生物质热解油气化试验研究

生物质是一种环境友好可再生资源，可以通过多种途径转化为液体燃料。生物质热解液化即是在缺氧状态下对生物质进行快速加热，然后再对热解产物进行快速冷凝，最后获得一种称为生物油的液体燃料的技术。该技术以及生物油的特点主要有：热解液化温度为500℃，远低于生物质热解气化所     

预处理技术在生物质热化学转化中的应用

随着化石燃料的不断消耗和气候的变化,生物质能作为一种可再生能源越来越受到关注。生物质可以通过生物法和热化学法转化成有用的燃料,热化学转化技术因其可以将生物质高效地转化生成气体、液体和固体燃料使其占有主导地位。对生物质进行预处理可以改变其物理化学特性,并且这些改变影响着后期热化学转化生物质产品的品质和收率。本文综述了生物质预处理技术在热化学转化技术方面的应用进展。对生物质进行烘焙预处理改变其可磨性,疏水性。生物质热裂解之前对原料进行脱灰分减少了生物质中的灰分,改变了生物质热裂解液化的产品分布。预处理液化相对直接高压液化生物油收率大大提高,同时最优化反应温度也大大降低。     

生物质热解液化与美拉德反应

对生物质热解液化和美拉德反应进行了介绍,指出美拉德反应不仅存在于生物质热解液化过程中,而且通过引入适量氨等调控措施,可以促进美拉德反应有选择性地生成吡嗪类杂环化合物等高值化学品,然后再通过分级冷凝将生物油分为化工生物油和燃料生物油,前者用于分离提取高值化学品,后者用于锅炉和窑炉的燃料.引入美拉德反应后,生物质热解液化技术经济性将会得到根本性的改善.     

纤维素与废轮胎微波共热解规律及产物特性

采用热重分析仪(TG)、微波共热解实验装置、红外分析仪(FTIR)以及气质联用仪(GC-MS)考察了纤维素与废轮胎微波共热解过程变化规律及产物生成特性.研究表明,不同共混比例[有效氢碳比(H/Ceff)为0.2,0.4,0.6]下热失重残炭率均低于理论值,微波共热解产物热解油产率相比理论值分别提高了4.7%,6.4%和6.0%,说明纤维素与废轮胎共热解过程存在协同效应,有利于液体产物热解油的生成.废轮胎微波热解油中检测到了79.5%的多环芳烃(PAHs),由于纤维素的加入氧自由基的作用使得热解油中PAHs完全消失,转化为高附加值的含氧有机物,热解油品质得到提高.     

纤维素与草酸的慢速和快速共热解反应特性研究

本研究利用热重-傅里叶变换红外光谱和卧式固定床热解反应装置，探究了纤维素与草酸的慢速和快速共热解反应特性。慢速共热解的失重曲线包括草酸分解和纤维素分解两个阶段，由于草酸与纤维素分解不同步，草酸主要通过其分解形成的挥发分影响纤维素的分解，且影响并不明显。而在快速共热解中，草酸与纤维素同步热解，原料及挥发分之间有着充分的交互反应，因此，草酸对纤维素的三相热解产物具有显著影响。相比于纤维素单独快速热解，快速共热解形成的生物油中左旋葡聚糖、左旋葡萄糖酮含量减少，1,4∶3,6-二脱水-α-D-吡喃葡萄糖含量显著提高；热解气中CO减少，CO₂增多；此外，纤维素分解更为彻底，热解炭具有更高的芳香化程度。     

玉米秸热解动力学研究

生物质能具有低硫和二氧化碳零排放的特点，其在能源结构中的地位越来越重要。作为一种高效生物质能转化途径，热化学转化可获得气、液和固态多种能源产物。其中，热解是热化学转化中最为基本的过程，是气化、液化及燃烧过程的初始和伴生反应，对热解的分析有助于热化学转化过程控制及高效转化工艺的开发。热解动力学是表征热解过程中反应过程参数对原料转化率影响的重要手段，通过动力学分析可深入了解反应过程和机理，预测反应速率及难易程度，为生物质热化学转化工艺的研究开发提供重要的基础数据。国外对纤维素热解动力学已进行了一些研究，但生物质作为纤维素、半纤维素、木质素等的复杂聚合物，其热解行为与单纯纤维素差别较大。因此本文的热解研究集中在玉米秸这种常见的软质秸秆类生物质原料。     

