CONE CALORIMETER A TOOL FOR MEASURING HEAT RELEASE RATE
|
|
|
- Angel Hensley
- 9 years ago
- Views:
Transcription
1 CONE CALORIMETER A TOOL FOR MEASURING HEAT RELEASE RATE Johan Lindholm, Anders Brink and Mikko Hupa Åbo Akademi Process Chemistry Centre, Biskopsgatan 8, FI Åbo, FINLAND Corresponding author: [email protected] Tel: ABSTRACT The cone calorimeter is considered the most significant bench scale instrument in fire testing. This apparatus has been adopted by the International Organization for Standardization (ISO ) for measuring heat release rate (HRR) of a sample. It has been shown that most fuels generate approximately 13.1 MJ of energy per kg of oxygen consumed. Therefore, HRR is based on the fact that the oxygen consumed during combustion is proportional to the heat released. This device analyses the combustion gases and measures the produced smoke from a test specimen that is being exposed to a certain heat flux. At least the oxygen concentration must be analyzed to calculate the released heat, but to improve the accuracy, carbon monoxide and carbon dioxide concentrations can also be analyzed. The data collected from this bench scale real fire test can be used for fire modelling, prediction of real scale fire behaviour, pass/fail tests etc. In this work the principle and use of this technique will be described. Since this method measures heat release rate indirectly by calculations based on oxygen consumption, the uncertainties originating from assumptions, calculations and the tested fuels will also be discussed. Keywords: Cone calorimeter, heat release rate, oxygen consumption, heat of combustion.
2 1 INTRODUCTION The cone calorimeter is a fire testing device based on the principle of oxygen consumption during combustion. This device is used by most leading fire research groups as a data source for properties of materials and as a source for input data to models when predicting fire behaviour. The cone calorimeter is considered the most significant bench scale instrument in fire testing (BABRAUSKAS, Vytenis and Peacock, Richard D., 1992). A fuel sample surface can be radiated with different heat fluxes by this device. The fuel sample ignites and burns in excess air. Amongst the results are time to ignition, mass loss, smoke amounts, gas analyses, heat release rate and other parameters related to burning properties of a fuel. Heat release rate is defined as the mass loss rate of the material times its heat of combustion. 1.1 Early development and standardisation The modern cone calorimeter started to take form in the early 1980 s. A new technique called oxygen consumption calorimetry based oxygen concentration measurement in the flue gases had been introduced (HUGGETT, Clayton, 1980). The development of a cone calorimeter was started already in the late 1950 s when similar types of measurements were started, and in the 1970 s the original NBS calorimeter (National Bureau of Standards, from 1988 NIST, National Institute of Standards and Technology) was built. The early versions were based on other measurements, and with burners instead of electrical heaters they were complex and difficult to use, but had good accuracy (BABRAUSKAS, Vytenis, 1983) (BABRAUSKAS, Vytenis, 1993). The first proposal to standardisation of cone calorimeter measurements was the ASTM P 190 in The full version was published in 1990 as the ASTM E The cone calorimeter method was also presented as a draft for ISO standard in 1990, and in 1993 the final form of the ISO was published. The latest version was revised in GENERAL DESCRIPTION 2.1 Parts The cone calorimeter consists of numerous essential parts and devices. Together these parts measure, log, set and adjust several parameters like temperatures, mass, gas flow and concentration. In Figure 1 these parts are described in a schematic picture.
3 Figure 1 Schematic picture of the Cone Calorimeter. Modified from (FTT Cone Calorimeter brochure) The specimen is placed on a metal sample holder, which is placed on the load cell. The load cell records the weight of the sample during the experiment. There are two types of sample holders. Depending on the specimen, the sample holder can have open or closed edges. If the specimen is of intumescent type (i.e. the specimen swells and forms a protective char layer), a wired grid can be fitted to keep the specimen in place when swelling occurs. The wired grid is always used when testing in horizontal position and with the edged frame sample holder. A spark igniter is situated right above the sample surface below the cone heater. This ignites the flammable gases leaving the sample when the sample is heated. When the whole sample area is burning, the igniter is turned off and moved to the side. Prior to the experiment during calibration, a water cooled heat flux measuring device is placed at the sample surface level. The cone heater is then set to the temperature that gives the wanted heat flux at the surface of the specimen. Normally, the cone is mounted horizontally, but vertical orientation is also possible. The name of this testing apparatus originates from the shape of the heater. The heater is wound to a conical shape from an over 3 m long resistance heating wire packed in magnesium oxide refractory. The flue gases from the burning sample are collected into the extraction hood situated directly above the heater. A flue gas fan is mounted in the flue gas line to set the flow
