聚苯乙烯的催化裂解研究

由于塑料性质稳定,难以自然降解,其废弃物不仅严重污染环境,更造成了资源浪费.因此,废旧塑料的再资源化对环境保护和可持续发展有着重要意义.废塑料再资源化回收技术是指将废塑料热裂解或催化裂解、回收燃料油和化工原料的技术~([1,2]).     

基于TG-FTIR的生物质催化热解试验研究

运用热重－傅里叶红外光谱联用技术(TG-FTIR),以麦秸为研究对象,探讨催化与非催化条件下生物质的热解挥发分析出特性,分析研究热解温度、催化剂种类对生物质热解主要析出产物的影响。通过热重TG和DTG曲线,获得了相关热解特性参数及动力学参数。结果表明,添加NiO和CaO存在两个失重峰,并促进麦秸热解反应进行,降低表观活化能,其中NiO对提高热解析出产率作用更显著。通过红外光谱对热解产物实时测量的分析表明,CO与CO2的析出与失重峰基本一致,而CH4的析出滞后于前两者。添加NiO和CaO有利于减少热解产物中的CO2的浓度,促进挥发分产物CO、CH4的生成。其中CaO更有利于生物质在温度800℃以下的热解性能改善,而NiO在800℃以上具有更好的催化作用。     

Thermogravimetric studies on catalytic effect of metal oxide nanoparticles on asphaltene pyrolysis under inert conditions

This study investigated the catalytic effect of NiO, Co₃O₄ and Fe₃O₄ nanoparticles toward asphaltene thermal decomposition (pyrolysis) under inert conditions. Asphaltene adsorbed onto the selected nanoparticles were subjected to thermal decomposition up to 800?°C in a thermogravimetric analyzer. The presence of nanoparticles caused a significant decrease in the asphaltene decomposition temperature and activation energy. Activation energies for the process were calculated using the Ozawa?CFlynn?CWall method. All the selected metal oxide nanoparticles showed high catalytic activity toward asphaltene decomposition in the following order NiO?>?Co₃O₄?>?Fe₃O₄. This study confirms that metal oxide nanoparticles can significantly enhance the thermal decomposition of heavy hydrocarbons, like asphaltenes.     

应用TG-FTIR联用研究催化剂对煤热解的影响

用TG-FTIR联用技术研究了碱金属、碱土金属和过渡金属对宝日希勒褐煤和包头烟煤热解的催化作用和挥发分析出的影响。结果表明,各种催化剂对褐煤和烟煤热解的催化效果分别为Ni>Fe~Ca>K和Ca~Fe>Ni>K,K2CO3对煤的热解没有明显的催化作用。催化剂使褐煤和烟煤热解转化率增加的最大值分别为10.1％和6.4％。烟煤热解生成的CH4比褐煤的多,不同的催化剂使煤热解挥发产物CO2、H2O、CH4和CO增加的幅度不一样,催化效果与温度和煤的变质程度有关。     

Non-isothermal pyrolysis of used lubricating oil and the catalytic effect of carbon-based nanomaterials on the process performance

Pyrolysis is a commonly used method for the recovery of used lubricating oil (ULO), which should be kinetically improved by a catalyst, due to its high level of energy consumption. In this research, the catalytic effects of carbon nanotube (CNT) and graphene nanoplatelets on the pyrolysis of ULO were studied through thermogravimetric analysis. First, the kinetic parameters of ULO pyrolysis including activation energy were calculated to be 170.12 and 167.01 kJ mol^?1 by FWO and KAS methods, respectively. Then, the catalytic effects of CNT and graphene nanoplatelets on pyrolysis kinetics were studied. While CNT had a negligible effect on the pyrolysis process, graphene nanoplatelets significantly reduced the temperature of maximum conversion during pyrolysis from 400 to 350 °C, due to high thermal conductivity and homogenous heat transfer in the pyrolysis process. On the other hand, graphene nanoplatelets maximized the rate of conversion of highly volatile components at lower temperatures (<?100 °C), which was mainly due to the high affinity of these components toward graphene nanoplatelets and also the effect of nanoplatelets’ edges which have free tails and can bond with other molecules. Moreover, graphene nanoplatelets decreased the activation energy of the conversion to 154.48 and 152.13 kJ mol^?1 by FWO and KAS methods, respectively.

