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Structure-reactivity correlations for reactions between H/D atoms with selected ethers: Reaction-rate coefficients from direct shock-tube measurements and transition-state theory H/D 原子与特定醚发生反应的结构-反应相关性:直接冲击管测量和过渡态理论得出的反应速率系数
IF 5.8 2区 工程技术 Q2 ENERGY & FUELS Pub Date : 2024-09-19 DOI: 10.1016/j.combustflame.2024.113689

Shock-tube experiments at elevated pressures between 2.0 and 2.7 bar were carried out to study H-atom abstractions between D atoms and selected ether compounds: dimethyl ether (DME), diethyl ether (DEE), dimethoxymethane (DMM), and methyl propyl ether (MPE). D-atom resonance absorption spectrometry (D-ARAS) behind reflected shock waves was used to monitor the consumption of D atoms. To study the bimolecular reactions between D atoms and the specific ether, gas mixtures of the selected ether compound and C2D5I diluted in argon (bath gas) were prepared; C2D5I was used as a precursor for D atoms. This innovative approach using Dual ARAS (D-ARAS and H-ARAS) allows the distinct detection of precursor decay followed by H-atom abstraction reactions and ether decay followed by H-atom release. For the study of the reaction D + DME → HD + products, the experiments covered a temperature range of 940–1050 K; for the reaction D + DEE → HD + products, the temperature range was 980–1260 K; for the reaction D + DMM → HD + products, the temperature range was 930–1300 K; and for the reaction D + MPE → HD + products, the temperature spans a range of 1000–1350 K. Experimentally determined rate coefficients have been expressed by the following Arrhenius equations:

ktotal(D+DME)(T) = 1.9×10−10 exp (−31.4 kJ/mol / RT) cm3s−1,

ktotal(D+DEE)(T) = 1.7×10−10 exp (−22.4 kJ/mol / RT) cm3s−1,

ktotal(D+DMM)(T) = 2.7×10−10 exp (−27.3 kJ/mol / RT) cm3s−1,

and ktotal(D+MPE)(T) = 5.1×10−10 exp (−31.5 kJ/mol / RT) cm3s−1.

The experimental results show an uncertainty of ±30 % and were supplemented by transition-state theory (TST) calculations based on molecular properties and energies from computations at the G4 level of theory. TST computations were conducted for H-atom abstraction from various types of primary and secondary carbon bonds. Bond-specific reaction rate-coefficient expressions were derived from theory and compared with experimental results to establish correlations between molecular structure and reactivity.

