United States Environmental Protection Agency Air and Energy Engineering Research Laboratory Research Triangle Park NC 27711 Research and Development EPA/600/S7-85/048 Jan. 1986 &EPA Project Summary Fundamental Combustion Research Applied to Pollution Formation Volume I. FCR Program Overview and Gas-Phase Chemistry W. R. Seeker, M. P. Heap, T. J. Tyson, J. C. Kramlich, and T. L Corley This volume (Volume I) is an overview of the entire contract and the summary of the technical effort in gas- phase chemistry. EPA's first fundamental combustion research (FCR) applied to pollution con- trol program was a subcontract ori- ented program focused on the simulta- neous control of nitrogen oxides (NOX) and participate from large, confined, 1-atmosphere, turbulent diffusion flames burning heavy residual oil and pulverized coal. The program had three major objectives: • To generate the understanding of combustor behavior necessary to aid EPA/AEERL's Combustion Re- search Branch (CRB) in developing control strategies to minimize NOX emissions from stationary sources. • To develop engineering models which would allow effective uti- lization of a large body of funda- mental information in the develop- ment of new NOX control techniques. • To identify critical information nec- essary for low NOX combustor de- velopment and to generate it in a time frame which was consistent with the needs of the CRB technol- ogy development programs. The FCR program was divided into three program areas and two support areas. The major program areas were concerned with (1) gas-phase chem- istry, (2) the physics and chemistry of two-phase systems, and (3) transport processes in reacting systems. This or- ganization was designed to address the critical phenomena that occurred to solid or liquid fuels in turbulent diffu- sion flames in order to describe fuel NO formation from stationary sources. The two support areas were for the devel- opment of measurement techniques and the development of analytical tools required during the program and for fu- ture investigations. Table 1 lists the major individual projects that made up the program and the organizations pri- marily responsible for the effort. This Project Summary was devel- oped by EPA's Air and Energy Engineer- ing Research Laboratory, Research Tri- angle Park, NC, to announce key findings of the research project that is fully documented in a separate report of the same title (see Project Report ordering information at back). Introduction This volume describes efforts associ- ated with gas-phase chemistry (GPC) and provides a detailed account of the FCR gas-phase effort which was divided into these principal tasks: 1. Elementary Kinetic Development. To develop an elementary gas- phase kinetic mechanism which describes combustion reactions for hydrocarbons—through C2 structures—and the fate of fuel ni- ------- Table 1. Fundamental Combustion Research Program Project Organization Gas-Phase Chemistry Kinetic Mechanism Development The Modeling of Fuel Nitrogen Chemistry in Combustion: The Influence of Hydro- carbon The Formation and Destruction of Nitroge- neous Species During Hydrocarbon/Air Combustion High Temperature Reactor Studies Physics and Chemistry of Two-Phase Systems The Physical and Chemical Effects Occur- ring During the Thermal Decomposition of Coal Particles Detailed Measurements of Long Pulverized Coal Flames for the Characterization of Pollutant Formation An Experimental Approach to the Study of Heavy Fuel Oil Spray Combustion in Shear Layers The Characterization of Coals During Ther- mal Decomposition Volatility of Fuel Nitrogen Pollutant Formation from Combusting Pul- verized Coal Clouds Pollutant Formation During the Combustion of Residual Fuel Oils in Backmixed Reac- tors Mechanisms of Nitric Oxide Reduction on Solid Particles Energy and Environmental Research Massachusetts Institute of Technology Exxon Research and Development Energy and Environmental Research Energy and Environmental Research International Flame Research Foundation United Technologies Research Center United Technologies Research Center Rockwell International Acurex Battelle Memorial Laboratory Institut Francais du Petrole Transport Phenomenon and Engineering Analysis Development of a Coherent Flame Model for Turbulent Chemically-Reacting Flames A Computer Program for General Flame Analysis Mathematical Modeling of Microscale Com- bustion of a Coal Particle Measurements Support Chemiluminescent Measurements of Nitric Oxide in Combustion Products Measurements of Fuel Nitrogen Species in Flames Spray Characterization The Application of Droplet-sizing Interfer- ometry and Holography to the Measure- ment of Spray Droplet Size California Institute of Technology/TRW Energy and Environmental Research Energy and Environmental Research Energy and Environmental Research University of Utah Energy and Environmental Research Spectron Development Laboratory trogen (including HCN, NHa, NO, and the respective intermediates). 2. Data Generation. To generate a sufficient data base for model veri- fication for the full mechanism (hy- drocarbons + full nitrogen). A suit- able quantity of data for development of the more complex portions of the gas-phase model do not exist. 3. Higher Hydrocarbons. To develop a methodology for modeling the combustion of complex hydrocar- bon fuels. Such modeling is not currently possible using elemen- tary reactions. The GPC effort fell into three principal subdivisions. Elementary GPC con- sisted of the compilation and testing of a comprehensive elementary gas-phase mechanism which describes fuel nitro- gen chemistry in hydrocarbon flames. The maximum complexity of the mech- anism was limited by the availability of elementary rate data (specifically, no hydrocarbons larger than C2 were con- sidered). The gas-phase mechanism was tested by comparing mechanistic predictions against well-characterized data. For the most complex simulations (i.e., utilizing the full hydrocarbon/nitro- gen mechanism) an insufficient number of data exist for adequate testing. Thus, a second thrust of the GPC effort was to generate the necessary data. These measurements consisted of species measurements from a jet-stirred com- bustor and a plug-flow burner. Assuming an accurate and complete gas-phase mechanism is assembled, only