alexa Chemical Kinetics Illustrations: Methane and Hydrogen Sulfide Combustion | Open Access Journals
ISSN: 2157-7048
Journal of Chemical Engineering & Process Technology
Like us on:
Make the best use of Scientific Research and information from our 700+ peer reviewed, Open Access Journals that operates with the help of 50,000+ Editorial Board Members and esteemed reviewers and 1000+ Scientific associations in Medical, Clinical, Pharmaceutical, Engineering, Technology and Management Fields.
Meet Inspiring Speakers and Experts at our 3000+ Global Conferenceseries Events with over 600+ Conferences, 1200+ Symposiums and 1200+ Workshops on
Medical, Pharma, Engineering, Science, Technology and Business

Chemical Kinetics Illustrations: Methane and Hydrogen Sulfide Combustion

Ivan A Gargurevich*
Chemical Engineering Consultant, Combustion and Process Technologies, 32593 Cedar Spring Court, Wildomar, CA 92595, USA
Corresponding Author : Ivan A Gargurevich
Chemical Engineering Consultant,Combustion and Process Technologies
32593 Cedar Spring Court, Wildomar, CA 92595, USA
Tel: 9516759455
E-mail: [email protected]
Received: February 10, 2016; Accepted: February 27, 2016; Published: February 29, 2016
Citation: Gargurevich IA (2016) Chemical Kinetics Illustrations: Methane and Hydrogen Sulfide Combustion. J Chem Eng Process Technol 7:280. doi:10.4172/2157-7048.1000280
Copyright: © 2016 Gargurevich IA. This is an open-access article distributed under the terms of the Creative Commons Attribution License, which permits unrestricted use, distribution, and reproduction in any medium, provided the original author and source are credited.

Visit for more related articles at Journal of Chemical Engineering & Process Technology


Methane combustion has to be one of the most studied systems but nevertheless because of the dependence of many of the rates of elementary reactions in the mechanism on pressure and temperature (unimolecular or chemically activated reactions) as well as combustion conditions, fuel-rich or lean, discrepancies can always be found between two close but different combustion mechanisms authored by different investigators(both in the kinetic coefficients of reactions as well as the results of modeling). Nevertheless, the major chemical pathways are well known