     

不同热裂解温度下ZSM-5对玉米秸秆催化热裂解烃类选择性影响

为探讨不同热裂解温度下ZSM-5对玉米秸秆催化热裂解特性及烃类选择性的影响,本研究利用TGA对比有无ZSM-5时玉米秸秆的热裂解失重曲线,利用Py-GC/MS对比玉米秸秆在450、500、550和600℃下的热裂解和催化热裂解产物分布。结果表明,ZSM-5的使用可以降低玉米秸秆最高分解速率时对应的热裂解温度,降低温度为23℃。未使用ZSM-5时,热裂解产物种类以及烃类选择性均随热裂解温度的升高不断增加,在600℃时,烃类选择性达到最高,为11.33%;使用ZSM-5后,烃类产率随热裂解温度的升高先增加后减少,在550℃时,烃类选择性达到最高,为29.24%。使用ZSM-5后,玉米秸秆催化热裂解主要产物中出现了甲苯、茚、萘、二甲基萘等烃类,甲苯的最高产率为4.76%,萘的最高产率为3.96%。     

Analysis of plasma-polymerized hydrocarbons by pyrolysis/gas chromatography

Plasma-polymerized oils, films and powders obtained from ethylene, acetylene, butadiene, and benzene were characterized by flash pyrolysis and gas chromatography (P/GC). None of the pyrograms resembled those of commercial polyethylene, polybutadiene, or polystyrene. Each of the plasma-polymer pyrograms did exhibit essentially the same fragments up to C₈, albeit in a different distribution, indicating that all samples are structurally similar. Analysis of the P/GC data shows these materials to contain a random arrangement of side chains, crosslinks, double bonds, and aromatic structures. Changes in the fragment distribution were obvious when the sample was a powder, solid film, or oily film produced from the same monomer. It was shown that powder products generally have a higher concentration of branches and/or crosslinks than the oil or film products. There are also differences in the pyrograms of products of the same form derived from dissimilar monomers. The results obtained from P/GC generally support those derived from infrared or NMR measurements performed earlier.     

An experimental and theoretical study of the catalytic effect of quaternary ammonium salts on the oxidation of hydrocarbons

The enhancement in the autoxidation of ethylbenzene by molecular oxygen in the presence of quaternary ammonium salts (QAS) was investigated from the experimental and theoretical points of view. The primary effect of the addition of QAS to the reaction medium was an increase in ethylbenzene conversion. Quantum chemical calculations, using B3LYP hybrid functional, revealed a weakening of C-O and O-H bonds of the hydroperoxide. These effects favor the formation of ethylbenzenyl and peroxyl radicals, respectively, both of which are involved in the propagation reaction that leads to the formation of hydroperoxide, the desired final product.     

Soot formation in isothermic pyrolysis of mixtures of various hydrocarbons

Soot formation upon the pyrolysis of binary and ternary mixtures of various hydrocarbons is studied. The experimental values of the specific surface areas S_sp of soot particles are compared to the calculated values obtained assuming that any of the hydrocarbons in the mixture are inhibitors. Analysis of the results obtained for the mixtures containing acetylene shows that, when the acetylene concentration is higher than a certain value, the nuclei of soot particles are formed from acetylene, whereas other hydrocarbons participate in     

Principles of catalytic dehydrogenation of alkyl aromatic hydrocarbons

Russian Chemical Bulletin -     

CO2 enhanced carbon nanotube synthesis from pyrolysis of hydrocarbons

We report on the role of CO(2) in improving carbon nanotube yield and crystallinity from catalytic chemical vapor deposition of hydrocarbons.     

