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1.
利用脉冲微波强化、扩展丝光等离子体反应装置,在常压和正压条件下,对低温脉冲微波等离子体裂解甲烷和氢气混合气制C2烃的反应进行了研究。考察了压力、微波功率、脉冲通/断时间以及氢气/甲烷比例、流量等参数对反应的影响。结果表明,在脉冲微波的作用下,常规高压放电形成的在空间呈非连续分布的丝状等离子体被强化和扩展成为连续分布的伞状等离子体,等离子体利用率和活性均得以大幅度提高;利用这种低温等离子体可以获得高的甲烷转化率,而且产物纯净,只有乙烯和乙炔;通过改变压力,还可能调节产物中C2H2/C2H4的物质的量比值,当气体总流量为300mL/min、物质的量比n(H2)/n(CH4)=2:1、压力为0.13MPa、微波峰值功率为120W、脉冲通/断比=400/400ms时,甲烷转化率可达59.2%,C2烃单程收率可达52%,其中乙炔单程收率达42.7%。  相似文献   

2.
碱性条件下废轮胎真空热裂解研究   总被引:6,自引:1,他引:5  
研究了废轮胎橡胶粉在450℃~600℃真空热解系统中热解的特性,以及温度和添加Na2CO3、NaOH对热解气液态产物的影响。实验表明,真空下废轮胎热解油收率在550℃时达到最大值,为48%左右。添加3%的NaOH能明显促进废轮胎橡胶热解,480 ℃时油产率达到最大值49.66%,随后随着温度的升高油产率呈现下降趋势。添加3%的Na2CO3对热解的促进作用不明显。热解气体产物主要有H2、CO、CH4、CO2、C2H4、C2H6以及少量其他化合物。NaOH的加入使气体产品中的H2相对体积分数明显增加,而CH4、CO、C2等的体积分数降低。通过GC和GC-MS分析热解石脑油发现,热解油品中含有11%以上的柠檬油精。  相似文献   

3.
采用电解液微弧碳氮化技术(PECN),在钛合金表面沉积出较厚的Ti(CxN1-x)膜层,用红外光谱研究了改性过程中的气封组成,分析了膜层的形成机理。结果表明:PECN处理过程中的气相产物主要是:CH4、NH3、C2H2、CO、CO2和H2O。各气体产物来自于PECN处理过程中有机物的分解,并且气体之间存在相互作用。随放电时间延长,各气体浓度呈现不同的变化趋势,导致气封中碳、氮势随之改变,继而引起Ti(CxN1-x)膜层中C/N原子比亦相应变化。PECN过程大致可分为:阴极电解析氢、有机物的热分解以形成气封,反应气体在等离子体的作用下分解、电离产生含碳、氮活性粒子,活性粒子向试样表面扩散,在试样表面吸附并发生化学反应形成Ti(CxN1-x)膜。  相似文献   

4.
本文介绍了一种新的燃烧体系--熔融盐循环热载体无烟燃烧技术。这种燃烧体系杜绝环境污染气体NOx和CO2的排放,可以实现真正零排放的目标。计算了以Fe2O3作为氧载体的无烟燃烧体系的热力学参数。用最小吉布斯自由能原则,分析了Fe2O3与CH4的平衡组成。分析表明,如果要想在产物中产生高纯度的CH4完全氧化产物CO2和H2O,Fe2O3与CH4必须达到高摩尔比,如果Fe2O3的量不足,就会产生较多的部分氧化产物如CO,H2甚至C  相似文献   

5.
大气压等离子体射流重整CH_4-CO_2制合成气   总被引:1,自引:0,他引:1  
采用大气压等离子体射流,以CH4和CO2直接作为放电气体进行常压下重整制合成气的实验研究,考察了等离子体射流的放电特征及放电距离、放电功率、原料气配比和流量对反应的影响。结果表明,该等离子体具有放电稳定、均匀的特征。重整反应的主要产物为合成气,只有少量的H2O和积炭生成。优化的反应条件为放电距离为9 mm,CH4和CO2的摩尔比为4/6。当原料气流量为1 000 mL/min,放电功率为88.4 W时,CH4和CO2的最高转化率为分别为94.99%和87.23%。甲烷和二氧化碳的转化率随放电功率的增加而增加,随流量的增加而减少。  相似文献   

