半导体催化膜上泵氧甲烷氧化偶联反应的研究Ⅰ.传递体系的反应

在常压及 6 5 0℃下 ,考察了CaO ,SrO ,La2 O3,ZnO ,TiO2 ,CeO2 和MnO2 膜上外加电流为 16～ 90mA时传递物系的甲烷氧化偶联反应结果 .结果发现 ,在n型和 p型半导体催化膜上 ,CO2 ,C2 H4 和C2 H6的生成速率都随泵氧量的增加而增大 ,而C2 烃选择性随泵氧量的增加而下降 ,但 p型半导体膜上的C2 烃选择性比n型半导体膜上的要高 ;p型半导体膜上C2 烃选择性与其电导率大小顺序相一致 .增强因子的分析结果表明 ,在传递体系中 ,p型半导体膜上增强因子的值小于 1,但随泵氧量的增加而存在极大值 .在CaO膜上 ,传递体系比开路体系的C2 烃选择性高 ,且随泵氧量的增加而下降     

C_2H_3与C_2H_5OH和CH_3HCO间的脱氢反应对乙醇-碳氢混合燃料燃烧过程的影响

在QCISD(T)/6-311++G(d,p)//B3LYP/6-311G(d,p)的水平下计算了乙醇及乙醇燃烧裂解产物与C2H3之间的脱氢反应机理,利用正则变分过渡态理论(CVT)结合小曲率隧道效应模型(SCT)计算400~2000 K范围内的速率,对比OH,H及CH3等自由基相似脱氢反应速率,选择2条具有较快反应速率的通道(C2H3+C2H5OH→TS1→C2H4+C2H5O和C2H3+CH3HCO→TS4→C2H4+CH3CO).将这2个反应耦合到正庚烷/乙醇混合燃料及异辛烷/乙醇混合燃料的机理中,利用CHEMKIN程序中预混火焰模型模拟混合燃料的燃烧过程并进行路径分析.对比相应的实验数据发现,改进的动力学模型对燃烧过程中C2H3路径上相近组分的预测精度有较大改善,而对C2H3路径上较远的组分丙炔(C3H4)和乙烯基乙炔(C4H4)等影响不大.     

反应条件对甲醇直接气相羰化反应的影响

在新研制的Mo C催化剂上 ,对甲醇直接气相羰化反应工艺条件与反应气中H2 的影响进行了研究 ,结果表明此新的Mo C催化剂初活性高 ,稳定性高。优化的工艺条件为 :反应温度 30 0℃ ,甲醇进料浓度 2 3% ,CO空速30 0 0L kgcat h ,此时甲醇转化率达 50 % ,醋酸甲酯选择性达 80 % (mol) ,产物时空收率为 8mol kgcat h ,已接近甲醇在有碘化物促进剂下间接气相羰化的水平。对反应气中H2 的影响研究表明 :H2 促进甲醇甲烷化反应 ,羰化产物选择性随H2 含量增加迅速下降 ,而且甲醇转化率也明显降低 ,H2 的影响是参与甲烷化反应 ,而没有引起催化剂失活 ,除去H2 后 ,催化剂活性很快恢复 ,其影响是可逆的。     

利用高通量技术研究钴基费托催化剂的宏观动力学

利用高通量技术设计并运行了16路平行动力学固定床反应器,用于测量不同接触时间下的稳态反应物消耗速率和产物生成速率,研究了钴基费托催化剂的宏观动力学,包括C1～C4烷烃与烯烃的稳态反应速率及其随床层的分布,以及它们与反应器温度的关系.在等温固定床非扩散限制的反应条件下,除C1和C2烃类外,Cn的生成速率及CO/H2的消耗速率均随接触时间的增加先上升后下降,且烯烃生成速率的最高点较烷烃更靠近反应器入口;反应温度对速率的影响与转化率有关:生成烷烃的表观活化能大于烯烃.高通量动力学反应器可用于生成宏观动力学数据库,以预测催化剂在工业固定床反应器中的行为.     