在 2.0 至 2.7 巴的高压下进行了冲击管实验,以研究 D 原子与选定的醚化合物(二甲醚 (DME)、二乙醚 (DEE)、二甲氧基甲烷 (DMM) 和甲基丙基醚 (MPE))之间的 H 原子抽取。利用反射冲击波背后的 D 原子共振吸收光谱(D-ARAS)来监测 D 原子的消耗。为了研究 D 原子和特定醚之间的双分子反应,制备了选定醚化合物和在氩气(浴气)中稀释的 C2D5I 的气体混合物;C2D5I 被用作 D 原子的前体。这种使用双原子吸收光谱分析仪(D-ARAS 和 H-ARAS)的创新方法可以对前体衰变后的 H 原子抽取反应和醚衰变后的 H 原子释放反应进行不同的检测。在研究 D + DME → HD + 产物反应时,实验温度范围为 940-1050 K;在研究 D + DEE → HD + 产物反应时,温度范围为 980-1260 K;在研究 D + DMM → HD + 产物反应时,温度范围为 930-1300 K;在研究 D + MPE → HD + 产物反应时,温度范围为 1000-1350 K。实验测定的速率系数用以下阿伦尼乌斯方程表示:ktotal(D+DME)(T) = 1.9×10-10 exp (-31.4 kJ/mol / RT) cm3s-1,ktotal(D+DEE)(T) = 1.7×10-10 exp (-22.4 kJ/mol / RT) cm3s-1,ktotal(D+DMM)(T) = 2.7×10-10 exp (-27.3 kJ/mol / RT) cm3s-1,以及 ktotal(D+MPE)(T) = 5.1×10-10 exp (-31. 5 kJ/mol / RT) cm3s-1。实验结果的不确定性为 ±30 %,并根据 G4 理论水平计算得出的分子性质和能量,通过过渡态理论 (TST) 计算进行了补充。TST 计算针对从各种类型的一级和二级碳键中抽离 H 原子。根据理论推导出了特定键的反应速率系数表达式,并与实验结果进行了比较,从而建立了分子结构与反应性之间的相关性。
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引用次数: 0
O2-Dependence of reactions of 1,2-dimethoxyethanyl and 1,2-dimethoxyethanylperoxy isomers 1,2-Dimethoxyethanyl 和 1,2-Dimethoxyethanylperoxy 异构体反应的 O2 依赖性
IF 5.8 2区 工程技术 Q2 ENERGY & FUELS Pub Date : 2024-09-19 DOI: 10.1016/j.combustflame.2024.113694
<div><p>Reaction mechanisms of <span><math><mover><mi>R</mi><mo>˙</mo></mover></math></span> and RO<span><math><mover><mi>O</mi><mo>˙</mo></mover></math></span> radicals derived from low-temperature oxidation of 1,2-dimethoxyethane (CH<sub>3</sub>O(CH<sub>2</sub>)<sub>2</sub>OCH<sub>3</sub>) were investigated using speciation from multiplexed photoionization mass spectrometry (MPIMS) measurements via Cl-initiated oxidation, in conjunction with electronic structure calculations. The experiments were conducted at 5 bar, from 450 K – 650 K, and O<sub>2</sub> concentrations from 1 · 10<sup>14</sup> cm<sup>–3</sup> – 6 · 10<sup>18</sup> cm<sup>–3</sup> to probe the effects on competing reaction channels of 1,2-dimethoxyethanyl (<span><math><mover><mi>R</mi><mo>˙</mo></mover></math></span>) and 1,2-dimethoxyethanylperoxy (RO<span><math><mover><mi>O</mi><mo>˙</mo></mover></math></span>) isomers. Several species were detected with photoionization spectral fitting – ethene, formaldehyde, methyl vinyl ether, and 2-methoxyacetaldehyde – and, as determined by electronic structure calculations, may form via unimolecular decomposition of 1,2-dimethoxyethanyl or 1,2-dimethoxyethanylperoxy. O<sub>2</sub>-dependent yield ratios show that the formation pathways for all species undergo a competition between O<sub>2</sub>-addition and unimolecular decomposition. Adiabatic ionization energies were also calculated and utilized along with exact mass determinations to infer contributions for other species derived exclusively from first- and second-O<sub>2</sub>-addition, including 1,2-dimethoxyethene, cyclic ethers, and dicarbonyls.</p><p>In addition to species formed from conventional low-temperature oxidation pathways, an important conclusion is derived from the detection of species produced from an O<sub>2</sub>-addition step involving ĊH<sub>2</sub>CH<sub>2</sub>OCH<sub>3</sub> (<span><math><mrow><mover><mi>R</mi><mo>˙</mo></mover><msup><mrow></mrow><mo>′</mo></msup></mrow></math></span>), which forms via prompt dissociation of the primary 1,2-dimethoxyethanyl radical (ĊH<sub>2</sub>O(CH<sub>2</sub>)<sub>2</sub>OCH<sub>3</sub>). Species derived from <span><math><mrow><mover><mi>R</mi><mo>˙</mo></mover><msup><mrow></mrow><mo>′</mo></msup></mrow></math></span> + O<sub>2</sub> – 1,3-dioxolane and methyl acetate – were detected at [O<sub>2</sub>] = 1.2 · 10<sup>17</sup> cm<sup>–3</sup> and formed on timescales parallel to the main <span><math><mover><mi>R</mi><mo>˙</mo></mover></math></span> + O<sub>2</sub> reactions. In addition, ion signal at <em>m/z</em> 106 was detected and increased with O<sub>2</sub> concentration from which connections are drawn to ketohydroperoxides produced by <span><math><mrow><mover><mi>Q</mi><mo>˙</mo></mover><msup><mrow></mrow><mo>′</mo></msup></mrow></math></span>OOH + O<sub>2</sub>. Detection of such species indicate that <em>β</em>-scission of 1,2-dimethoxyethanyl is sufficiently facile such that timescales of <span><math><mrow><mover><m
通过 Cl 引发的氧化作用,利用多路复用光离子化质谱(MPIMS)测量得到的标样,结合电子结构计算,研究了 1,2 二甲基乙烷(CH3O(CH2)2OCH3)低温氧化产生的 R˙和 ROO˙自由基的反应机理。实验在 5 巴、450 K - 650 K 和氧气浓度为 1 - 1014 cm-3 - 6 - 1018 cm-3 的条件下进行,以探究 1,2 二甲基乙氧基乙烷(R˙)和 1,2 二甲基乙氧基乙酰过氧(ROO˙)异构体对竞争反应通道的影响。通过光离子化光谱拟合检测到了几种物质--乙烯、甲醛、甲基乙烯基醚和 2-甲氧基乙醛,根据电子结构计算确定,这些物质可能是通过 1,2-二甲氧基乙烷或 1,2-二甲氧基乙酰过氧的单分子分解形成的。与 O2 有关的产率表明,所有物种的形成途径都经历了 O2 加成和单分子分解之间的竞争。此外,还计算了绝热电离能,并利用精确的质量测定来推断完全由第一和第二 O2-加成产生的其他物种的贡献,包括 1,2-二甲氧基乙烯、环醚和二羰基。除了传统的低温氧化途径形成的物种外,通过检测涉及ĊH2CH2OCH3 (R˙′)的 O2-加成步骤产生的物种也得出了一个重要结论,该步骤是通过迅速解离初级 1,2-二甲氧基乙烷基(ĊH2O(CH2)2OCH3)形成的。在[O2] = 1.2 - 1017 cm-3 时检测到了来自 R˙′ + O2 的物种--1,3-二氧戊环和醋酸甲酯,其形成的时间尺度与主要的 R˙ + O2 反应平行。此外,还检测到 m/z 106 处的离子信号,该信号随 O2 浓度的增加而增加。这些物种的检测表明,1,2-二甲氧基乙烷的β-裂解非常容易,因此 R˙′ + O2 的时间尺度可与传统的 R˙ + O2 途径相竞争。
{"title":"O2-Dependence of reactions of 1,2-dimethoxyethanyl and 1,2-dimethoxyethanylperoxy isomers","authors":"","doi":"10.1016/j.combustflame.2024.113694","DOIUrl":"10.1016/j.combustflame.2024.113694","url":null,"abstract":"&lt;div&gt;&lt;p&gt;Reaction mechanisms of &lt;span&gt;&lt;math&gt;&lt;mover&gt;&lt;mi&gt;R&lt;/mi&gt;&lt;mo&gt;˙&lt;/mo&gt;&lt;/mover&gt;&lt;/math&gt;&lt;/span&gt; and RO&lt;span&gt;&lt;math&gt;&lt;mover&gt;&lt;mi&gt;O&lt;/mi&gt;&lt;mo&gt;˙&lt;/mo&gt;&lt;/mover&gt;&lt;/math&gt;&lt;/span&gt; radicals derived from low-temperature oxidation of 1,2-dimethoxyethane (CH&lt;sub&gt;3&lt;/sub&gt;O(CH&lt;sub&gt;2&lt;/sub&gt;)&lt;sub&gt;2&lt;/sub&gt;OCH&lt;sub&gt;3&lt;/sub&gt;) were investigated using speciation from multiplexed photoionization mass spectrometry (MPIMS) measurements via Cl-initiated oxidation, in conjunction with electronic structure calculations. The experiments were conducted at 5 bar, from 450 K – 650 K, and O&lt;sub&gt;2&lt;/sub&gt; concentrations from 1 · 10&lt;sup&gt;14&lt;/sup&gt; cm&lt;sup&gt;–3&lt;/sup&gt; – 6 · 10&lt;sup&gt;18&lt;/sup&gt; cm&lt;sup&gt;–3&lt;/sup&gt; to probe the effects on competing reaction channels of 1,2-dimethoxyethanyl (&lt;span&gt;&lt;math&gt;&lt;mover&gt;&lt;mi&gt;R&lt;/mi&gt;&lt;mo&gt;˙&lt;/mo&gt;&lt;/mover&gt;&lt;/math&gt;&lt;/span&gt;) and 1,2-dimethoxyethanylperoxy (RO&lt;span&gt;&lt;math&gt;&lt;mover&gt;&lt;mi&gt;O&lt;/mi&gt;&lt;mo&gt;˙&lt;/mo&gt;&lt;/mover&gt;&lt;/math&gt;&lt;/span&gt;) isomers. Several species were detected with photoionization spectral fitting – ethene, formaldehyde, methyl vinyl ether, and 2-methoxyacetaldehyde – and, as determined by electronic structure calculations, may form via unimolecular decomposition of 1,2-dimethoxyethanyl or 1,2-dimethoxyethanylperoxy. O&lt;sub&gt;2&lt;/sub&gt;-dependent yield ratios show that the formation pathways for all species undergo a competition between O&lt;sub&gt;2&lt;/sub&gt;-addition and unimolecular decomposition. Adiabatic ionization energies were also calculated and utilized along with exact mass determinations to infer contributions for other species derived exclusively from first- and second-O&lt;sub&gt;2&lt;/sub&gt;-addition, including 1,2-dimethoxyethene, cyclic ethers, and dicarbonyls.