hydrocarbon fuels of C2 or simpler structure can be simulated. The likeli- hood that the elementary mechanistic approach can be extended to more complex hydrocarbons is remote. Hence, a third thrust of GPC was to de- velop a quasi-global method of incorpo- rating some aspects of higher hydrocar- bon chemistry into the model. Elementary Gas-Phase Chemistry Work on the elementary gas-phase mechanism proceeded in three well- characterized divisions: methodology development, collection of reactions and rates, and testing and modification of the mechanism. The mechanism development methodology is a system of rules and procedures governing the testing of mechanism components and the com- bination of the components into more complex mechanisms. The objective of the methodology is to provide an efff- cient way to assemble and test the mechanism while ensuring internal consistency within the mechanism. Im- portant features include: (1) careful se- lection of data for simulation such that critical questions are resolved (e.g., shock-tube ignition delays are used to resolve questions on chain initiation and branching portions of a mecha- nism), and (2) previously proven por- tions of a mechanism may be modified only after repeating the original proving simulations. The assembled elementary reactions can be conveniently divided into the subsets H2/02, CO/H2/02, CH20, NH3, and HCN, as shown in Figure 1. An ex- tensive series of tests of the proposed mechanism were conducted comparing predictions against various types of shock-tube and flame data. The results indicated that the H2/02 and CO/H2/O2 subsets yielded excellent ------- Hydrocarbons r ' i I 1 I I L . r~ i ---- i W2/Oa \ m/t-i /n — , — NH3 1 HCN T | 1 1 1 1 -1 T 1 i i i I i i i i i 1. ' i i c/ 1 Y4 ^ CaH | ( 2 ,H i 20 CaW4 "*" CaWe ^~ ^^^™ | J | 1 • Fuel Nitrogen i (Hydrocarbons \ \ 1 Figure 1. Overview of kinetic mechanisms. agreement with the verification data in all cases. The comparisons included shock-tube ignition delays and radical growth rates, flat-flame profiles, and flat-flame speeds. General features of methane oxidation were well repro- duced; however, radical profiles and the appearance of C2 species were not predicted as well. The nitrogen chem- istry generally predicted the overall re- duction of fixed nitrogen into N2 quite well, but was less successful in predict- ing the reduced nitrogen speciation. In general, the success of the predictions corresponded to the number and qual- ity of the fundamental data used to derive the rates. Thus, the least studied systems showed the least successful re- productions: HCN chemistry, and hy- drocarbon/nitrogen interaction. Data Generation An abundant quantity of data suitable for mechanism verification for simple compounds is in the literature. The usable quantity of data decreases as the compounds involved become more complex. Only a very small amount of literature data is available for testing the entire (hydrocarbons + fuel nitrogen) mechanism. Thus, one of the tasks of the elementary gas-phase chemistry program was to generate such a body of useful data. The approach was to obtain data on the fate of doped nitrogen in well char- acterized hydrocarbon combustion en- vironments. Two experiments were used: the Exxon jet-stirred reactor and the Exxon Multiburner (a flat-flame fir- ing into an isothermal plug-flow reac- tor). Temperatures ranged from 1800 to 2000 K and equivalence ratios were varied from 0.7 to 1.8. Fuels were methane, ethylene, or propane, and fuel-nitrogen was represented by am- monia or an ammonia/nitric oxide mix- ture. The measurements included the standard combustion products (O2, CO, CO2, H2, and total hydrdcarbons) and ni- trogen specification (HCN, NH3, NO, and N02). Modeling of Nitrogen Conversion in Higher Hydrocarbon Environments Modeling of combustion processes by elementary reactions is, of necessity, limited to hydrocarbons of C2 or simpler structure. Modeling of the combustion of higher hydrocarbons has in the past usually been performed by assuming some kind of global oxidative pyrolysis step. Among the possibilities discussed are: 1. Global oxidation of the hydrocar- bon fuel to CO2 and H2O following an empirically determined rate constant. 2. Two semi-global steps: in the first, the parent hydrocarbon is oxidized to CO and H20; and the second consists of the oxidation of the CO to C02. 3. Quasi-global methods combine global steps with elementary kinet- ics. The usual form has the hydro- carbon oxidized to CO and H2 by a global step. The CO and H2 are subsequently oxidized by an ele- mentary kinetic mechanism. The novel quasi-global approach pro- posed in this study follows the general form: Parent Hydrocarbon Global Distribution of Hydrocarbon Fragments Detailed Kinetics H20 The justification of this technique is that the oxidative pyrolysis of most complex hydrocarbons into an array of fragments of C2 or simpler structure is a rapid process compared to subsequent reactions (in particular, fuel-nitrogen chemistry). The principal accomplish- ments in this task are: 1. Demonstration of the feasibility of the approach outlined above. A study of the literature covering the pyrolysis into hydrocarbon frag- ments justifies the assumptions of the quasi-global mode. Some of the data needed to assign speciation to the hydrocarbon fragments have been obtained. 2. ------- W. Seeker, M. Heap, T. Tyson, J. Kramlich, and T. Corley are with Energy and Environmental Research Corp., Irvine, CA 92718-2798. Jon E. Haebig is the EPA Project Officer (see below). The complete report, entitled "Fundamental Combustion Research Applied to Pollution Formation: Volume I. FCR Program Overview and Gas-phase Chemistry,"(Order No. PB 86-122 660/AS; Cost: $28.95, subject to change) will be available only from: National Technical Information Service 5285 Port Royal Road Springfield, VA22161 Telephone: 703-487-4650 The EPA Project Officer can be contacted at: Air and Energy Engineering Research Laboratory U.S. Environmental Protection Agency Research Triangle Park, NC 27711 J United States Environmental Protection Agency Center for Environmental Research Information Cincinnati OH 45268 Official Business Penalty for Private Use $300 EPA/600/S7-85/048 U.S.OFFiCIALM.'U ^™,ALTY[YS.P9S!AGE" j WIVATE ' 0000329 PS AG£NCT ------- |