乙炔基自由基(C2H·)与二氧化氮(NO2)气体反应势能面的理论研究

在 CCSD(T)/6-311G(d,p)//B3LYP/6-311G(d,p)+ZPE 水平上对反应C2H+NO2 进行了计算, 建立了反应势能面并得到了3种产物. 利用RRKM理论估算了反应的总速率和分支比. 总速率为1.427×10-12×T0.556×exp(190.547/T) cm3*molecule-1*s-1, 其中主要产物P1(HCCO+NO)比例大于96%, 次要产物P2(HCNO+CO)和P3(HCN+CO2)小于4%.     

CO(υ)高振动激发态向C_2H_2的振动传能研究

用时间分辨窝里叶红外发射谱研究了高振动激发态CO向C2H2的传能，得到了CO（v＝1－3）各振动态布展及其随时间的变化,利用微分法解出弛豫微分方程组，获得CO（v=1-3）向C2H2的传能速率常数分别为：2．0±0．1，6.0±0．2和9．1±0.8（10-13cm3·molecule-1·s-1）．传能速率随着振动量子数的增加而迅速增加．CO的振动能应向C2H2的对称伸缩模v2近共振V－V传递．传能过程中还可能形成二聚体络合物，加速了CO（v）向C2H2的传能．用abinitio方法确定了CO...C2H2两种可能的直线构型．     

乙烯酮自由基(HCCO·)与二氧化氮(NO2)反应势能面的理论研究

在CCSD(T)/6-311G(d,p)//MP2/6-311G(d,p)+ZPE水平上对反应HCCO+NO2进行了计算, 建立了反应势能面. 此反应由反应物通过三步反应到达产物. 首先, NO2的O原子进攻HCCO自由基中与H相邻的C原子, 形成异构体1[ONOC(H)CO]或2[H(CONOC)O]. 然后, 异构体1和2通过N-O键的断裂形成产物NO和OC(H)CO. 最后, 产物中的OC(H)CO可以通过C-C键的断裂进一步分解为HCO和CO. 由HCCO+NO2反应得到产物NO+HCO+CO.     

H3PO→H2POH异构化反应的直接动力学研究

在QCISD(T)/6-311C++G(2df,2pd)//QCISD/6-311C++G(d,p)+ZPE水平上,对H3PO的异构化反应H3PO→(1)H2POH(trans)→(2)H2POH(cis)进行了计算研究.结果表明,H原子由P原子向O原子迁移反应(1)的能垒为250.0kJ/mol,是反应速率控制步骤,而O_H键绕P_O键旋转的构型转化反应(2)的能垒只为12.3kJ/mol.利用经典过渡态理论(TST)与变分过渡态理论(CVT)分别计算了反应(1)在200～2000K温度区间内的速率常数kTST和kCVT,获得了经小曲率隧道效应(SCT)及Eckart模型校正后的速率常数kTST/Eckart和kCVT/SCT.对只涉及H原子迁移的反应(1),量子力学隧道效应的影响在低温段非常明显,而变分效应对反应速率常数的影响很小.     

C2H3和NO2反应势能面的理论研究

在CCSD(T)／6—311G(d，p)／／B3LYP／6—3llG(d，p)水平上给出了反应C2H3 NO2的详细势能面信息，并列出了中间体和过渡态的几何构型．通过深入分析反应路径及反应机理，得到5个能量可行的产物和6条反应通道，其中产物C2H3O NO的形成又有利，而产物CH2CO HNO则是次要产物，其他产物在通常条件下可以忽略．     

二氧化碳插入单氢钌配合物反应中的水效应研究

分别研究了在干燥THF及H2O/THF条件下CO2与TpRu(PPh3)(CH3CN)H [Tp=Hydrotris(pyrazolyl)borate]的反应,发现水对CO2插入TpRu(PPh3)(CH3CN)H 的反应具有显著促进作用.原位高压^1H,^31P和^13C核磁共振研究显示,在水存在下 ,CO2插入Ru-H键形成水合甲酸盐配合物TpRu(PPh3)(CH3CN)(η^1-OCHO)·H2O键而 得到增强,进而显著降低CO2插入TpRu(PPh3)(CH3CN)H中Ru-H键的活化能。TpRu (PPh3)(CH3CN)(η^1-OCHO)·H2O很快部分转化为另一甲酸盐配合物TpRu(PPh3)（ H2O）(η^1-OCHO)，二者最后达成平衡，后者由于甲酸盐配体与水分子配体间形成 分子内氢键而稳定。     

