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<title>School of Chemistry (Scholarly Articles)</title>
<link>http://hdl.handle.net/10379/1154</link>
<description/>
<pubDate>Sun, 29 Oct 2017 23:48:42 GMT</pubDate>
<dc:date>2017-10-29T23:48:42Z</dc:date>
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<title>Ignition characteristics of 2-methyltetrahydrofuran: An experimental and kinetic study</title>
<link>http://hdl.handle.net/10379/6900</link>
<description>Ignition characteristics of 2-methyltetrahydrofuran: An experimental and kinetic study
Tripathi, Rupali; Lee, Changyoul; Fernandes, Ravi X.; Olivier, Herbert; Curran, Henry J.; Sarathy, S. Mani; Pitsch, Heinz
The present paper elucidates oxidation behavior of 2-methyltetrahydrofuran (2-MTHF), a novel second-generation biofuel. New experimental data sets for 2-MTHF including ignition delay time measurements in two different combustion reactors, i.e. rapid compression machine and high-pressure shock tube, are presented. Measurements for 2-MTHF/oxidizer/diluent mixtures were performed in the temperature range of 639-1413 K, at pressures of 10, 20, and 40 bar, and at three different equivalence ratios of 0.5, 1.0, and 2.0. A detailed chemical kinetic model describing both low-and high-temperature chemistry of 2-MTHF was developed and validated against new ignition delay measurements and already existing flame species profiles and ignition delay measurements. The mechanism provides satisfactory agreement with the experimental data. For identifying key reactions at various combustion conditions and to attain a better understanding of the combustion behavior, reaction path and sensitivity analyses were performed. (C) 2016 by The Combustion Institute. Published by Elsevier Inc.
This work was performed as part of the Cluster of Excellence “Tailor-Made fuels from Biomass”, which is funded by the Excellence Initiative by the German federal and state governments to promote science and research at German universities. The work performed by the Clean Combustion Research Center was supported by competitive research funding from King Abdullah University of Science and Technology (KAUST). The work at NUI Galway was kindly supported by Saudi Aramco under the FUELCOM program.
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<pubDate>Mon, 10 Oct 2016 00:00:00 GMT</pubDate>
<guid isPermaLink="false">http://hdl.handle.net/10379/6900</guid>
<dc:date>2016-10-10T00:00:00Z</dc:date>
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<title>An RCM experimental and modeling study on CH4 and CH4/C2H6 oxidation at pressures up to 160 bar</title>
<link>http://hdl.handle.net/10379/6899</link>
<description>An RCM experimental and modeling study on CH4 and CH4/C2H6 oxidation at pressures up to 160 bar
Ramalingam, Ajoy; Zhang, Kuiwen; Dhongde, Avnish; Virnich, Lukas; Sankhla, Harsh; Curran, Henry J.; Heufer, Alexander
The oxidation of CH4 and CH4/C2H6 mixtures were studied at pressures relevant to knocking in large bore natural gas engines. The experiments were carried out in a rapid compression machine (RCM) at end of compression (EOC) temperatures ranging between 885 and 940 K at compressed gas pressures of 105, 125, 150, and 160 bar at varying equivalence ratios (0.417, 0.526, and 1.0) and dilution percentages (0, 10, and 30% Exhaust Gas Recirculation - EGR) that were defined in a test matrix. This study describes the method and limitations of performing high-pressure experiments of this magnitude in an RCM, modeling, and validation of the kinetic mechanism against experimental data. While the recently published AramcoMech 2.0 could well predict the ignition delay times (IDTs) for CH4 within the uncertainty ranges at comparatively higher pressures and lower temperatures (885-940 K), the predicted reactivity is, in general, lower than that of AramcoMech 1.3 as shown in our previous screening study. Based on the comparison between both mechanisms as well as sensitivity analysis on the predicted IDTs, the reaction rate constant for (H) over dot-atom abstraction from CH4 by H(O) over dot(2) radical was optimized in order to achieve better agreement with the new data while maintaining the agreement to the previous data sets. The modified mechanism predicts well the IDTs and the trend of their variation caused by the change in pressure, equivalence ratio, dilution percentage, and mixture variation with C2H6. (C) 2017 Elsevier Ltd. All rights reserved.
