平朔煤热解过程中PAHs的释放特性

利用热解-气质联用仪(PY-GC-MS)研究了平朔煤在不同热解温度下多环芳烃(PHAs)的释放规律,并探讨了该过程中PAHs的生成机理。研究结果表明,16种PAHs的生成总量随着热解温度的升高先增大后减少,在800℃达到最大值。且PAHs环数分布规律对热解温度具有显著的依赖性,不同环数的PAHs,其最大生成量时所对应的热解温度亦不同。随着热解温度的升高,煤结构中的桥键、芳香环上的脂肪侧链以及较难断裂的甲基、酚羟基等依次断裂,使得PAHs的生成量不断增加,当温度升高至1 000、1 200℃时,伴随着缩合反应加剧,大环PAHs的生成量继续增加。由总体趋势看出,平朔煤大分子网络结构的热裂解主要发生在600~800℃,热解缩合反应主要发生在高温下。平朔煤热解过程中的PAHs除小部分来自煤中可萃取的芳烃结构挥发外,主要来自煤中大分子芳香结构裂解以及热解生成自由基碎片的高温聚合。     

典型烟煤热解机理的反应动力学模拟

建立合理有效的烟煤大分子模型，采用基于反应力场（Reactive Force Field，ReaxFF）的分子动力学方法模拟1400-2600 K典型烟煤的热解过程，得出产物分布和中间自由基的演变历程。研究表明，随着热解温度的升高，焦炭产量先增加后降低，焦油产量的变化趋势与焦炭相反，热解气产量单调增加。煤在低温下热解主要发生一次反应，生成焦油自由基碎片和小分子气体；高温下焦油碎片的二次反应显著，生成含量较多但数量较少的焦炭及含量与数量较多的小分子气体。2000 K是一次反应向二次反应的温度转折点。在高温热解时，煤中的C与H逐渐迁移到焦炭和焦油中，而含氧官能团较为活跃，O逐渐迁移到热解气中。二次反应阶段，O最活泼，H次之，C最稳定。热解过程中最先产生的气体是H₂O；NH₃主要来源于二次反应；H₂S在二次反应阶段被消耗转化为其他产物；H₂产量最多，且随热解温度升高而增加，尤其在二次反应中大量生成，主要源于裂解产生的氢自由基碰撞和芳香结构的缩合。基于ReaxFF模拟结果得到煤热解失重活化能为39.45 kJ/mol。     

木质素二聚体模型化合物热解机理的量子化学研究

β-O-4连接是木质素主体结构单元之间的主要联结方式。采用密度泛函理论方法B3LYP,在6-31G (d, p)基组水平上,对β-O-4型木质素二聚体模型化合物(1-愈创木基-2-(2-甲氧基苯氧基)-1,3丙二醇)的热解反应机理进行了研究。提出了三种热解反应途径:C_β-O键均裂的后续反应、C_α-C_β键均裂的后续反应以及协同反应。对各种反应的反应物、产物、中间体和过渡态的结构进行了能量梯度全优化,计算了各热解反应途径的标准动力学参数。分析了各种主要热解产物的形成演化机理以及热解过程中温度对热解机理的影响。计算结果表明,C_β-O键的均裂反应和协同反应路径(1)和(3)是木质素二聚体热解过程中主要的反应路径,而C_α-C_β键的均裂反应和协同反应路径(2)和(5)是主要的竞争反应路径;热解的主要产物是酚类化合物如愈创木酚、1-愈创木基-3-羟基丙酮、3-愈创木基-3-羟基丙醛、愈创木基甲醛和乙烯等。在热解低温阶段协同反应是热解过程中的主要反应形式,而在高温阶段自由基均裂反应是热解过程的主要反应形式。     

Kinetic Study on Pyrolysis of Extracted Oil Palm Fiber. Isothermal and non-isothermal conditions

