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1.
在常压下研究了不同等离子体放电模式及反应器结构对氨分解制氢反应的影响.实验中调节反应器结构分别产生了介质阻挡放电和交流弧放电两种放电模式.通过对两种放电模式的放电图像、电压-电流波形和氨分解过程中等离子体区活性物种的发射光谱(OES)研究发现,与介质阻挡放电相比,交流弧放电为局部强放电,具有更高的电源效率和电子密度.因此,在介质阻挡放电中氨气分子大部分通过生成电子激发态物种NH3*,再与载能电子碰撞断裂N―H键进行氨分解反应;而在交流弧放电中载能电子具有更高的平均电子能量,可直接断裂氨气分子的N―H键生成NH2和NH等高活性物种,促进氨分解反应的进行.结果表明,交流弧放电的氨分解效果要明显优于介质阻挡放电.在交流弧放电模式下不同类型反应器对氨气分解转化率由高到低的顺序为:管-管管-板针-板板-板.在输入功率为30 W,气隙间距为6 mm时,管-管交流弧放电的氨气转化率达到60%左右,而板-板介质阻挡放电的氨气转化率仅为4%.  相似文献   

2.
氧气常压介质阻挡放电的发射光谱及能量传递机理   总被引:2,自引:0,他引:2  
为研究氧气常压介质阻挡放电中的物理化学行为, 以纯氧作为放电体系, 用发射光谱(optical emission spectroscopy)诊断技术分析了等离子体中可能存在的化学活性物种. 利用在500-950 nm范围的氧原子发射光谱计算出等离子体中的电子温度为(1.02±0.03) eV; 观测了760 nm处的具有清晰转动结构的氧气A带(atmospheric band)O2(b1∑+g-X3∑-g), 并用其转动结构计算了转动温度(气体温度)为(650±20) K; 在500-700 nm范围观测了氧气的第一负带系(first negative system) O+2(b4∑-g-a4∏u), 在190-240 nm范围观测了微弱但特征清晰的氧气的Hopfield带系O+2(c4∑+u-b4∑-g). 研究发现, 在氧气常压介质阻挡放电等离子体中存在多种激发态氧原子、激发态氧气分子、基态和激发态氧气分子离子等反应活性物种, 这些活性物种的形成涉及氧气分子的激发、解离和电离等多种过程, 每个过程都包含多个能量传递步骤, 氧分子解离产生的氧原子是导致一系列高激发态氧原子生成和氧气电离激发的主要因素.  相似文献   

3.
介质阻挡放电等离子体催化天然气偶联制C2   总被引:1,自引:0,他引:1       下载免费PDF全文
在常压、室温的介质阻挡放电连续流动反应器中, 对介质阻挡放电等离子体作用下天然气偶联反应制C2烃进行了研究. 考察了放电频率、放电的电极结构、放电电压、放电的电极数目、氢气、甲烷进料流量和催化剂等参数对甲烷转化率和产物(碳二烃和碳三烃)的选择性影响规律, 同时探讨了反应过程. 结果表明合适的工艺条件为: 电源频率20 kHz, 电极结构为两个电极上都覆盖绝缘介质的b型, 放电电压20~40 kV, 进料流量20~60 mL·min-1, H2/CH4为1/4; 甲烷的转化率随电压的升高而增大, 随甲烷进料流量的增大而减小, 碳二烃的选择性随电压的升高而减小, 随甲烷进料流量的增大而增大. 甲烷的转化率可达45%, 碳二烃选择性可达76%, 产品(碳二烃和碳三烃)的总选择性接近100%; 连续反应100 h无积碳; 催化剂可改善产品碳二烃的选择性; 碳二烃和碳三烃的生成主要是通过自由基和甲烷分子反应获得的.  相似文献   

