Explosive Nature of Hydrogen in a Partial Pressure Vacuum

Similar documents
The Basics of Natural Gas

Lecture 35: Atmosphere in Furnaces

Safety issues of hydrogen in vehicles Frano Barbir Energy Partners 1501 Northpoint Pkwy, #102 West Palm Beach, FL 33407, U.S.A.

COMBUSTION. In order to operate a heat engine we need a hot source together with a cold sink

Most chemical plants contain flammable materials

Process Safety Management of Highly Hazardous & Explosive Chemicals. Safe Work Practices

Hydrogen Detection in Oil Refineries

Chapter 19 Purging Air from Piping and Vessels in Hydrocarbon Service

CSB Public Meeting February 7, 2010, Natural Gas Explosion Kleen Energy Middletown, Connecticut

Certain specific properties of compressed gases make them highly useful in various research activities.

Presented by: Rich Perry Marsh Risk Consulting

Molar Mass and the Ideal Gas Law Prelab

Failure Analysis Associates. Cell Phone Usage At Gasoline Stations

Module 5: Combustion Technology. Lecture 33: Combustion air calculation

Nitrogen Blanketing for Methanol Storage and Transportation

A.17. OXIDIZING PROPERTIES (SOLIDS)

Explosion Hazards of Hydrogen-Air Mixtures. Professor John H.S. Lee McGill University, Montreal, Canada

Gaseous hydrogen. Safetygram 4

PROCEDURES PREVENTION OF ACCIDENTAL IGNITION

Guidelines for Use and Handling of HFO-1234yf

SAFE TRANSFER OF POWDERS INTO FLAMMABLE LIQUIDS David E. Kaelin Sr., Senior Process Safety Specialist

Hydrogen Detection in Oil Refineries

STOICHIOMETRY OF COMBUSTION

Gas Burner Technology & Gas Burner Design for Application

527 CMR: BOARD OF FIRE PREVENTION REGULATIONS 527 CMR 14.00: FLAMMABLE AND COMBUSTIBLE LIQUIDS, FLAMMABLE SOLIDS OR FLAMMABLE GASES

Determination of the enthalpy of combustion using a bomb calorimeter TEC. Safety precautions

Ensuring safety and uptime by managing condensable gases

INITIAL ASSESSMENT OF THE IMPACT OF JET FLAME HAZARD FROM HYDROGEN CARS IN ROAD TUNNELS AND THE IMPLICATION ON HYDROGEN CAR DESIGN

Continuous Monitoring of Flue and Combustible or Hazardous Gases and Vapors

Control Device Requirements Charts For Oil and Gas Handling and Production Facilities

FLAMMABLE AND COMBUSTIBLE LIQUIDS. n OSHA Changes

Hydrogen as a fuel for internal combustion engines

Flare Pilot System Safety

Introductory Laboratory EST - Experiment 9 Calorimetry Introductory Laboratory Energy Science and Technology. Experiment 9. Physical Chemistry

MULTIPLE CHOICE. Choose the one alternative that best completes the statement or answers the question.

Continuous flow direct water heating for potable hot water

TODAY S THERMAL OXIDIZER SOLUTIONS TO MEET TOMORROW S CHALLENGES

MIXED HYDROGEN/NATURAL GAS (HCNG) TECHNOLOGY- VISIT AT COLLIER TECHNOLOIES

Group A/B Dust Explosion Classification Chilworth Hazard and Risk Profile (CHARP) - Standard package of tests

MATERIAL SAFETY DATA SHEET "LIQUID FIRE" DRAIN LINE OPENER 09/2007 PHYSICAL/CHEMICAL CHARACTERISTICS:

Determination of the Empirical Formula of Magnesium Oxide

A Practical Guide to Free Energy Devices

Emergency Response Guide

System Diagnosis. Proper vehicle diagnosis requires a plan before you start

Combustion Pulsation and Noise by Dan Banks, P.E., Banks Engineering Inc.