Pyrolysis of extracted oil palm fibers under isothermal and non-isothermal conditions was carried out in a thermogravimetric analyzer. Isothermal curves showed that increasing pyrolysis temperature resulted in a faster pyrolysis and a higher conversion of oil palm fibers into gaseous products. Raw material sizes (below 1.0 mm) had insignificant effects on the isothermal pyrolysis, but the fibers with a size fraction of 1.0 to 2.0 mm resulted in a lesser conversion. Two-step reactions were found in the non-isothermal pyrolysis as evidenced by the presence of two peaks in the derivative thermogravimetry curves. Raw material sizes had no obvious effects on the temperature at which the maximum rate of pyrolysis occurred, but affected the rate of sample mass loss. For the low and high temperature regimes, a three-dimensional diffusion mechanism and a first-order of reaction mechanism respectively were used to describe the non-isothermal pyrolysis kinetics of extracted oil palm fibers. This revised version was published online in July 2006 with corrections to the Cover Date.     

Control of the Composition and Structure of Silicon Oxycarbide and Oxynitride Glasses Derived from Polysiloxane Precursors

The reactions involved in the preparation of silicon oxycarbide and oxynitride glasses by pyrolysis of polysiloxane precursors respectively under argon and ammonia are reviewed. The influence of the composition and structure of the precursor and of these pyrolysis reactions on the pyrolysis yield, the composition, and the structure of the glass is discussed. The free-carbon content of the glass depends on the substituents in the precursor and on the nature of the pyrolysis atmosphere. The composition of the oxynitride or the oxycarbide phase depends on the O/Si ratio of the precursor. The structure of these phases is not directly related to the structure of the precursors, but rather depends on their composition and on the pyrolysis temperature.     

Gas Evolution from the Pyrolysis of Jordan Oil Shale in A Fixed-bed Reactor

Jordan oil shale from El-Lajjun deposit was pyrolysed in a fixed-bed pyrolysis reactor and the influence of the pyrolysis temperature between 400 to 620°C and the influence of the pyrolysis atmosphere using nitrogen and nitrogen/steam on the product yield and gas composition were investigated. The gases analysed were H₂, CO, CO₂ and hydrocarbons from C₁ to C₄. The results showed for both nitrogen and nitrogen/steam that increase the pyrolysis bed temperature from 400 to 520°C resulted in a significant increase in the oil yield, after which temperature the oil yield decreased. The alkene/alkane ratio including ethene/ethane, propene/propane, and butene/butane ratios, can be used as an indication of pyrolysis temperature and the magnitude of cracking reactions. Increasing alkene/alkane ratio occurring with increasing pyrolysis temperature. The alkene/alkane ratio for nitrogen/steam pyrolysis atmosphere was lower than the one found under nitrogen atmosphere. This revised version was published online in July 2006 with corrections to the Cover Date.     

FLASHCHAIN模型应用于汪清油页岩热解研究

采用~(13)C-NMR技术表征出汪清三个矿区油页岩的碳原子化学结构,并获得碳骨架结构的12个重要参数。利用热重和傅里叶红外联用技术(TG-FTIR)得出了在50℃/min升温速率和热解终温600℃下油页岩热解时轻质气体的生成规律。采用基于燃料化学结构的FLASHCHAIN模型对热解产物的析出进行了模拟,并与实验结果相比较。结果表明,FLASHCHAIN模型用来模拟汪清油页岩热解时,在520℃之前有较好的效果,当温度高于520℃时,由于二次热解反应及页岩中矿物质分解对热解过程的影响,导致模型的预测值与实验值存在一定的误差,且随着温度的升高两者之间的误差也随之加大。     

Influences of Temperature and Coal Particle Size on the Flash Pyrolysis of Coal in a Fast-entrained Bed

IntroductionCoal is the major primary energy source in China,which accounts for about three quarters of the total en-ergy consumption.Most of coal in China contains a rel-atively high content of volatile substances.The reserveof lignite accounts for about…     

循环流化床内废轮胎的热解油化

介绍了以循环流化床反应器为主体的废轮胎热解油化装置,实验过程,实验结果及分析。通过评价热解条件对气体成分及油、碳和气产物产率的影响,以及热解油品的成分分析,得出如下结论：（１）较高的温度和较好的停贸时间会生成过多的不凝气（主要成分为ＣＨ４、Ｈ２,Ｃ２ＨＶ和ＣＯ等）,降低油的产率,过低的温度和加热速率导致严重的碳化,同样会降低油产率。（２）热解油品的组成成分非常复杂,芳烃占了很大比例,其次是烷烃和非     