&lt;/p&gt;&lt;p&gt;In addition to species formed from conventional low-temperature oxidation pathways, an important conclusion is derived from the detection of species produced from an O&lt;sub&gt;2&lt;/sub&gt;-addition step involving ĊH&lt;sub&gt;2&lt;/sub&gt;CH&lt;sub&gt;2&lt;/sub&gt;OCH&lt;sub&gt;3&lt;/sub&gt; (&lt;span&gt;&lt;math&gt;&lt;mrow&gt;&lt;mover&gt;&lt;mi&gt;R&lt;/mi&gt;&lt;mo&gt;˙&lt;/mo&gt;&lt;/mover&gt;&lt;msup&gt;&lt;mrow&gt;&lt;/mrow&gt;&lt;mo&gt;′&lt;/mo&gt;&lt;/msup&gt;&lt;/mrow&gt;&lt;/math&gt;&lt;/span&gt;), which forms via prompt dissociation of the primary 1,2-dimethoxyethanyl radical (ĊH&lt;sub&gt;2&lt;/sub&gt;O(CH&lt;sub&gt;2&lt;/sub&gt;)&lt;sub&gt;2&lt;/sub&gt;OCH&lt;sub&gt;3&lt;/sub&gt;). Species derived from &lt;span&gt;&lt;math&gt;&lt;mrow&gt;&lt;mover&gt;&lt;mi&gt;R&lt;/mi&gt;&lt;mo&gt;˙&lt;/mo&gt;&lt;/mover&gt;&lt;msup&gt;&lt;mrow&gt;&lt;/mrow&gt;&lt;mo&gt;′&lt;/mo&gt;&lt;/msup&gt;&lt;/mrow&gt;&lt;/math&gt;&lt;/span&gt; + O&lt;sub&gt;2&lt;/sub&gt; – 1,3-dioxolane and methyl acetate – were detected at [O&lt;sub&gt;2&lt;/sub&gt;] = 1.2 · 10&lt;sup&gt;17&lt;/sup&gt; cm&lt;sup&gt;–3&lt;/sup&gt; and formed on timescales parallel to the main &lt;span&gt;&lt;math&gt;&lt;mover&gt;&lt;mi&gt;R&lt;/mi&gt;&lt;mo&gt;˙&lt;/mo&gt;&lt;/mover&gt;&lt;/math&gt;&lt;/span&gt; + O&lt;sub&gt;2&lt;/sub&gt; reactions. In addition, ion signal at &lt;em&gt;m/z&lt;/em&gt; 106 was detected and increased with O&lt;sub&gt;2&lt;/sub&gt; concentration from which connections are drawn to ketohydroperoxides produced by &lt;span&gt;&lt;math&gt;&lt;mrow&gt;&lt;mover&gt;&lt;mi&gt;Q&lt;/mi&gt;&lt;mo&gt;˙&lt;/mo&gt;&lt;/mover&gt;&lt;msup&gt;&lt;mrow&gt;&lt;/mrow&gt;&lt;mo&gt;′&lt;/mo&gt;&lt;/msup&gt;&lt;/mrow&gt;&lt;/math&gt;&lt;/span&gt;OOH + O&lt;sub&gt;2&lt;/sub&gt;. Detection of such species indicate that &lt;em&gt;β&lt;/em&gt;-scission of 1,2-dimethoxyethanyl is sufficiently facile such that timescales of &lt;span&gt;&lt;math&gt;&lt;mrow&gt;&lt;mover&gt;&lt;m","PeriodicalId":280,"journal":{"name":"Combustion and Flame","volume":null,"pages":null},"PeriodicalIF":5.8,"publicationDate":"2024-09-19","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"142242880","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":2,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
引用次数: 0
Temperature of burning iron microparticles with in-situ resolved initial sizes 原位解析初始尺寸的铁微颗粒燃烧温度
IF 5.8 2区 工程技术 Q2 ENERGY & FUELS Pub Date : 2024-09-19 DOI: 10.1016/j.combustflame.2024.113737
<div><p>Simultaneous, <em>in-situ</em>, optical diagnostics are performed to measure initial diameters and the temporal temperature evolution of iron microparticles burning in hot laminar oxidizing atmospheres with 10–30<!--> <!-->vol% O<span><math><msub><mrow></mrow><mrow><mn>2</mn></mrow></msub></math></span>. The pre-ignition particle diameter and temperature evolution during combustion are monitored using synchronized high-speed diffuse backlight-illumination and two-color pyrometry techniques, respectively. Average temperature histories are obtained for particles sorted into three size fractions centered at 40, 45, and 50<!--> <!--> <span><math><mi>μ</mi></math></span>m with a span of 5<!--> <!--> <span><math><mi>μ</mi></math></span>m. Increasing the oxygen level from 10 to 30<!--> <!-->vol%, particles burn faster and reach a higher peak temperature that increases approximately from 2400 to 3200<!--> <!-->K. From their temperature trajectories, the peak temperatures of individual particles are extracted and correlated with their initial diameters. It is observed that the maximum particle temperature decreases with the increasing particle diameter, attributed to the enlarged radiative and evaporative heat losses relative to the chemical heat release of the larger particles that burn in the diffusion-limited regime. In addition, the size dependence of the maximum particle temperature enhances considerably when the particle peak temperature increases from approximately <span><math><mrow><mn>2400</mn><mspace></mspace></mrow></math></span>K to around <span><math><mrow><mn>2800</mn><mspace></mspace></mrow></math></span>K, but its further variation is small as the particle peak temperature continues approaching the boiling point of the particles. This observation does not align with previous non-size-resolved measurements that have lower temporal resolutions and wider particle size distributions. Possible reasons for this inconsistency are discussed. A theoretical analysis is performed to quantitatively reveal the role of surface radiation and evaporation in the size dependence of the particle peak temperature. The results suggest that at relatively low particle temperatures the size dependence is determined mainly by radiation and that the effect of evaporation becomes more dominant at higher particle temperatures. Moreover, with increasing particle temperature, radiation strengthens the size dependence of the particle peak temperature. On the contrary, evaporation weakens the size dependence at higher temperatures because of the increasing sensitivity of vapor pressure (evaporative heat loss) to the temperature according to Clausius–Clapeyron relation.</p><p><strong>Novelty and significance statement</strong></p><p>This work presents, for the first time, the simultaneous, <em>in-situ</em> measurements of the initial sizes and time-resolved temperatures of micrometer-sized iron particles burning at elevated gas temperatures. Using current size-res
在 10-30 Vol% O2 的热层流氧化气氛中燃烧的铁微粒的初始直径和时间温度演变进行了同步的原位光学诊断测量。点火前的颗粒直径和燃烧过程中的温度变化分别采用同步高速漫反射照明技术和双色高温计技术进行监测。获得了以 40、45 和 50 μm 为中心、跨度为 5 μm 的三个粒度分级的颗粒的平均温度历史记录。将氧气含量从 10% 增加到 30%,颗粒的燃烧速度更快,达到的峰值温度也更高,大约从 2400 K 增加到 3200 K。据观察,颗粒的最高温度随着颗粒直径的增大而降低,这是由于相对于在扩散受限状态下燃烧的较大颗粒的化学热释放,辐射和蒸发热损失增大所致。此外,当颗粒峰值温度从 2400K 左右升高到 2800K 左右时,最大颗粒温度的大小依赖性显著增强,但当颗粒峰值温度继续接近颗粒的沸点时,其进一步变化很小。这一观察结果与以往时间分辨率较低、粒度分布较广的非粒度分辨测量结果不一致。本文讨论了造成这种不一致的可能原因。进行了理论分析,以定量揭示表面辐射和蒸发在颗粒峰值温度的尺寸依赖性中的作用。结果表明,在相对较低的颗粒温度下,粒度相关性主要由辐射决定,而在较高的颗粒温度下,蒸发的影响变得更加主要。此外,随着颗粒温度的升高,辐射加强了颗粒峰值温度的尺寸依赖性。与此相反,根据克劳修斯-克拉皮戎关系,蒸发会减弱在较高温度下的粒度依赖性,因为蒸气压力(蒸发热损失)对温度的敏感性不断增加。利用当前的尺寸分辨测量方法,可以统计出若干直径颗粒的温度演变过程,并显著提高了精确度。这个在广泛操作条件下的高保真实验数据库对于铁燃料界验证和改进铁颗粒燃烧的数值模型非常有参考价值。由于实验设计新颖,在这项工作中观察到了孤立燃烧的铁颗粒的初始直径和最高温度之间的负相关关系,并对其进行了理论解释。这一结果与以往时间分辨率较低、粒度分布较广的非粒度分辨测量结果并不一致。
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引用次数: 0
Low-temperature reactivity, extinction, and heat release rate of non-premixed cool flame at elevated pressures 高压下非预混冷焰的低温反应性、熄灭和热释放率
IF 5.8 2区 工程技术 Q2 ENERGY & FUELS Pub Date : 2024-09-19 DOI: 10.1016/j.combustflame.2024.113727