ENERGY CARRIERS AND CONVERSION SYSTEMS Vol. II - Pressurized Hydrogen Storage - Jo Suzuki, Kunihiro Takahashi

Ethanol Vehicle and Infrastructure Codes and Standards Citations

Review of the prospects for using hydrogen as a fuel source in internal combustion engines

METHOD EXPLOSIVE ATMOSPHERE

Compressed Gas Cylinder Safety

Balancing chemical reaction equations (stoichiometry)

Natural Gas Information Contents

Online Chemistry Course (OLCC) Chemical Safety: Protecting Ourselves And Our Environment

Austin Peay State University Department of Chemistry CHEM Empirical Formula of a Compound

Determination of the enthalpy of combustion using a bomb calorimeter TEC

CHEM 105 HOUR EXAM III 28-OCT-99. = -163 kj/mole determine H f 0 for Ni(CO) 4 (g) = -260 kj/mole determine H f 0 for Cr(CO) 6 (g)

Engine Efficiency and Power Density: Distinguishing Limits from Limitations

Site and Storage Conditions for Class 3.1 Flammable Liquids

E - THEORY/OPERATION

OUTCOME 2 INTERNAL COMBUSTION ENGINE PERFORMANCE. TUTORIAL No. 5 PERFORMANCE CHARACTERISTICS

PRESSURES GENERATED IN COMBUSTION CHAMBERS BY THE IGNITION OF AIR - GAS MIXTURES

Ultrasonic Gas Leak Detection

MOTOR FUEL DISPENSING SAFETY

NITROGEN OXIDES FORMATION in combustion processes COMBUSTION AND FUELS

ALVERNIA UNIVERSITY OSHA REGULATION: 29 CFR WELDING, CUTTING, AND BRAZING ( HOT WORK ) SECTION: 3600

Chapter 5 - Aircraft Welding

General Confined Space Awareness

STORE HAZARDOUS SUBSTANCES SAFELY. incompatibles gas cylinders

University of Pittsburgh Safety Manual Subject: COMBUSTIBLE METALS. EH&S Guideline Number: Effective Date 09/10/13.

A GUIDE TO SELECTING YOUR INDUSTRIAL OVEN

Hydrogen Powered Bus Fleets Hydrogen Supply & Fueling. National Fuel Cell Bus Workshop October 5, New Orleans, LA

Combustible Dust Ensuring Safety and Compliance. Brian Edwards, PE Conversion Technology Inc. ENVIRONMENTAL & SAFETY CONSULTING ENGINEERS

Waste Oil Collection / Storage

COMPRESSED GASES. 1.2 The contents of each cylinder and container must be clearly identified (by tag or stamp) on the cylinder.

ESSAY. Write your answer in the space provided or on a separate sheet of paper.

During Various Aluminum Fabricating Operations

Micro Mole Rockets Hydrogen and Oxygen Mole Ratio As adapted from Flinn ChemTopic- Labs - Molar Relationships & Stoichiometry

Pressure Vessels (Air Compressors) and LPG Tanks

Coal-To-Gas & Coal-To-Liquids

Boiler NOx Emissions and Energy Efficiency

COMBUSTION. By: Michael Biarnes. In collaboration with: Bill Freed and Jason Esteves. E Instruments International LLC -

Combustion Calorimetry

UCLA - Compressed Gas Cylinder Storage and Handling

Practical Guidelines for Electrical Area Classification in Combustion Turbine-Generator Power Plants

Halogen Lamps. Lamp Construction

Possibility of Combustion Furnace Operation with Oxygen-Enriched Gas from Nitrogen Generator

WORKING IN CONFINED SPACES GUIDELINES

Propane Gas Underground Systems: Residential Infrastructure Requirements and Energy Benefits

CONE CALORIMETER A TOOL FOR MEASURING HEAT RELEASE RATE

Handling and Storage of Flammable Materials at the Work Site

A Practical Guide to Free Energy Devices

MATERIAL SAFETY DATA SHEET. PRODUCT IDENTIFIER Carbon Dioxide, Refrigerated Liquid