6.
研究了低温等离子体协助催化条件下甲烷选择性催化还原NO反应(SCR).反应气体经等离子体活化后,生成NO2,HCHO,CH3NO和CH3NO2等活性更高的中间产物.程序升温表面反应表明,这些中间产物可在等离子体后置催化装置上进一步反应,从而使NOx还原为N2.在考察的一系列催化剂(包括γ-Al2O3,Ag/γ-Al2O3,B2O3/γ-Al2O3,Ga2O3/γ-Al2O3,In2O3/γ-Al2O3等)中,B2O3/γ-Al2O3表现出最好的催化活性.当反应温度为300oC时,NOx转化率达到最高.与γ-Al2O3催化剂相比,在10wt%B2O3/γ-Al2O3催化剂上,300oC时,NOx转化为N2的转化率从33.4%提高至51.0%.催化剂的酸性对于经等离子体活化后的反应气体在催化剂上的SCR反应起到重要作用.同时,催化剂上吸附态NOx对于NOx的转化也起到一定作用.  相似文献   

7.
低温等离子体协助B2O3/γ-Al2O3 选择催化还原NO(英文)   总被引:1,自引:0,他引:1  
研究了低温等离子体协助催化条件下甲烷选择性催化还原NO反应(SCR).反应气体经等离子体活化后,生成NO2,HCHO,CH3NO和CH3NO2等活性更高的中间产物.程序升温表面反应表明,这些中间产物可在等离子体后置催化装置上进一步反应,从而使NOx还原为N2.在考察的一系列催化剂(包括γ-Al2O3,Ag/γ-Al2O3,B2O3/γ-Al2O3,Ga2O3/γ-Al2O3,In2O3/γ-Al2O3等)中,B2O3/γ-Al2O3表现出最好的催化活性.当反应温度为300oC时,NOx转化率达到最高.与γ-Al2O3催化剂相比,在10wt%B2O3/γ-Al2O3催化剂上,300oC时,NOx转化为N2的转化率从33.4%提高至51.0%.催化剂的酸性对于经等离子体活化后的反应气体在催化剂上的SCR反应起到重要作用.同时,催化剂上吸附态NOx对于NOx的转化也起到一定作用.  相似文献   

8.
生物质空气-水蒸气气化制取合成气热力学分析   总被引:6,自引:4,他引:2  
基于Gibbs自由能最小化原理,计算了包括H2O(l)和C(s)在内的,生物质空气 水蒸气气化体系热力学平衡,对比分析了常压气化和加压气化的特点,通过回归分析得到了不同压力下,气化产物中可燃气体分率最高时的水蒸气/生物质质量比(S/B,Steam to Biomass Ratio)与空气当量比(ER,Equivalence Ratio)的关系曲线,为探讨适于制取合成气的气化工艺和条件提供初步的理论指导。研究表明,相对于常压气化,加压气化体系的平衡温度较高,平衡状态下可燃气体分数较低,但CH4含量明显增加;一定温度和当量比下,加压气化使得气化产物中可燃气体分数达到最高所对应的S/B比增大,即需要消耗更多水蒸气;通过调节S/B比,可以比较方便地控制产物中H2和CO的比例。以常压为例,T=1173K,S/B=0.17时,气化产物中H2/CO约为1.1∶1,而S/B=1.02时,气化产物中H2/CO约为2∶1;不同压力下最佳S/B比和ER有很好的线性关系,温度为1173K时,最佳S/B比与压力及ER〖的关系为S/B=-1.48×ER-4.49 E×10-5×p2 + 5.83 E×10-3×p + 0.32。  相似文献   

9.
利用固定床反应器研究了哈密煤温和液化固体产物(MLS)在热解过程中含硫气体的释放规律以及不同形态硫的变迁规律,并分析了矿物质对硫变迁规律的影响。结果表明,在实验考察的条件范围内,MLS热解过程中大部分的硫残留在半焦中,仅有不到10%的硫迁移到焦油中或转化为含硫气体逸出。热解生成的含硫气体以H2S为主,当热解温度为400℃时H2S的逸出速率达到最大。通过改进方法测定了M LS及其热解半焦中各种形态硫的含量,发现M LS热解过程中以硫化物硫和有机硫的分解和转化为主。随着热解温度的升高,MLS中有机硫逐渐分解并以含硫气体的形式逸出;当热解温度低于600℃时,M LS中硫化物硫逐渐转化为含硫气体、有机硫和少量的黄铁矿硫;当热解温度高于600℃时,M LS中碱性矿物质吸收气相中的H2S转化为硫化物硫,硫化物硫缓慢增加。醋酸酸洗可以保留M LS中大部分的硫化物硫,且酸洗后M LS热解生成的H2S逸出速率增大,峰温向低温方向移动;当热解温度高于600℃时,有机硫和硫化物硫的脱硫反应速率降低,并且M LS中的碱性矿物质与H2S反应生成金属硫化物,导致H2S逸出速率明显降低。  相似文献   

