Formation of the surface NO during N2O interaction at low temperature with iron-containing ZSM-5

Interaction of N2O at low temperatures (473-603 K) with Fe-ZSM-5 zeolites (Fe, 0.01-2.1 wt %) activated by steaming and/or thermal treatment in He at 1323 K was studied by the transient response method and temperature-programmed desorption (TPD). Diffuse reflectance infrared fourier transform spectroscopy (DRIFTS) of NO adsorbed at room temperature as a probe molecule indicated heterogeneity of surface Fe(II) sites. The most intensive bands were found at 1878 and 1891 cm(-1), characteristic of two types mononitrosyl species assigned to Fe2+(NO) involved in bi- and oligonuclear species. Fast loading of atomic oxygen from N2O on the surface and slower formation of adsorbed NO species were observed. The initial rate of adsorbed NO formation was linearly dependent on the concentration of active Fe sites assigned to bi- and oligonuclear species, evolving oxygen in the TPD at around 630-670 K. The maximal coverage of a zeolite surface by NO was estimated from the TPD of NO at approximately 700 K. This allowed the simulation of the dynamics of the adsorbed NO formation at 523 K, which was consistent with the experiments. The adsorbed NO facilitated the atomic oxygen recombination/desorption, the rate determining step during N2O decomposition to O2 and N2, taking place at temperatures > or =563 K.     

The importance of NO+ (H2O)4 in the conversion of NO+ (H2O)n to H3O+ (H2O)n: I. Kinetics measurements and statistical rate modeling

The kinetics for conversion of NO(+)(H(2)O)(n) to H(3)O(+)(H(2)O)(n) has been investigated as a function of temperature from 150 to 400 K. In contrast to previous studies, which show that the conversion goes completely through a reaction of NO(+)(H(2)O)(3), the present results show that NO(+)(H(2)O)(4) plays an increasing role in the conversion as the temperature is lowered. Rate constants are derived for the clustering of H(2)O to NO(+)(H(2)O)(1-3) and the reactions of NO(+)(H(2)O)(3,4) with H(2)O to form H(3)O(+)(H(2)O)(2,3), respectively. In addition, thermal dissociation of NO(+)(H(2)O)(4) to lose HNO(2) was also found to be important. The rate constants for the clustering increase substantially with the lowering of the temperature. Flux calculations show that NO(+)(H(2)O)(4) accounts for over 99% of the conversion at 150 K and even 20% at 300 K, although it is too small to be detectable. The experimental data are complimented by modeling of the falloff curves for the clustering reactions. The modeling shows that, for many of the conditions, the data correspond to the falloff regime of third body association.     

胶溶法制备镧-钡共稳定氧化铝的性能

以硝酸为胶溶剂, 两种拟薄水铝石为前驱体, 用胶溶法制备了镧-钡共稳定的氧化铝. 采用X 射线衍射(XRD)、表面分析仪(BET)、氨气程序升温脱附(NH3-TPD)和NO2程序升温脱附(NO2-TPD)技术对所制备的镧改性和镧钡共改性氧化铝的结构特性和表面性能进行了表征. XRD结果表明, 改性氧化铝在1273 K焙烧后均以γ-Al2O3相存在. 当BaO添加量达到14%(w)时, 有少量BaCO3生成. BET结果表明, 在1273 K下焙烧5 h后, 5%(w)La2O3稳定的氧化铝(Ba-0)和5%La2O3与8%BaO共同稳定的氧化铝(Ba-8)均具有较大的比表面积, 各种氧化铝的吸附等温线表明它们的孔形状均为狭缝型孔和瓶型孔, 孔径分布曲线表明, 仅有样品Ba-8的孔径分布较宽, 孔径为6-10 nm, 其它三种样品的孔径均集中在10 nm; NH3-TPD结果表明, 随着氧化钡添加量的逐渐增多, 氧化铝表面的酸量、酸强度逐步减少. NO2-TPD结果表明, 添加BaO后载体对NO2的吸附量增多, 随着BaO含量的增多, 体相Ba(NO3)2增多. 由于样品Ba-8同时具有很好的织构性质、适中的表面酸量和酸强度分布及NO2吸附脱附能力, 使得以它为载体的催化剂具有最好的催化性能,丙烷的起燃温度和完全转化温度分别为526 K和593 K.     

