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An Aromatics and cC_5H_(5-8) Model with Improved Transport for Flat Flames, Flow Reactors and Shock Tubes

机译:具有改进的扁平火焰,流量反应器和冲击管的运输工具的芳烃和CC_5H_(5-8)模型

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Presenting improvements to a detailed, quantitative, 1-dimensional, kinetic, aromatics and cC_5H_(5-8) submodel with thermodynamics and transport. The model, with ~250 species and ~2000 reactions, includes a full NO_x chemistry sub-model. Transport parameters: ε, σ and α are all determined by empirical or experimental data. Most μ values are given by experimental values for the parent compounds and empirically for their radicals. Z_(rot) has been set to 1 or experimental values. Shock tube conditions are explored. Flow reactor and flat flame results are updated. Selected experiments on toluene, benzene, cyclopentene (CPE) and cyclopentadiene are examined. A new method is implemented to avoid arbitrarily time-shifting the modeling data to match the fuel concentration at 50% consumption. Instead, the method of least squares fits the experimental data to a 1st-3rd order polynomial. The least squares value is compared against the modeling calculations and a root-mean squared (RMS) goodness of fit (GoF) is calculated. The time shift is then determined numerically to the millisecond by minimizing the GoF. Similarly when tuning the model using the concentrations of 1,3-cyclopentadiene (CPD) Indene, Benzene or sums of C_4 and C_3 species a GoF is used to iteratively determine the best rate constants. With this latest version of the model it is no longer necessary to tune rate constants for naphthalene, 1,2-dihydronaphthalene or 1-phenyl-1,3-butadiene. The model is compared to the experimental oxidation of CPD in an atmospheric pressure flow reactor and a shock tube. Side products for two reactions have been changed from 2H to H_2 to avoid early and unrealistic chain branching: 2 cC_5H_6 → 1,2 dihydronaphthalene + H_2 and 2 cC_5H_6 → 1-phenyl-1,3-butadiene + H_2. The main naphthalene formation route is now 2 cC_5H_5 → C_(10)H_8 + H_2 with k=10~(11)×e~(-34000/(8.314×T)) cm~3 mol~(-1)s~1. Other changes in derived rates are discussed.
机译:提高详细,定量,1维,动力学,芳烃和CC_5H_(5-8)子模型,具有热力学和运输。该模型,具有〜250种和2000个反应,包括全NO_X化学子模型。传输参数:ε,σ和α全部由经验或实验数据确定。大多数μ值由母体化合物的实验值和凭经验赋予它们的自由基给出。 Z_(腐烂)已设置为1或实验值。探索冲击管条件。流动反应器和扁平火焰结果已更新。检查了甲苯,苯,环戊烯(CPE)和环戊二烯的选定实验。实现了一种新方法,以避免任意时转移建模数据以将燃料浓度与50%的消耗相匹配。相反,最小二乘法将实验数据拟合到第一-3级多项式的实验数据。将最小二乘值与建模计算进行比较,并计算拟合(GOF)的根均方平方(RMS)良好。然后,通过最小化GOF来数值方式向毫秒确定时移。类似地,当使用1,3-环戊二烯(CPD)茚的浓度调节模型时,使用C_4和C_3物种的苯或GOF的总和来迭代地确定最佳速率常数。利用这种最新版本的模型,不再需要抑制萘,1,2-二氢萘或1-苯基-1,3-丁二烯的常数。将模型与大气压流量反应器和冲击管中CPD的实验氧化进行比较。两种反应的侧面产品已从2h转变为2小时,以避免早期和不切实际的链支化:2 Cc_5H_6→1,2二氢萘+ H_2和2 CC_5H_6→1-苯基-1,3-丁二烯+ H_2。主萘形成途径现在是2 CC_5H_5→C_(10)H_8 + H_2,K = 10〜(11)×e〜(-34000 /(8.314×t))cm〜3 mol〜(-1)s〜1 。讨论了衍生率的其他变化。

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