固定床反应器中添加CO2对费托合成反应的影响

用固定床反应器研究了Fe-Mn催化剂上原料气中添加CO2对费托合成反应的影响.结果表明,在533K与反应总压为1.50MPa时,大量CO2的添加使得生成CO2的选择性迅速降低,烃的生成速率降低,烃的收率也有所降低,产物向轻组分方向偏移,有机含氧化合物的生成速率降低;在593K与合成气(H2 CO)分压为1.50MPa时,随着CO2分压的增加,CO消耗速率变化不大,而烃的生成速率缓慢升高,烃的收率有所升高,CO2的生成速率缓慢降低,H2O的生成速率明显加快.由于CO2的添加,促使水煤气变换反应向逆反应方向进行,降低了催化剂表面氢物种浓度,抑制了加氢反应,低碳烃的烯/烷比有所增大,同时提高了重质烃的选择性,且随着CO2分压的增加,有机含氧化合物的生成速率呈上升的趋势.     

Reactions in a Mixture of CH4 and CO2 under the Action of Microwave Discharge at Atmospheric Pressure

Reactions between CH4 and CO2 under the action of continuous microwave discharge atatmospheric pressure were studied in a special homemade reactor. The main products were CO and H2,while acetylene and ethylene were also found in the products. Experimental results show that conversionsof CH4 and CO2 could be higher than 90% without the presence of any catalyst. Effects of CO2/CH4molar ratio and total flow rate of the feed gas on the reaction were also investigated.     

Reactions in a Mixture of CH_4 and CO_2 under the Action of Microwave Discharge at Atmospheric Pressure

Reactions between CH_4 and CO_2 under the action of continuous microwave discharge at atmospheric pressure were studied in a special homemade reactor. The main products were CO and H2, while acetylene and ethylene were also found in the products. Experimental results show that conversions of CH4 and CO2 could be higher than 90% without the presence of any catalyst. Effects of CO2/CH4 molar ratio and total flow rate of the feed gas on the reaction were also investigated.     

Reactions in a Mixture of CH4 and CO2 under the Aciton of Microwave Discharge at Atmospheric Pressure

Reactions between CH4 and CO2 under the action of continuous microwave discharge at atmospheric pressure were studied in a special homemade reactor,The main products were CO and H2,while acetylene and ethylene were also found in the products.Experimental results show that conversions of CH4 and CO2 could be higher than 90% without the presence of any catalyst,Effects of CO2/CH4 molar ratio and total flow rate of the feed gas on the reaction were also investigated.     

用无声放电转化甲烷和二氧化碳同时制备合成气与烃

在低温常压条件下,研究了在无声放电反应器中以A型分子筛为催化剂从甲烷和二氧化碳合成烃和合成气,实现了在无声放电反应器中同时合成烃和合成气。实验在原料气流量200－600ml/min、原料气甲烷和二氧化碳摩尔比1／1－3／1及输入功率100－500W的范围内进行。研究结果表明,低原料气流量有利于甲烷和二氧化碳的转化,而高原料气流量有利于烃的生成;原料气甲烷和二氧化碳摩尔比对制得合成气的H2／CO摩尔比的影响最显著;甲烷和二氧化碳转化率及合成气和烃的产率均随输入功率的增加而提高。而所研究的范围内,当原料气流理为200ml/min、甲烷和二氧化碳摩尔比为1／1、输入功率为500S时,甲烷和二氧化碳转化率达到最高值,分别为64％和39％。以此法制备的合成气的H2／CO摩尔可以在很宽的范围内变化,本研究合成气H2／CO摩尔比的变化范围是0.7-3.1。     

