煤-焦炉气共热解特性研究Ⅱ.热解半焦燃烧反应性的研究

实验采用ＴＧ１５１型高压热天平对不同热解压力和热解升温速率下煤焦炉气共热解半焦燃烧反应性进行了考察。主要考察半焦燃烧的特征参数如着火温度（Ｔｉ）、最大燃烧速率峰温（ＴＭ）和燃尽温度（Ｔｆ），最大燃烧速率（ＲＭ）以及燃尽时间（ｔ），通过燃烧特征参数（燃尽时间ｔ）和ＴＧ及ＤＴＧ数据的相关动力学分析（Ｒｆ图）来描述半焦燃烧反应性能。结果表明，热解压力越高，其半焦燃烧反应性越差，在慢速升温情况下尤为明显；热解升温速率越快其半焦燃烧反应性越好，在较高压力下更为明显。先锋褐煤与焦炉气共热解半焦的反应活性与其加氢热解半焦的反应活性相当，但两者均略低于氮气氛下热解半焦的反应性。     

小龙潭褐煤不同气氛下液化性能的研究

根据褐煤含水量高的特点,研究了以水为溶剂,不同气氛条件下小龙潭褐煤的液化行为。结果表明,小龙潭褐煤具有较好的液化活性,在420℃,H₂气氛下以四氢萘为溶剂时煤的液化转化率可达到94.5%。煤液化过程中,稳定热解产生的自由基活性氢主要来自于供氢溶剂,而气相H₂不具活性,不能直接为液化过程提供活性氢。当以水为溶剂取代四氢萘进行褐煤直接液化时,相对于H₂和N₂气氛,CO 气氛下表现出较好的液化性能。这表明发生了水煤气变换反应并生成了活性氢,该活性氢可以使得煤热解产生的自由基稳定,生成低分子的液化产物,提高了液化转化率。由于在较低的CO初压下反应生成的活性氢数量有限,因而液化转化率不高。实验表明,以水为溶剂在CO气氛下进行褐煤的液化是一种新的褐煤直接液化技术。     

Evaluation of combustion characteristics of different size elbistan lignite by using TG/DTG and DTA

In this research, the relationship between particle size and combustion kinetics and combustion properties of lignite samples was examined by utilizing the thermogravimetric (TG/DTG) and differential thermal analysis (DTA) techniques. The lignite samples separated into different size fractions were subjected to non-isothermal thermogravimetric analysis between ambient and 900°C in the presence of 50 mL min⁻¹ air flow rate. Activation energy (E) and Arrhenius constant (A _r) of combustion reaction of each size was evaluated by applying Arrhenius kinetic model to the resulting data. Combustion properties of the samples were interpreted by careful examination of the curves. The apparent activation energies in major combustion region were calculated as 41.03 and 53.11 kJ mol⁻¹ for the largest size (−2360+2000 μm) and the finest size (−38 μm), respectively.     

Thermogravimetric analysis of peat decomposition under different oxygen concentrations

Smoldering combustion of peat is of global concern as a natural hazard to consume sequestered carbon and form wide-area haze. It is affected by thermal decomposition kinetics of peat and the diffusion and availability of oxygen. In this work, thermal decomposition behavior of peat was investigated using thermogravimetric analysis under the atmosphere with different oxygen concentrations. The results showed that thermal decomposition process of peat could be divided into three stages: dehydration, oxidative pyrolysis of organic matters into volatiles and char, and oxidation of the generated char. The apparent activation energies of peat decomposition under different oxygen concentrations were calculated by model-free methods of Kissinger, FWO, Starink, Gyulai, and Friedman. A two-step reaction model was proposed to describe thermal decomposition kinetics of peat (excluding dehydration stage) and the effect of oxygen concentration on the kinetic parameters was discussed. These results provide basic data for smoldering modeling of peat.     

