Optimization of adiabatic flame temperature of natural gas combustion under different conditions

Author:

Bani‐Hani Ehab Hussein1,Al‐Khatib Fadi1,El Haj Assad Mamdouh2,Alshabi Mohammad3,Castellanos Humberto Garcia4ORCID,Aryanfar Yashar56ORCID,Deifalla Ahmed7,Ragab Adham E.8

Affiliation:

1. Mechanical Engineering Department, College of Engineering Australian University Kuwait Kuwait

2. Sustainable and Renewable Energy Engineering Department University of Sharjah Sharjah United Arab Emirates

3. Department of Mechanical and Nuclear Engineering University of Sharjah Sharjah United Arab Emirates

4. Engineering Sciences Tecnológico Nacional de México IT Ciudad Juárez Chihuahua Mexico

5. Department of Electric Engineering and Computation Autonomous University of Ciudad Juárez Chihuahua Mexico

6. State Key Laboratory of Hydrology‐Water Recourses and Hydraulic Engineering, College of Mechanics and Materials Hohai University Nanjing Jiangsu China

7. Future University in Egypt New Cairo Egypt

8. Department of Industrial Engineering, College of Engineering King Saud University Riyadh Saudi Arabia

Abstract

AbstractThe combustion of natural gas consisted of methane , ethane , and propane is theoretically investigated to obtain the optimum adiabatic flame temperature (AFT). The investigation includes the development of combustion equations that take into consideration different compositions of natural gas. The final equation to calculate the AFT is derived and used in the optimization study. The optimization study using genetic algorithm investigates the effect of changing the composition of the gas mixture, the inlet temperature of used air, and the amount of excess air used on the AFT. It is possible to get the required composition of each component, the air inlet temperature, and the excess air by reading the chart to get the required AFT. The heat capacity of all reactants and products is used as a function of temperature. Results showed that the optimum values for , percentages in the gas mixture, air inlet temperature, and the amount of excess air are 0.478, 0.166, 0.356 mol %, 1.848, 382.104 K, respectively. These optimum values lead to a value of about 1300 K for the AFT. The derived equation shows the AFT at different natural gas compositions along with different process parameters such as the amount of excess air. Thus, the required combustion temperature can be controlled by adjusting the natural gas composition or the combustion temperature can be specified based on the provided composition of the natural gas stream by using either the derived equations or output chart. (R1. 1).

Publisher

Wiley

Subject

General Environmental Science,Waste Management and Disposal,Water Science and Technology,General Chemical Engineering,Renewable Energy, Sustainability and the Environment,Environmental Chemistry,Environmental Engineering

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