4.
腈类化合物广泛用于医药和精细化学品合成。然而,许多腈类的生产过程产生大量污染物。本文采用介质阻挡放电(DBD)等离子体活化甲醇和氨气分子,发现等离子体引发的CH_3OH/NH_3偶联反应可合成二甲基氰胺、二甲基氨基乙腈和氨基乙腈等高附加值含N有机化合物。系统研究了反应器结构、放电条件、反应条件和填充材料对甲醇转化率和产物选择性的影响。实验结果表明,在最优条件下,甲醇的转化率达到51.5%,腈类化合物选择性达到22.1%。CH_3OH/NH_3等离子体发射光谱结果表明,C≡N自由基物种可能是生成腈类化合物的重要中间体。该CH_3OH/NH_3等离子体偶联反应为二甲基氰胺、二甲基氨基乙腈和氨基乙腈提供了一种绿色合成方法,也为甲醇和氨气精细化利用开辟了一种新途径。  相似文献   

5.
介质阻挡放电和CuZSM-5结合体系中等离子体对C2H4的作用   总被引:2,自引:0,他引:2  
孙琪  杨佳  石雷  牛金海  宋志民 《化学学报》2009,67(15):1779-1783
采用吸附、程序升温脱附及氧化和发射光谱等技术研究了介质阻挡放电对气相和催化剂表面吸附乙烯的作用. 实验表明, 介质阻挡放电等离子体能脱附催化剂表面吸附物种(如CO2和H2O等), 并引发表面化学反应生成新物种(如在等离子体作用下C2H4和O2生成CO2和H2O); 改变催化剂表面积碳化合物结构, 并降低其起燃点; 引发气相中乙烯发生反应生成中间物种或碎片(如CN和CH等). 在富氧体系NO/O2/N2中加入C2H4, 能使介质阻挡放电等离子体和CuZSM-5“一段法”结合体系产生协同效应, 提高NOx转化率. 该协同效应的产生与等离子体在气相及催化剂表面引发化学反应, 产生参与NOx还原反应的新稳态物种和短寿命高能活性物种有关.  相似文献   

6.
在常压下,研究了添加气的种类(N2,He,Ar,H2,NH3,CO和CO2)对介质阻挡放电低碳烷烃(甲烷、乙烷和丙烷)转化制低碳烯烃的影响.结果表明,以甲烷或乙烷为原料时,N2,He,Ar和CO的引入有利于提高原料的转化率和总烯烃的选择性;而CO2,H2和NH3的引入对甲烷、乙烷的转化率无明显影响,但H2和NH3的引入会使总烯烃的选择性显著降低.以丙烷为原料时,所研究的添加气均可提高丙烷的转化率,而只有CO的引入可提高总烯烃选择性.综上所述,80%(摩尔分数)CO添加量最有利于低碳烷烃转化成低碳烯烃,对应的甲烷、乙烷和丙烷的转化率分别提高了14.4%,17.6%和42.8%,总烯烃的选择性分别提高了19.9%,25.0%和11.9%.以CH4为例,通过对放电电流波形和等离子体区物种的发射光谱(OES)研究发现,引入CO能显著增加等离子体的电子密度,并且体系中出现激发态O*物种(777.5和844.7 nm),这种O*物种能够促进C—H键的断裂,有利于烯烃的生成.因此,等离子体区电子密度的增加和激发态O*物种的出现可能是CH4-CO体系中CH4有效转化的主要原因.  相似文献   

7.
甲烷二氧化碳介质阻挡放电转化产物分布研究   总被引:7,自引:0,他引:7  
针对介质阻挡放电甲烷二氧化碳转化实验,分析了反应的产物分布,探讨了进料组成和反应器结构对反应的影响.反应产物包括:高H2/CO摩尔比的合成气、气态烃、高辛烷值的汽油组分、醇和酸等含氧有机物.对所述电极结构,产物的选择性随碳数增加而降低;高的甲烷进料浓度有利于烃的生成,对醇和酸的最佳甲烷进料体积分数范围在67.4%~75.1%;放电间隙越小,原料转化率和烃、酸的选择性越大,大的放电间隙对醇的生成有利.  相似文献   

