气相色谱法测定高浓度煤层气中的甲烷和乙烷

正煤层气是煤的伴生矿产资源,与天然气是同一种性质的可燃性气体,其组成主要为甲烷,还含有少量的氧气、氢、二氧化碳以及烃类化合物,是一种热值高且无污染的新型能源~([1])。一般把煤炭开采过程抽排出甲烷浓度大于25%的瓦斯称为高浓度煤层气。煤层气中的甲烷浓度是确定煤气资源储量、丰度及开采的重要参数,可综合煤层的面积、厚度等条件预测煤矿的产气能力,并制定勘探开发方案。因     

气相色谱法测定碳酸二甲酯的含量

选用HP-INNOWAX毛细管色谱柱及氢火焰离子化检测器(FID)，采用二阶程序升温，以正丁醇为内标物，建立了测定碳酸二甲酯(DMC)含量的气相色谱法。当DMC的体积分数(X)为0．02％～0．64％时，DMC与正丁醇的峰面积比(Y)与DMC的体积分数(X)有良好的线性关系，线性回归方程为Y=0．4427X-0．0406，相关系数r=0．9994．检出限为0．1nL。对实际样品进行测定，加标回收率为93．7％～97．0％，相对标准偏差为0．84％～1．27％。方法适用于DMC的含量分析。     

甲烷催化燃烧反应机理及催化剂研究进展

在煤矿开采及燃气轮机等工业应用或移动源领域存在甲烷大体量排放,且传统高温焚烧法会导致二次污染,因此,在低温下实现甲烷高效转化成为亟待解决的问题.从能源利用和环境保护角度,催化燃烧技术是实现甲烷废气高效净化的有效措施.本文综述了近年来催化机理和催化剂的研究进展.首先,在实验和理论基础上,总结概括了甲烷氧化机理,其中,重点...     

低浓度甲烷热氧化流向变换反应器的动态行为及余热回收研究（英文）

废弃煤矿的低体积分数甲烷(1%-3%)通常被直接排放到大气中,但其较高的升温潜势带来了严重的环境问题。在流向变换反应器中直接热氧化甲烷是一种有吸引力的解决方案,但潜在的爆炸和不稳定燃烧等风险限制了其应用。阐明低含量甲烷在流向变换反应器中热氧化的动力学行为是开发工业级反应器的基础。为此,采用数值模拟的方法分析了低含量甲烷热氧化流向变换反应器的自热操作边界,深入研究了热空气导出量对流向变换反应器行为的影响。结果显示,甲烷体积分数超过0.2%即可实现自热操作;甲烷体积分数从0.5%提升至3.0%,最高床温仍维持在1200℃左右。当甲烷体积分数超过0.5%,可以回收部分热量;相同甲烷含量条件下,最高床温随着热气抽出量的增加而增加;随着甲烷体积分数从0.5%提升到3.0%,允许导出的热空气从12.5%几乎线性地增加到32%。进一步研究发现,以30-50 s的时间间隔反向流动可以确保甲烷的完全转化和床温稳定。上述结果表明,甲烷体积分数在1%-3%时,采用热氧化处理可以实现余热回收;此外,通过调整换向时间和热空气导出量可以实现床层温度控制。     

乙醇混合燃料近红外定量分析

采用近红外光谱(NIR)透射法对乙醇混合燃料各成分进行定量分析；其中乙醇体积分数为84．5％～98．2％，汽油体积分数0～15％；通过偏最小二乘法(PLS)建立模型，乙醇含量NIR模型校正集测定系数(R^2)为0．9969，模型校正集标准差(SEE)和预测集标准差(SEP)分别为0．23和0．38，汽油含量NIR模型校正集测定系数为0．9939，模型校正集标准差和预测集标准差分别为0．38和0．39，对含量较小的干扰物质丙酮预测结果也理想；近红外和多元校正技术可作为乙醇混合燃料中成分含量测定简单、快速方法之一。     