4 Heat of combustion (MJ/kg O 2 ) rate of combustion products. The gas sampling ring is situated before the fan in the flue gas line. Prior to reaching the gas analyzers, the gas sampled in the ring is first passed through two filters to remove particles, then through a cold trap and a drying agent to remove possible water. Between the gas sampling ring and the fan there is also a smoke measurement system. This measures the produced amount of smoke by a laser photometric beam. The only analyzer needed to perform fundamental cone calorimeter experiments is the oxygen analyzer. Additional analyzers, such as carbon monoxide and carbon dioxide analyzers are usually fitted to gain better understanding of the burning process and to decrease the uncertainties in the results. For further analysis of combustion products and gas species for example a Fourier Transform Infrared spectrometer (FTIR) can be coupled through a heated line. 2.2 Relationship between oxygen consumption and heating value Heat release rate (HRR) is calculated from the oxygen concentration in the flue gases. The heat released from a fuel has been shown to be proportional to the oxygen consumed during combustion. (HUGGETT, Clayton, 1980) 13.1 is a key value in the cone calorimeter measurements and calculations. In the study by Huggett, many fuels are shown to have almost the same value for heat of combustion. The values are close to each other even if there is a big variation in the fuel types. An average of these values is calculated to 13.1 MJ/kg O 2 (Figure 2) with an accuracy of ±5% Average: 13, Figure 2 Heat of combustion for a range of different fuels. Data source: HUGGETT, Clayton
5 The cone calorimeter software calculates the heat release rate by the following equation: (Equation 1) Where = rate of heat release (kw) C = orifice plate coefficient (kg ½ m ½ K ½ ) = pressure drop across the orifice plate (Pa) = gas temperature at the orifice plate (K) = measured mole fraction of O 2 in the exhaust air If the fuel to be tested is known, the real value for heat of combustion can be used when performing experiments by entering this value into the cone calorimeter software. By doing this, the error in the final result is decreased. 3 PERFORMING EXPERIMENTS Prior to performing any experiments, some daily setup and calibrations are needed. The gas analyzers and the laser smoke measurement system always stay turned on to be ready to use, without having to wait for warm-up and stabilisation, but the rest of the equipment has to be powered and set up. The filters on the gas sampling line are checked and changed if necessary. Drierite (calcium sulphate with cobalt chloride indicator, >98% CaSO 4, <2% CoCl 2 ) is used as dying agent for the sample gas before it reaches the analyzer. This is also checked and, if needed, changed to fresh. While the exhaust control still is turned off the differential pressure transducer is zeroed. After this the exhaust control is turned on and the duct flow is set to 24 l/s using the flue gas fan. 3.1 Calibrations The smoke measurement system and the gas analyzers for analyzing oxygen, carbon monoxide and carbon dioxide concentrations in the flue gases always stay turned on and are ready for use. The smoke measurement system is calibrated for zero value by completely blocking the laser beam and full range is reached by unblocking the beam. The gas analyzers are calibrated daily using nitrogen for zero level and CO/CO 2 span gas (0.85/8.5 %) for the wanted range for the CO and CO 2 analyzers. Air is used to span the O 2 analyzer to %. The orifice plate coefficient (device specific, see Eq.1), or the C-factor, is calibrated with a methane burner. The flow of methane is adjusted to produce approximately 5 kw. Since the value for heat of combustion for pure methane is known, and the gas analyzers are calibrated, a calibration of this type can determine the C-factor.
6 The sample holder should be set to a level that the sample surface is 25 mm below the cone. Finally, the temperature of the cone must be set to produce the wanted heat flux at the sample surface. The heat flux is usually set to 25, 50, 75 or 100 kw/m 2. This is done by placing a water cooled heat flux gauge 25 mm below the cone and adjusting the cone temperature until the wanted heat flux is reached. 3.2 Measurements The size of the standard specimen is 100 x 100 mm 2. The maximum specimen thickness allowed is 50 mm. The sample is wrapped in aluminium foil so that only the top surface is being radiated by the heat from the conical heater. The sides of the sample should not be exposed to the radiative heat. Before the spark igniter is placed in position above the sample surface and the actual burning test is started, baseline data is collected for 60 seconds. The experimental data is then measured from this baseline. 4 INTERPRETATION OF RESULTS The results from a cone calorimeter experiment include a range of parameters and data types that can be used for several different purposes, for example: Fire modelling Prediction of real scale fire behaviour Ranking of products by fire performance Pass/fail tests when developing new materials and products Parts of the results from an experiment with a 19 mm thick wooden sample are graphically shown in Figure 3. In addition to these, several average and peak values are calculated and registered. Time to ignition, peak heat release rate, heat release rate after certain user defined times, total heat release (THR, Eq.2), mass loss and average effective heat of combustion are thermal parameters logged during the experiment. Examples of logged smoke parameters are total smoke released (TSR, Eq. 3), CO and CO 2 yields. CO and smoke are typically results from incomplete combustion and can be wanted products, if the burning process is disturbed by flame retardants.
7 Effective Heat of Combustion (MJ/kg) Smoke production rate (m 2 /s) Heat Release Rate (kw/m 2 ) Total heat release (MJ/m 2 ) Time (s) Time (s) 0, , , Time (s) Time (s) Figure 3 Examples of results from experiment with 19 mm thick wood sample at 50 kw/m 2. Top left: Heat release rate vs. time. Top right: Total heat release (cumulative) vs. time. Bottom left: Effective heat of combustion vs. time. Bottom right: Smoke production rate vs. time. (Equation 2) (Equation 3) Figure 3 consists of four graphs. These are examples of results from a cone calorimeter experiment. In the top left HRR graph two peaks can be seen. The first peak is the higher and comes directly after ignition. As the heat release rate is proportional to the oxygen consumed, this means that a lot of oxygen is consumed immediately after ignition and here the peak heat release rate is then found. The second peak around seconds appears when the surface starts to break up and oxygen reaches the inner parts of the sample and starts to burn more efficiently. The peaks and the form of the heat release rate graph follow the peaks and the form of the smoke production graph (bottom right) very well.