8.
构建了CH_4-O_2-N_2-H_2O反应体系,对介质阻挡放电条件下甲烷水蒸气重整和部分氧化制氢反应过程进行了研究,考察了H2O/CH4物质的量比、O_2/N_2物质的量比、气体总流量、放电电压及放电频率等参数对制氢效率的影响,并基于发射光谱原位诊断法分析了反应机理。结果表明,甲烷转化率和氢气产率随着H_2O/CH_4物质的量比、O_2/N_2物质的量比和放电电压的增加而增加,而随着反应气体总流量的增加而减小,随着放电频率的增加先增大后减小,在9.8 kHz处取得最大值。在H_2O/CH_4物质的量比1.82、O_2/N_2物质的量比2.1、总流量136 mL/min、放电电压18.6 kV及放电频率9.8 kHz的条件下,甲烷转化率与氢气产率分别达47.45%和21.33%。甲烷和水蒸气等反应物分子通过电子解离产生CH_x·、H·、OH·、O·等自由基,进而通过自由基间的碰撞反应生成H_2;H·自由基一方面来源于CH_4的电子解离;另一方面来源于水蒸气一次解离以及OH·的进一步离解。部分氧化反应主要表现为O_2电子解离形成的O·自由基以及水蒸气一次反应产物OH·自由基进一步离解形成的O·自由基对CH_2·自由基的氧化。  相似文献   

9.
刘佳驹  贺鹏  王利国  刘辉  曹妍  李会泉 《催化学报》2018,39(8):1282-1293
CO2作为重要的碳氧资源, 具有来源丰富、价格低廉、安全等突出优点. 近年来, 由于蕴含的巨大利用潜力,CO2间接利用制备基础化学品、能源燃料对于可持续制备大宗化工品中具有重要研究意义, 日益受到研究者和工业界的广泛重视.甲醇与乙二醇是化学工业中的两种重要大宗原料. 甲醇不仅是重要的有机化工原料、清洁环保的液体燃料, 同时也是氢气和能量储存的良好载体. 乙二醇作为一种重要的有机化工原料, 在聚酯等领域具有广泛应用.CO2经碳酸乙烯酯氢解制备甲醇/乙二醇是典型的原子经济反应, 对资源、能源和环境的可持续发展具有重要意义. 需要指出的是,CO2与环氧乙烷环加成制备碳酸乙烯酯已具备成熟的工业化技术. 因此, 该路线研究重点在于发展碳酸乙烯酯选择加氢联产甲醇和乙二醇高效稳定的催化体系. 近年来, 铜基多相催化剂催化碳酸乙烯酯加氢联产甲醇乙二醇得到了广泛重视. 由于铜基催化剂存在活性较低、高温易失活等问题, 开发高效且具有良好稳定性的铜基催化剂是目前碳酸乙烯酯加氢研究重点.本文针对碳酸乙烯酯选择氢解合成甲醇乙二醇新型铜基催化体系构建和构效关系研究, 采用硅溶胶蒸氨法制备高分散 Cu/SiO2过程中引入多羟基β-环糊精修饰催化剂前驱体的合成策略, 并通过惰性气体中煅烧后的积碳有效抑制活性铜物种的团聚, 获得了β-环糊精改性的 Cu/SiO2催化剂. 通过 N2吸脱附、XRD、N2O 滴定、H2-TPR、TEM 和 XPS 等系统表征,发现β-环糊精可有效调控催化剂结构和表面不同价态活性铜物种分布. 碳酸乙烯酯加氢性能评价结果表明引入适量β-环糊精的 5β-25%Cu/SiO2具有较优催化活性, 乙二醇选择性 98.8% 和甲醇选择性 71.6%, 且相应的催化活性可达 1178 mgEC gcat-1h-1. 高活性的原因很可能归因于不同价态 Cu0与 Cu+物种协同催化作用及适宜的 Cu+/(Cu0+Cu+) 比例. 结合密度泛函理论模拟计算, 我们提出了 Cu0促进氢气解离、Cu+吸附活化碳酸乙烯酯分子中酯羰基的反应机理. 催化剂重复使用和表征结果表明, 5β-25%Cu/SiO2具有良好的稳定性, 使用前后铜粒子大小和铜物种分布几乎未发生明显变化. 本文为解决铜基催化剂高温易烧结等难题提供了简单有效的活性铜物种稳定化方法, 并为CO2经碳酸乙烯酯绿色合成甲醇、乙二醇高效稳定铜基催化新体系的构筑提供了有益借鉴.  相似文献   