加热速率和粒径对聚乙烯在超临界水中转化的影响

随着塑料制品的广泛使用，废塑料在中国每年呈递增趋势，在城市垃圾中特别是沿海地区废塑料的质量分数己增加到8％～10％，而体积分数达到30％以上，造成严重的“白色污染”。回收利用废塑料不仅可以解决环境污染问题，而且可以将废弃物转化为资源。废塑料降解油化可以得到价值较高的液体燃料或化工原料，是一种较为理想的回收利用方法。     

HPLC法测定苦参碱阴道凝胶中的有关物质

用HPLC法测定苦参碱阴道凝胶中的有关物质，采用ODS色谱柱，以pH=4．0的0．25％(体积分数)磷酸缓冲溶液-三乙胺-乙腈(体积比为96：0．2：4)为流动相，流速为1．0mL／min，检测波长为210nm，苦参碱的浓度为0．786～1．834μg/mL时与色谱峰面积有良好的线性关系，相关系数为0．9994。有关物质含量测定结果稳定，相对标准偏差为2．33％。     

NOx催化的甲烷气相氧化反应

 考察了没有固体催化剂时NOx对甲烷气相氧化的催化作用，并用原位红外光谱研究了CH4－O2－NOx体系随温度的变化．实验结果表明，NOx对甲烷气相氧化有很高的催化活性．在20％CH4－10％O2体系中加入0．05％～0．2％的NO后，反应温度可降低200～300℃，在650～700℃下反应时，CH4转化率和CO选择性可分别达到38％和90％，产物中的n（H2）／n（CO）比为0．4～0．7．反应产物中可观察到有甲醛、甲醇和乙烯等，通过改变反应条件可以控制各组分的相对浓度．     

茶叶中9种有机磷农药残留量快速测定方法

为建立了茶叶中9种有机磷农药的气相色谱检测方法,将试样在气相色谱仪DB—XLB色谱柱中分离,FPD检测器鉴定。结果表明,9种有机磷能够很好地分离,在0．05～1．0灿∥mL线性关系良好（r≥0．999）。在0．05—0．20mg／kg的添加水平范围内的平均回收率为78．6％～105％,相对标准偏差为1．4％～7．8％。9种有机磷方法检出限0．005～0．01mg／kg。     

SO_2对甲烷在金属铁表面还原NO的反应影响

采用卧式程序控温电加热陶瓷管反应器,在N2和模拟烟气气氛中、300~1 100℃下,研究了SO2对甲烷在金属铁及其氧化物表面还原NO反应的影响。采用XRD等手段对反应前后铁催化剂样品的组成变化进行了表征,分析了SO2在甲烷-铁脱硝反应中的作用机理。结果表明,甲烷在金属铁及氧化铁表面能够高效率地还原NO,NO还原效率不受烟气中SO2的影响。在SO2体积分数为0.01%~0.04%的N2气氛中,温度高于700℃时,金属铁上NO还原率和SO2脱除率可同时达到100%。在SO2体积分数为0.01%~0.04%的模拟烟气中,当温度高于850℃时,NO还原效率达到90%以上;温度为950℃时,NO还原效率达到98%,SO2对NO还原效率的影响可忽略。当反应温度为1 000℃时,在含0.02%SO2的模拟烟气中,甲烷的体积分数为1.13%时,持续100 h金属铁表面上的NO还原效率都能保持95%以上。     

超低浓度甲烷在Cu/γ-Al2O3催化颗粒流化床中的燃烧特性

采用流化床燃烧技术,使用自制Cu/γ-Al₂O₃颗粒作为催化剂床料,实验研究了超低浓度甲烷在流化床中催化燃烧时床层温度(450~700℃)、流化风速比ω(1.5~4)、进气甲烷体积分数(0.3%~2%)等对甲烷燃烧效率的影响。结果表明,床层温度是影响甲烷催化燃烧反应的关键因素,甲烷的转化率随着床层温度的升高而增加;床层温度达到650℃时,甲烷含量低于1%的超低浓度甲烷其转化率超过95%,继续提高床层温度至700℃且控制流化风速比ω≤2可以实现甲烷的完全转化;甲烷转化率随着流化风速和进气甲烷浓度的增加而降低,当ω>3.5时,温度对甲烷转化的影响减弱,未燃烧的甲烷含量增大。动力学实验发现,床层温度较低时,催化反应受动力学控制,测得催化反应的活化能E_a为1.26×10⁵J/mol,反应级数m为0.73,当温度t>450℃时,扩散作用影响显著,反应级数增大。     