A detailed reaction mechanism for hexamethyldisiloxane combustion via experiments and ReaxFF molecular dynamics simulations

Hexamethyldisiloxane (HMDSO) is one of the main impurities in the syngas produced from sewage and landfill plants. In order to utilize this syngas or control the characteristics of the generated silica particles, it is crucial to understand the chemical kinetics of HMDSO combustion. This study investigated the process of HMDSO combustion using synchrotron radiation mass spectrometry (SRMS), gas chromatography (GC), and ReaxFF molecular dynamics simulations. First, the force field used for ReaxFF simulation was validated by comparing the energies of different bond lengths, bond angles, and dihedral angles with the ones from DFT calculations. Good agreements were found. Then, ReaxFF simulations of HMDSO combustion with this force field were conducted under various conditions, which include different equivalence ratios (0.67, 1.0, and 1.5) and temperatures ranging from 2000 to 3500 K. The oxidation characteristics of HMDSO were analyzed, including the evolution of gas products and particle formation. Finally, based on the results from experiments and ReaxFF simulations, the reaction pathways, reaction lists, and reaction kinetics data during HMDSO combustion were obtained. A detailed reaction mechanism was proposed and validated by applying it in modeling the H₂/HMDSO/O₂ combustion systems. The temperature and part of the gas products such as CO and CO₂ as well as SiO could be well predicted.     

空气污染组分H2O和CO2对乙烯燃烧性能的影响

超燃冲压发动机在高空工作时, 以高温高速纯净空气作氧化剂使燃料燃烧. 但在地面实验中, 高温空气往往通过燃烧加热方式获得, 从而使空气包含了H2O和CO2污染组分. 本文用电阻加热来流空气并添加污染组分的方法, 研究了燃烧室模型中乙烯的燃烧状态和壁面压力受污染组分的影响. 用化学反应动力学模拟的方法, 在绝热刚性反应器模型中用H2O和CO2取代空气中的N2, 研究了污染组分对点火延迟和燃烧温度的影响, 并从链反应机理的角度讨论了实验和动力学模拟结果.     

多孔物质气固反应动力学研究

利用自主研制的微型流化床反应分析仪（MFBRA）在等温条件下测试了高比表面活性炭氧化反应,并根据基于固体转化的热分析动力学方法及考虑气体在微孔内扩散与反应的应用化工动力学方法求算了动力学参数．在内外扩散抑制最小化的实验条件下,粒径小于5μm的活性炭在700-1000℃的燃烧反应动力学研究表明,根据微型流化床中实验数据,采用等温热分析动力学方法求算得内扩散控制区活化能约为95kJ／mol;弓l入化工动力学方法中的随机孔模型对低温区等温燃烧数据拟合,可得孔结构参数在0．17m^-3左右,反应活化能为178kJ／mol,约为内扩散反应活化能的两倍,最为接近本征的碳燃烧反应活化能．     

柠檬酸镧催化双基推进剂的非等温热分解反应动力学

采用TG-DTG和DSC技术研究了含二缩三乙二醇二硝酸酯(TEGDN)和硝化甘油(NG)的混合酯、硝化棉(NC)和用作燃烧催化剂的柠檬酸镧组成的双基推进剂在常压和流动态氮气气氛下的非等温热分解反应动力学. 结果表明, 该双基推进剂的热分解过程存在2个失重阶段: 第I失重阶段为混合酯的挥发分解过程; 第II失重阶段为主放热分解反应, 机理服从三级化学反应, 减速型α-t曲线, 动力学参数: Ea=231.14 kJ·mol-1, A=10^23.29 s-1, 动力学方程为dα/dt=10^22.99(1-α)³ e^-2.78×104/T. 由外推起始点温度(Te)和峰顶温度(Tp)计算得出该双基推进剂的热爆炸临界温度值分别为Tbe=463.62 K, Tbp=477.88 K. 反应的活化熵(⊿S^≠)、活化焓(⊿H^≠)和活化能(⊿G^≠)分别为219.75 J·mol-1·K-1, 239.23 kJ·mol-1和135.96 kJ·mol-1.     