8 The total heat release (THR) curve in Figure 3 (top right graph) increases almost linearly until 900 seconds, when the second peak in the heat release rate (HRR) curve starts to decrease. This is also explained by Equation 2. Sample thickness is another important parameter. In order to be able to produce comparable results, the samples have to have the same thickness, as shown in Figure 4. Figure 4 HRR for PMMA for thicknesses between 1.5 and 25 mm. From (SHARTEL, B. and Hull, T. R., 2007) 4.1 Sources of errors Heat release rate cannot be directly measured. It has to be calculated from several other measurements, and as a consequence, it includes some errors and assumptions. As mentioned above in section 2.2, the error in the value for the heat of combustion can be up to 5% (HUGGETT, Clayton, 1980). Zhao and Dembsey did an extensive study on measurement uncertainty for the cone calorimeter (ZHAO, Lei and Dembsey, Nicholas A., 2008). They concluded that the relative uncertainty of HRR decreases as HRR increases. The relative error when firing methane is approximately 20-30% for 1 kw fires, 10% for 3 kw fires and less than 10% for 5 kw fires. The uncertainties for HRR measurements are considered reasonable. Enright and Fleischmann also studied the assumptions and uncertainties in the cone calorimeter apparatus and measurement (ENRIGHT, Patrick A. and Fleischmann, Charles M., 1999). If the fuel is known or if additional analyzers, such as H 2 O, CO and CO 2 analyzers, besides the required oxygen analyzer, are used, it decreases the uncertainties. The uncertainty of the calculations is very strongly coupled with the oxygen analyzer accuracy.
9 5 CONCLUSIONS The cone calorimeter is a key tool fire research. The accuracy of the results from cone calorimeter experiments mainly depend on the accuracy of the oxygen analyzer, since it uses the oxygen consumption principle. The results can be used in models for upscaling experiments and in fire testing when developing new materials. Fire hazard and development can also be predicted by cone calorimeter tests. 6 ACKNOWLEDGEMENT The Academy of Finland is gratefully acknowledged for their financial contribution to this work. 7 REFERENCES BABRAUSKAS, Vytenis Development of the Cone Calorimeter - A Bench-scale Heat Release Rate Apparatus Based on Oxygen Consumption. Fire and Materials. 8(2), pp BABRAUSKAS, Vytenis Ten years of Heat Release Research with the Cone Calorimeter. Heat Release and Fire Hazard. I. BABRAUSKAS, Vytenis and Richard D. PEACOCK Heat Release Rate: The Single Most Important Variable In Fire Hazard. Fire Safety Journal. 18, pp ENRIGHT, Patrick A. and Charles M. FLEISCHMANN Uncertainty of Heat Release Rate Calculation of the ISO Cone Calorimeter Standard Test Method. Fire Technology. 35(2), pp FTT Cone Calorimeter brochure. [online]. [Accessed January 2009]. Available from World Wide Web: HUGGETT, Clayton Estimation of rate of heat release by means of oxygen consumption measurements. Fire and Materials. 4(2), pp MOURITZ, A. P. and A. G. GIBSON Fire Properties of Polymer Composite Materials. Dordrecht: Springer. MOURITZ, A.P., Z. MATHYS, and A.G. GIBSON Heat release of polymer composites in fire. Composites Part A: Applied science and manufacturing., pp SHARTEL, B. and T. R. HULL Development of fire-retarded materials - Interpretation of cone calorimeter data. Fire and materials. 31(5), pp ZHAO, Lei and Nicholas A. DEMBSEY Measurement uncertainty analysis for calorimetry apparatuses. Fire and Materials. 32(1), pp.1-26.
Flying imposes considerable physiological demand
Technical Communication Heat Release Characteristics of the basic materials used for flying clothing Wg Cdr V S Sachdev *, TM Kotresh +, MK Vyawahare #, GP Agrawal ** ABSTRACT The fabrics used for overalls
Module 5: Combustion Technology. Lecture 33: Combustion air calculation
1 P age Module 5: Combustion Technology Lecture 33: Combustion air calculation 2 P age Keywords: Heat of combustion, stoichiometric air, excess air, natural gas combustion Combustion air calculation The
Continuous flow direct water heating for potable hot water
Continuous flow direct water heating for potable hot water An independently produced White Paper for Rinnai UK 2013 www.rinnaiuk.com In the 35 years since direct hot water systems entered the UK commercial
COMBUSTION. In order to operate a heat engine we need a hot source together with a cold sink
COMBUSTION In order to operate a heat engine we need a hot source together with a cold sink Occasionally these occur together in nature eg:- geothermal sites or solar powered engines, but usually the heat
Gas emission measurements with a FTIR gas analyzer - verification of the analysis method Kari Pieniniemi 1 * and Ulla Lassi 1, 2
ENERGY RESEARCH at the University of Oulu 117 Gas emission measurements with a FTIR gas analyzer - verification of the analysis method Kari Pieniniemi 1 * and Ulla Lassi 1, 2 1 University of Oulu, Department
FLAMMABILITY REQUIREMENTS FOR 25.853-1 AIRCRAFT SEAT CUSHIONS
FLAMMABILITY REQUIREMENTS FOR 25.853-1 AIRCRAFT SEAT CUSHIONS ANM-110 1. PURPOSE. This Advisory Circular (AC) provides guidance material for demonstrating compliance with the Federal Aviation Regulations
TECHNICAL BULLETIN 117-2013
State of California Department of Consumer Affairs BUREAU OF ELECTRONIC & APPLIANCE REPAIR HOME FURNISHINGS & THERMAL INSULATION 4244 SOUTH MARKET COURT, SUITE D SACRAMENTO, CA 95834-1243 TECHNICAL BULLETIN
Greenhouse gas emissions from direct combustion of various fuels (e.g. grain dryer)
Greenhouse gas emissions from direct combustion of various fuels (e.g. grain dryer) The most significant greenhouse gas from direct combustion is carbon dioxide (CO 2 ) Large number of other compounds