Understanding the fundamental characteristics of high-pressure cool flames is crucial for the development of advanced and efficient low-temperature combustion engine technologies. The pressure dependency of multi-oxygen addition branching reactions in low-temperature chemistry significantly influences the dynamics, structure, and reactivity of cool flame. This study investigates the non-premixed cool flame of diethyl ether (DEE) at elevated pressures. The results show that pressure rise promotes low-temperature chemistry and significantly extends the extinction limit of cool flame. It is found that the cool flame heat release rate is correlated with the product of pressure and the square root of the pressure-weighted strain rate, QaP·P, which is different from that of hot flames, QaP. The radical index concept for atmospheric cool flames is extended to high-pressure cool flames allowing to decouple the mass and thermal transports from the chemical kinetics term to evaluate the fuel reactivity at elevated pressures. The radical index shows that the low-temperature reactivity of DEE is enhanced with the pressure and is higher than n-dodecane by a factor of 19, 18.3, and 16.4 for 1, 3, and 5 atm, respectively. Kinetic analysis reveals that pressure rise results in QOOH stabilization and promotions of the second O2 addition and the chain-branching reaction pathway for multiple OH radical productions.

了解高压冷焰的基本特征对于开发先进高效的低温燃烧发动机技术至关重要。低温化学中多氧添加支化反应的压力依赖性极大地影响了冷却火焰的动力学、结构和反应性。本研究调查了二乙醚(DEE)在高压下的非预混合冷焰。结果表明,压力升高会促进低温化学反应,并显著延长冷焰的熄灭极限。研究发现,冷焰放热速率与压力和压力加权应变速率平方根的乘积 Q∼aP-P 相关,这与热焰的 Q∼aP 不同。大气冷却火焰的激进指数概念被扩展到高压冷却火焰,从而将质量和热运输与化学动力学项相分离,以评估高压下的燃料反应性。自由基指数显示,二乙二醇的低温反应性随压力升高而增强,在 1、3 和 5 个大气压下分别比正十二烷高 19、18.3 和 16.4 倍。动力学分析表明,压力升高会导致 QOOH 稳定化,并促进第二次 O2 加成和多个 OH 自由基生成的链分支反应途径。
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引用次数: 0
Experimental and kinetic modeling study of RP-3 kerosene: Development of a four-component surrogate for enhanced prediction of aromatic intermediates RP-3 煤油的实验和动力学模型研究:开发四组分替代物以加强对芳烃中间体的预测
IF 5.8 2区 工程技术 Q2 ENERGY & FUELS Pub Date : 2024-09-19 DOI: 10.1016/j.combustflame.2024.113736

RP-3 kerosene is currently the primary jet fuel used in China. However, limited attention has been paid to development of surrogate models that can predict formations of aromatics during RP-3 oxidation in a detailed way, such as by species mole fraction profiles. The present study aims to enrich the experimental database by measuring species mole fraction profiles, particularly focusing on aromatic intermediates, and propose a new surrogate model with a detailed kinetic model to enhance predictive accuracy for these intermediates. Oxidation experiments of real RP-3 kerosene were conducted using an atmospheric flow reactor at temperatures ranging from 800 to 1150 K and equivalence ratios of 0.5 and 2.0. The mole fraction profiles of species including oxygen, major products, important small molecular intermediates and several primary aromatic intermediates were measured using online gas chromatography (GC) and gas chromatography-mass spectrometry (GC–MS). Based on the chemical composition and fundamental physical properties of RP-3 kerosene, a surrogate consisting of 55.0 % n-undecane, 18.7 % trans-decalin, 19.8 % p-xylene and 6.5 % tetralin (by weight) was formulated. A detailed kinetic model of the surrogate was developed and validated against the measured data. Compared to the surrogate models proposed in the previous studies, the current model demonstrates superior predictive capabilities in forecasting the generation of major aromatic intermediates. According to the rate of production (ROP) analysis for the model, benzene generation is associated with three components: decalin, p-xylene and n-undecane. Decalin exhibits the highest contribution to benzene formation under both lean and rich conditions. Toluene predominantly originates from p-xylene, while indene and naphthalene are primarily produced by tetralin. These findings emphasize the significance of decalin as a representative bicyclic cycloalkane component and tetralin as a representative indane/tetralin component in establishing a surrogate for RP-3 fuel to enhance prediction of aromatic intermediates. Furthermore, validation through experimental data from the literature including species mole fraction profiles and ignition delay times confirms the broad applicability of this model.

RP-3 煤油是中国目前使用的主要航空燃料。然而,人们对开发能详细预测 RP-3 氧化过程中芳烃形成的代用模型(如物种摩尔分数剖面)的关注有限。本研究旨在通过测量物种摩尔分数剖面丰富实验数据库,特别是侧重于芳香族中间产物,并提出一种具有详细动力学模型的新替代模型,以提高对这些中间产物的预测准确性。在温度为 800 至 1150 K、当量比为 0.5 和 2.0 的条件下,使用大气流动反应器对实际 RP-3 煤油进行了氧化实验。使用在线气相色谱法(GC)和气相色谱-质谱法(GC-MS)测量了氧气、主要产物、重要的小分子中间产物和几种初级芳香族中间产物等物种的分子分数分布。根据 RP-3 煤油的化学成分和基本物理性质,配制了一种由 55.0 % 的正十一烷、18.7 % 的反式萘酚、19.8 % 的对二甲苯和 6.5 % 的四氢呋喃(按重量计)组成的代用品。建立了代用物的详细动力学模型,并根据测量数据进行了验证。与之前研究中提出的代用模型相比,目前的模型在预测主要芳香族中间体的生成方面表现出更强的预测能力。根据模型的生产率(ROP)分析,苯的生成与三个组分有关:癸醛、对二甲苯和正十一烷。在贫油和富油条件下,癸醛对苯的形成贡献最大。甲苯主要来源于对二甲苯,而茚和萘则主要由四氯化萘生成。这些发现强调了以癸醛为代表的双环环烷组分和以四氢呋喃为代表的茚/四氢萘组分在建立 RP-3 燃料替代物方面的重要意义,从而加强了对芳香族中间产物的预测。此外,通过文献中的实验数据(包括物种分子分数曲线和点火延迟时间)进行验证,证实了该模型的广泛适用性。
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引用次数: 0
Experimental and numerical study of soot formation in laminar n-butylcyclohexane and n-butylbenzene diffusion flames at elevated pressures 高压下正丁基环己烷和正丁基苯扩散层流火焰中烟尘形成的实验和数值研究
IF 5.8 2区 工程技术 Q2 ENERGY & FUELS Pub Date : 2024-09-17 DOI: 10.1016/j.combustflame.2024.113741