甲烷部分氧化制合成气反应中催化剂积炭的研究(英文)

Ｎｉ／Ａｌ_２Ｏ_３催化剂上甲烷部分氧化制合成气反应是在固定床流动反应装置上进行的。考察了催化剂的床层温度、反应压力、空速和原料气配比对催化剂积炭产生的影响。实验结果表明,积炭速率随催化剂床层温度的升高而降低,当温度低于７０℃时,积炭速率骤增：积炭总是发生在催化剂床层的下段;若空速超过３．０×１０~５ｈ~（－１）,积炭速率随空速增加而明显降低。从ＦＴＩＲ实验结果可知,吸附在Ｎｉ／Ａｌ_２Ｏ_３催化剂表面上的ＣＯ,一部分歧化生成了ＣＯ_２和Ｃ。综上所述,催化剂表面积炭主要来源于以下两个反应： ２ＣＯ→Ｃ＋ＣＯ_２,ＣＯ＋Ｈ_２　＝ Ｃ＋Ｈ_２Ｏ     

Hydrogen production by catalytic decomposition of methane using a Fe-based catalyst in a fluidized bed reactor

Catalytic decomposition of methane using a Fe-based catalyst for hydrogen production has been studied in this work. A Fe/Al2O3 catalyst previously developed by our research group has been tested in a fluidized bed reactor (FBR). A parametric study of the effects of some process variables,including reaction temperature and space velocity,is undertaken. The operating conditions strongly affect the catalyst performance. Methane conversion was increased by increasing the temperature and lowering the space velocity. Using temperatures between 700 and 900℃ and space velocities between 3 and 6LN/(gcat·h),a methane conversion in the range of 25%-40% for the gas exiting the reactor could be obtained during a 6 hrun. In addition,carbon was deposited in the form of nanofilaments (chain like nanofibers and multiwall nanotubes) with similar properties to those obtained in a fixed bed reactor.     

甲烷在MoO_3／HZSM－5分子筛催化剂上的非氧催化转化

研究了反应温度、空速、Ｍｏ担载量和焙烧温度对ＭｏＯ３／ＨＺＳＭ－５催化剂上甲烷的芳构化反应的影响．ＨＺＳＭ－５分子筛的Ｂｒｏｎｓｔｅｄ酸性、孔道结构和Ｍｏ在分子筛中的分布是影响催化性能的重要因素．ＨＺＳＭ－５上Ｍｏ担载量为２～３％时活性最佳，在１０１３Ｋ反应温度下甲烷转化率可达９％，芳烃选择性大于９０％．空速影响的实验表明乙烯是反应的初始产物．在此基础上提出了＂甲烷酸助异裂活化＂的新概念、＂金属钼类碳烯中间物＂的新观点和甲烷芳构化的可能机理．     

Direct partial oxidation of methane to methanol： Reaction zones and role of catalyst location

Direct partial oxidation of methane to methanol was investigated in a specially designed reactor. Methanol yield of about 7%-8% was obtained in gas phase partial oxidation. It was proposed that the reactor could be divided into three reaction zones, namely pre-reaction zone, fierce reaction zone, and post-reaction zone, when the temperature was high enough to initiate a reaction. The oxidation of methane proceeded and was completed mostly in the fierce reaction zone. When the reactant mixture entered the post-reaction zone, only a small amount of produced methanol would bring about secondary reactions, because molecular oxygen had been exhausted in the fierce reaction zone. A catalyst, if necessary, should be placed either in the pre-reaction zone, to initiate a partial oxidation reaction at a lower temperature, or in the fierce reaction zone to control the homogeneous free radical reaction.     