10.
戴超  季聪  顾璠 《化学通报》2017,80(6):568-572
本文研究了CO2为气化介质时,等离子体辅助煤气化过程中焦油组分苯发生的非热转化特性,建立了焦油组分苯、CO2单电极尖端放电非平衡态等离子体反应体系。通过煤气分析仪对转化反应的产物进行分析,并采用可见发射光谱技术对等离子体进行诊断。结果表明,在该反应体系中,苯转化生成的气态产物是CO与CO2的混合气,而H元素直接被氧化生成H20。能量密度对于苯转化反应起主导作用。在相同能量密度条件下,降低苯浓度也能够提高苯的转化率,但改变气速增加反应时间并不能提高苯的转化率。此外,通过光谱分析可得苯的非热转化可由CO2直接解离产生的O自由基触发。  相似文献   

11.
应用等离子体辅助煤气化反应装置对大同煤进行了实验研究,考察了供气量、供粉速率、发生器输入功率、水蒸气压力以及添加不同质量分数的CaCO3 和CaO对煤气化反应的影响,并对不同条件下产品气体的组成进行了分析。实验结果表明,装置的最佳工艺参数为供煤速率150 g/min、供气量18 m3/h、等离子体发生器输出功率100 kW、水蒸气出口压力0.3 MPa。加入添加剂CaCO3和CaO的质量分数分别为10%和5%时,催化效果最好。根据CaCO3和CaO的实验数据可知,在等离子体辅助煤气化过程中CaCO3起催化作用为主,CO2还原为辅。  相似文献   

12.
Plastic waste is a valuable organic resource. However, proper technologies to recover usable materials from plastic are still very rare. Although the conversion/cracking/degradation of certain plastics into chemicals has drawn much attention, effective and selective cracking of the major waste plastic polyethylene is extremely difficult, with degradation of C?C/C?H bonds identified as the bottleneck. Pyrolysis, for example, is a nonselective degradation method used to crack plastics, but it requires a very high energy input. To solve the current plastic pollution crisis, more effective technologies are needed for converting plastic waste into useful substances that can be fed into the energy cycle or used to produce fine chemicals for industry. In this study, we demonstrate a new and effective chemical approach by using the Fenton reaction to convert polyethylene plastic waste into carboxylic acids under ambient conditions. Understanding the fundamentals of this new chemical process provides a possible protocol to solve global plastic‐waste problems.  相似文献   

13.
The Design Optimization of a Plasma Reactor for Chemical Waste Destruction   总被引:1,自引:0,他引:1  
The heat flux and destruction and removal efficiency (DRE) measurements have been made on 100, 150 and 200 mm diameter plasma reactors to optimize the performance. The DRE was measured for pressure and gas atomization techniques of waste injection using both argon and CO2 gases. As a result, the design of the reactor was optimized and the waste throughput was increased by ~17% with improved destruction performance. The 150 mm diameter reactor was found to perform better using gas atomization of feed injection using carbon dioxide at the given power and waste feed rate.  相似文献   

14.
Propane steam reforming using a sliding discharge reactor was investigated under atmospheric pressure and low temperature (420 K). Non-thermal plasma steam reforming proceeded efficiently and hydrogen was formed as a main product (H2 concentration up to 50%). By-products (C2-hydrocarbons, methane, carbon dioxide) were measured with concentrations lower than 6%. The mean electrical power injected in the discharge is less than 2 kW. The process efficiency is described in terms of propane conversion rate, steam reforming and cracking selectivity, as well as by-products production. Chemical processes modelling based on classical thermodynamic equilibrium reactor is also proposed. Calculated data fit quiet well experimental results and indicate that the improvement of C3H8 conversion and then H2 production can be achieved by increasing the gas fraction through the discharge. By improving the reactor design, the non-thermal plasma has a potential for being an effective way for supplying hydrogen or synthesis gas.  相似文献   

