CFB富氧燃烧中CO_2对煤焦与NO还原作用的影响

为了考察高浓度CO_2对煤焦与NO还原所带来的影响,本文在悬浮床反应器上开展了。N_2和CO_2气氛下煤焦与NO的还原实验。结果表明:在无煤焦或矿物组分催化下CO不与NO发生反应;900℃N_2气氛下,在煤焦与NO反应初期NO还原率保持不变,而在整个反应过程中碳比反应率和CO_2生成比例则持续增大;N_2气氛下,煤焦与NO反应的含碳产物在700℃时以CO_2为主,而随着温度升高CO的生成比例增大,900℃时CO的生成占主导地位;高浓度的CO_2对煤焦-NO还原反应有明显的抑制作用,且温度越高抑制作用越显著,这可能是因CO_2气化抢占碳活性位所致。     

O2/CO2气氛下CO对煤焦异相还原NO影响的研究

为揭示O₂/CO₂燃烧过程中高浓度的CO对煤焦异相还原NO的影响,在1073 K温度下使用山西褐煤在卧式炉上进行了实验。分别对O₂/CO₂浓度比及CO浓度下NO的还原特性进行详细实验研究。研究结果表明:在O₂/CO₂气氛下,O₂浓度为30%时具有较高的还原率;相同O₂浓度下O₂/CO₂气氛较空气气氛NO还原率高,表明在CO存在的条件下,高浓度的CO₂会促进NO的还原;当CO浓度从1.5%逐渐升高时,NO的还原率逐渐降低,到CO浓度为5%时,NO还原率比没有加入CO时还要低,而在空气气氛下CO浓度的变化对NO的还原率影响较小。     

NO2对中温干法脱硫反应影响的实验研究

利用鼓泡床反应器对NO2对中温干法脱硫反应的影响开展了实验研究.分别采用分析纯CaO和工业级石灰两种物质作为吸收剂,在250℃和350℃两个反应温度下研究NO2对吸收剂转化率的影响.结果表明,NO2的存在可以提高吸收剂转化率;250℃下NO2的作用显著高于350℃;250℃下NO2浓度的增加对吸收剂转化率基本没有影响;在350℃时,对于分析纯CaO,NO2浓度的增加降低了吸收剂转化率,这主要是由于SO2与NO2的竞争反应引起的;工业级石灰内含杂质较多,对一些反应有催化作用,因而其反应现象与分析纯CaO略有不同.     

采用详细化学反应机理研究煤富氧燃烧NO_x生成机制

本文采用详细化学反应机理,建立氧煤燃烧气固反应模型,分析煤在富氧燃烧条件下NO_x生成机制,研究不同O₂浓度和分级燃烧对NO_x排放的影响。富氧燃烧时,NO_x生成主要路径为:HCN→CN→NCO→NO和HCN→CN→NCO→HNCO→HN₂→NH→HNO→NO。初始O₂增大,挥发分和HCN析出时间提前,高的O₂初始浓度对燃料N转化率有促进作用;煤富氧分级燃烧时,主燃区还原气氛有利于NO还原为N₂,其主要还原路径如下:NO+CO→N+CO₂、NO+H→N+OH和NO+N→N₂+O,当主燃区过量空气系数SR₁从1.15减小到0.6,N最终转化率（t=1000 ms）只是从0.379减小到0.339,相对于未分级燃烧时变化了10.55%,与煤空气分级燃烧相比,煤富氧分级燃烧对N转化率影响较小。     

高浓度CO2气氛下燃煤氮、硫污染物的释放特性

采用污染物在线分析仪、气相便携红外分析仪研究了程序升温条件下改变氧化介质时煤中氮,硫的释放特性以及含硫物相的浓度变化规律,探讨了不同气氛,CO2浓度与O2浓度单独变化时对NO、SO2析出特性的影响机理.结果表明:O2/CO2燃烧气氛下NO、SO2排放峰值及总量均低于O2/N2气氛.CO2气氛下烟气中存在大量的CO,有利于NO的降解,同时也促进了烟气中其他含硫物相的形成,随着CO2浓度的增加,特别是在燃烧后期,NO、SO2的排放显著降低.O2浓度改变对NO和SO2的释放影响不同:O2浓度升高促进了SO2的析出;但是O2浓度在一定范围内增加对NO的排放并无明显影响,随着O2浓度进一步增加,NO的释放峰向低温区迁移,同时排放量降低.     