The soot formation characteristics of laminar nitrogen-diluted n-butylcyclohexane and n-butylbenzene diffusion flames were experimentally and numerically investigated at pressures from 2 to 7 bar. In the experiment, laser-induced incandescence (LII), time-resolved LII, and color-ratio pyrometry were used to measure soot volume fraction, soot particle diameter, and flame temperature. The results show that n-butylbenzene has a significantly higher soot propensity than n-butylcyclohexane. The soot growth and oxidation in both flames are enhanced with increasing pressure. The difference is that the promotion effect of pressure on the soot formation in the n-butylcyclohexane flame continues to weaken as the pressure increases, while this phenomenon does not occur in n-butylbenzene flames. Within the studied pressure range, the mean particle sizes (Dpmean) in n-butylcyclohexane and n-butylbenzene flames show a good linear relationship with pressure. The pressure dependence of Dpmean in n-butylbenzene flames is stronger than that of n-butylcyclohexane flames at pressures between 2 and 6 bar. The experiment and simulation results indicate that the enhancement of the promotion effect of pressure on the soot formation in the n-butylbenzene flame may be due to the combined effect of an increase in the soot surface reactivity and an increase in the number density of soot particles. The reaction pathway analysis suggests that the stepwise dehydrogenation reactions of cyclohexene are the main source of benzene formation in n-butylcyclohexane flames and pyrene is mainly formed via the reaction between indenyl and benzyl radicals in n-butylbenzene flames.

在 2 至 7 巴的压力下,对氮稀释的正丁基环己烷和正丁基苯扩散层流火焰的烟尘形成特性进行了实验和数值研究。实验中使用了激光诱导炽热(LII)、时间分辨 LII 和比色高温计来测量烟尘体积分数、烟尘颗粒直径和火焰温度。结果表明,正丁基苯的烟尘倾向明显高于正丁基环己烷。随着压力的增加,两种火焰中的烟尘增长和氧化作用都会增强。不同的是,压力对正丁基环己烷火焰中烟尘形成的促进作用会随着压力的增加而减弱,而这种现象在正丁基苯火焰中不会出现。在研究的压力范围内,正丁基环己烷和正丁基苯火焰中的平均粒径(Dpmean)与压力呈良好的线性关系。在 2 至 6 巴的压力范围内,正丁基苯火焰中 Dpmean 的压力依赖性要强于正丁基环己烷火焰。实验和模拟结果表明,压力对正丁基苯火焰中烟尘形成的促进作用的增强可能是由于烟尘表面反应活性增加和烟尘颗粒数量密度增加的共同作用。反应途径分析表明,在正丁基环己烷火焰中,环己烯的逐步脱氢反应是苯形成的主要来源,而在正丁基苯火焰中,芘主要是通过茚基和苄基自由基的反应形成的。
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引用次数: 0
Experimental and kinetic modeling studies on low-temperature oxidation of 1-decene in a jet-stirred reactor 喷射搅拌式反应器中 1-癸烯低温氧化的实验和动力学模型研究
IF 5.8 2区 工程技术 Q2 ENERGY & FUELS Pub Date : 2024-09-17 DOI: 10.1016/j.combustflame.2024.113720

Olefins are important components in gasoline fuels as well as essential intermediates in the combustion of carbon-based fuels and oxy-fuels. Therefore, it is essential to investigate the oxidation chemistry of olefins, especially of long-chain olefins, to gain a deeper insight into the combustion of these fuels. 1-Decene is an important industrial chemical product and is often regarded as one of the representatives of long-chain olefins. This work investigated the low-temperature oxidation of 1-decene in a jet-stirred reactor with atmospheric pressure, temperature range of 700 – 900 K and equivalence ratio of 1.0. Twelve main oxidation species were detected and measured, by gas chromatography-mass spectrometry, including carbon dioxide, ethylene, ethane, acrolein, 1,3-butadiene, 1-butene, 1-pentene and benzene, etc. Based on previous reports, a detailed low-temperature oxidation kinetic model of 1-decene was developed and validated against the experimental data and literature data. In the model of 1-decene, the rate of production analysis revealed that the majority of 1-decene was consumed by H-abstractions to generate the primary radicals and OH-addition reaction onto C(1) to generate 1-decanol-2-yl radical. Sensitivity analyses show that H2O2 (+ M) = OH + OH (+ M) was the most sensitive reaction to promote 1-decene consumption. The decomposition of hydrogen peroxide was the main source of the hydroxyl radical. Simulation results indicate that ignition delay time of 1-decene is higher than that of n-decane in the low-temperature at equivalence ratios of 0.5 – 2.0 and pressure of 20, 40 bar.