15.
The technical feasibility of using an induction-coupled plasma (ICP) torch to synthesize ozone at atmospheric pressure is explored. Ozone concentrations up to ~250 ppm were achieved using a thermal plasma reactor system based on an ICP torch operating at 2.5 MHz and ~11 kVA with an argon/oxygen mixture as the plasma-forming gas. The corresponding production rate and yield were ~20 g ozone/hr and ~2g ozone/kWh, respectively. A gaseous oxygen quench formed ozone by rapid mixing of molecular oxygen with atomic oxygen produced by the torch. The ozone concentration in the reaction chamber was measured by Fourier Transform infrared (FTIR) spectroscopy over a wide range of experimental conditions and configurations. The geometry of the quench gas flow, the quench flow velocity, and the quench flow rate played important roles in determining the ozone concentration. The ozone concentration was sensitive to the torch RF power, but was insensitive to the torch gas flow rates. These observations are interpreted within the framework of a simple model of ozone synthesis.  相似文献   

16.
In this study, a technique of combining steam reforming with partial oxidation of CO2-containing natural gas in a gliding arc discharge plasma was investigated. The effects of several operating parameters including: hydrocarbons (HCs)/O2 feed molar ratio; input voltage; input frequency; and electrode gap distance; on reactant conversions, product selectivities and yields, and power consumptions were examined. The results showed an increase in either methane (CH4) conversion or synthesis gas yield with increasing input voltage and electrode gap distance, whereas the opposite trends were observed with increasing HCs/O2 feed molar ratio and input frequency. The optimum conditions were found at a HCs/O2 feed molar ratio of 2/1, an input voltage of 14.5?kV, an input frequency of 300?Hz, and an electrode gap distance of 6?mm, providing high CH4 and O2 conversions with high synthesis gas selectivity and relatively low power consumptions, as compared with the other processes (sole natural gas reforming, natural gas reforming with steam, and combined natural gas reforming with partial oxidation).  相似文献   

17.
Experiments were performed in a thermal plasma furnace to examine the reduction of TiO2 by hydrogen plasma. The plasma gas composition was 50% hydrogen–50% argon, the plasma torch input power was 13 kW, the TiO2 initial mass was 10 g and the processing time was varied from 10 to 90 min. The reaction product contained between 67% and 73% titanium by mass for all tests. This level of reduction was consistent with chemical equilibrium modeling. There was no detectable enhancement of reduction due to the presence of atomic hydrogen. The Ti-O microstructures produced were characterized using quantitative SEM analysis. The microstructures showed a number of similarities with structures described by previous researchers.  相似文献   

18.
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   

19.
Depolymerization of Polyethylene Using Induction-Coupled Plasma Technology   总被引:5,自引:0,他引:5  
A significant, valuable percentage of today's municipal solid wastestream consists of polymeric materials, for which almost no economicrecycling technology currently exists. This polymeric waste is incinerated,landfilled, or recycled via downgraded usage. Thermal plasma treatment is apotentially viable means of recycling these materials by converting themback into monomers or into other useful compounds. The technical, laboratoryscale, feasibility of using an induction-coupled RF plasma (ICP) heatedreactor for this purpose has been demonstrated in the presentstudy. Polyethylene powder was injected axially through the center of anICP torch. Results from the initial set of experiments, analyzed using astatistical design of experiment technique, showed that plasma plate power,central gas flow rate, probe gas flow rate, powder feed rate, and theinteraction between the quench gas flow rate and power input were the keyprocess parameters affecting the yield of ethylene in the product gasstream. The gaseous products obtained were mainly mixtures of ethylene andpropylene. The amount of propylene obtained was significantly higher thananticipated and was believed to be due to -scission reactionsoccurring at the higher plasma temperatures.  相似文献   

20.
苏际  周军成  刘春燕  王祥生  郭洪臣 《催化学报》2010,31(10):1195-1199
 将 H2/O2 非平衡等离子体现场产生的气态 H2O2和丙烯与耦合反应器中钛硅沸石 TS-1 直接接触, 实现了丙烯气相环氧化反应. 结果表明, 非平衡等离子体生成气态 H2O2 的速率由介质阻挡放电的输入功率决定, 环氧丙烷的生成速率和选择性取决于钛硅沸石催化剂和反应条件. 在 H2 和 O2 进料流量分别为 170 和 8 ml/min, 介质阻挡放电输入功率为 3.5 W, 环氧化反应温度为 110 oC, 丙烯进料量为 18 ml/min, 催化剂用量为 0.8 g 的条件下, 生成环氧丙烷产率达 246.9 g/(kg•h)、环氧丙烷选择性和 H2O2 有效利用率分别为 95.4% 和 36.1%, 反应 36 h 内未见催化剂失活.  相似文献   

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