CACHE Modules on Energy in the Curriculum Hydrogen as a Fuel Module Title: Hydrogen Flammability Module Author: Dr. Daniel A. Crowl Author Affiliation: Michigan Technological University Course: Stoichiometry, process design, process safety Text Reference: Felder and Rousseau, Elementary Principles of Chemical Processes, 3rd ed., New York: John Wiley and Sons, 2005. Crowl and Louvar, Chemical Process Safety, Fundamentals with Applications, 2nd ed., Upper Saddle river, NJ: Prentice Hall, 2002. Concepts: Flammability of gas. Problem Motivation: Fuels are flammable because we burn these fuels to produce energy. However, the property of flammability also creates a hazard in that a leakage or evaporation of the fuel might produce a flammable atmosphere when it is not expected. This may lead to a fire or explosion if an ignition source is found. This module will look at the issue of fuel flammability. The flammable limits define the range of fuel concentrations in air over which the mixture is flammable. If a flammable mixture is formed due to the leakage or evaporation of a fuel, a fire or explosion is likely. The flammable limits are defined at a temperature of 25oC and 1 atm. As the temperature increases the flammability range typically increases – the lower limit decreases and the upper limit increases. The experimental procedure to determine the flammable limits is an empirical procedure. The flammable limits do not have a theoretical basis like heat capacity. It is always recommended that flammable limits be obtained as close as possible to actual process conditions. Basic Definitions: Lower Flammable Limit (LFL) The volume percent fuel in air below which combustion is not possible – the mixture is too lean. The units are volume percent fuel in air. Upper Flammable Limit (UFL) 2nd Draft D. A. Crowl June 25, 2010 Page 1 The volume percent fuel in air above which combustion is not possible – the mixture is too rich. The units are volume percent fuel in air. Problem Information Example Problem Statement: The flammable limits for three fuels are provided below: Hydrogen: Gasoline: Methane: LFL UFL 4.0% 1.3% 5.0% 75% 7.2% 15.0% Molecular Weight kg/mol 0.002 0.106 0.016 a. A storage room has dimensions of 4 m x 4 m x 4 m. Calculate the amount of each chemical species, in kg, that must leak or evaporate into the room to form a flammable mixture. b. A cylinder containing 200 SCF of hydrogen is stored in this room. If the cylinder leaks out into the room, will it form a flammable mixture? Assume a temperature of 30oC and a pressure of 1 atm. Additional data: Gasoline: MW: Density: 106 720 kg/m3 Example Problem Solution: a. The room has dimensions of 4 m x 4 m x 4 m. The total volume is 4 x 4 x 4 = 64 m3. Hydrogen: The lower flammable limit is 4% by volume hydrogen in air. Thus, the hydrogen gas required to reach the LFL is 0.04 64 m3 2.56 m3 The molar density of any ideal gas at 1 atm and 30oC = 303K is: P 1 atm 40.2 mol/m3 5 RgT 8.2057 10 m3 atm/mol K 303 K The total amount of hydrogen at the LFL is 2.56 m 40.2 mol/m 102.9 mol 3 3 102.9 mol = 0.206 kg Only 0.206 kg of hydrogen needs to leak out in order to form a flammable mixture. Gasoline: The LFL is 1.3%. The total volume of gasoline vapor required to reach the LFL is 0.013 64 m3 0.832 m3 2nd Draft D. A. Crowl Page 2 June 25, 2010 The total moles of gasoline in this vapor is 0.832 m 40.2 mol/m 33.4 mol 3 3 33.4 mol = 3.54 kg Methane: The LFL is 5.0%. The total volume of gasoline vapor required to reach the LFL is 0.05 64 m3 3.2 m3 The total moles of methane in this vapor is 3.2 m 40.2 mol/m 128.6 mol 3 3 128.6 mol = 2.06 kg b. Convert SCF to m3 2.832 102 m3 3 200 SCF 5.66 m 3 1 ft The volume fraction of fuel is thus 5.66 m3 0.088 8.8 vol. % hydrogen 64 m3 Yes, the mixture is flammable. 2nd Draft D. A. Crowl Page 3 June 25, 2010 Home Problem Statement: A storage room has dimensions of 4 m x 4 m x 4 m. Calculate the amount of each chemical species, in kg, that must leak or evaporate into the room to form a flammable mixture. Perform the calculation for the upper flammable limit. 2nd Draft D. A. Crowl Page 4 June 25, 2010