Chemical reaction; Chemical kinetics
Methane combustion model assembly
In this section an attempt will made to present the approach to developing the major features for the combustion of methane based on the concepts presented in previous chapters. The starting point is the understanding that methane combustion involves (1) a chain reaction mechanism and (2) that its chemistry obeys the Hierarchical structure of Hydrocarbon combustion.
It must be kept in mind that the mechanism that is assembled must explain the overall reaction for combustion of methane or,
CH4 + 2O2 < = = > CO2 + 2H2O (CO, H2 as well, depending on stoichiometry)
Thus, the initiation of methane combustion involves the attack by small radicals present in the flame or for example in a fuel-rich flame,
CH4 + H < = => CH3 + H2
Other reactions would involve the attack by OH, O radicals depending on combustion conditions. The formation of such small radicals are initiated by the high temperature decomposition of the fuel or,
CH4 + M < = = > CH3 + H + M
Another important reaction in chain mechanisms is branching or,
H + O2 < = = > O + OH
The mechanism must know explain the formation of intermediates such as CO and even C2 hydrocarbons in fuel-rich flames.
The fate of the methyl radical is most important since it can lead to formaldehyde formation or C2 hydrocarbon intermediates.
The formation of formaldehyde is as follows,
CH3 + O < = = > CH2O + H
CH2O leads to the formation of carbon monoxide by small radical attack,
CH2O + H < = = > CHO + H
CH2O + OH < = => CHO + H2O
CHO + M < = => CO + H + M
Carbon monoxide oxidation by OH leads to the final product of combustion carbon dioxide.
CO + OH < = = > CO2 + H
As mentioned above the formation of C2 intermediates is an important event in fuel-rich flames. Methyl radical again plays an important role,
CH3 + CH3 + M < = = C2H6 + M
Then by a sequence of reactions involving the small radicals H, OH, O, and molecular Oxygen O2, ethane is broken down to C2H2 (acetylene) first and finally to CH2 radical species or,
H, OH, O O2
C2H6 < = = > C2H6 < = = > C2H4 < = = > C2H3 < = = > C2H2
Acetylene C2H2 leads to CH2 and then CO,
C2H2 + O < = = > CH2 + CO
CH2 + O2 < = = > CO2 + H + H
A flowchart for C1/C2 Hydrocarbon oxidation from Warnatz [1] is shown in Figure 1 as a summary of the discussion.
A very well known Methane combustion mechanism consisting of hundreds of reactions for methane including formation of NOx species is the GRI Mechanism 3.0 which is included in Appendix 2 as an illustration.
Hydrogen sulfide combustion model assembly
The combustion of Hydrogen sulfide [2] follow similar principles as methane discussed above: chain reaction mechanism and thermal decomposition of the fuel as radical initiation reaction. The overall reaction is:
H2S + 1.5 O2 < = = > SO2 + H2O (Sx, SO depending on stoichiometry)
The mechanism needs to explain the formation of SOx and Sx depending on stoichiometric conditions.
The formation of small radicals is initiated by the high temperature decomposition of H2S or,
H2S + M < = = > HS + H + M
Most important also is chain branching:
H + O2 < = => H + OH
Under fuel-rich conditions the main path for decomposition would be
H2S + H < = => HS + H
The formation of oxygenated species starts with,
HS + O < = = > SO + H
SO + O +M < = = > SO2 + M
Under fuel-lean conditions SO3 can be produced by the reaction.
SO2 + O + M < = = > SO3 + M
The formation of Sulfur vapor can be explained by the following reaction,
HS + H < = = > S + H2
Molecular growth of the Sulfur species then takes place by radical addition reactions,
S + S + M < = = > S2 + M
S2 + S + M < = = > S3 + M
Appendix 3 illustrates a combustion mechanism for Hydrogen sulfide under reducing conditions including the formation of S2 or sulfur vapor species [2].
Chemical vapor deposition: polycrystalline silicon
This example is attributed to Dobkin and Zuraw [3]. The reaction mechanism for deposition of polycrystalline Silicon from Silane in the gas phase on silicon wafers is presented. See Figure 2 for the experimental set-up, consisting of a plug flow reactor operating at 600°C and 0.5 torr. The temperature of the gas is high enough for radicals to possibly play a role in reactions in the gas phase (not discussed here).
The first step is the chemisorption of silane, SiH4 (g), onto the surface of the wafer or,
SiH4 (g) + [*] = = > [SiH3]ads + [H]ads
Where [*] is an active site on the surface, it could consist of a dangling bond. This reaction is followed by the rapid decomposition of adsorbed SiHx to Si(s)
[SiH3]ads = => [SiH2]ads +[H]ads = => [SiH]ads + [H]ads = => Si(s) +[H] ads
As Dobkin and Zuraw point out, the desoption of hydrogen turns out to be complex and rather counterintuitive. Instead of neighboring H atoms getting together to form an H2 molecule which desorbs, desorption takes place in two steps. First, a hydrogen atom is promoted into a fast-moving weakly-bound (H’) but still adsorbed localized surface atom H’ or,
[H]ads = = > H’ + [*]
The delocalized hydrogen atom then wanders along the surface until it reacts with a surface hydrogen to form molecular hydrogen H2,
[H]ads + H’ = = > H2 (g)

Figures at a glance

Figure Figure
Figure 1 Figure 2
Select your language of interest to view the total content in your interested language
Post your comment

Share This Article

Recommended Conferences

Article Usage

  • Total views: 8059
  • [From(publication date):
    February-2016 - Jul 26, 2017]
  • Breakdown by view type
  • HTML page views : 7989
  • PDF downloads :70

Post your comment

captcha   Reload  Can't read the image? click here to refresh

Peer Reviewed Journals
Make the best use of Scientific Research and information from our 700 + peer reviewed, Open Access Journals
International Conferences 2017-18
Meet Inspiring Speakers and Experts at our 3000+ Global Annual Meetings

Contact Us

© 2008-2017 OMICS International - Open Access Publisher. Best viewed in Mozilla Firefox | Google Chrome | Above IE 7.0 version