SiO2—Al2O3和MgO催化剂上吸附CH3NO2的TPD和IR研究

用TPD和IR方法研究了CH_3NO_2在典型固体酸SiO_2-Al_2O_3和固体碱MgO催化剂上的吸附分解。结果表明,在SiO_2-Al_2O_3表面CH_3NO_2吸附转化为表面甲酰胺物种,后者在高温下分解为CO_2和NH_3。在MgO表面CH_3NO_2吸附形成多种表面化学物种,它们在升温过程中脱附,并通过表面亚硝基甲烷物种分解为NO、C_2H_4、C_2H_6和N_2O.讨论了CH_3NO_2分解过程中表面酸、碱中心的作用。     

沥青基球状活性炭担载尿素用于NO2的低温选择性催化还原行为研究

将作为还原剂的尿素担载于沥青基球状活性炭(PSAC)上研究了NO₂的低温选择性催化还原(SCR)反应。结果表明,PSAC上尿素担载量的提高可以增大NO₂与尿素的反应几率;当尿素担载量由8%提高到30%时,SCR反应脱硝活性显著提高,脱硝时间相应延长。在30~90℃,升高反应温度会减小NO₂在PSAC表面的吸附量,从而导致NO_x的脱除量减小。增加反应气氛中NO₂和O₂的浓度均有利于脱硝活性的提高,但当O₂进料浓度大于9%时,继续增加O₂进料浓度对脱硝活性的改善作用变得微弱。降低空速有利于提高脱硝活性和延长脱硝时间。当反应温度为30℃、空速为2000h^-1、NO₂和O₂的进料浓度分别为0.05%和21%时,尿素担载量为8%的PSAC可在49h内实现85%以上的NO_x转化率。     

等离子体协同CuO/TiO2-γ-Al2O3催化CH4脱除NO

对合成的12%CuO/15%TiO2/γ-Al2O3催化剂进行了BET和XRD表征, 并结合等离子体与催化协同脱除NO的反应装置, 考察了单一等离子体、单一催化剂以及等离子体与催化协同脱除NO+CH4+O2的反应结果, 研究了上述三种条件下NO和CH4的转化率. BET表征结果表明, 15%TiO2/γ-Al2O3的孔径分布在微孔和介孔之间; XRD结果表明, 催化剂表面有CuO晶相; 反应活性数据表明, 单一等离子体存在时, NO和CH4的转化率随着等离子体的输入功率增大而逐渐增加, 反应体系引入体积分数为2.5%的O2气促进了NO和CH4的转化; 使用单一催化剂时, NO和CH4的转化率随温度升高而分别增大至30%和20%. 同时NO转化率随O2气浓度的增加先增加后降低, CH4随O2气浓度的增加转化率逐渐增大; 等离子体与催化剂协同作用NO+CH4+O2反应中, NO和CH4的转化率随O2气浓度的增加与只有催化剂存在条件下的变化趋势一致, 但是增大了NO的低温转化率, 同时CH4的转化率提高到了90%.     

H2O和SO2对Ce(1)Mn(3)Ti催化剂催化氧化NO性能的影响

为了提高MNO_x/TiO₂催化剂催化氧化NO的活性,在载体TiO₂上负载醋酸锰的同时掺杂了一定量的硝酸铈,构成了Ce(1)Mn(3)Ti催化剂,并对催化剂进行XRD、BET和XPS等表征。重点考察了H₂O和SO₂对催化剂活性的影响,通过FT-IR、SEM和BET等表征手段对毒化前后的催化剂组成及结构进行了分析。结果表明,Ce(1)Mn(3)Ti催化剂具有较好的活性,在空速41 000 h^-1、NO体积分数为300×10^-6及O₂含量10%的条件下,反应温度200℃时NO转化率可达58%,250℃时NO转化率达到最高值85%。单独加入4%H₂O使得催化剂活性降低,升高反应温度,H₂O对催化剂的影响减弱;同时通入4%H₂O和100×10^-6SO₂,在反应温度250℃时,NO转化率下降并维持在48%左右,停止通入后恢复到61%。H₂O和SO₂使催化剂活性物种硫酸盐化失活。     

Adsorption and dissociation of NO on stepped Pt (533)