水热污泥与煤在混燃过程中的协同效应特性研究

以城市污泥衍生的水热污泥(SS-derived hydrochar)为对象,结合傅里叶红外光谱分析(FT-IR)、X射线荧光光谱分析(XRF)和X射线衍射分析(XRD)等对比研究了水热污泥与三种不同品阶煤(褐煤、烟煤和无烟煤)在有机/无机结构与燃料特性上的异同;同时,通过热重(TG)与偏差分析(Deviation)考察水热污泥与各阶煤在不同混合比例条件下的协同燃烧行为及其作用机制。结果表明,污泥经过水热处理后其有机结构和燃烧行为均提升至与煤相似的水平,该过程不仅改善污泥的燃烧特性,并增强其与煤之间的协同燃烧效应。水热污泥中适量的轻质组分与(碱)碱土金属能在混合燃烧过程中加速煤的失重速率,其对三种煤的促进作用可达4.4%-16.1%(褐煤)、1.9%-9.4%(烟煤)和4.8%-12.1%(无烟煤)。总体而言,水热污泥与褐煤混合而成的燃料在燃料性能上具有较大的优势,并且其混合比例以30%(水热污泥):70%(褐煤)与50%(水热污泥):50%(褐煤)为宜。     

增压O_2/CO_2气氛下煤燃烧特性实验研究

增压O2/CO2燃烧是一种可高效分离回收CO2的新兴燃烧技术,其燃烧机理与常压空气、常压O2/CO2燃烧存在较大差异。在加压热重分析仪上研究了增压条件下总压、氧浓度、气氛及粒径等反应参数对美国烟煤和淮北无烟煤燃烧特性的影响,确定了煤的着火温度,并对其进行燃烧动力学分析。结果表明,增压O2/CO2气氛下,随着压力或氧浓度的增加,DTG曲线向低温区移动,煤样整体燃烧速率加快。压力提升、氧浓度增加及煤粉细化均可改善O2/CO2气氛下煤样的着火特性。常压O2/CO2气氛下煤粉燃烧基本属于一级反应;增压O2/CO2气氛下,低温区属于0.5级反应,而高温区属于1.5级反应。     

燃烧反应过程中胜利脱灰褐煤微结构演变特性研究

对胜利脱灰褐煤的燃烧反应性进行了测试,并利用FT-IR、XPS、XRD和Raman等对不同条件下的未反应残留物进行了表征,以分析胜利脱灰褐煤在燃烧过程中微结构演变特性。结果表明,在燃烧反应过程中,煤样的脂肪族官能团不断消耗,碳氧官能团和芳烃骨架的消耗与生成交替进行,褐煤表面C-C/C-H键合结构所占比例先增加后减少,碳-氧键合结构所占比例先减小后增加,未反应残留物的芳香度不断升高,褐煤的石墨缺陷指数先增加后降低,而脂肪族侧链指数则呈现先减少后增加的变化规律,表明随着燃烧反应进行对褐煤未反应残留物的石墨化程度逐渐提高,特别是在燃烧反应后期,石墨化程度显著提高。     

Kinetic Analysis of the Thermal Decomposition of Synthetic Malachite by CRTA

The kinetic behavior of the thermal decomposition of synthetic malachite was investigated by means of CRTA under different conditions of reduced pressure, flowing gases and quasi-isobaric atmospheres. The thermal decomposition was found to proceed at lower temperatures under the influence of the self-generated gases, CO₂ and H₂O. From a viewpoint of chemical equilibrium, the normal and opposite effects on the overall kinetics were observed for the self-generated CO₂ and H₂O, respectively. The complexity of the present reaction is also reflected by the variations of the apparent kinetic parameters which depend on the applied and self-generated atmospheric conditions. The practical usefulness of CRTA when applied to a complicated thermal decomposition is discussed as exemplified by the kinetic approaches to the present reaction. This revised version was published online in August 2006 with corrections to the Cover Date.     