10.
介质阻挡放电与 CuZSM-5 结合方式对脱除 NOx 的影响   总被引:1,自引:0,他引:1  
陈刚  孙琪  石雷  牛金海  宋志民 《催化学报》2010,31(7):817-821
 研究了介质阻挡放电 (DBD) 与 CuZSM-5 结合方式, 即 DBD 和 CuZSM-5 两段分置 (两段法) 或将 CuZSM-5 放入 DBD 区 (一段法), 对脱除氮氧化物的影响. 结果表明, 在 NO/N2 或 NO/C2H4/N2 无氧体系中, DBD 与 CuZSM-5 结合产生的协同效应很小; 在 NO/O2/N2 富氧体系中, DBD 与 CuZSM-5 结合导致氮氧化物转化率下降; 而在 NO/C2H4/O2 /N2 富氧体系中, 在 250 ºC, 空速 12 000 h1, 输入放电能量密度 (Ein) 155 J/L 的条件下, 单纯催化、单纯等离子体放电、一段法和两段法时氮氧化物转化率分别为 39%, 1.5%, 79% 和 52%. 两段法产生了中等程度的协同效应, 主要是第一段等离子体放电产生新稳态物种 (如 NO2, CO 和 CO2 等) 起作用; 而一段法产生的协同效应较大, 主要是由于等离子体放电产生的新稳态物种和激发态短寿命物种 (如 N2*, NO*, CH 和 CN 等) 共同起作用.  相似文献   

11.
The experiments are carried out in the system of continuous flow reactors with dielectric-barrier discharge (DBD) for studies on the conversion of natural gas to C2 hydrocarbons through plasma catalysis under the atmosphere pressure and room temperature. The influence of discharge frequency, structure of electrode, discharge voltage, number of electrode, ratio of H2/CH4, flow rate and catalyst on conversion of methane and selectivity of C2 hydrocarbons are investigated. At the same time, the reaction process is investigated. Higher conversion of methane and selectivity of C2 hydrocarbons are achieved and deposited carbons are eliminated by proper choice of parameters. The appropriate operation parameters in dielectric-barrier discharge plasma field are that the supply voltage is 20-40 kV (8.4-40 W), the frequency of power supply is 20 kHz, the structure of (b) electrode is suitable, and the flow of methane is 20-60 ml · min-1. The conversion of methane can reach 45%, the selectivity of C2 hydrocarbons i  相似文献   

12.
The plasma technology served as a tool in unconventional catalysis has been used in natural gas conversion, because the traditional catalytic methane oxidative coupling reaction must be performed at high temperature on account of the stability of methane molecule. The focus of this research is to develop a process of converting methane to C2 hydrocarbons with non-equilibrium plasma technology at room temperature and atmospheric pressure. It was found that methane conversion increased and the selectivity of C2 hydrocarbons decreased with the voltage. The optimum input voltage range was 40-80 V corresponding to high yield of C2 hydrocarbons. Methane conversion decreased and the selectivity of C2 hydrocarbons increased with the inlet flow rate of methane. The proper methane flow rate was 20-40 ml/min (corresponding residence time 10-20 s). The experimental results show that methane conversion was 47% and the selectivity of C2 hydrocarbons was 40% under the proper condition using atmospheric DBD cold plasma technology. It was found that the breakdown voltage of methane VB was determined by the type of electrode and the discharge gap width in this glow discharge reactor. The breakdown voltage of methane VB,min derived from the Paschen law equation was established.  相似文献   