We present an experimental and theoretical investigation of the adsorption, desorption, and dissociation of NO on the stepped Pt (533) surface. By combining temperature programmed desorption and reflection absorption infrared spectroscopy, information about the adsorption sites at different temperatures is obtained. Surprisingly, metastable adsorption structures of NO can be produced through variation of the dosing temperature. We also show that part of the NO molecules adsorbed on the step sites dissociates around 450 K. After dissociation the N atoms can desorb either by combining with an O fragment, or with another N atom, resulting in NO and N(2). The N(2) production can be enhanced by coadsorbing CO on the surface: CO scavenges the oxygen atom, thereby suppressing associative recombinative desorption of N and O atoms. Density functional theory calculations are used to reveal the adsorption energies and vibrational frequencies of adsorbed NO as well as barriers for dissociation of NO and for diffusion of N atoms. The combined experimental results and theoretical calculations reveal that dissociation of NO is the rate limiting step in the formation of N(2).     

N2 emission in NO and N2O reduction on Rh(100) and Rh(110)

The angular distribution of desorbing N(2) was studied in both the thermal decomposition of N(2)O(a) on Rh(100) at 60-140 K and the steady-state NO (or N(2)O) + D(2) reaction on Rh(100) and Rh(110) at 280-900 K. In the former, N(2) desorption shows two peaks at around 85 and 110 K. At low N(2)O coverage, the desorption at 85 K collimates at about 66 degrees off normal towards the [001] direction, whereas at high coverage, it sharply collimates along the surface normal. In the NO reduction on Rh(100), the N(2) desorption preferentially collimates at around 71 degrees off normal towards the [001] direction below about 700 K, whereas it collimates predominantly along the surface normal at higher temperatures. At lower temperatures, the surface nitrogen removal in the NO reduction is due to the process of NO(a) + N(a) --> N(2)O(a) --> N(2)(g) + O(a). On the other hand, in the steady-state N(2)O + D(2) reaction on Rh(110), the N(2) desorption collimates closely along the [001] direction (close to the surface parallel) below 340 K and shifts to ca. 65 degrees off normal at higher temperatures. In the reduction with CO, the N(2) desorption collimates along around 65 degrees off normal towards the [001] direction above 520 K, and shifts to 45 degrees at 445 K with decreasing surface temperature. It is proposed that N(2)O is oriented along the [001] direction on both surfaces before dissociation and the emitted N(2) is not scattered by adsorbed hydrogen.     

O2/CO2气氛下木醋调质石灰石再燃/先进再燃脱硝性能研究

在O₂/CO₂气氛下利用沉降炉脱硝实验台,对木醋调质石灰石和醋酸钙的再燃/先进再燃脱硝特性以及氨气的选择性非催化还原脱硝特性进行了研究。结果表明,木醋调质石灰石和醋酸钙的再燃脱硝效率随温度的升高先提高后降低,1 323 K时获得最高脱硝效率分别为82.70%和78.52%;再燃脱硝氧浓度不宜过高,合适的再燃比为14%~17%,停留时间为0.8 s。氨气选择性非催化还原脱硝在1 173 K时获得最高脱硝效率为95.41%,温度窗口为1 142~1 335 K;随着氧浓度的增大,脱硝效率不断降低,反应适宜的氨氮比为1.5,停留时间为1.2 s。按氨氮比0.75向再燃区喷入氨气可显著提高木醋调质石灰石和醋酸钙的再燃脱硝效率,同时脱硝反应适宜的温度区间也得到显著拓宽,1 323 K时两者获得的先进再燃脱硝效率分别为93.49%和92.79%。     

Kinetic and product study of the gas-phase reactions of OH radicals, NO(3) radicals, and O(3) with (C(2)H(5)O)(2)P(S)CH(3) and (C(2)H(5)O)(3)PS