煤在合成气、氢气和氮气气氛下的热解研究

采用固定床反应器，在合成气气氛下对中国寻甸褐煤、蒙古Shiveeovoo褐煤和Khoot油页岩进行了热解研究。升温速率10 ℃/min，褐煤热解温度400 ℃～800 ℃，油页岩热解温度300 ℃~600 ℃，研究结果与氢气和氮气气氛下的热解进行了比较。结果表明,与加压热解不同，褐煤在不同气氛下常压热解半焦和焦油收率差别不大，但对油页岩，合成气和氢气气氛下热解焦油收率高于氮气，气体收率低于氮气。黄铁矿硫在不同气氛下热解均极易脱除，并部分转化为有机硫。油页岩的总硫脱除率远低于褐煤，与油页岩的高灰分含量有关。与氮气甚至氢气相比，合成气下寻甸褐煤的高总硫脱除率和低有机硫含量与合成气中的CO有关。但CO在油页岩热解脱硫中不起作用，也与油页岩高灰分含量有关。研究结果也表明合成气可代替氢气进行加氢热解。     

Effect of pressures on decomposition reaction kinetics of double-base propellant catalyzed with cerium citrate

The decomposition reaction kinetics of the double-base (DB) propellant (No. TG0701) composed of the mixed ester of triethyleneglycol dinitrate (TEGDN) and nitroglycerin (NG) and nitrocellulose (NC) with cerium(III) citrate (CIT-Ce) as a combustion catalyst was investigated by high-pressure differential scanning calorimetry (PDSC) under flowing nitrogen gas conditions. The results show that pressure (2 MPa) can decrease the peak temperature and increase the decomposition heat, and also can change the mechanism function of the exothermal decomposition reaction of the DB gun propellant under 0.1 MPa; CIT-Ce can decrease the apparent activation energy of the DB gun propellant by about 35 kJ mol⁻¹ under low pressure, but it can not display the effect under high pressure; CIT-Ce can not change the decomposition reaction mechanism function under a pressure.     

提纯烟气脱硫渣载氧体煤化学链燃烧性能研究

基于电厂烟气脱硫渣，采用多步酸洗工艺加以提纯并制备获得CaSO₄载氧体。在高温固定床反应器上研究了还原反应温度、载氧体过量系数Φ、多次还原氧化循环等因素对提纯脱硫渣载氧体与煤化学链燃烧特性和气相硫演化规律的影响。结果表明，提纯脱硫渣载氧体有较高的反应活性，能够促进煤的充分转化；综合考虑碳的转化以及气相硫释放的抑制，最优反应工况中还原反应温度确定为900℃、载氧体过量系数Φ=1.0为最佳。经过五次还原氧化循环实验发现，随着循环次数的增加，CaSO₄副反应的进行及气相硫的不断释放，导致提纯脱硫渣载氧体循环反应活性略有降低，反应稳定性受到了一定的影响。     

Influence of mass-transfer effect on isoconversional calculations

A theoretical simulation of the influence of mass-transfer effect on the kinetics of solid–gas reactions has been carried out. The influence of mass-transfer phenomena on the shape of the thermoanalytical curves and on the apparent activation energy, calculated by advanced isoconversional methods (Vyazovkin method) is discussed. The Vyazovkin equation has been adapted to CRTA data and, a modification of this equation, to account for pressure correction term in the reaction rate was achieved. To check the equations developed in this paper, the standard isoconversional procedure has been modified, instead of a set of experiments performed under different heating rates (or reaction rates C in the case of CRTA) for a given conversion we use a set of experiments under different pressure of the gas self-generated in the reaction at one heating rate β (or reaction rate C), respectively.The results obtained allow for trustworthy estimates of the activation energy from advanced isoconversional method in reaction systems whose kinetics are affected by the pressure of the gases self-generated by the reaction. Theoretical considerations are verified on simulated non-isothermal TG, and non-isothermal non-linear controlled rate thermal analysis (CRTA) data. Experimental data of calcite have been used.     

Reverse Spin‐Crossover and High‐Pressure Kinetics of the Heme Iron Center Relevant for the Operation of Heme Proteins under Deep‐Sea Conditions

By design of a heme model complex with a binding pocket of appropriate size and flexibility, and by elucidating its kinetics and thermodynamics under elevated pressures, some of the pressure effects are demonstrated relevant for operation of heme‐proteins under deep‐sea conditions. Opposite from classical paradigms of the spin‐crossover and reaction kinetics, a pressure increase can cause deceleration of the small‐molecule binding to the vacant coordination site of the heme‐center in a confined space and stabilize a high‐spin state of its Fe center. This reverse high‐pressure behavior can be achieved only if the volume changes related to the conformational transformation of the cavity can offset the volume changes caused by the substrate binding. It is speculated that based on these criteria nature could make a selection of structures of heme pockets that assist in reducing metabolic activity and enzymatic side reactions under extreme pressure conditions.     