1.3 Properties of Coal
1.3 Properties of Classification is classified into three major types namely anthracite, bituminous, and lignite. However there is no clear demarcation between them and coal is also further classified
The prediction of flue gas emissions from the combustion in the industrial tubular heaters
Ovidius University Annals of Chemistry Volume, Number 1, pp.137-11, 9 The prediction of flue gas emissions from the combustion in the industrial tubular heaters Mirela VELICU a, Claudia-Irina KONCSAG b
Fire Performance Standard
Fire Performance Standard At present, in cable industry, Fire Retardant, Low Smoke Halogen Free (LSZH), Low Smoke Fume (LSF) and Fire Resistant cables are all described as Fire survival Cables. Flame Retardant
18 June 2001 GUIDELINES ON FIRE TEST PROCEDURES FOR ACCEPTANCE OF FIRE-RETARDANT MATERIALS FOR THE CONSTRUCTION OF LIFEBOATS
INTERNATIONAL MARITIME ORGANIZATION 4 ALBERT EMBANKMENT LONDON SE1 7SR Telephone: 020 7735 7611 Fax: 020 7587 3210 Telex: 23588 IMOLDN G IMO E Ref. T4/4.01 MSC/Circ.1006 18 June 2001 GUIDELINES ON FIRE
Andrea Basti* Italian National Institute of Nuclear Physics (INFN) Gran Sasso National Laboratory (LNGS) *Research Grant Holder
Evaluation of the possibility to use waterscreen for people evacuation from the Gran Sasso National Laboratory inside the Gran Sasso highway tunnel in case of fire The case of The Gran Sasso National Laboratory
Module 1: History of Fuels. Lecture 6: Fundamental definitions, properties and various measurements
1 P age Module 1: History of Fuels Lecture 6: Fundamental definitions, properties and various measurements 2 P age Keywords: Characterisation, analytical methods, standards 1.3 Fundamental definitions,
Advantage of Using Water-Emulsified Fuel on Combustion and Emission Characteristics
Advantage of Using Water-Emulsified Fuel on Combustion and Emission Characteristics T. Yatsufusa *1, T. Kumura, Y. Nakagawa, Y. Kidoguchi The University of Tokushima Abstract In the present study, the
Fire testing for BCA compliance
Fire testing for BCA compliance SFS NSW Chapter December 2010 Vince Dowling Fire Science and Technology Australia Standards and Specifications Type Purpose Examples Test method How to do the test and what
Calculation of Liquefied Natural Gas (LNG) Burning Rates
Calculation of Liquefied Natural Gas (LNG) Burning Rates Carolina Herrera, R. Mentzer, M. Sam Mannan, and S. Waldram Mary Kay O Connor Process Safety Center Artie McFerrin Department of Chemical Engineering
Module 5: Combustion Technology. Lecture 34: Calculation of calorific value of fuels
1 P age Module 5: Combustion Technology Lecture 34: Calculation of calorific value of fuels 2 P age Keywords : Gross calorific value, Net calorific value, enthalpy change, bomb calorimeter 5.3 Calculation
Approval Standard for Plastic Suspended Ceiling Panels
Approval Standard for Plastic Suspended Ceiling Panels Class Number 4651 February 1978 2002 FM Approvals LLC. All rights reserved. Foreword The FM Approvals certification mark is intended to verify that
The proof is here!! Ron Goethals, Philadelphia; June 18, 2014
The proof is here!! The proof is here!! The proof is here!! The proof is here!! The proof is here!! The proof is here!! Highly flame-retarded non-halogen bedding compounds show remarkable effects on: BURNING
PREPARATION FOR CHEMISTRY LAB: COMBUSTION
1 Name: Lab Instructor: PREPARATION FOR CHEMISTRY LAB: COMBUSTION 1. What is a hydrocarbon? 2. What products form in the complete combustion of a hydrocarbon? 3. Combustion is an exothermic reaction. What
LASER CUTTING OF STAINLESS STEEL
LASER CUTTING OF STAINLESS STEEL Laser inert gas cutting is the most applicable process type used for cutting of stainless steel. Laser oxygen cutting is also applied in cases where the cut face oxidation
STOICHIOMETRY OF COMBUSTION
STOICHIOMETRY OF COMBUSTION FUNDAMENTALS: moles and kilomoles Atomic unit mass: 1/12 126 C ~ 1.66 10-27 kg Atoms and molecules mass is defined in atomic unit mass: which is defined in relation to the 1/12
D A T A C O M M U N I C A T I O N S C O M P E T E N C E C E N T E R
F l a m e T e s t S t a n d a r d s f o r D a t a C o m m u n i c a t i o n s C a b l e M a r c h 2 0 0 7 D A T A C O M M U N I C A T I O N S C O M P E T E N C E C E N T E R Table of Contents Executive
Validation of Modeling Tools for Detection Design in High Airflow Environments
Validation of Modeling Tools for Detection Design in High Airflow Environments Joshua B. Dinaburg Dr. Jason Floyd, Ph.D. Dr. Sai Thumuluru, Ph.D FM Global MODELING DETECTION RESPONSE Establish validated
General Chemistry I (FC, 09-10) Lab #3: The Empirical Formula of a Compound. Introduction
General Chemistry I (FC, 09-10) Introduction A look at the mass relationships in chemistry reveals little order or sense. The ratio of the masses of the elements in a compound, while constant, does not
DETERMINING THE ENTHALPY OF FORMATION OF CaCO 3
DETERMINING THE ENTHALPY OF FORMATION OF CaCO 3 Standard Enthalpy Change Standard Enthalpy Change for a reaction, symbolized as H 0 298, is defined as The enthalpy change when the molar quantities of reactants
Weight Loss Determined from Mass Spectrometry Trend Data in a Thermogravimetric/Mass Spectrometer System
Weight Loss Determined from Mass Spectrometry Trend Data in a Thermogravimetric/Mass Spectrometer System Carlton G. Slough TA Instruments, 109 Lukens Drive, New Castle DE 19720, USA ABSTRACT The use of
Fire Testing of Recycled Materials for Building Applications
Fire Testing of Recycled Materials for Building Applications Robert H. White Abstract To gain wide market acceptance of new building products made from recycled materials, fire testing may be necessary.