基于简单碰撞理论煤粉燃烧动力学模型的研究--PART Ⅱ:颗粒表面的氧气浓度分布模型

为了较准确地预报炉内煤粉燃烧速率,正确区分TGA中滞止煤粉表面与炉内载流煤粉表面氧气浓度的变化规律是非常关键的。从TGA中非稳态条件下坩埚内颗粒表面氧气浓度分布的数理解知,煤样的氧化过程是同时进行的,只是上部的氧化速率大一些,底部的氧化速率小一些;同一样品,同一升温速率,试样的堆积厚度的差异,会影响实验结果的重复性。分析表明,在初始和反应结束时,坩埚内颗粒表面氧气浓度等于环境浓度;反应速率达到最大值时,颗粒表面氧气浓度达到最小值。颗粒在炉内流动燃烧过程中,环境中氧气浓度值是单调减少的,煤焦表面氧的浓度是非线性变化的。     

贫煤焦催化还原NO的实验研究

本文通过实验研究了在贫氧条件下贫煤焦对ＮＯ的还原作用，并与添加催化剂的贫煤焦对ＮＯ的还原进行了比较．研究结果表明，原始贫煤焦对ＮＯ的还原能力很弱，添加催化剂后ＮＯ还原率明显提高，说明催化剂对贫煤焦还原ＮＯ具有很好的催化作用．在贫氧条件下催化剂可以降低贫煤焦与ＮＯ反应的活化能。提高反应速率．反应区氧气浓度和温度对ＮＯ的还原也有重要的影响．     

700～85°C内H2O对CaO上NH3氧化的影响

本文验证了先前建立的FTIR定量方法对高H2O含量下NO和NH3测量的精度,研究了700～850°C内H2O对CaO上NH3氧化的影响.结果表明:含H2O高达15%时,NO和NH3的测量结果仍具有高精度,误差分别为±2%和±3%;H2O抑制CaO上NH3氧化的活性及副产物NO2的生成;NH3转化率随H2O浓度增大先迅速降低而后降低缓慢;同一温度下,NO产物选择性不随H2O浓度变化而改变;基于H2O Langmuir吸附于CaO表面竞争活性位,建立了H2O抑制CaO上NH3氧化的动力学模型,与实验结果符合良好.     

磁场对碳纸上磁电沉积的AuPt颗粒性能的影响

AuPt纳米颗粒是一种催化锂空气电池空气电极上氧气还原反应和氧气析出反应的双功能催化剂．在电沉积制备AuPt颗粒的过程中施加了磁场,恒电流沉积条件下,随着磁场强度的增加,AuPt催化剂颗粒的粒径从1 μm减小到200 nm,同时催化活性增大．垂直于电场方向的磁场有助于提高AuPt/C空气电极的催化能力．使用脉冲电沉积,结晶粒径可减小至约100 nm．通过调节电场和磁场参数,可原位制备具有不同形貌、不同组成和催化性能的AuPt催化剂．     

微波处理对模型焦脱除NO特性的影响

运用自制的微波电加热反应系统,进行了不同微波功率、温度和试验方式对模型焦脱除NO反应性能的影响研究。结果表明:一定程度的微波改性可以促进模型焦吸收NO;NO还原率随微波功率的增大先增大后减小;常温下改性时间为90s时,存在最佳改性功率480 W,该功率改性的模型焦NO还原率最高;常温下改性模型焦的NO还原率普遍高于同功率下的800℃改性模型焦的NO还原率.对部分模型焦进行压汞分析和XPS分析,结果表明,微波处理改变了模型焦的孔隙结构和表面官能团,比表面积和孔容积的增大以及表面含氧官能团的减少有利于NO的吸收。微波热效应和非热效应共同作用影响模型焦还原NO过程。恒温800℃下间歇施加微波方式的NO还原提高率远低于程序升温式。     

燃煤流化床加入氧化钙的氮转化机理

实验研究了 ＣａＯ及与 ＣＯ对 Ｎ２Ｏ、 ＮＯ的催化还原作用。结果表明 ＣａＯ／ＣＯ对 Ｎ２Ｏ的作用表现在可以降低Ｎ２Ｏ的初始分解温度和提高Ｎ２Ｏ的转化率５只有在ＣＯ的共同作用下ＣａＯ可以提高ＮＯ的转化率。以此为基础,分析了不同规模的流化床燃烧不同挥发份含量的煤时加入ＣａＯ后影响Ｎ２Ｏ／ＮＯ排放的不同机理。     