离子液体作用下微波辐照生物质快速热解制备生物质油(英文)

以离子液体1-丁基-3-甲基咪唑氯([Bmim]Cl)和1-丁基-3甲基咪唑四氟化硼([Bmim]BF4)为催化剂,在微波加热作用下,研究了稻草和锯屑的热解。微波加热20 min,稻草和锯屑的生物油产率分别为38%和34%。考察了微波加热时间、微波功率和离子液体用量对生物质油产率的影响。当以相同的离子液体为催化剂时,稻草微波热解得到的生物质油产率大于锯屑的。生物油成分主要有糠醛、醋酸和1-羟基-2-丁酮等,其含量主要取决于生物质原料和加入的离子液体的类型。     

钾元素对生物质及其三组分热解的影响

采用机械混合法将KCl加入到纤维素、半纤维素、木质素以及稻壳和稻壳模拟物等生物质中,得到了一系列不同K含量的生物质样品,通过热重(TG)实验考察了K元素对生物质热解特性的影响.结果表明,K元素对生物质三组分热解特性的影响比较复杂,纤维素的最大热解失重速率随着KCl添加量的增加而降低,但KCl对半纤维素和木质素热解特性的影响不显著.无论是否添加KCl,模拟生物质的热解特性均可以认为是三组分热解的简单叠加.但酸预处理稻壳三组分间的稳定结构,导致其DTG曲线在300 ℃左右的热解峰由稻壳模拟物的尖峰变为肩峰,其热解焦炭收率也比稻壳模拟物的略低.此外,实验还采用浸渍法向酸预处理稻壳中添加了KCl.TG实验结果表明,K元素的存在对生物质热解具有一定的催化作用,但KCl的添加方式不同,生物质的热解特性有明显差别,生物质样品经机械混合添加KCl后,其热解焦炭收率呈下降趋势(纤维素除外),浸渍法添加的KCl导致酸预处理稻壳的最大热解失重速率和焦炭收率升高.     

生物质加压液化制备甲基糖苷与酚类物质

以甲醇为液化剂、浓硫酸为催化剂,对竹子、杨木、松木和桉木四种生物质原料的加压液化进行了实验研究。结果表明,在200℃下反应30 min后,这些生物质原料可转化得到气体、固体残渣和液体生物油三种产品,且竹子的液化率最高。将竹子液化产物进一步分级处理,得到烷基多糖苷和木素解离多酚两类化学品。其中,多糖苷产品的主要成分为己糖苷类化合物,占83.38%(质量分数);多酚类产品的主要成分为4-乙基-2-甲氧基苯酚、丁香酚和3,4-二甲氧基苯酚等,占65.79%(质量分数)。同时,根据原料的物质构成和液化油的组成结构分析,提出了液化反应的机理:纤维类生物质中的纤维素和半纤维素在酸性条件下发生醇解反应生成甲基糖苷,小部分甲基糖苷进一步转化生成乙酰丙酸甲酯;原料中的木质素在降解过程中,由于酚羟基和甲氧基的供电子效应,使Cα-Caromatic键发生断裂,生成苯酚、愈创木酚等酚类物质。     

微拟球藻热解及其催化热解制备生物油研究

在氮气气氛下对微拟球藻直接热解及其在H-ZSM-5上的催化热解实验进行了研究。在573K～773K考察了热解温度对热解油产物分布的影响。与木质纤维素生物质的热解相比,微拟球藻的热解不仅温度更低,而且油的收率更高。催化剂H-ZSM-5在热解中起到了脱极性官能团和芳构化的作用,使得热解油中的芳香族化合物含量增多,极性化合物含量减少。与木质纤维素生物质相比,微拟球藻热解获得的油热值更高,适合进一步加工为燃油。     