WHITE PAPER Fire & safety performance standards
WHITE PAPER Fire & safety performance standards Terminologies describing Fire Performance Terminologies describing Fire Performance often present a challenge to understand as how they apply to a cable
Sulfur Tail Gas Thermal Oxidizer Systems By Peter Pickard
Sulfur Tail Gas Thermal Oxidizer Systems By Peter Pickard Introduction SRU s (Sulfur Recovery Units) are critical pieces of equipment in refineries and gas plants. SRUs remove sulfur compounds from certain
HFM Heat Flow Meter Thermal Conductivity Analyzer
HFM Heat Flow Meter Thermal Conductivity Analyzer Introduction An insulating material is a material with low thermal conductivity, which in the construction industry, equipment manufacturing, or the production
The Empirical Formula of a Compound
The Empirical Formula of a Compound Lab #5 Introduction A look at the mass relationships in chemistry reveals little order or sense. The ratio of the masses of the elements in a compound, while constant,
Diagnostics for Mobile Homes: HVAC
Diagnostics for Mobile Homes: HVAC Adam Harris NYSWDA Wade Thompson - IWTC Objectives Identify different types of HVAC used in mobile homes Provide an overview of duct systems Demonstrate various tests
Automotive Air Quality Sensors: industrial innovations to protect people s health
Pioneering sensor and detector technology Automotive Air Quality Sensors: industrial innovations to protect people s health COST Action TD1105 3 rd Management Committee Meeting Barcelona, Spain, 21st June
Introductory Laboratory EST - Experiment 9 Calorimetry - 1 - Introductory Laboratory Energy Science and Technology. Experiment 9. Physical Chemistry
Introductory Laboratory EST - Experiment 9 Calorimetry - 1 - Introductory Laboratory Energy Science and Technology Experiment 9 Physical Chemistry Calorimetry Abstract The heat of combustion of Naphthalene
The Minimum Ignition Energy of Coal Dust in an Oxygen Enriched Atmosphere
739 A publication of CHEMICAL ENGINEERING TRANSACTIONS VOL. 31, 2013 Guest Editors: Eddy De Rademaeker, Bruno Fabiano, Simberto Senni Buratti Copyright 2013, AIDIC Servizi S.r.l., ISBN 978-88-95608-22-8;
Reduction in air pollution using the basa njengo magogo method and the applicability to low-smoke fuels
Reduction in air pollution using the basa njengo magogo method and the applicability to low-smoke fuels Lukas J Le Roux Materials Science and Manufacturing, CSIR, Pretoria Mark Zunckel Shirley McCormick
Remember the best arguments are based on the strongest evidence and can explain why opposing arguments are incorrect.
Magnesium and carbon dioxide Student sheet Burning magnesium in carbon dioxide what will happen? Either the magnesium will go out or it will continue to burn. Which will it be? You will use the evidence
A.17. OXIDIZING PROPERTIES (SOLIDS)
A.17. OXIDIZING PROPERTIES (SOLIDS) 1. METHOD 1.1. INTRODUCTION It is useful to have preliminary information on any potentially explosive properties of the substance before performing this test. This test
INTERNATIONAL ASSOCIATION OF CLASSIFICATION SOCIETIES. Interpretations of the FTP
INTERNATIONAL ASSOCIATION OF CLASSIFICATION SOCIETIES Interpretations of the FTP CONTENTS FTP1 Adhesives used in A or B class divisions (FTP Code 3.1, Res A.754 para. 3.2.3) June 2000 FTP2 Pipe and duct
MATHESON STACK EMISSION CALIBRATION PROGRAM. Experience the MATHESON Commitment to Supply Chain Excellence
MATHESON STACK EMISSION CALIBRATION PROGRAM MATHESON STACK EMISSION CALIBRATION PROGRAM MATHESON is a single source for industrial, medical, specialty, and electronics gases as well as gas handling equipment,
QUANTITATIVE INFRARED SPECTROSCOPY. Willard et. al. Instrumental Methods of Analysis, 7th edition, Wadsworth Publishing Co., Belmont, CA 1988, Ch 11.
QUANTITATIVE INFRARED SPECTROSCOPY Objective: The objectives of this experiment are: (1) to learn proper sample handling procedures for acquiring infrared spectra. (2) to determine the percentage composition
Monitoring Air Emissions on Ships. Restricted Siemens AG 2014 All rights reserved.