Rate constants for the reactions of OH radicals and NO3 radicals with O,O-diethyl methylphosphonothioate [(C(2)H(5)O)(2)P(S)CH(3); DEMPT] and O,O,O-triethyl phosphorothioate [(C(2)H(5)O)(3)PS; TEPT] have been measured using relative rate methods at atmospheric pressure of air over the temperature range 296-348 K for the OH radical reactions and at 296 +/- 2 K for the NO(3) radical reactions. At 296 +/- 2 K, the rate constants obtained for the OH radical reactions (in units of 10(-11) cm(3) molecule(-1) s(-1)) were 20.4 +/- 0.8 and 7.92 +/- 0.27 for DEMPT and TEPT, respectively, and those for the NO(3) radical reactions (in units of 10(-15) cm(3) molecule(-1) s(-1)) were 2.01 +/- 0.20 and 1.03 +/- 0.10, respectively. Upper limits to the rate constants for the reactions of O(3) with DEMPT and TEPT of <6 x 10(-20) cm(3) molecule(-1) s(-1) were determined in each case. Rate constants for the OH radical reactions, measured relative to k(OH + alpha-pinene) = 1.21 x 10(-11) e(436/T) cm(3) molecule(-1) s(-1), resulted in the Arrhenius expressions k(OH + DEMPT) = 1.08 x 10(-11) e(871+/-25)/T cm(3) molecule(-1) s(-1) and k(OH + TEPT) = 8.21 x 10(-13) e(1353+/-49)/T cm(3) molecule(-1) s(-1) over the temperature range 296-348 K, where the indicated errors are two least-squares standard deviations and do not include the uncertainties in the reference rate constant. Diethyl methylphosphonate was identified and quantified from the OH radical and NO(3) radical reactions with DEMPT, with formation yields of 21 +/- 4%, independent of temperature, from the OH radical reaction and 62 +/- 11% from the NO(3) radical reaction at 296 +/- 2 K. Similarly, triethyl phosphate was identified and quantified from the OH radical and NO(3) radical reactions with TEPT, with formation yields of 56 +/- 9%, independent of temperature, from the OH radical reaction and 78 +/- 15% from the NO(3) radical reaction at 296 +/- 2 K.     

反应条件对Cu/Al-Ce-PILC上丙烯选择性催化还原NO反应的影响

 采用聚合羟基复合阳离子合成交联黏土Al-Ce-PILC, 经SO2-4改性后,以浸渍法制备了铜基交联黏土催化剂Cu/Al-Ce-PILC, 并将其应用于C3H6选择性还原NO的反应,考察了预处理气氛、 O2和C3H6浓度、空速、水蒸气和SO2等反应条件对催化剂性能的影响. 结果表明, He预处理后催化剂表面的Cu物种以Cu+和Cu2+两种形式存在,而H2预处理后仅以Cu+存在, NO转化率最大值由23%升至56%. 反应体系中适当的O2和C3H6浓度可促进NO还原为N2, 但过高的浓度反而可降低NO的还原活性, O2同时可起到抑制积炭、清洁催化剂表面的作用. NO转化率随着空速的增大而降低. 10%水蒸气的存在可抑制NO的还原和C3H6的氧化,其转化率曲线向高温方向位移. 但是,由于金属氧化物交联柱表面的疏水特性, Cu/Al-Ce-PILC较Cu/ZSM-5具有较强的耐湿热稳定性, NO和C3H6最大转化率仅分别下降13%和5%. SO2的存在明显抑制了催化剂的低温活性,但对高温活性有一定促进作用.     

预吸附氧对NO在Pt(110)表面吸附和分解的影响

 利用程序升温反应谱、X射线光电子能谱和高分辨电子能量损失谱研究了NO在清洁和预吸附氧的Pt(110)表面的吸附和分解. 在清洁的Pt(110)表面,室温下低覆盖度时NO以桥式吸附为主,高覆盖度时NO以线式吸附为主. 加热过程中部分NO(主要是桥式吸附物种)分解,生成N2和N2O. 室温下O2在Pt(110)表面发生解离吸附. Pt(110)表面预吸附氧会抑制桥式吸附NO的生成,并导致其脱附温度降低40 K. 降低脱附温度有利于桥式吸附NO的分子脱附,从而抑制分解反应. 这些结果从表面化学的角度合理地解释了铂催化剂在富氧条件下对NO分解能力的降低.     

Fe-Ce-ZSM-5 a new catalyst of outstanding properties in the selective catalytic reduction of NO with NH(3)

A Fe-Ce-ZSM-5 catalyst elaborated from a new synthesis route exhibits very high NO conversion (75-100%) in the selective catalytic reduction of NO by NH(3) in a wide temperature window (523-823 K), even in the presence of H(2)O and SO(2).     