烯烃是汽油燃料的重要成分,也是碳基燃料和含氧燃料燃烧的重要中间体。因此,研究烯烃(尤其是长链烯烃)的氧化化学性质对于深入了解这些燃料的燃烧过程至关重要。1-Decene 是一种重要的工业化工产品,通常被视为长链烯烃的代表之一。这项研究考察了 1-癸烯在大气压、700-900 K 温度范围和 1.0 等效比的喷射搅拌反应器中的低温氧化过程。通过气相色谱-质谱法检测和测量了 12 种主要氧化物,包括二氧化碳、乙烯、乙烷、丙烯醛、1,3-丁二烯、1-丁烯、1-戊烯和苯等。在以往报告的基础上,建立了详细的 1-癸烯低温氧化动力学模型,并根据实验数据和文献数据进行了验证。在 1-癸烯模型中,生成速率分析表明,大部分 1-癸烯被 H-萃取消耗,生成一级自由基,并与 C(1) 发生羟基加成反应,生成 1-癸醇-2-基自由基。敏感性分析表明,H2O2 (+ M) = OH + OH (+ M) 是促进 1-癸烯消耗的最敏感反应。过氧化氢的分解是羟基自由基的主要来源。模拟结果表明,在当量比为 0.5 - 2.0、压力为 20 和 40 巴的低温条件下,1-癸烯的点火延迟时间比正癸烷的点火延迟时间长。
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引用次数: 0
Multi-stream FPV-LES modeling of ammonia/coal co-firing on a semi-industrial scale complex burner with pre-heated secondary, tertiary, and staged combustion air 在带有预热二次、三次和分段燃烧空气的半工业规模复合燃烧器上进行氨/煤联合燃烧的多流 FPV-LES 建模
IF 5.8 2区 工程技术 Q2 ENERGY & FUELS Pub Date : 2024-09-16 DOI: 10.1016/j.combustflame.2024.113729
<div><p>The study investigates ammonia/coal co-firing using a non-adiabatic multi-stream flamelet/progress variable (FPV) approach on a 760 kWth semi-industrial test furnace of Central Research Institute of Electric Power Industry (CRIEPI). The furnace features an advanced low NO<sub>x</sub> CI-α burner with preheated secondary, tertiary, and staged combustion air streams, closely resembling conditions in commercial-scale power plant burners. Two ammonia injection cases are investigated, one where ammonia is injected through the burner and the other where it is injected through a measurement port positioned 1.0 m downstream, both at a fixed ammonia co-firing ratio of 20 % based on LHV. To address varying oxidizer stream temperatures for primary, secondary, tertiary, and staged air streams, an additional dimension is introduced to the flamelet chemtable. The thermochemical space has seven dimensions, three for fuel mixture fractions (volatile matter, char off-gases, and ammonia), and dimensions for the mixture fraction variance, reaction progress variable, total enthalpy, and oxidizer temperature. The seven-dimensional non-adiabatic (7D-NA) FPV-LES model's accuracy is assessed by comparing its predictions with measured data as well as with previous modelling results that had certain limitations, such as six- dimensional non-adiabatic (6D-NA) FPV-LES model that ignored difference in oxidizer temperature and five-dimensional adiabatic (5D-AD) FPV-LES model that ignored both difference in oxidizer temperature and heat loss in flamelet chemtable. In both cases of ammonia injection, 7D NA-FPV-LES model improved over previous model's predictions by accurately capturing the burner exit flow field. It successfully identified trend between the two cases, predicting a slightly higher peak temperature near burner exit in case injecting ammonia through downstream due to development of stronger internal recirculation zone. Results showed peak NO notably higher and closer to burner when ammonia injected through downstream, consistent with measured data due to prevalence of NO reduction for ammonia injected through burner in proximity of burner.</p></div><div><h3>Novelty and significance statement</h3><p>The novelty of this research is that it introduces an approach that can be accurately applied to the FPV-LES modeling of actual commercial power plant burners with highly complex oxidizer streams at varying temperatures. This approach has been validated on the complex CI-α burner of the CRIEPI test furnace of semi-industrial scale, which has preheated secondary, tertiary, and staged air streams, resembling actual conditions encountered in commercial power plant burners. The proposed approach can consider multiple oxidizer streams and it can also consider variation in oxidizer composition (although oxidizer composition is fixed in this study). This research will be significant in adoption of multi-mixture fraction FPV-LES approach to complex burners of commercial
该研究在电力工业中央研究院(CRIEPI)的一台 760 kWth 半工业试验炉上采用非绝热多流火焰/进度变量(FPV)方法研究了氨/煤联合燃烧。该炉采用先进的低氮氧化物 CI-α 燃烧器,带有预热二次、三次和分段燃烧气流,与商业规模电厂燃烧器的条件非常相似。研究了两种氨气喷射情况,一种是通过燃烧器喷射氨气,另一种是通过位于下游 1.0 米处的测量端口喷射氨气,两种情况都是在基于 LHV 的 20% 固定氨气共燃比率下进行的。为了解决一次、二次、三次和分段气流中氧化剂气流温度不同的问题,小火焰化学表还引入了一个额外的维度。热化学空间有七个维度,其中三个维度为燃料混合物分数(挥发物、炭化废气和氨),另一个维度为混合物分数变量、反应进展变量、总焓和氧化剂温度。通过将七维非绝热(7D-NA)FPV-LES 模型的预测结果与实测数据以及具有一定局限性的先前建模结果(如忽略氧化剂温度差的六维非绝热(6D-NA)FPV-LES 模型和忽略氧化剂温度差和火焰小化中热量损失的五维绝热(5D-AD)FPV-LES 模型)进行比较,评估了该模型的准确性。在两种注入氨气的情况下,7D NA-FPV-LES 模型都能准确捕捉燃烧器出口流场,从而改进了之前模型的预测结果。它成功地识别了两种情况之间的趋势,预测在通过下游喷入氨水的情况下,由于内部再循环区的增强,燃烧器出口附近的峰值温度略高。结果表明,当氨水通过下游注入时,氮氧化物峰值明显更高,且更靠近燃烧器,这与测量数据一致,因为通过燃烧器注入的氨水在燃烧器附近普遍存在氮氧化物还原现象。这种方法已在半工业规模的 CRIEPI 试验炉的复杂 CI-α 燃烧器上得到验证,该燃烧器具有预热二次、三次和分段气流,与商业电厂燃烧器中遇到的实际条件相似。建议的方法可以考虑多个氧化剂流,还可以考虑氧化剂成分的变化(尽管在本研究中氧化剂成分是固定的)。这项研究对于在商业发电厂的复杂燃烧器中采用多混合分数 FPV-LES 方法具有重要意义。此外,该研究还为在带有复杂燃烧器的半工业规模熔炉中进行氨/煤联合燃烧提供了有价值的见解,符合全球去碳化目标,强调了在实际规模的商业发电厂中使用氨等零碳燃料。
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引用次数: 0
Turbulent flame propagation of C10 hydrocarbons/air expanding flames: Possible unified correlation based on the Markstein number C10 碳氢化合物/空气膨胀火焰的湍流火焰传播:基于马克斯坦数的可能统一相关性
IF 5.8 2区 工程技术 Q2 ENERGY & FUELS Pub Date : 2024-09-14 DOI: 10.1016/j.combustflame.2024.113724
<div><p>In this study, we experimentally analyzed the influence of turbulence and thermal-diffusional effect on the morphology and turbulent flame speed of premixed expanding flames. The turbulent flames of the n-decane/air and decalin/air mixtures were measured using a fan-stirred constant volume combustion bomb generating near-isotropic turbulence at elevated pressures (1, 2, and 5 bar), temperature (443 K), and a wide range of equivalence ratios (0.8–1.6). The results found that the wrinkling degree of the flame front was greater for <span><math><mrow><mi>M</mi><mi>a</mi></mrow></math></span><0 compared to <span><math><mrow><mi>M</mi><mi>a</mi></mrow></math></span>>0. However, the distribution patterns of the curvature radius of the flame contours exhibited similarities across different equivalence ratios. Furthermore, an increase in turbulence intensity would aggravate the randomness of flame contour distribution. The turbulent expanding flames of n-decane/air and decalin/air mixtures were self-similar under different turbulence intensities and pressures, and this self-similar propagation followed a correlation between the normalized turbulent flame speed and the turbulent flame Reynolds number (<span><math><mrow><mi>R</mi><msub><mi>e</mi><mrow><mi>T</mi><mo>,</mo><mi>f</mi></mrow></msub></mrow></math></span>) to the one-half power. The similarity in normalized turbulent flame speeds was extended from normal alkanes (C4-C8) and isomeric alkanes (C8, C16) to longer straight-chain alkane (n-decane) and cycloalkane (decalin). As the increase of equivalence ratio, their normalized turbulent flame speeds increased nonlinearly due to the thermal-diffusional effect. Additionally, it was found that the classical, effective, and experimental Lewis numbers were confirmed as unsuitable parameters for characterizing the role of thermal-diffusional effect on the turbulent flame speed for hydrocarbon fuels with large molecular weight. Finally, two possible unified correlations were proposed based on the Markstein number, <span><math><mrow><mrow><mo>(</mo><mrow><mi>d</mi><mo>〈</mo><mi>r</mi><mo>〉</mo><mo>/</mo><mi>d</mi><mi>t</mi></mrow><mo>)</mo></mrow><mo>/</mo><mrow><mo>(</mo><mrow><mi>σ</mi><msub><mi>S</mi><mi>L</mi></msub></mrow><mo>)</mo></mrow><mo>=</mo><mn>0.178</mn><msup><mrow><mi>e</mi></mrow><mrow><mo>−</mo><mn>0.231</mn><mi>M</mi><mi>a</mi></mrow></msup><mi>R</mi><msubsup><mi>e</mi><mrow><mi>T</mi><mo>,</mo><mi>f</mi></mrow><mrow><mn>1</mn><mo>/</mo><mn>2</mn></mrow></msubsup></mrow></math></span> and <span><math><mrow><mrow><mo>(</mo><mrow><mi>d</mi><mo>〈</mo><mi>r</mi><mo>〉</mo><mo>/</mo><mi>d</mi><mi>t</mi></mrow><mo>)</mo></mrow><mo>/</mo><mrow><mo>(</mo><mrow><mi>σ</mi><msub><mi>S</mi><mi>L</mi></msub></mrow><mo>)</mo></mrow><mo>=</mo><mrow><mo>(</mo><mrow><mn>0.170</mn><mo>−</mo><mn>0.0447</mn><mi>M</mi><mi>a</mi><mo>+</mo><mn>0.0067</mn><mi>M</mi><msup><mrow><mi>a</mi></mrow><mn>2</mn></msup></mrow><mo>)</mo></mrow><mi>R</mi><msubsu
在这项研究中,我们通过实验分析了湍流和热扩散效应对预混合膨胀火焰形态和湍流火焰速度的影响。在高压(1、2 和 5 巴)、高温(443 K)和较宽的当量比(0.8-1.6)范围内,使用产生近各向同性湍流的扇形搅拌恒容燃烧弹测量了正癸烷/空气和癸烷/空气混合物的湍流火焰。结果发现,Ma<0 与 Ma>0 相比,火焰前沿的皱缩程度更大。然而,火焰轮廓曲率半径的分布模式在不同等效比之间表现出相似性。此外,湍流强度的增加会加剧火焰轮廓分布的随机性。在不同的湍流强度和压力下,正癸烷/空气和癸烷/空气混合物的湍流膨胀火焰具有自相似性,这种自相似性的传播遵循归一化湍流火焰速度与湍流火焰雷诺数(ReT,f)二分之一幂之间的相关性。归一化湍流火焰速度的相似性从普通烷烃(C4-C8)和异构烷烃(C8、C16)扩展到更长的直链烷烃(正癸烷)和环烷烃(癸烷)。随着当量比的增加,由于热扩散效应,它们的归一化湍流火焰速度呈非线性增加。此外,研究还发现,经典的、有效的和实验的路易斯数被证实不适合用来描述热扩散效应对大分子量烃类燃料湍流火焰速度的影响。最后,基于马克斯坦数提出了两种可能的统一相关性:(d〈r〉/dt)/(σSL)=0.178e-0.231MaReT,f1/2 和 (d〈r〉/dt)/(σSL)=(0.170-0.231MaReT,f1/2)。0447Ma+0.0067Ma2)ReT,f1/2,可以预测正构烷烃、异构烷烃和癸醛等大分子量烃类燃料的湍流火焰速度。
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The results found that the wrinkling degree of the flame front was greater for &lt;span&gt;&lt;math&gt;&lt;mrow&gt;&lt;mi&gt;M&lt;/mi&gt;&lt;mi&gt;a&lt;/mi&gt;&lt;/mrow&gt;&lt;/math&gt;&lt;/span&gt;&lt;0 compared to &lt;span&gt;&lt;math&gt;&lt;mrow&gt;&lt;mi&gt;M&lt;/mi&gt;&lt;mi&gt;a&lt;/mi&gt;&lt;/mrow&gt;&lt;/math&gt;&lt;/span&gt;&gt;0. However, the distribution patterns of the curvature radius of the flame contours exhibited similarities across different equivalence ratios. Furthermore, an increase in turbulence intensity would aggravate the randomness of flame contour distribution. The turbulent expanding flames of n-decane/air and decalin/air mixtures were self-similar under different turbulence intensities and pressures, and this self-similar propagation followed a correlation between the normalized turbulent flame speed and the turbulent flame Reynolds number (&lt;span&gt;&lt;math&gt;&lt;mrow&gt;&lt;mi&gt;R&lt;/mi&gt;&lt;msub&gt;&lt;mi&gt;e&lt;/mi&gt;&lt;mrow&gt;&lt;mi&gt;T&lt;/mi&gt;&lt;mo&gt;,&lt;/mo&gt;&lt;mi&gt;f&lt;/mi&gt;&lt;/mrow&gt;&lt;/msub&gt;&lt;/mrow&gt;&lt;/math&gt;&lt;/span&gt;) to the one-half power. The similarity in normalized turbulent flame speeds was extended from normal alkanes (C4-C8) and isomeric alkanes (C8, C16) to longer straight-chain alkane (n-decane) and cycloalkane (decalin). As the increase of equivalence ratio, their normalized turbulent flame speeds increased nonlinearly due to the thermal-diffusional effect. Additionally, it was found that the classical, effective, and experimental Lewis numbers were confirmed as unsuitable parameters for characterizing the role of thermal-diffusional effect on the turbulent flame speed for hydrocarbon fuels with large molecular weight. Finally, two possible unified correlations were proposed based on the Markstein number, &lt;span&gt;&lt;math&gt;&lt;mrow&gt;&lt;mrow&gt;&lt;mo&gt;(&lt;/mo&gt;&lt;mrow&gt;&lt;mi&gt;d&lt;/mi&gt;&lt;mo&gt;〈&lt;/mo&gt;&lt;mi&gt;r&lt;/mi&gt;&lt;mo&gt;〉&lt;/mo&gt;&lt;mo&gt;/&lt;/mo&gt;&lt;mi&gt;d&lt;/mi&gt;&lt;mi&gt;t&lt;/mi&gt;&lt;/mrow&gt;&lt;mo&gt;)&lt;/mo&gt;&lt;/mrow&gt;&lt;mo&gt;/&lt;/mo&gt;&lt;mrow&gt;&lt;mo&gt;(&lt;/mo&gt;&lt;mrow&gt;&lt;mi&gt;σ&lt;/mi&gt;&lt;msub&gt;&lt;mi&gt;S&lt;/mi&gt;&lt;mi&gt;L&lt;/mi&gt;&lt;/msub&gt;&lt;/mrow&gt;&lt;mo&gt;)&lt;/mo&gt;&lt;/mrow&gt;&lt;mo&gt;=&lt;/mo&gt;&lt;mn&gt;0.178&lt;/mn&gt;&lt;msup&gt;&lt;mrow&gt;&lt;mi&gt;e&lt;/mi&gt;&lt;/mrow&gt;&lt;mrow&gt;&lt;mo&gt;−&lt;/mo&gt;&lt;mn&gt;0.231&lt;/mn&gt;&lt;mi&gt;M&lt;/mi&gt;&lt;mi&gt;a&lt;/mi&gt;&lt;/mrow&gt;&lt;/msup&gt;&lt;mi&gt;R&lt;/mi&gt;&lt;msubsup&gt;&lt;mi&gt;e&lt;/mi&gt;&lt;mrow&gt;&lt;mi&gt;T&lt;/mi&gt;&lt;mo&gt;,&lt;/mo&gt;&lt;mi&gt;f&lt;/mi&gt;&lt;/mrow&gt;&lt;mrow&gt;&lt;mn&gt;1&lt;/mn&gt;&lt;mo&gt;/&lt;/mo&gt;&lt;mn&gt;2&lt;/mn&gt;&lt;/mrow&gt;&lt;/msubsup&gt;&lt;/mrow&gt;&lt;/math&gt;&lt;/span&gt; and &lt;span&gt;&lt;math&gt;&lt;mrow&gt;&lt;mrow&gt;&lt;mo&gt;(&lt;/mo&gt;&lt;mrow&gt;&lt;mi&gt;d&lt;/mi&gt;&lt;mo&gt;〈&lt;/mo&gt;&lt;mi&gt;r&lt;/mi&gt;&lt;mo&gt;〉&lt;/mo&gt;&lt;mo&gt;/&lt;/mo&gt;&lt;mi&gt;d&lt;/mi&gt;&lt;mi&gt;t&lt;/mi&gt;&lt;/mrow&gt;&lt;mo&gt;)&lt;/mo&gt;&lt;/mrow&gt;&lt;mo&gt;/&lt;/mo&gt;&lt;mrow&gt;&lt;mo&gt;(&lt;/mo&gt;&lt;mrow&gt;&lt;mi&gt;σ&lt;/mi&gt;&lt;msub&gt;&lt;mi&gt;S&lt;/mi&gt;&lt;mi&gt;L&lt;/mi&gt;&lt;/msub&gt;&lt;/mrow&gt;&lt;mo&gt;)&lt;/mo&gt;&lt;/mrow&gt;&lt;mo&gt;=&lt;/mo&gt;&lt;mrow&gt;&lt;mo&gt;(&lt;/mo&gt;&lt;mrow&gt;&lt;mn&gt;0.170&lt;/mn&gt;&lt;mo&gt;−&lt;/mo&gt;&lt;mn&gt;0.0447&lt;/mn&gt;&lt;mi&gt;M&lt;/mi&gt;&lt;mi&gt;a&lt;/mi&gt;&lt;mo&gt;+&lt;/mo&gt;&lt;mn&gt;0.0067&lt;/mn&gt;&lt;mi&gt;M&lt;/mi&gt;&lt;msup&gt;&lt;mrow&gt;&lt;mi&gt;a&lt;/mi&gt;&lt;/mrow&gt;&lt;mn&gt;2&lt;/mn&gt;&lt;/msup&gt;&lt;/mrow&gt;&lt;mo&gt;)&lt;/mo&gt;&lt;/mrow&gt;&lt;mi&gt;R&lt;/mi&gt;&lt;msubsu","PeriodicalId":280,"journal":{"name":"Combustion and Flame","volume":null,"pages":null},"PeriodicalIF":5.8,"publicationDate":"2024-09-14","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"142232086","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":2,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
引用次数: 0
The effects of C/N cross-reactions on the NH3/C3H8 combustion: A shock-tube and modeling study C/N 交叉反应对 NH3/C3H8 燃烧的影响:冲击管和模型研究
IF 5.8 2区 工程技术 Q2 ENERGY & FUELS Pub Date : 2024-09-14 DOI: 10.1016/j.combustflame.2024.113716