Fast catalytic hydroxylation of hydrocarbons with ruthenium porphyrins

Ruthenium porphyrin complexes such as carbonylruthenium(II) tetrakispentafluorophenylporphyrin [Ru(II)(TPFPP)(CO)] were found to be efficient catalysts for the hydroxylation of alkanes in the presence of 2,6-dichloropyridine N-oxide as the oxidant under mild, nonacidic conditions. Up to 14 800 turnovers (TO) and rates of 800 TO/min were obtained for the hydroxylation of adamantane. The hydroxylation of cis-decalin afforded cis-9-decalol and cis-decalin-9,10-diol, exclusively, thus, excluding a long-lived radicals mechanism. The kinetics of product evolution in a typical catalytic oxygenation showed an initial induction period followed by a fast, apparently zero-order phase with maximum rates and high efficiencies. Deuterium isotope effects (kH/kD) in the range of 4.2-6.4 were found for the hydroxylation of alkanes. A Hammett treatment of the data for the oxidation of para-substituted toluene derivatives showed a linear correlation with a highly negative rho+ value of -2.0. On the basis of kinetic and spectroscopic evidence, Ru(VI)(TPFPP)(O)2, Ru(II)(TPFPP)(CO), and Ru(IV)(TPFPP)Cl2 observed during catalysis were ruled out as candidates for the active catalyst responsible for the high efficiencies and turnover rates in the oxidation reactions. The fastest rates of adamantane hydroxylation with 2,6-dichloropyridine N-oxide were achieved by the reductive activation of Ru(IV)(TPFPP)Cl2 with a zinc amalgam. This redox activation is consistent with the formation of an active Ru(III) intermediate in situ by a one-electron reduction of the Ru(IV) porphyrin. EPR spectra characteristic of Ru(III) have been observed upon the reduction of Ru(IV)(TPFPP)Cl2 with a zinc amalgam. In the adamantane oxidation mediated with Ru(III)(TPFPP)(OEt), it was found that, during this process, the Ru(III) porphyrin was gradually converted to a dioxoRu(VI) porphyrin. Concomitant with this conversion, the reaction rates decreased. Catalyst activation was also stimulated by autoxidation of the solvent CH2Cl2. On the basis of these data, a mechanism is proposed that incorporates a "fast" cycle involving metastable Ru(III) and oxoRu(V) intermediates and a "slow" oxidation cycle, mediated by oxoRu(IV) and trans-dioxoRu(VI) porphyrin complexes.     

Gasification and catalytic conversion of biomass by flash pyrolysis

The influence of the water content, the gasification atmosphere and the action of inorganic catalysts on biomass pyrolysis is discussed. The pyrolysis conditions are characterized by a heating rate of a wood sample of 250–300°C/s and a residence time of the gas in the hot zone of the reactor of less than 1 s. Volumes, carbon contents, weights and energy balances at different temperatures (600–1000°C) are tabulated. The total volume of pyrolysis gas and the yields increase with increasing temperature and water content. This increase is especially due to the production of hydrogen. A large part of the gasified hydrogen comes from water. Water that has not been driven off from green wood is more gasifiable than water that is re-added or from the atmosphere. Three types of catalysts were tested: alumina, aluminosilicate material and nickel-supported catalyst. The results show that it is possible to control the distribution of gas species by controlling the water content of the biomass and selecting the catalyst on which the wood is pyrolysed. A nickel catalyst on mordenite seems to be very efficient in directing pyrolysis gas production towards synthesis gas.     

基于Fe负载的HZSM-5催化热解制备生物油实验研究

通过离子交换法制备含2%Fe(质量分数)的HZSM-5催化剂,采用X射线衍射仪(XRD)、激光粒度分析仪以及比表面积及孔径分析仪对催化剂进行表征,并在550℃下进行木屑的催化热解实验。对无催化剂和不同比例催化剂条件下得到的生物油进行GC-MS分析,结果表明,在Fe负载的HZSM-5作用下,生物油产率明显升高(最大增幅7%),轻质组分产率明显升高,重质组分产率略微升高。同时,轻质组分中的酮类、呋喃等含氧化合物含量降低,酚类、酸含量升高;重质组分中的酮类、呋喃类等含氧化合物含量明显降低,酚类、萘类含量明显增多。Fe负载的HZSM-5催化剂对木屑的热解反应有较好的催化效果,加强了对热解初始蒸汽的择形修饰,从而抑制了生物质三组分木质素初始热解产物中的醌类等容易一次或二次结焦物质的生成,孔道结构对蒸汽的二次反应被抑制,产物向较小分子的轻质产物上富集。     