STUDIES ON FISCHER TROPSCH SYNTHESIS OVER Fe-Cu-K CATALYST Ⅰ.CATALYTIC PERFORMANCE

The influence of reaction pressure, temperature, space velocity (GHSV), particle size of catalyst and H2/CO ratio of feed-gas on the steady-state product distribution, conversion of CO, H2 and syngas, olefin to paraffin ratio and CO2/ H2O ratio for FTS reaction were investigated using a coprecipitated copper- potassium promoted iron catalyst. The test was carried out in a fixed-bed reactor. Increasing the reaction temperature from 493. 2 to 5-13. 2 K shifted the hydrocarbon distribution toward the heavier hydrocarbons (C5-C23) and selectively increased CO conversion to CO2. The hydrocarbon distribution was found to be dependent on the H2/CO feed-gas ratio in the range from 1.23 to 2. 22. The CO2/H2O ratio in product decreased as the flow of feed-gas rate increased, which suggests that H2O is a primary product and its reaction with CO to form CO2 occurs via a secondary process. The CO conversion increased with the decrease of catalyst particle size from 10 to 60 mesh (2. 0- 0. 3 mm), while the CO convers     

Modeling of microreactor for syngas production by catalytic partial oxidation of methane

Fixed-bed reactors for the catalytic partial oxidation of methane (CPOM) to produce synthesis gas still pose hot spots problems. Microreactor is a good alternative reactor proposed to resolve these problems. In this paper, synthesis gas (hydrogen and carbon monoxide) production was investigated by a two-dimensional numerical model of single microchannel. CFD modeling with detailed chemistry was conducted to understand the CPOM on platinum (Pt) catalyst. Gas inlet velocity, microchannel pressure, and fuel to air ratio (F/A) are selected as the effective parameters on microchannel performance. Study results show that Reynolds number has considerable effect on methane conversion, hydrogen to carbon monoxide ratio (H2/CO), and product distribution. Increasing gas inlet velocity causes all the above parameters to decrease. It is noted that increasing microchannel pressure and decreasing the ratio of fuel to air cause the decrease of the H2/CO ratio.     

生物质气化重整合成二甲醚

以松木粉为原料，采用空气 水蒸气气化制备了富氢气化气，通过添加甲烷重整富氢气化气，调整了合成气化学当量比，在260 ℃、4 MPa、12 000 h－1条件下，对生物质合成气一步法合成二甲醚进行了实验研究。结果表明：引入甲烷重整，活化了富氢气化气中过量的CO2，甲烷的最佳加入量为CH4/CO2=1，生物质碳转化率达到70%以上，尾气中二甲醚选择性达到69.6%。     

Supercritical carbon dioxide: an inert solvent for catalytic hydrogenation?

Various surface species originating from the reaction between CO2 and H2 over Al2O3-supported Pt, Pd, Rh, and Ru model catalysts were investigated by attenuated total reflection infrared (ATR-IR) spectroscopy under high-pressure conditions. Two different spectroscopic cells were used: a variable-volume view cell equipped with ATR-crystal and transmission IR windows (batch reactor) and a continuous-flow cell also equipped with a reflection element for ATR-IR spectroscopy. The study corroborated that CO formation from dense CO2 in the presence of hydrogen occurs over all Pt-group metals commonly used in heterogeneous catalytic hydrogenations in supercritical CO2 (scCO2). In the batch reactor cell, formation of CO was detected on all metals at 50 and 90 degrees C, with the highest rate on Pt. Additional surface species were observed on Pt/Al2O3 at 150 bar under static conditions. It seems that further reaction of CO with hydrogen is facilitated by the higher surface concentration at higher pressure. In the continuous-flow cell, CO coverage on Pt/Al2O3 was less prominent than that in the batch reactor cell. A transient experiment in the continuous-flow cell additionally revealed CO formation on Pt/Al2O3 at 120 bar after switching the feed from a H2-ethane to a H2-CO2 mixture. The in situ ATR-IR measurements indicate that CO formation in CO2-H2 mixtures is normally a minor side reaction during hydrogenation reactions on Pt-group metal catalysts, and dense ("supercritical") CO2 may be considered as a relatively "inert" solvent in many practical applications. However, blocking of specific sites on the metal surface by CO and consecutive products can affect structure sensitive hydrogenation reactions and may be at the origin of unexpected shifts in the product distribution.     

生物质气化再燃特性实验研究

生物质能是指利用自然界的植物、粪便以及城乡有机废物转化成的能源。生物质能是唯一的碳基可再生能源，燃用生物质燃料可以实现CO2净排放为零。生物质能的再利用十分有效，可以发电，可以合成新的化学物，还可以减少NOx、SOx及颗粒物排放。因此，生物质能是解决化石能源短缺和污染问题的主要可再生能源。