DFT Thermodynamic Research of the Pyrolysis Mechanism of the Carbon Matrix Precursor Toluene for Carbon Material

IntroductionAs far as the carbon matrix precursor for carbon material is concerned, the pyrolysis car-bonization mechanism and initial pyrolysis carbonization reaction process are still a field notfully to be understood and to be studied[l--3J. This kind of research is very important for effi-ciently utilizing the organic substance sources and developing new carbon materials (carbon/carbon composite, carbon fiber, graphic material for atomic reactor, medical carbon materialand graphic e1ectrod…     

硬木热解过程中颗粒内部二次反应的数值研究 I、单颗粒热解模型的构建

为了研究生物质（硬木）热解过程中颗粒内部的二次反应，弥补常规实验研究在该领域内的不足，构建合适的数学模型进行数值模拟是一个很好的途径。本文介绍了硬木单颗粒热解综合模型的构建方法。针对所研究的问题，模型中细致考虑了包含一次焦油二次裂解的生物质热解动力学过程。为了准确描述热解产物在热解颗粒内部的传递和二次反应过程，模型包含了对热解过程中颗粒内部各种气相产物在孔隙率不断变化的生物质颗粒内的生成、消耗、积累以及在压力驱动下的输运等行为的描述。模型参数的选取尽可能真实地模拟了实际过程，引入转化率或温度对涉及到的各种物理性质参数进行了修正。构建的模型在理论上较全面地描述了单颗粒生物质热解的复杂过程，可以利用它对颗粒内部的二次反应过程进行进一步的研究。     

水介质条件下油页岩热解机理研究

利用高压釜反应装置,对柳树河油页岩进行了饱和水和不饱和水介质条件下的热压模拟实验,研究了两种条件下油页岩热解产物(气体、油和热沥青)的生成机理.实验结果表明,在油页岩的热解过程中,同时经历自由基反应和碳正离子反应.水在高温的物化性质较在常温常压时发生了巨大的变化,具有酸催化剂和碱催化剂的作用,促使按碳正离子机理进行反应...     

Pyrolysis behavior of phosphorus polyesters

The pyrolysis behavior of aromatic–aliphatic polyesters containing either a pendant 9,10-dihydro-9-oxa-10-phosphaphenanthrene-10-oxide (DOPO) group or a phosphine oxide group incorporated into the polymer backbone was studied using a combination of thermogravimetry and pyrolysis-GC/MS. The behavior of the phosphorus polyesters was compared to that of non-phosphorus-containing reference polymers. It could be shown that the DOPO group mainly does not interfere with the polyester decomposition. It produces two main pyrolysis products, o-hydroxybiphenyl and dibenzofuran, with the latter one requiring a higher pyrolysis temperature. Minor products containing the DOPO ring result from secondary decomposition reactions. In contrast, the phosphine oxide group strongly modifies the polyester pyrolysis behavior by decreasing the degradation temperature and changing the composition of pyrolysis products. Among of those, phosphinites and a phosphinate could be identified indicating rearrangement processes of the phosphine oxide group taking place upon pyrolysis. Mass spectra of organophosphorus products and pyrolysis schemes of polyesters are discussed.     

MOCVD过程中金属有机源(C~3H~7)~2Te和(CH~3)~2Cd热裂解机理 质谱实时研究

采用质谱技术实时研究了金属有机源DIPTe和DMCd在MOCVD反应器中热裂解的性质。着重分析了可能发生的气相反应及热裂解机理,并探讨了在CdTe,HgCdTe实际生长条件下两个有机源之间可能发生的相互作用及其对热裂解温度的影响。     

Effects of temperature and holding time during torrefaction on the pyrolysis behaviors of woody biomass