Compressed Gas Cylinder Safety

INTERNAL COMBUSTION RECIPROCATING PISTON ENGINES

CATALYSTS IN COMBUSTION TECHNOLOGY AND FLUE GAS CLEANING COMBUSTION AND FUELS

Calculate Available Heat for Natural Gas Fuel For Industrial Heating Equipment and Boilers

Calculation of Liquefied Natural Gas (LNG) Burning Rates

Process Safety Management of Highly Hazardous & Explosive Chemicals. Application, Exclusions & Definitions

INTERNAL COMBUSTION (IC) ENGINES

Technical Note 802 Leak Testing of Polyethylene Pipe For Municipal and Industrial Applications Part 1 Pre-Test Considerations

Transcription:

Explosive Nature of Hydrogen in a Partial Pressure Vacuum Trevor Jones Project Engineer Solar Atmospheres Inc. Souderton, PA www.solaratm.com & www.solarmfg.com

Hydrogen Consumption: Hydrogen is the most abundant element in the universe Worldwide consumption of hydrogen is around 103 million kg per day (44 billion scfd) United states consumes 20% of worldwide supply More hydrogen gas is consumed than natural gas by the commercial sector (ref. 1)

History on Hydrogen Applications: Fuel Cells Food Chemical processing Pharmaceuticals Aerospace

History on Hydrogen Applications (continued) Electronics Petroleum Recovery and Refinery Power Generation Metal production n and fabrication Heat Treating

Vacuum Furnaces

Hydrogen s s Role in a Vacuum Furnace Partial Pressure: Hydride / De-Hydride of tantalum, titanium, and other metals Dilutant in Vacuum Carburizing Reducing gas for oxide reduction Formed from dissociated ammonia gas in the gas nitriding process

Characteristics of Hydrogen Higher Heating Value Lower Heating Value Stoichiometric Mixture in Air 141.90 Mj/kg 11.89 Mj/m³ 119.90Mj/kg 10.505 Mj/m³ 29.53 (vol.%) LEL % by Volume 4 UEL % by Volume 74.2 Ft.³ Air Required to Burn 1 Ft.³ of Gas 2.5 Minimum Self-ignition Temperature of Stoichiometric Mixture 1085 F Adiabatic Flame Temperature in Air 3712.73 F Minimum Ignition Energy of Stoichiometric Mixture (mj) 0.02 (ref. 1 & 2)

(ref. 2)

Project Goals Understand the explosive nature of hydrogen gas at atmospheric pressure and in near vacuum conditions Determine minimal levels of energy to ignite hydrogen / air mixtures Determine if Nitrogen or Argon gas will act as a dilutant for hydrogen / air reactions Develop recommendations for the safe use of hydrogen in vacuum systems

Solar s s Hydrogen / Air Reaction Chamber

Atmosphere Energy Sources Vacuum

Procedure for Conducting Tests: 1. Pump down vessel to 0.1 Torr 2. Backfill vessel with air to desired pressure 3. Backfill vessel with H 2 to obtain final test pressure and gas ratio 4. Ignite mixture with either spark or heater element

Pressure (torr) 750 700 650 600 550 500 450 400 350 300 250 200 150 100 50 0 Experimental Results: Minimum Ignition Points 5000 Voltage Spark 1/16" Gap Experimental Theoretical 0 10 20 30 40 50 60 70 % Hydrogen in air

Pressure (torr) 750 700 650 600 550 500 450 400 350 300 250 200 150 100 50 0 Experimental Results: Minimum Ignition Points 5000 Voltage Spark 1/4" Gap Experimental Theoretical 0 10 20 30 40 50 60 70 80 90 % Hydrogen in Air

Pressure (torr) 750 700 650 600 550 500 450 400 350 300 250 200 150 100 50 0 Experimental Results: Minimum Ignition Points Heated Element Wire Experimental Theoretical 0 10 20 30 40 50 60 70 % Hydrogen in air