Pressurized CO<Subscript>2</Subscript>-enhanced gasification of coal

Carbon dioxide was considered as a co-gasifying agent in a coal gasification reactor. The work presented herein describes the simulation results for the process and the experimental data on coal char gasification with CO₂ addition as the rate-controlling step for the entire process. To study the potentially beneficial effect of the introduction of CO₂ into the gasification system, several simulations were conducted using the commercial process simulation software ChemCAD 6.3^®. The results of a Gibbs equilibrium reactor were evaluated. The Boudouard reaction is a critical path for the development of this process, and the kinetics were studied experimentally. Four chars derived from the pyrolysis of Polish coals of different origins were selected for the experiments. The kinetic characteristics of this system were examined using a custom-designed pressurized fixed-bed reactor. To determine the effect of pressure on the gasification rate, several preliminary studies on the gasification of coal chars were performed isothermally at the temperature of 950 °C and pressures of 1, 10, and 20 bars. In contrast to the thermodynamic calculations, the experimental data revealed that increasing the CO₂ pressure leads to a higher reaction rate for medium-rank coal chars and low-rank lignite coal char, resulting in higher efficiency for carbon monoxide production. The pressure influences the reactivity more strongly when varied from 1 to 10 bars; a further increase in pressure affects the rate almost insignificantly. The observed behavior representing the changes in carbon conversion degree during gasification is satisfactorily described by the grain model.     

Pressure catalyzed bond dissociation in an anthracene cyclophane photodimer

The anthracene cyclophane bis-anthracene (BA) can undergo a [4 + 4] photocycloaddition reaction that results in a photodimer with two cyclobutane rings. We find that the subsequent dissociation of the dimer, which involves the rupture of two carbon-carbon bonds, is strongly accelerated by the application of mild pressures. The reaction kinetics of the dimer dissociation in a Zeonex (polycycloolefin) polymer matrix were measured at various pressures and temperatures. Biexponential reaction kinetics were observed for all pressures, consistent with the presence of two different isomers of bis(anthracene). One of the rates showed a strong dependence on pressure, yielding a negative activation volume for the dissociation reaction of ΔV(++) = -16 ?(3). The 93 kJ/mol activation energy for the dissociation reaction at ambient pressure is lowered by more than an order of magnitude from 93 to 7 kJ/mol with the application of modest pressure (0.9 GPa). Both observations are consistent with a transition state that is stabilized at higher pressures, and a mechanism for this is proposed in terms of a two-step process where a flattening of the anthracene rings precedes rupture of the cyclobutane rings. The ability to catalyze covalent bond breakage in isolated small molecules using compressive forces may present opportunities for the development of materials that can be activated by acoustic shock or stress.     

Morphology and mechanical property of high-density polyethylene parts prepared by gas-assisted injection molding

The crystal morphology, melting behavior, and mechanical properties of high-density polyethylene (HDPE) samples obtained via gas-assisted injection molding (GAIM) under different gas pressures were investigated. Moreover, the non-isothermal crystallization kinetics of HDPE under different cooling rates was also studied. The obtained samples were characterized via differential scanning calorimetry, two-dimensional wide-angle X-ray scattering (2D-WAXS), tensile testing, dynamic mechanical analysis (DMA) and scanning electron microscopy techniques. It was found that the properties were intimately related to each other. Macroscopically, the flow-induced morphology of the various HDPE samples was characterized with a hierarchical crystalline structure, possessing oriented lamellar structure, shish?Ckebab structure, and common spherulites in the skin, sub-skin, and gas channel region, respectively. The 2D-WAXS results demonstrated that the degree of orientation of the high gas pressure sample was larger than that of the low pressure sample at the corresponding layer. The tensile testing results of GAIM parts showed that the mechanical properties of the GAIM parts were improved with an increase of the gas pressure. Furthermore, the DMA was utilized to obtain the dynamic mechanical properties of the GAIM samples, and the results indicated that significant improvement of the orientation was observed with an increase of the gas pressure.