ! This course is linked to the use of IMPACT, so it is assumed that: You know how to use IMPACT.
3.7.7 Student Book © 2004 Propane Education & Research CouncilPage 1 Replacing DOT IM tank valves and fittings requires careful application of precautions.
Natural Gas Fire Safety. INGREDIANTS OF FIRE The best approach to fire safety is to not have a fire in the first place… but how? The answer is: remove.
Army Aviation Support Facility #1 Phoenix, Arizona
Lab Safety. Disposal Special disposal procedures need to be followed. Do not dispose of these materials in the sink or trash can Dispose of waste as directed.
Workplace Hazardous Materials Information System. This system provides workers and employers nationwide with vital information about hazardous materials.
FLAMMABLE AND COMBUSTIBLE LIQUIDS 1 Bureau of Workers’ Comp PA Training for Health & Safety (PATHS) OSHA 29CFR PPT
Subpart F - Fire Protection & Prevention ( ) Flammables/combustibles - Approved containers Fire protection program/equipment 2A fire extinguishers.
Flammable and Combustible Liquids Standard 29 CFR Part City of Council Bluffs Presented by: SilverStone Group © 2006, 2012 Zywave, Inc. All rights.
Flammable Liquids Directorate of Training and Education
Safe Handling of Flammable and Combustible Liquids.
Oxyacetylene Fusion Welding Safety Review
DAN ITW Oxygen Safety.
Safe Handling of Flammable and Combustible Liquids
Fire Safety and Prevention Plan
Health & Safety at Work Hazards from Aerosols
Fire Safety and Prevention Plan
Flammable and Combustible Liquids
Health & Safety at Work Hazards from Aerosols
Safe Handling of Flammable and Combustible Liquids
Presentation transcript:

SAFETY INSTRUCTIONS, GAS, INSTALLATION  Maintain permanently a good ventilation of the building which might receive hydrogen plant.  The light fittings, switches and sockets installed in the hydrogen gas area shall be antideflagrating type and approved for hydrogen.  A 9Kg (minimum) powder type fire extinguisher shall be provided.  Instructions : "NO SMOKING" and "IT IS FORBIDDEN TO BRING IN FIRE UNDER WHATSOEVER FORM“ shall be displayed.  The room shall be used only for hydrogen production.  Access to the generator shall be prohibited to anyone non-authorized to operate it.  All parts in contact with oxygen gas must be degreased.  Never handling the caustic potash of the electrolyte solution without individual safety protection equipment.

SAFETY INSTRUCTIONS TO DISPLAY OUTSIDE AND INSIDE THE HYDROGEN BUILDING OUTSIDE AND INSIDE THE HYDROGEN BUILDING

OUTSIDE AND INSIDE THE HYDROGEN BUILDING OUTSIDE AND INSIDE THE HYDROGEN BUILDING SAFETY INSTRUCTIONS TO DISPLAY

OUTSIDE AND INSIDE THE HYDROGEN BUILDING NEAR THE OXYGEN OUTPUT SAFETY INSTRUCTIONS TO DISPLAY

HYDROGEN GAS PROPERTIES FORMULA H2H2 PARTICULARITIES  Colorless  Odorless  Flammable gas (invisible flame)  Non toxic gas FLAMMABILITY LIMITS IN AIR  Lower 4%  Upper74,5% FLAMMABILITY LIMITS IN OXYGEN MINIMUM AUTO IGNITION TEMPERATURE  Air570°C  Oxygen560°C FLAME CHARACTERISTICS  AirFlame temperature 1.430°C Max.speed flame2,65 m/s  OxygenFlame temperature 2.830°C Max. speed flame14,36 m/s (à 20°C, 1 ATM.)  Lower 4%  Upper74,5% (à 20°C, 1 ATM.)

As for all gas installations, specific risks related to each installationhave to be known. As for all gas installations, specific risks related to each installation have to be known. Principal danger sources about hydrogen plants are : Principal danger sources about hydrogen plants are : Gas inflammation in case of excess of warmth, sparks or flame Gas inflammation in case of excess of warmth, sparks or flame Risk of an « explosive » atmosphere in case of a hydrogen gas concentration higher than 4% Risk of an « explosive » atmosphere in case of a hydrogen gas concentration higher than 4% Gas auto ignition risk in case of a temperature higher than 500°C Gas auto ignition risk in case of a temperature higher than 500°C Leakage risk due to the high fluidity of hydrogen gas and the difficulty of its detection Leakage risk due to the high fluidity of hydrogen gas and the difficulty of its detection In case of inflammation, hydrogen gas is odorless, colorless and its flame is invisible. In case of inflammation, hydrogen gas is odorless, colorless and its flame is invisible. RISKS DUE TO A HYDROGEN GAS PLANT