钙基载氧体煤化学链燃烧脱硫试验研究

在钙基载氧体燃煤化学链燃烧技术过程中由于煤气化产物与载氧体之间的副反应导致反应过程中产生大量的SO₂气体。本文选择MAC铁矿石,CaO和石灰石作为脱硫剂,在小型加压固定床上研究不同温度、压力、Ca/S比条件下SO₂气体的脱除问题。结果表明,单独采用CaSO₄载氧体时,随温度升高SO₂气体浓度逐渐增加。添加铁矿石后,SO₂排放浓度降低,主要与Fe₂O₃能够催化抑制CaSO₄分解有关。添加CaO和石灰石脱硫剂后,随温度、压力以及Ca/S比增加,两种脱硫剂的脱硫效率均增加,且在相同的实验条件下得到的CaO的脱硫效果更佳。     

First-principles-based kinetic Monte Carlo simulation of nitric oxide decomposition over Pt and Rh surfaces under lean-burn conditions

First-principles-based kinetic Monte Carlo simulation was used to track the elementary surface transformations involved in the catalytic decomposition of NO over Pt(100) and Rh(100) surfaces under lean-burn operating conditions. Density functional theory (DFT) calculations were carried out to establish the structure and energetics for all reactants, intermediates and products over Pt(100) and Rh(100). Lateral interactions which arise from neighbouring adsorbates were calculated by examining changes in the binding energies as a function of coverage and different coadsorbed configurations. These data were fitted to a bond order conservation (BOC) model which is subsequently used to establish the effects of coverage within the simulation. The intrinsic activation barriers for all the elementary reaction steps in the proposed mechanism of NO reduction over Pt(100) were calculated by using DFT. These values are corrected for coverage effects by using the parametrized BOC model internally within the simulation. This enables a site-explicit kinetic Monte Carlo simulation that can follow the kinetics of NO decomposition over Pt(100) and Rh(100) in the presence of excess oxygen. The simulations are used here to model various experimental protocols including temperature programmed desorption as well as batch catalytic kinetics. The simulation results for the temperature programmed desorption and decomposition of NO over Pt(100) and Rh(100) under vacuum condition were found to be in very good agreement with experimental results. NO decomposition is strongly tied to the temporal number of sites that remain vacant. Experimental results show that Pt is active in the catalytic reaction of NO into N₂ and NO₂ under lean-burn conditions. The simulated reaction orders for NO and O₂ were found to be +0.9 and ?0.4 at 723?K, respectively. The simulation also indicates that there is no activity over Rh(100) since the surface becomes poisoned by oxygen.     

Electrochemical promotion of NO reduction by C3H6 and CO on Rh/YSZ catalyst — Electrodes

The selective catalytic reduction of NO by propylene or CO in the presence of excess oxygen is a system of great technological importance. The effect of Electrochemical Promotion (or Non-faradaic Electrochemical Modification of Catalytic Activity — NEMCA) was used to promote this reaction (C₃H₆ or CO/NO/O₂) on Rh/YSZ catalyst-electrodes. It was found that both the catalytic activity and the selectivity of the Rh catalyst-electrode is affected dramatically upon varying its potential with respect to a Au pseudoreference electrode. Catalytic rate enhancements up to 15000% and 6000% were observed in the case of NO reduction by propylene, while the product selectivity to N₂ production is affected significantly (up to 200%) upon positive potential application. Remarkable promotion of the catalytic activity was also observed in the case of NO reduction by CO, since up to 20-fold increases both in catalytic rates and in NO conversion were obtained under NEMCA conditions. Paper presented at the 6th Euroconference on Solid State Ionics, Cetraro, Calabria, Italy, Sept. 12–19, 1999.     