Kinetics of the oxidative coupling of methane in the presence of model catalysts

The kinetics of the oxidative coupling of methane (OCM) in the presence of La/MgO and NaWMn/SiO₂ catalysts in a flow reactor at low reactant conversions was studied. It was found that, in spite of different compositions and properties of the test catalysts, the formation of ethane from methane and ethylene from ethane can be described within the framework of the Mars-van Krevelen redox model in both cases. The rate laws of side reactions, which lead to the formation of carbon oxides, are different from the rate laws of the target reactions of the conversion of methane into ethane and ethane into ethylene. The kinetic parameters required for the numerical simulation of the OCM process were determined for either of the catalysts.     

Methane oxidation in a mixed ionic–electronic conducting ceramic hollow fibre reactor module

A reactor module, consisting of six gas-tight hollow fibre membranes made of the mixed ionic–electronic conducting perovskite, , has been tested for oxygen permeation and stability during methane oxidation in the temperature range of 540 to 960°C. Rigorous leak testing was undertaken and it was demonstrated that the module could be adequately sealed. Oxygen permeation fluxes were similar to those reported by previous workers. At higher temperatures of operation, it appeared that mass transfer limited the oxygen flux, as this flux was dependent upon the flow rates on either side of the membrane. In this way, reactant flow rates could be used to manipulate the transmembrane oxygen flux. It was found that the product distribution on the methane side was dependent upon this flux, with carbon monoxide and hydrogen production being favoured at low fluxes and carbon dioxide and water production being favoured at higher fluxes. Furthermore, at low oxygen flow rates, periodic increases in the transmembrane oxygen flux were observed. The cause of this behaviour is unclear but may be as a result of phase/stoichiometric changes associated with the membrane material.     

T形微反应器共沉淀法制备Mg-Al层状双金属氢氧化物及其粒径可控性

采用T形微反应器通过共沉淀法制备了Mg-Al层状双金属氢氧化物(LDHs)纳米颗粒, 考察了流速、混合盐溶液浓度和温度等对产物粒径及其分布的影响. 实验结果表明, 所制备的LDHs样品的形貌和晶体结构与传统共沉淀法结果一致, 但本方法制备的样品粒径小、分布窄. 随着流速增大, 温度升高, 所合成的LDHs样品平均粒径减小, 分布变窄; 而随着混合盐溶液浓度的增大, 所得LDHs样品粒径增大, 分布变宽.     

Oxidative coupling of methane in a fixed bed reactor over perovskite catalyst： A simulation study using experimental kinetic model

The oxidative coupling of methane （OCM） to ethylene over a perovskite titanate catalyst in a fixed bed reactor was studied experimentally and numerically. The two-dimensional steady state model accounted for separate energy equations for the gas and solid phases coupled with an experimental kinetic model. A lumped kinetic model containing four main species CH4, O2, COx （CO2, CO）, and C2 （C2H4 and C2H6） was used with a plug flow reactor model as well. The results from the model agreed with the experimental data. The model was used to analyze the influence of temperature and feed gas composition on the conversion and selectivity of the reactor performance. The analytical results indicate that the conversion decreases, whereas, C2 selectivity increases by increasing gas hourly space velocity （GHSV） and the methane conversion also decreases by increasing the methane to oxygen ratio.     

Non-isothermal two-membrane reactors for reversible gas phase reactions

The performance of a non-isothermal two-membrane reactor for reversible chemical reactions in gas phase has been analyzed by numerical simulation. The analyzed reactions were of the form: aA = bB + cC. Two membranes, that are permeable to all the components of the reaction mixture, are supposed to be the most permeable to one of the two reaction products, satisfying the condition of reverse products permselectivities. The reactant is taken to be the slowest permeating component. A negative temperature influence on the permeabilities of components has been assumed. Co-current plug flow pattern has been accepted. It has been shown that it is possible to enhance reactant conversion above that of a conventional reactor for both endothermic and exothermic reversible reactions, including adiabatic and non-adiabatic case. By using a two-membrane reactor, considerable lowering of feed temperatures is enabled for an endothermic reaction. For endothermic reactions, there is the optimum feed temperature, whereas for exothermic reactions, the higher the temperature, the lower is the attained conversion. In reactor design, the optimal external heat exchange for both endothermic and exothermic reactions can be determinated.