Temperature vs. H2 Concentration 1150 Ignition Points 1100 Temperature (F ) 1050 1000 950 900 850 0 10 20 30 40 50 60 70 % Hydrogen in Air

Experimental Results: Minimum Ignition Points - Comparing All Three Tests Pressure (torr) 750 700 650 600 550 500 450 400 350 300 250 200 150 100 50 0 0 10 20 30 40 50 60 70 80 90 % Hydrogen in Air 1/4" High Voltage Spark Heated Wire 1/16" Gap Spark

Visuals of Explosions at Different Pressures Atmospheric Sub-Atmospheric

Minimum Ignition Energy vs. % Hydrogen in Air Minimum Ignition energy, mjoules 10 1 0.1 Pressure 0.2 atm Pressure 0.33 atm Pressure 0.5 atm Pressure 1.0 atm 0.01 0 5 10 15 20 25 30 35 40 45 50 55 60 65 70 Hydrogen in air, percent by volume (ref. 3)

Quenching Distance vs. % Hydrogen in Air at Various Pressures 1 Distance (between parallel plates) cm 0.1 Pressure 0.2 atm Pressure 0.33 atm Pressure 0.5 atm Pressure 1.0 atm 0.01 0 10 20 30 40 50 60 70 Hydrogen in air, percent by volume (ref. 3)

Contained Reactions Ignitions under 150 torr Pressure (torr) 300 250 200 150 100 50 0 Initial Pressure 0 0.5 1 1.5 2 2.5 Time (sec) Final Pressure P

Inert Gas as a Dilutant for Hydrogen / Air Burning

Experimental Results Inert Gas as a Dilutant for Hydrogen / Air Burning Hydrogen alone will easily burn if vented out of a pipe into open air and ignited with an energy source Extremely lean hydrogen mixtures (<5%) will not burn in open air if diluted with inert gas Lean H 2 mixtures (5-25%) mixed with inert gas will burn, however will not support a flame once energy source is taken away (Forming Gas) 25-100% hydrogen in inert gas will burn and sustain a flame once energy source is taken away Argon showed slightly better flammable suppression compared to nitrogen

Conclusions 0.02 mj is all the energy required to ignite a stoichiometric mixture of hydrogen & air at atmospheric pressure (ref. 3) As the pressure of the hydrogen & air mixture decreases, the amount of energy required to ignite the mixture increases more than an order of magnitude (ref. 3) Lower pressures than 0.2 atm (150 torr) can be ignited with a larger diameter vessel and increased energy source (ref. 3) Larger spark gaps result in wider flammability limits As hydrogen is increased in concentration, a higher temperature is required to ignite the mixtures The use of inert gas as a dilutant does lower the flammability limit of hydrogen however only slightly

Safety Precautions Stay below 1/2 the LEL of hydrogen (2% or 15 torr) Pump down to 0.1 torr, then backfill with inert gas to atmospheric pressure prior to exposure to air Perform a leak test on the vacuum chamber and be sure the leak up rate is less than 0.015 torr per hour Design intrinsically safe & redundant safety controls when using hydrogen Oxygen probe to detect an air leak in the vacuum system. If oxygen is present then perform 5 volume change purge with argon Use an inert diluting gas to lower the flammability limit

Future Experiments

References: Ref. 1 - Bose Tapan; Hay, Rober; and Ohi Jim: Sourcebook for Hydrogen Applications. Hydrogen Research Institute and National Renewable e Energy Laboratory., 1998 Ref. 2 - Barbir, Frano: Safety Issues of Hydrogen Vehicles. Energy part Barbir, Frano: Safety Issues of Hydrogen Vehicles. Energy partners., 2001; http://iahe.org/hydrogen Ref. 3 - Drell Isadore; Belles Frank: Report 1383 Survey of Hydrogen Combustion Properties. Lewis Flight Propulsion Laboratory, National Advisory Committee for Aeronautics., Cleveland, Ohio: April 1957