Monitoring Air Emissions on Ships siemens.com/answers Why emission monitoring in the marine industry? Main drivers: Meeting regulations: NOx and SOx reduction Energy optimization; CO 2 reduction Resolution
NITROGEN OXIDES FORMATION in combustion processes COMBUSTION AND FUELS
NITROGEN OXIDES FORMATION in combustion processes NITROGEN OXIDES FORMED DURING COMBUSTION N 2 O - nitrous oxide NO - nitric oxide NO 2 - nitrogen dioxide N = 14, O 2 =16, NO = 30, NO 2 = 46 CONTRIBUTION
The soot and scale problems
Dr. Albrecht Kaupp Page 1 The soot and scale problems Issue Soot and scale do not only increase energy consumption but are as well a major cause of tube failure. Learning Objectives Understanding the implications
OPTICAL DETECTION OF KCl VAPOR AND ATOMIC K RELEASES FROM BIOMASS FUELS COMBUSTED IN SINGLE PARTICLE REACTOR
OPTICAL DETECTION OF KCl VAPOR AND ATOMIC K RELEASES FROM BIOMASS FUELS COMBUSTED IN SINGLE PARTICLE REACTOR Tapio Sorvajärvi*, Juha Toivonen Tampere University of Technology Department of Physics, Optics
THE HUMIDITY/MOISTURE HANDBOOK
THE HUMIDITY/MOISTURE HANDBOOK Table of Contents Introduction... 3 Relative Humidity... 3 Partial Pressure... 4 Saturation Pressure (Ps)... 5 Other Absolute Moisture Scales... 8 % Moisture by Volume (%M
LESSON PLAN 1. Fire Science. Key Terms and Concepts. ash chemical reaction combustion Consumer Product Safety Commission endothermic exothermic
LESSON PLAN 1 Fire Prevention Fire and Fire Prevention Combustion occurs when the three elements of the fire triangle heat, fuel and oxygen are present. Understanding this basic chemical reaction can help
Honors Chemistry: Unit 6 Test Stoichiometry PRACTICE TEST ANSWER KEY Page 1. A chemical equation. (C-4.4)
Honors Chemistry: Unit 6 Test Stoichiometry PRACTICE TEST ANSWER KEY Page 1 1. 2. 3. 4. 5. 6. Question What is a symbolic representation of a chemical reaction? What 3 things (values) is a mole of a chemical
POROUS BURNER - A New Approach to Infrared
Page: 1 POROUS BURNER - A New Approach to Infrared 1. Preface There are several possibilities to produce infrared radiation in the technical sense. Regarding the source of energy you can distinguish between
Underwriters Laboratories Testing Information
Underwriters Laboratories Testing Information R-8078 Underwriters Laboratories Inc. R-13173 Classified Spray Fiber Surface burning characteristics applied to inorganic reinforced cement board with a maximum
Thermal diffusivity and conductivity - an introduction to theory and practice
Thermal diffusivity and conductivity - an introduction to theory and practice Utrecht, 02 October 2014 Dr. Hans-W. Marx Linseis Messgeräte GmbH Vielitzer Str. 43 D-95100 Selb / GERMANY www.linseis.com
Texas Commission on Environmental Quality Page 1 Chapter 117 - Control of Air Pollution from Nitrogen Compounds
Texas Commission on Environmental Quality Page 1 SUBCHAPTER G: GENERAL MONITORING AND TESTING REQUIREMENTS DIVISION 1: COMPLIANCE STACK TESTING AND REPORT REQUIREMENTS 117.8000, 117.8010 Effective June
Saeid Rahimi. Effect of Different Parameters on Depressuring Calculation Results. 01-Nov-2010. Introduction. Depressuring parameters
Effect of Different Parameters on Depressuring Calculation Results Introduction Saeid Rahimi 01-Nov-2010 Emergency depressuring facilities are utilized to accomplish at least one of the following objectives:
Requirements for Fire Protection of Light Weight Floor Systems **Act 1 Revisited**
PHRC Webinar Series Tuesday, September 9, 2014 1:00 pm Requirements for Fire Protection of Light Weight Floor Systems **Act 1 Revisited** Presented by: Bryan Heitzmann Credit(s) earned on completion of
North American Stainless
North American Stainless Flat Products Stainless Steel Grade Sheet 310S (S31008)/ EN 1.4845 Introduction: SS310 is a highly alloyed austenitic stainless steel designed for elevated-temperature service.
FIRE PERFORMANCE OF FLAME RETARDED POLYMERS USED IN CONSUMER ELECTRONICS
FIRE PERFORMANCE OF FLAME RETARDED POLYMERS USED IN CONSUMER ELECTRONICS Matthew Bundy* & Thomas Ohlemiller National Institute of Standards and Technology, Gaithersburg, MD, USA ABSTRACT An experimental
Determination of the Empirical Formula of Magnesium Oxide
Determination of the Empirical Formula of Magnesium Oxide GOAL AND OVERVIEW The quantitative stoichiometric relationships governing mass and amount will be studied using the combustion reaction of magnesium
How To Test For Premer Retardant
TEST REPORT NEBS COMPLIANCE CHOMERICS PREMIER CONDUCTIVE PLASTIC Prepared by: CHOMERICS R&D 84 DRAGON COURT WOBURN, MA 01801 Test Report Number: TR 1007 EN 0206 Chomerics Approved Signatory: This report
A Study of Matter. Video Notes
A Study of Matter Video Notes In this lesson you will: Define physical property, chemical property and chemical change. Describe the phases of matter. Label properties as physical or chemical. Label changes
Engine Heat Transfer. Engine Heat Transfer
Engine Heat Transfer 1. Impact of heat transfer on engine operation 2. Heat transfer environment 3. Energy flow in an engine 4. Engine heat transfer Fundamentals Spark-ignition engine heat transfer Diesel
Approval Standard for Fume Exhaust Ducts or Fume and Smoke Exhaust Ducts
Approval Standard for Fume Exhaust Ducts or Fume and Smoke Exhaust Ducts Class Number 4922 April 2001 2002 FM Approvals LLC. All rights reserved. Foreword The FM Approvals certification mark is intended
Energy Efficient Operations and Maintenance Strategies for Boilers
Energy Efficient Operations and Maintenance Strategies for Boilers Large, complex and widely used, industrial boilers are major consumers of fuel. Proper operations and maintenance (O&M) procedures must
Dubai Municipality Standard DMS 1: Part 5: 2004
Specification for precast concrete blocks Part 5: Normal-weight concrete-polystyrene sandwich masonry blocks Issue Date Revision Revision Description Prepared by Approved by Authorized by 19/12/2004 Issue
Chapter Test B. Chapter: Measurements and Calculations
Assessment Chapter Test B Chapter: Measurements and Calculations PART I In the space provided, write the letter of the term or phrase that best completes each statement or best answers each question. 1.