As for all dangerous gas, it is absolutely necessary to stay extremely vigilant during the use of hydrogen gas. As for all dangerous gas, it is absolutely necessary to stay extremely vigilant during the use of hydrogen gas. Even if all employees in charge of the hydrogen plant are informed about the risks due to the hydrogen gas, employees become generally less vigilant after several years of experiment. This is due to a too big trust in the use of hydrogen gas and that trust is increasing with years. Even if all employees in charge of the hydrogen plant are informed about the risks due to the hydrogen gas, employees become generally less vigilant after several years of experiment. This is due to a too big trust in the use of hydrogen gas and that trust is increasing with years. The direct consequence of this kind of comportment brings harmful effects on the safety measures and on the conditions of hydrogen use, for example : The direct consequence of this kind of comportment brings harmful effects on the safety measures and on the conditions of hydrogen use, for example : -Risk to forget to wear antistatic clothes -Risk to forget to switch off its mobile phone during the filling of a balloon -Risk to open brutally or too quickly the hydrogen cock of the draw off panel -Risk to increase the hydrogen pressure of the draw off panel in order to « accelerate » the filling of the balloon, -Lack of vigilance :.During the hydrogen production (lack of daily verifications on the plant).Where the balloon is filled HARMFUL EFFECTS LINKED TO HABITUATION RISKS

It is imperative to respect the following safety instructions: It is imperative to respect the following safety instructions: It is forbidden to smoke or to bring in fire under whatsoever form near the hydrogen production plant It is forbidden to smoke or to bring in fire under whatsoever form near the hydrogen production plant The use of mobile phones is forbidden during the filling of a balloon The use of mobile phones is forbidden during the filling of a balloon Eliminate all risks of sparks emission due to static electricity (friction of the balloon on a wall, brutal opening of the draw off panel cock, filling pressure too high) by connecting systematically all the metallic parts of the building to the ground, plus the filling table and the filling mantle (if this one is metallic) Eliminate all risks of sparks emission due to static electricity (friction of the balloon on a wall, brutal opening of the draw off panel cock, filling pressure too high) by connecting systematically all the metallic parts of the building to the ground, plus the filling table and the filling mantle (if this one is metallic) Eliminate all the clothes able to create static electricity (Nylon, synthetic…). Wear if possible pure cotton clothes. Eliminate all the clothes able to create static electricity (Nylon, synthetic…). Wear if possible pure cotton clothes. Check the presence of chalk in the balloon (inside and outside) before using it (chalk is an antistatic agent) Check the presence of chalk in the balloon (inside and outside) before using it (chalk is an antistatic agent) The filling pressure of a sounding balloon shall not exceed 2 bars The filling pressure of a sounding balloon shall not exceed 2 bars The balloon filling phase has to be done on a filling table in order to avoid all risks of friction The balloon filling phase has to be done on a filling table in order to avoid all risks of friction SAFETY INSTRUCTIONS TO OBSERVE

STORAGE OF THE BALLOONS STORAGE OF THE BALLOONS In order to avoid an artificial ageing of the balloons that could bring a loss of elasticity or a loss of tightness, and then some balloons bursting or some gas leakages, following measures must be taken: The balloons must be preserved inside their origin packing, in a dark room having a temperature between 10 and 20° C and a relative moisture close to 60%.In the worst case, the temperature of the room should not reach 35 ° C. The balloons must be classified in the order of their manufacturing date to always use the older one first. FILLING OF THE BALLOONS FILLING OF THE BALLOONS Check the presence of chalk in the balloon (inside and outside) before using it (chalk is an antistatic agent) Check the presence of chalk in the balloon (inside and outside) before using it (chalk is an antistatic agent) The balloon filling phase has to be done on a filling table in order to avoid all risks of friction The filling pressure of a sounding balloon shall not exceed 2 bars The filling of the balloon has to be done slowly in order to avoid risk of hydrogen inflammation due to the static electricity created by the friction of the gas between the chalk particles. The filling of the balloon has to be done 15mn before launching it. When the balloon is filled, avoid to expose it to sunlight. In dry areas, it is highly recommended to connect the filling cock to the ground. SAFETY INSTRUCTIONS TO OBSERVE METEOROLOGICAL BALLOONS

INSTRUCTIONS FOR THE CELLS REPROOF TEST  Periodical pressure proof tests every 5 years at 1.5 time the service pressure.  The proof test has to be witnessed by an expert from the competent National Department.  Proof test certificate shall be issued after the stamping of the cell.  Proof test has to be performed with a hydraulic pump.  Proof test has to be made in case of visible defects on the cell such as :  Notch or groove 5% deeper than the thickness of the cell,  Lamination (fold, overlap, entrapment, flaking of the metal),  Punch marks, collar not fixed, Grinding recess or suspect stain.  Systematic reject has to be decided in case of visible defects on the cell such as :  Projection on the surface of the cell visible to the naked eye,  Dent greater than 0.5% of the outside diameter of the cell,  Crack or tearing of metal,  Damage due to fire,  Arcing or blow torch damage.  Systematic reject of the cylinders has to be decided after 15 years of operation.

PLEASE CONTACT SAGIM S.A. 35, RUE SCHEURER-KESTNER SAINT-ÉTIENNE (France) Tel. : Fax : THANK YOU FOR MORE INFORMATIONS