A viable strategy to improve ammonia (NH3) combustion stability is blending ammonia with high-reactivity fuels. Propane (C3H8) is the prevalent component in liquefied petroleum gas (LPG), emerging as a compelling choice for co-firing with ammonia in various practical applications. The ignition delay times (IDTs) of stoichiometric NH3/C3H8 mixtures in Ar dilution (90 %) with varying C3H8 fractions (XC3H8) of 0–30 % were conducted at pressures of 1.75 and 10 bar, and temperatures ranging from 1305 to 1890 K in a shock tube. The NH3-C3H8 model was developed based on the NH3 model optimized by Li et al., the C3H8 submodel in the NUIG 1.1 model, and some new cross-reactions were considered in the NH3-C3H8 model. The NH3-C3H8 model was extensively validated against IDTs measured in this work as well as laminar flame speeds (LFSs) and species profiles (SPs) of NH3/C3H8 from the literature. The comparison of the prediction performance between the NH3-C3H8 model and the M-NUIG model was conducted for ignition, flame propagation, and NH3 consumption. The effects of the cross-reactions on IDTs, LFSs, and SPs of NH3/C3H8 were studied in detail by the sensitivity analysis and rate of production (ROP) analysis using the NH3-C3H8 model. The newly added C/N cross-reactions play an important role in the prediction of the IDTs, LFSs, and SPs of NH3/C3H8 combustion.