Austin Peay State University Department of Chemistry CHEM 1111. Empirical Formula of a Compound
Cautions Magnesium ribbon is flammable. Nitric acid (HNO 3 ) is toxic, corrosive and contact with eyes or skin may cause severe burns. Ammonia gas (NH 3 ) is toxic and harmful. Hot ceramic crucibles and
Trace Gas Exchange Measurements with Standard Infrared Analyzers
Practical Environmental Measurement Methods Trace Gas Exchange Measurements with Standard Infrared Analyzers Last change of document: February 23, 2007 Supervisor: Charles Robert Room no: S 4381 ph: 4352
Chemistry 12 Worksheet 1-1 - Measuring Reaction Rates
Chemistry 12 Worksheet 1-1 - Measuring Reaction Rates 1. A chemist wishes to determine the rate of reaction of zinc with hydrochloric acid. The equation for the reaction is: Zn (s) + 2HCl (aq) oh 2(g)
Adiabatic Bomb Calorimetry
CHEM 366 II-1 Adiabatic Bomb Calorimetry Introduction Obtaining energy in the form of heat from the combustion or oxidation of thermodynamically unstable (and often kinetically inert) hydrocarbons and
IDEAL AND NON-IDEAL GASES
2/2016 ideal gas 1/8 IDEAL AND NON-IDEAL GASES PURPOSE: To measure how the pressure of a low-density gas varies with temperature, to determine the absolute zero of temperature by making a linear fit to
Experimental Evaluation of the Discharge Coefficient of a Centre-Pivot Roof Window
Experimental Evaluation of the Discharge Coefficient of a Centre-Pivot Roof Window Ahsan Iqbal #1, Alireza Afshari #2, Per Heiselberg *3, Anders Høj **4 # Energy and Environment, Danish Building Research
to control the heat alongside the boiler to protect the more sensitive metal components against thermal, erosive and corrosive degradation
Testing procedures for refractory material in bottom grid of biomass/waste-fired CFBs 1 Karol Nicia, Edgardo Coda Zabetta 2 Mikko Hupa, Leena Hupa 1 Foster Wheeler Oy, Varkaus, Finland 2 Process Chemistry
ATMOSPHERIC EMISSIONS FROM GAS FIRED HOME HEATING APPLIANCES
ATMOSPHERIC EMISSIONS FROM GAS FIRED HOME HEATING APPLIANCES Stefano Cernuschi, Stefano Consonni, Giovanni Lonati, Michele Giugliano, Senem Ozgen DIIAR Environmental Sect., Politecnico di Milano, P.za
Limiting Reagent Worksheet #1
Limiting Reagent Worksheet #1 1. Given the following reaction: (Balance the equation first!) C 3 H 8 + O 2 -------> CO 2 + H 2 O a) If you start with 14.8 g of C 3 H 8 and 3.44 g of O 2, determine the
Examination syllabuses for Manual Stack emissions monitoring. Environment Agency Version 9 January 2015
Examination syllabuses for Manual Stack emissions monitoring Environment Agency Version 9 January 2015 Record of amendments Version Date Section Amendment number 6 August 09 Level 1 Updated Level 1 syllabus
FIELD TESTS OF FUEL EFFICIENCY MAGNETS J A CRABB JULY 1997 SWEEG REPORT 80
FIELD TESTS OF FUEL EFFICIENCY MAGNETS J A CRABB JULY 1997 SWEEG REPORT 80 List of symbols T f average temperature at the flow header, C T r average temperature at the return header, C f average water
11-1 Stoichiometry. Represents
11-1 Stoichiometry What is stoichiometry? Calculations that relate the quantities of substances. It is the study of quantitative (measurable amounts) relationships in chemical reactions and equations.
Carbon Dioxide Membrane Separation for Carbon Capture using Direct FuelCell Systems
Carbon Dioxide Membrane Separation for Carbon Capture using Direct FuelCell Systems DFC Technology Used as Electrochemical Membrane for CO 2 Purification and Capture during Power Generation FCE s Direct
North American Stainless
Introduction: North American Stainless Flat Products Stainless Steel Grade Sheet 309S (S30908)/ EN1.4833 SS309 is a highly alloyed austenitic stainless steel used for its excellent oxidation resistance,
DETERMINATION OF THE HEAT STORAGE CAPACITY OF PCM AND PCM-OBJECTS AS A FUNCTION OF TEMPERATURE. E. Günther, S. Hiebler, H. Mehling
DETERMINATION OF THE HEAT STORAGE CAPACITY OF PCM AND PCM-OBJECTS AS A FUNCTION OF TEMPERATURE E. Günther, S. Hiebler, H. Mehling Bavarian Center for Applied Energy Research (ZAE Bayern) Walther-Meißner-Str.