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<pubDate>Tue, 13 Jun 2017 00:00:00 GMT</pubDate>
<guid isPermaLink="false">http://hdl.handle.net/10379/6899</guid>
<dc:date>2017-06-13T00:00:00Z</dc:date>
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<title>Simplified approach to the prediction and analysis of temperature inhomogeneity in rapid compression machines</title>
<link>http://hdl.handle.net/10379/6882</link>
<description>Simplified approach to the prediction and analysis of temperature inhomogeneity in rapid compression machines
Yousefian, Sajjad; Gauthier, François; Morán-Guerrero, Amadeo; Richardson, Robert R.; Curran, Henry J.; Quinlan, Nathan J.; Monaghan, Rory F.D.
Substantial progress has been made in understanding and reducing temperature inhomogeneity in rapid compression machines (RCMs) with the help of computational modeling. To date, however, it has not been possible to investigate and map the full range of possible RCM designs, working gases, and, operating conditions. In this work,, we present a framework which simplifies the task of comprehensive and general RCM performance prediction. A set of thermophysical and geometrical parameters has been defined to characterize the design and operating conditions of a general RCM. Dimensional analysis was applied to reduce the number of variables, and a sensitivity analysis, based on computational simulations, was used to rank the dimensionless parameters and eliminate unimportant-ones. The results of this analysis show that Reynolds number,, Prandtl number, aspect ratio,: and crevice volume ratio are the most important parameters determining temperature inhomogeneity. A further set of computational simulations was conducted to predict postcompression temperature inhomogeneity over the full range of RCM design and operating parameters. These results are well-represented by a simple power-law equation that correlates a dimensionless temperature inhomogenity parameter (mass-averaged over the main chamber) as a function of postcompression time with just three parameters-Peclet number (the product of Reynolds and, Prandtl numbers), aspect ratio, and crevice volume ratio. This equation-can serve as a simple and general tool for RCM designers and users who wish to determine optimal configurations that minimize temperature inhomogeneity for combustion experiments.
</description>
<pubDate>Tue, 03 Nov 2015 00:00:00 GMT</pubDate>
<guid isPermaLink="false">http://hdl.handle.net/10379/6882</guid>
<dc:date>2015-11-03T00:00:00Z</dc:date>
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<title>Assessing the predictions of a NOx kinetic mechanism on recent hydrogen and syngas experimental data</title>
<link>http://hdl.handle.net/10379/6874</link>
<description>Assessing the predictions of a NOx kinetic mechanism on recent hydrogen and syngas experimental data
Zhang, Yingjia; Mathieu, Olivier; Petersen, Eric L.; Bourque, Gilles; Curran, Henry J.
A detailed chemical kinetic mechanism has been developed to describe the pyrolysis and oxidation of the hydrogen/NOx and syngas/NOx systems. The thermodynamic data of nitrogenous compounds have been updated based on the study of Bugler et al. (2016). The rate constants of individual elementary reactions associated with the Zeldovich mechanism, the N/O sub-mechanism (NO2, N2O and NO3), the H/N/O sub mechanism (HNO/HON, HNO2/HONO and HONO2) and the NH3 mechanism (NNH and NH2OH) have been selected through a synthetic comparison of the data available in the literature and the adoption of the latest available published rate constant data. The proposed mechanism has been validated against a large number of experimental data including pyrolysis histories, ignition delay time data, species profile versus time and temperature and flame speed measurements over a wide range of initial combustion conditions and various experimental devices including shock tubes, flow reactors, jet-stirred reactors and spherical combustion bombs.The simulations of the proposed model have also been compared to those from five recently published kinetic models available in the literature. It was found that although these mechanisms generally reproduced well the data for which they were validated, they did not globally capture the combustion characteristics of all of the hydrogen/NOx and syngas/NOx systems.Finally, the proposed model has been used to simulate the formation of NO at practical gas-turbine relevant conditions. A detailed flux analysis has been performed to kinetically explore the NO formation mechanism under various combustion conditions. (C) 2017 The Combustion Institute. Published by Elsevier Inc. All rights reserved.
</description>
<pubDate>Tue, 02 May 2017 00:00:00 GMT</pubDate>
<guid isPermaLink="false">http://hdl.handle.net/10379/6874</guid>
<dc:date>2017-05-02T00:00:00Z</dc:date>
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