柳树河油页岩微波干燥及其对热解特性的影响

在对家用微波炉改造基础上搭建了微波干燥实验台,研究了柳树河油页岩微波干燥特性及对热解特性的影响。结果表明,微波干燥所需的时间为传统干燥所需时间的20%;微波干燥速率要明显大于传统干燥速率;Page模型适用于描写柳树河油页岩微波干燥过程。微波干燥的油页岩同热风干燥后及原样油页岩的热解活化能随转化率的变化曲线基本一致,整体呈先上升后下降的趋势,在转化率为0.7时达到最大值;热解活化能在80~200 kJ/mol变动;微波干燥油页岩热解反应有机质分解段的活化能增加。     

Microwave drying of granules containing a moisture-sensitive drug: a promising alternative to fluid bed and hot air oven drying

The impact of microwave drying and binders (copolyvidone and povidone) on the degradation of acetylsalicylic acid (ASA) and physical properties of granules were compared with conventional drying methods. Moist granules containing ASA were prepared using a high shear granulator and dried with hot air oven, fluid bed or microwave (static or dynamic bed) dryers. Percent ASA degradation, size and size distribution, friability and flow properties of the granules were determined. Granules dried with the dynamic bed microwave dryer showed the least amount of ASA degradation, followed by fluid bed dryer, static bed microwave oven and hot air oven. The use of microwave drying with a static granular bed adversely affected ASA degradation and drying capability. Dynamic bed microwave dryer had the highest drying capability followed by fluid bed, static bed microwave dryer and conventional hot air oven. The intensity of microwave did not affect ASA degradation, size distribution, friability and flow properties of the granules. Mixing/agitating of granules during drying affected the granular physical properties studied. Copolyvidone resulted in lower amount of granular residual moisture content and ASA degradation on storage than povidone, especially for static bed microwave drying. In conclusion, microwave drying technology has been shown to be a promising alternative for drying granules containing a moisture-sensitive drug.     

Gas chromatographic-mass spectrometric study of the oil fractions produced by microwave-assisted pyrolysis of different sewage sludges

The pyrolysis of sewage sludge was studied in a microwave oven using graphite as microwave absorber. The pyrolysis temperature ranged from 800 to 1000 degrees C depending on the type of sewage sludge. A conventional electrical furnace was also employed in order to compare the results obtained with both methods. The pyrolysis oils were trapped in a series of condensers and their characteristics such as elemental analysis and calorific value were determined and compared with those of the initial sludge. The oil composition was analyzed by GC-MS. The oils from the microwave oven had n-alkanes and 1-alkenes, aromatic compounds, ranging from benzene derivatives to polycyclic aromatic hydrocarbons (PAHs), nitrogenated compounds, long chain aliphatic carboxylic acids, ketones and esters and also monoterpenes and steroids. The oil from the electric oven was composed basically of PAHs such as naphthalene, acenapthylene, phenanthrene, fluoranthene, benzo[a]anthracene, benzofluoranthenes, benzopyrenes, indenepyrene, benzo[ghi]perylene, and anthanthrene. In contrast, these compounds were not produced in the case of microwave-assisted pyrolysis.     

The drying of sulphide-bearing materials in a microwave oven: A caveat

The drying of sulphide-bearing materials in a microwave oven should be undertaken with caution. Several sulphide minerals and sulphide-bearing materials have shown a susceptibility to oxidation (which may even be violent) during microwave drying and this could affect the results of subsequent work on these materials.     

Corundum impregnation conditions for preparing supported Ni catalysts for the synthesis of a uniform layer of carbon nanofibers

Impregnation techniques for corundum (S _BET = 0.5 m²/g) as a support for Ni catalysts for C₃–C₄ alkane pyrolysis into catalytic filamentous carbon (CFC) are compared. The effects of the following factors on the uniformity of the active component (Ni) deposition on the inert support and on the CFC yield (g CFC)/(g Ni) are reported: (1) pH of the nickel nitrate solution, (2) presence of aluminum(III) nitrate in the solution, (3) addition of viscosifying agents (glycerol, glucose, sucrose) to the solution, (4) catalyst calcination conditions before pyrolysis, and (5) catalyst drying technique. The surface morphology of the Ni catalysts and of the carbon deposits resulting from the catalytic pyrolysis of C₃–C₄ alkanes in the presence of hydrogen has been investigated by scanning electron microscopy. The optimum way of preparing the supported Ni catalysts is by carrying out the incipient wetness impregnation of corundum with a nickel nitrate solution (0.05–0.1 mol/l) containing glycerol (20–25 vol %), drying the product in a microwave oven, and burning away the glycerol before alkane pyrolysis.     