13.
The plasma technology served as a tool in unconventional catalysis has been used in natural gas conversion,because the traditional catalytic methane oxidative coupling reaction must be performed at high temperature on account of the stability of methane molecule.The focus of this research is to develop a process of converting methane to C2 hydrocarbons with non-equilibrium plasma technology at room temperature and atmospheric pressure.It was found that methane conversion increased and the selectivity of C2 hydrocarbons decreased with the voltage.The optimum input voltage range was 40-80 V corresponding to high yield of C2 hydrocarbons.Methane conversion decreased and the selectivity of C2 hydrocarbons increased with the inlet flow rate of methane.The proper methane flow rate was 20-40 ml/min (corresponding residence time 10-20 s).The experimental results show that methane conversion was 47% and the selectivity of C2 hydrocarbons was 40% under the proper condition using atmospheric DBD cold plasma technology.It was found that the breakdown voltage of methane VB was determined by the type of electrode and the discharge gap width in this glow discharge reactor.The breakdown voltage of methane VB,min derived from the Paschen law equation was established.  相似文献   

14.
本文利用介质阻挡放电(DBD)方法, 在室温和常压下将甲烷和氧气的混合气体进行等离子体活化, 通过甲烷和氧等离子体直接气相反应高收率合成H2O2. 该方法能有效克服氢氧直接法合成H2O2受到原料气配比严格限制的缺点.  相似文献   

15.
Introduction 2-Hydroxy-1,4-naphthoquinone (HNQ), existing in natural plants,1,2 is popularly separated and purified as dye or pigment. Recent research results show that, with the function to prevent the formation of protein coenzyme of HIV-I, HNQ can inhibit HIV virus from copying and propagating,3,4 HNQs derivatives and di-chloroallyl lawsone are also the inhibitor for RNA syn-thesis of cancer.5 It is well known that there is a rela-tionship between the side chain attached to HNQ an…  相似文献   

16.
CO2/H2和(CO/CO2)+H2低压合成甲醇催化过程的本质   总被引:8,自引:0,他引:8  
通过在Cu/ZnO/Al2O3催化剂上CO2+H2,CO+H2和(CO/CO2)+H2催化反应动力学研究对合成甲醇动力学和反应机理进行了细致分析,提出合成甲醇的反应机理,解释了在(CO/CO2)+H2合成甲醇过程中少量CO2的作用及合成甲醇的直接碳源。  相似文献   

17.
The experiments are carried out in the system of continuous flow reactors with dielectric-barrier discharge (DBD) for studies on the conversion of natural gas to C2 hydrocarbons through plasma catalysis under the atmosphere pressure and room temperature. The influence of discharge frequency, structure of electrode, discharge voltage, number of electrode, ratio of H2/CH4, flow rate and catalyst on conversion of methane and selectivity of C2 hydrocarbons are investigated. At the same time, the reaction process is investigated. Higher conversion of methane and selectivity of C2 hydrocarbons are achieved and deposited carbons are eliminated by proper choice of parameters. The appropriate operation parameters in dielectric-barrier discharge plasma field are that the supply voltage is 20–40 kV (8.4–40 W), the frequency of power supply is 20 kHz, the structure of (b) electrode is suitable, and the flow of methane is 20–60 mL · min−1. The conversion of methane can reach 45%, the selectivity of C2 hydrocarbons is 76%, and the total selectivity of C2 hydrocarbons and C3 hydrocarbons is nearly 100%. The conversion of methane increases with the increase of voltage and decreases with the flow of methane increase; the selectivity of C2 hydrocarbons decreases with the increase of voltage and increases with the flow of methane increase. The selectivity of C2 hydrocarbons is improved with catalyst for conversion of natural gas to C2 hydrocarbons in plasma field. Methane molecule collision with radicals is mainly responsible for product formation.  相似文献   