催化热解生物质制取富氢气体的研究

在实验室自制的固定床反应器上, 考察了秸秆和锯屑的热解行为, 研究了热解产物分布特别是富氢气体的体积分数和产率, 着重研究了（5种金属氧化物和2种碳酸盐催化剂）的催化效果。结果表明,温度从500 ℃提高到850 ℃, 秸秆和锯屑的热解气产率分别从29.0%提高到40.6%, 35.0％提高到46.5%, 而对应的富氢气体的体积分数分别从41.2％提高到48.2%, 40.6％提高到47.0%；在5种金属氧化物中，Cr2O3显示了最好的催化效果，在750 ℃时对应的热解气产率与不使用催化剂相比提高了10％，富氢气体的体积分数提高了13％；催化剂（CaCO3和Na2CO3）占生物质的质量分数对热解气和富氢气体产率有明显的影响，当质量分数从0增加到30％时， 热解气和富氢气体产率增加较明显，而后其值的增加可以忽略， 因此推荐使用的催化剂质量分数为30％。     

催化热解废轮胎制衍生油

催化热解废轮胎对于资源利用及环境保护具有重要意义,近年来引起人们关注.在废轮胎胶粉热解反应中加入催化剂,不仅会加速胶粉裂解速率,缩短反应时间,而且可以通过催化剂择形催化改变产物分布,从而提高目的产物衍生油的收率和性能.国内外对废轮胎催化热解已做了大量研究,以期提高衍生油中高附加值单环芳烃的含量,同时降低S, N和Cl含量,虽然已取得较大进展,但衍生油收率较低,大大降低了该技术的可行性.
　　本文采用带搅拌器的1000 mL不锈钢反应器,在常压条件下研究了反应温度和催化剂类型对废轮胎胶粉热解反应及产物衍生油性能的影响,通过元素分析、馏程模拟和色谱-质谱等表征手段检测了衍生油的理化性能.结果表明,在废轮胎胶粉热解反应过程中,随反应温度上升,出油速率先增加后降低.至500 oC时,热解衍生油收率最高达55.65 wt%,所得衍生油呈黑棕色,具有轻质油含量低、S和N含量高、粘度低和流动性好的特点,其轻质芳烃含量低,却含有大量可以转变为芳烃的脂肪烃类.因此,为了提高衍生油中轻质油和轻质芳烃收率,降低S和N含量,尽量维持较高的衍生油收率,在热解反应过程中引入少量ZSM-5, USY,β, SAPO-11和ZSM-22等常见催化剂,利用催化剂独特的孔道结构和酸分布,达到定向催化和转化的目的,提高轻质芳烃含量.同时,为了克服催化剂与胶粉难以接触进行反应的问题,在反应温度升至200 oC时,维持一定时间保证胶粉发生溶胀和液化反应形成液体烃类,使得催化剂不仅能够均匀分散于液体烃中与其接触进行反应,而且有效提高了反应物料与催化剂之间传质传热效率,使得裂解反应在均相中进行,降低因传热不均匀而造成的结焦和过度裂化反应.在催化热解过程中,1.0 wt%催化剂的加入可明显缩短反应时间,在保证衍生油收率基本不变的情况下,获得的衍生油呈黄棕色,轻质油收率较高为70–75 wt%, S和N含量分别降至0.3–0.58wt%和0.78–1.0 wt%.以具有较高酸性和孔径分布的ZSM-5, USY,β和SAPO-11为催化剂时,衍生油中总芳烃含量可达到50 wt%,其中单环芳烃含量高达45 wt%.