Influence of feed characteristics on the microwave-assisted pyrolysis used to produce syngas from biomass wastes

A series of biomass wastes (sewage sludges, coffee hulls and glycerol) were subjected to pyrolysis experiments under conventional and microwave heating. The influence of the initial characteristics of the raw materials upon syngas production was studied. Glycerol yielded the highest concentration of syngas, but the lowest H₂/CO ratio, whereas sewage sludges produced the lowest syngas production with the highest H₂/CO molar ratio. Coffee hull displayed intermediate values for both parameters. Microwave heating produced greater gas yields with elevated syngas content than conventional pyrolysis. Moreover, microwave pyrolysis always achieved the desired effect with temperature increase upon the pyrolysis products, whatever biomass material was employed. This could be due to the hot spot phenomenon, which only occurs under microwave heating. In addition, a comparison of the energy consumption of the traditional and microwave-assisted pyrolysis is also presented. Results point at microwave system as less time and energy consuming in comparison to conventional system.     

微藻微波催化裂解研究及动力学分析

采用微波设备对微藻粉末进行热解实验,分别研究了活性炭、H₃PO₄、NaOH、MgCl₂、MgO对微藻微波裂解的影响,以及不同功率(200、600、900 W)下微藻裂解失重的变化。结果表明,对于所研究的五种无机添加剂,均能够显著增加固体产物产率,明显减少气体产物产率,添加剂对液体产率的影响不是很显著,但H₃PO₄和MgCl₂使液体产率提高,NaOH使液体产率降低。微藻的微波裂解过程大致可以分成脱水、干燥、快速裂解和缓慢裂解四个阶段。采用Flynn-Wall-Ozawa法对微藻微波裂解进行动力学分析,计算出相应的微藻快速裂解阶段的活化能,活化能基本上随反应的进行而增大。     

沉积-沉淀-微波干燥法制备金属氧化物负载的金簇合物及其在CO氧化和 硫化物氧化反应中的催化性能

采用沉积-沉淀法再辅以微波干燥和焙烧制备了金属氧化物负载的金簇合物和小的金纳米粒子.干燥方法影响了金颗粒尺寸.在炉干燥过程中Au(III)因部分还原而致使Au聚集.相反,在微波干燥下,因快速和加热均一而使Au(III)得以保持,在Al2O3上负载的Au颗粒尺寸小至1.4 nm.该法可用于具有几种不同微波吸收效率的金属氧化物载体,如MnO2,Al2O3和TiO2.这些催化剂在低温CO氧化和硫化物选择有氧氧化反应中的催化活性比常规方法制备的更高.     

生物质废弃物的热解研究

生物质能是可再生能源,在生长过程中通过光合作用将碳和能量固定下来,利用生物质能CO2排放很少.为实现可持续能源生产和减少温室气体排放的目的,中国已于2006年1月开始实施《中华人民共和国可再生能源法》.     

Efficient preparation of nanocrystalline anatase TiO2 and V/TiO2 thin layers using microwave drying and/or microwave calcination technique

This study has demonstrated that the synthesis of TiO₂ and V/TiO₂ thin layers may be significantly improved and extended if microwave energy is employed during the drying and/or calcination step. Thin nanoparticulate titania layers were prepared via the sol-gel method using titanium n-butoxide as a precursor. As prepared films were then analyzed by means of various characterization techniques (Raman spectroscopy, UV/Vis, AFM, XPS) in order to determine their functional properties. The photocatalytic activities of prepared layers were quantified by the decoloring rate of Rhodamine B. All thermal treatments in microwave field were done in the same manner, by using an IR pyrometer in the microwave oven and monitoring the temperature of the heating. Nevertheless the microwave and thermally prepared materials were different. This in turn may lead to differences in their functional and also photocatalytic properties.