18.
Currently, worldwide attention is focused on controlling the continually increasing emissions of greenhouse gases, especially carbon dioxide. To this end, a number of investigations have been carried out to convert the carbon dioxide molecules into value-added chemicals. As carbon dioxide is thermodynamically stable, it is necessary to develop an efficient carbon dioxide utilization method for future scaled-up applications. Recently, several approaches, such as electrocatalysis, thermolysis, and non-thermal plasma, have been utilized to achieve carbon dioxide conversion. Among them, non-thermal plasma, which contains chemically active species such as high-energy electrons, ions, atoms, and excited gas molecules, has the potential to achieve high energy efficiency without catalysts near room temperature. Here, we used radio-frequency (RF) discharge plasma, which exhibits the non-thermal feature, to explore the decomposition behavior of carbon dioxide in non-thermal plasma. We studied the ionization and decomposition behaviors of CO2 and CO2-H2 mixtures in plasma at low gas pressure. The non-thermal plasma was realized by our custom-made inductively coupled RF plasma research system. The reaction products were analyzed by on-line quadrupole mass spectrometry (differentially pumped), while the plasma status was monitored using an in situ real-time optical emission spectrometer. Plasma parameters (such as the electron temperature and ion density), which can be tuned by utilizing different discharge conditions, played significant roles in the carbon dioxide dissociation process in non-thermal plasma. In this study, the conversion ratio and energy efficiency of pure carbon dioxide plasma were investigated at different values of power supply and gas flow. Subsequently, the effect of H2 on CO2 decomposition was studied with varying H2 contents. Results showed that the carbon dioxide molecules were rapidly ionized and partially decomposed into CO and oxygen in the RF field. With increasing RF power, the conversion ratio of carbon dioxide increased, while the energy efficiency decreased. A maximum conversion ratio of 77.6% was achieved. It was found that the addition of hydrogen could substantially reduce the time required to attain the equilibrium of the carbon dioxide decomposition reaction. With increasing H2 content, the conversion ratio of CO2 decreased initially and then increased. The ionization state of H2 and the consumption of oxygen owing to CO2 decomposition were the main reasons for the V-shape plot of the CO2 conversion ratio. In summary, this study investigates the influence of power supply, feed gas flow, and added hydrogen gas content, on the carbon dioxide decomposition behavior in non-thermal RF discharge plasma.  相似文献   

19.
This paper presents an in-house-designed dielectric barrier discharge (DBD) plasma reformer for hydrogen production via partial oxidation reforming of methane. We examined the effects of oxygen/carbon (O/C) molar ratio, feed flow rate, discharge gap, discharge zone length, filler diameter, filler shape, filler materials, discharge voltage, and discharge frequency on the hydrogen production performance i.e., CH4 conversion rate, H2 yield, and selectivity of products (H2, CO, and CO2). The experimental results showed that the parameters of the discharge zone played an important role in the CH4 conversion rate. For instance, CH4 conversion rate increased with increasing discharge zone lengths. When the discharge zone length increased from 5 to 20 cm, CH4 conversion rate increased from 6.87% to 22.26%, which corresponds to an improvement of 224%. Also, the fillers in the discharge zone strongly influenced the hydrogen production performance. Using reactors with fillers generated higher CH4 conversion rates. Moreover, using fillers with more appropriate dielectric constants is advantageous for practical application. The H2 yield and hydrogen selectivity increased with increasing discharge frequency. Specifically, when the discharge frequency increased from 1.5 to 7.0 kHz, H2 yield increased from 1.10% to 9.49%, and hydrogen selectivity increased from 21.18% to 30.06%. It is believed that the current results would serve as a good guideline in hydrogen production from hydrocarbon fuels by plasma reforming.  相似文献   

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