Torrefaction is the thermal treatment techniques performed at relatively low temperature (<300 °C) in an inert atmosphere, which aims to improve the fuel properties attractively. In this study, woody biomass (Leucaena leucocephala) was torrefied at various temperatures and holding times and the pyrolysis behaviors of the torrefied wood were examined in detail by using TG-MS technique. It was found that the carbon content and the calorific value of the torrefied leucaena increased significantly when temperature and holding time during the torrefaction increased. From the TG-MS analysis, the pyrolysis behaviors of the torrefied leucaena were significantly different from those of the raw leucaena. The char yield at 800 °C for the torrefied leucaena was increased when increasing the holding time during the torrefaction. On the other hand, the tar yield during the pyrolysis decreased significantly with the increase in the holding time during the torrefaction. Through the results from the TG-MS analysis, it was concluded that the structure of leucaena was changed by the torrefaction at temperature below 275 °C and the cross-linking reactions occurred during the pyrolysis resulting in increase in char yields and decrease in tar yields. It was also suggested that the longer the holding time during the torrefaction, the more the cross-linking reactions proceed during the pyrolysis. The results obtained from the study provide the basic information for the pyrolyser and/or gasifier design by using torrefied biomass as a fuel.     

异丁烷高温热解反应动力学和机理

用激波管激光纹影技术测定了异丁烷高温热解反应信号，对热解过程中重要单分子反应的降变行为作了理论计算，建立了由五十个基元反应组成的反应机理并进行了计算机模拟，本文得到引发反应i-C_4H_(10)→CH_3＋i-C_3H_7在温度为1500－1850 K，压1.00×10~4-2.00×10~4 Pa时的速率常数为k_1＝6.22×10~(11) exp(－457000/RT)±50％(S~(-1))．这一结果与降变理论计算符合得很好．     

Synthesis of 1,1,9,9-tetrafluoro[2.2]paracyclophane and its polymerization by vapor deposition method

1,1,9,9-Tetrafluoro[2.2]paracyclophane ( 1 ) was prepared successfully as white crystals in 72% yield via two-step reactions from 1,9-diketo[2.2]-paracyclophane. The polymerization of 1 by the vapor deposition method was carried out at pyrolysis temperature range of 400 to 800°C and deposition temperature range of ?20 to 20°C, and a tough, transparent poly(α,α-difluoro-p-xylylene) film was obtained in 72% yield at the pyrolysis temperature of 750°C and the deposition temperature of ?20°C. It was found that the pyrolysis of 1 gave a reactive α,α-difluoro-p-xylylene, which polymerized on the head-to-tail addition to give poly(α,α-difluoro-p-xylylene). Some properties such as solubility, thermal stability, glass transition temperature, and density for poly(α,α-difluoro-p-xylylene) were studied. © 1995 John Wiley & Sons, Inc.     

城市生活垃圾典型有机组分混合热解特性的研究

利用自行设计的较大物量(约10 g)的热重分析装置对城市生活垃圾典型有机组分（纸屑、木屑、织物、塑料、橡胶、厨余）的混合热解特性进行了实验研究，并用最小二乘法计算得到由若干平行反应组成的热解反应动力学模型，实验结果与模型计算结果吻合较好。在此基础上对城市生活垃圾典型有机组分混合热解中的交互影响和非线性规律进行了分析。结果表明，城市生活垃圾典型有机组分混合热解动力学模型由2个～4个平行反应组成；混合热解中有反应发生合并的现象；热效应和组分比例对混合物综合热解特性有显著影响。     

Detailed chemical kinetic modeling of butylbenzene pyrolysis

A chemical kinetic model was constructed for the pyrolysis of butylbenzene. The mechanism was based on free radical reactions. All relevant reactions were considered, and a final selection of 60 reactions involving 29 molecules and free radicals was made. The rate constants and thermodynamic parameters were taken from the literature or estimated using accepted literature methods such as group additivity. The results from the model were compared to experimental rates and product selectivity for butylbenzene pyrolysis over a temperature range of 778 K to 868 K and to an experimental rate at 923 K. The rates agreed within a factor of two and were usually much closer. The experimental and theoretical yields of the major products, styrene, ethane, toluene, and propylene, agreed within two percentage points. The agreement for seven minor products was not quite as good, with the worst case being an overprediction of the yield of allylbenzene by a factor of 2.6.