提高氨(NH3)燃烧稳定性的可行策略是将氨与高活性燃料混合。丙烷(C3H8)是液化石油气(LPG)中的主要成分,在各种实际应用中成为与氨气共同燃烧的理想选择。在压力为 1.75 和 10 巴、温度为 1305 至 1890 K 的冲击管中,对氩气稀释(90%)的化学计量 NH3/C3H8 混合物以及 0-30% 的不同 C3H8 分数(XC3H8)进行了点火延迟时间(IDTs)试验。NH3-C3H8 模型是在 Li 等人优化的 NH3 模型和 NUIG 1.1 模型中的 C3H8 子模型基础上开发的,NH3-C3H8 模型还考虑了一些新的交叉反应。NH3-C3H8 模型与本研究中测量的 IDT 以及文献中 NH3/C3H8 的层流火焰速度(LFS)和物种剖面(SP)进行了广泛的验证。对 NH3-C3H8 模型和 M-NUIG 模型在点火、火焰传播和 NH3 消耗方面的预测性能进行了比较。通过使用 NH3-C3H8 模型进行敏感性分析和生成率(ROP)分析,详细研究了交叉反应对 NH3/C3H8 的 IDT、LFS 和 SP 的影响。新增加的 C/N 交叉反应在预测 NH3/C3H8 燃烧的 IDT、LFS 和 SP 方面发挥了重要作用。
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引用次数: 0
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Combustion and Flame
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