Chapter Three: STOICHIOMETRY
p70 Chapter Three: STOICHIOMETRY Contents p76 Stoichiometry - The study of quantities of materials consumed and produced in chemical reactions. p70 3-1 Counting by Weighing 3-2 Atomic Masses p78 Mass Mass
G26 Corp. 9721-L11 Revised 07-2001 LENNOXOEMPARTS.COM. Service Literature G26 SERIES UNITS
Service Literature G26 SERIES UNITS G26 series units are high-efficiency upflow gas furnaces manufactured with DuralokPlust aluminized steel clamshell-type heat exchangers. G26 units are available in heating
furnishings flammability characteristics
Technical Bulletin 110104 New Options for Textiles The performance of Ingeo fibers in the standard flammability tests described below confirm that Ingeo fibers, without any flame retardant (FR) treatment,
Energy Saving Fact Sheet Boilers
Energy Saving Fact Sheet Boilers Turn a burning issue into real energy savings You need a boiler to heat your premises and provide hot water or to generate steam for use in industrial processes. Unfortunately,
Measurement of Charge-to-Mass (e/m) Ratio for the Electron
Measurement of Charge-to-Mass (e/m) Ratio for the Electron Experiment objectives: measure the ratio of the electron charge-to-mass ratio e/m by studying the electron trajectories in a uniform magnetic
EUROPEAN STANDARDS PERSONAL PROTECTIVE CLOTHING FOR FLAME RESISTANT. Alexander Gstettner, Lenzing AG Austria
EUROPEAN STANDARDS FOR FLAME RESISTANT PERSONAL PROTECTIVE CLOTHING Alexander Gstettner, Lenzing AG Austria W a t e r How are the standards organized? A 1 Testing Methods Standards specifiying performance
MEMORANDUM GRADE 11. PHYSICAL SCIENCES: CHEMISTRY Paper 2
MEMORANDUM GRADE 11 PHYSICAL SCIENCES: CHEMISTRY Paper 2 MARKS: 150 TIME: 3 hours Learning Outcomes and Assessment Standards LO1 LO2 LO3 AS 11.1.1: Plan and conduct a scientific investigation to collect
User's Guide for the Cone Calorimeter
NBS Special Publication 745 User's Guide for the Cone Calorimeter William H. Twilley and Vytenis Babrauskas Fire Measurement and Research Division Center for Fire Research National Bureau of Standards
Calculate Available Heat for Natural Gas Fuel For Industrial Heating Equipment and Boilers
For Industrial Heating Equipment and Boilers Prepared for California Energy Commission (CEC) Prepared By: Southern California Gas Company (A Sempra Energy Utility) E3M Inc. May 2012 i Disclaimer The CEC
IB Chemistry. DP Chemistry Review
DP Chemistry Review Topic 1: Quantitative chemistry 1.1 The mole concept and Avogadro s constant Assessment statement Apply the mole concept to substances. Determine the number of particles and the amount
SUPPLEMENTARY TOPIC 3 ENERGY AND CHEMICAL REACTIONS
SUPPLEMENTARY TOPIC 3 ENERGY AND CHEMICAL REACTIONS Rearranging atoms. In a chemical reaction, bonds between atoms in one or more molecules (reactants) break and new bonds are formed with other atoms to
Paper 1 (7405/1): Inorganic and Physical Chemistry Mark scheme
AQA Qualifications A-level Chemistry Paper (7405/): Inorganic and Physical Chemistry Mark scheme 7405 Specimen paper Version 0.5 MARK SCHEME A-level Chemistry Specimen paper 0. This question is marked
Fire Resistance and Safety in Case of Fire
Fire Resistance and Safety in Case of Fire Franck GYPPAZ Nexans Research Center [email protected] April 2014 Page 1/12 Table of content 1 Introduction... 3 2 Fire development... 3 2.1 Ignition...
T U R B I N E G A S M E T E R
TURBINE GAS METER TURBINE GAS METER CGT 1 2 3 4 5 6 7 Design and function page 2 General technical data page 3 Measurement outputs page 4 Dimensions and weights page 5 Performance page 7 Pressure loss
Determination of Thermal Conductivity of Coarse and Fine Sand Soils
Proceedings World Geothermal Congress Bali, Indonesia, - April Determination of Thermal Conductivity of Coarse and Fine Sand Soils Indra Noer Hamdhan 1 and Barry G. Clarke 2 1 Bandung National of Institute
Effects of Temperature, Pressure and Water Vapor on Gas Phase Infrared Absorption by CO 2
Effects of Temperature, Pressure and Water Vapor on Gas Phase Infrared Absorption by CO 2 D. K. McDermitt, J. M. Welles, and R. D. Eckles - LI-COR, inc. Lincoln, NE 68504 USA Introduction Infrared analysis
Latest Low-NOx Combustion Technology for Pulverized-coal-fired Boilers
Hitachi Review Vol. 58 (29), No.5 187 Latest Low- Combustion Technology for Pulverized-coal-fired Boilers Kenichi Ochi Kenji Kiyama Hidehisa Yoshizako, Dr. Eng. Hirofumi Okazaki Masayuki Taniguchi, Dr.
SALT SPRAY AND IMMERSION CORROSION TESTING OF PM STAINLESS STEEL MATERIALS. W. Brian James Hoeganaes Corporation. Cinnaminson, NJ 08077
SALT SPRAY AND IMMERSION CORROSION TESTING OF PM STAINLESS STEEL MATERIALS W. Brian James Hoeganaes Corporation Cinnaminson, NJ 08077 Leander F. Pease III Powder-Tech Associates Inc. Andover, MA 01845