A new technique for the measurement of the product CO/CO2 ratio at the surface of char particles burning in a fluidized bed

A new experimental technique is proposed to measure the product CO/CO₂ ratio at the surface of spherical char particles during fluidized bed combustion. It is based on the measurement of the burning rate of a single char particle under low oxygen concentration conditions and on the use of an accurate prediction of the particle Sherwood number. This technique was applied to spherical char particles obtained from a bituminous coal which is characterized by a low attrition and fragmentation propensity. The product CO/CO₂ ratio was measured at a bed temperature of 850 °C and at a fluidization velocity of 0.3 m/s in a lab-scale apparatus operated with a bed of 0.5–0.6 mm sand. The char particle size was varied between 2 and 7 mm and the inlet oxygen concentration between 0.1% and 2.0%. Results showed that under the experimental conditions investigated carbon was mostly oxidized to CO₂ within the particle boundary layer, with a maximum fraction of carbon escaping as CO of 10–20% at the lowest oxygen concentrations and largest particle sizes.     

The reactions of NO with diesel soot, fullerene, carbon nanotubes and activated carbons doped with transition metals

This work investigates the reactions of NO with eight different types of carbon particles: activated pinewood charcoal, activated charcoals doped with iron, nickel, copper or platinum nitrates, fullerene, carbon nanotubes and soot produced from a heavy duty diesel engine. For this mixtures of NO and argon were passed through a fixed bed of carbonaceous particles mixed with quartz sand, held at a temperature between 25 and 850 °C. The concentrations of CO, CO₂, NO, NO₂ and N₂O in the off-gases were measured; the concentration of N₂ was inferred by atomic balance. The balance on atomic oxygen closed well for all the materials studied. The results are discussed in terms of an elementary reaction mechanism; estimates are made of apparent activation energies for the overall reactions forming CO and CO₂.     

炉内喷钙脱硫过程数值模拟

建立了一套较为完整的对炉内喷钙脱硫过程进行模拟的方法，获得了炉内气固两相流动、温度分布、石灰石颗粒脱硫化学反应和SO2浓度分布的详细情况。石灰石颗粒的硫化反应主要发生在颗粒与烟气均匀混合之前。     

原位漫反射红外光谱研究NO在Ag/SAPO-34催化剂上的选择性催化还原

原位漫反射红外光谱研究NO在Ag/SAPO 34催化剂上的选择性催化还原过程。考察了以丙烯为还原剂 ,在富氧及 573～ 773K温度条件下的反应。通过比较初始混合气中加氧或不加氧时反应的原位光谱 ,探讨了氧在NO还原过程中的作用。结果表明 ,氧能充分促进丙稀活化以及增加NOx 吸附态含量 ,并且氧的存在是有效产生有机 氮氧化物 (R NO2 ,R ONO)不可缺少的条件。基于光谱实验 ,认为反应机理为 :NO ,丙烯和氧反应 ,在Ag/SAPO 34催化剂上生成吸附的有机 氮氧化物 ,再由这些吸附物种分解成N2 ,催化还原的关键是形成有机 氮氧化物中间体。     

Oscillations, period doublings, and chaos in CO oxidation and catalytic mufflers

Early experimental observations of chaotic behavior arising via the period-doubling route for the CO catalytic oxidation both on Pt(110) and Ptgamma-Al(2)O(3) porous catalyst were reported more than 15 years ago. Recently, a detailed kinetic reaction scheme including over 20 reaction steps was proposed for the catalytic CO oxidation, NO(x) reduction, and hydrocarbon oxidation taking place in a three-way catalyst (TWC) converter, the most common reactor for detoxification of automobile exhaust gases. This reactor is typically operated with periodic variation of inlet oxygen concentration. For an unforced lumped model, we report results of the stoichiometric network analysis of a CO reaction subnetwork determining feedback loops, which cause the oscillations within certain regions of parameters in bifurcation diagrams constructed by numerical continuation techniques. For a forced system, numerical simulations of the CO oxidation reveal the existence of a period-doubling route to chaos. The dependence of the rotation number on the amplitude and period of forcing shows a typical bifurcation structure of Arnold tongues ordered according to Farey sequences, and positive Lyapunov exponents for sufficiently large forcing amplitudes indicate the presence of chaotic dynamics. Multiple periodic and aperiodic time courses of outlet concentrations were also found in simulations using the lumped model with the full TWC kinetics. Numerical solutions of the distributed model in two geometric coordinates with the CO oxidation subnetwork consisting of several tens of nonlinear partial differential equations show oscillations of the outlet reactor concentrations and, in the presence of forcing, multiple periodic and aperiodic oscillations. Spatiotemporal concentration patterns illustrate the complexity of processes within the reactor.