ZrO2催化剂上吸附CH3NO2的分解

用TPD和IR谱研究了CH_3NO_2在ZrO_2催化剂上的吸附活化和分解反应。结果表明,室温下CH_3NO_2在ZrO_2表面发生不可逆化学吸附,它们在TPD过程中可完全分解生成HCN、CO_2、CO、NH_3、H_2O和微量NO。其中H_2O和NO的脱附峰出现在383K附近。其它产物在543K附近出现极大值。IR结果表明,CH_3NO_2在ZrO_2上吸附形成诸如[CH_2NO_2],和/或吸附物种。这些吸附物种在升高温度时转化为表面态“HCN”。“HCN”或脱附,或进一步向表面“HCONH_2”和/或“HCOO~-”转化,后两种表面物种分解可产生CO_2、NH_3和CO。将这些结果与CH_3NO_2在SiO_2-Al_O_3和MgO催化剂上的结果进行了比较,讨论了酸-碱双功能性ZrO_2催化剂上CH_3NO_2活化分解的特点。     

闭路循环动态针捕集-气相色谱法分析地下水中的硝基苯和苯胺

动态针捕集(Needle trap,NT)是一种集采样、提取、浓缩、进样于一体的免溶剂分析技术,适于痕量有机目标组分的采样分析.本研究通过对比6种采样技术,研究了基于超声的闭路循环动态顶空-NT分析地下水中的硝基苯及苯胺的方法,确定了NT对地下水目标物顶空采样的最佳条件;通过对比GC普通分流/不分流进样口和一种多模式OPTIC2进样口,优化NT的解吸条件,得出的OPTIC2进样口对目标物响应值高且峰形尖锐.填充一层吸附剂的NT对目标物的残留低于0.79％,苯胺的检出限为2.9～3.7μg/L,硝基苯的检出限为0.7～1.9 μg/L.苯胺和硝基苯的回收率在83％～113％之间.     

Pretreatment of Alumina and Its Influence on the Properties of Co/Alumina Catalysts for Fischer-Tropsch Synthesis

16.6%Co/γ-Al_2O_3 catalysts prepared by incipient wetness impregnation method were used for Fischer-Tropsch synthesis.The support was pre-treated with different concentration of NH_4NO_3 aqueous solution.The effect of support pre-treatment on the properties of support and performance of supported- cobalt-based catalysts was investigated.To treat the support with NH_4NO_3 aqueous solution enlarged the pore ofγ-Al_2O_3,decreased the impurity Na_2O content,and weakened the surface acidity ofγ-Al_2O_3. The change in the properties of the support decreased the interaction between cobalt species and support, enhanced the CO hydrogenation rate and the C_(5 )selectivity.For all catalysts,increasing the reaction temperature increased the CO hydrogenation rate or the CO conversion,slightly decreased the total hydrocarbon selectivity,and favored the formation of methane and light hydrocarbons,while the chain growth probability decreased.For 16.6%Co/γ-Al_2O3 catalysts,prepared with the support treated with 100 g/L NH_4NO3 aqueous solution,the CO conversion,the CH_4 selectivity,and the C_(5 )selectivity were 83.13%,6.86% and 82.75% respectively,and the chain growth probability was 0.83 under the condition of 493 K,1.5 MPa,500 h~(-1)and the molar ratio of H_2 to CO being 2.0 in feed.     

Dealumination and characterization of chabazite for catalytic application

Dealumination of the small-pore zeolite chabazite (CHA) was performed with ammonium hexafluorosilicate under solid and liquid-state conditions to increase the Si-to-Al ratio from 2.0 to 6.0. In the solid state, the mesopore fraction increased with repeating hydrothermal synthesis at 423 K, which was confirmed by nitrogen adsorption?Cdesorption. In the liquid state, the formation of mesopores decreased substantially and the resulting CHA had an Si-to-Al ratio of ca. 5. The result of desorption of NO?CNO₂ from the Cu ion-exchanged dealuminated CHA in the solid state indicated that the presence of mesopores reduced NO?CNO₂ adsorption and desorption of NO₂ occurred at 383 and 683 K whereas for the high-silica analog SSZ-13 desorption of NO₂ occurred mostly at 473 and at 673 K.     

NO气体在TiO2表面的吸附行为

采用TPD (Temperature Programmed Desorption)试验方法测定了NO在TiO₂表面吸附后的脱附谱, 揭示了气体脱附量的变化规律. 结果表明, NO在TiO₂表面吸附后可在两个峰值温度450和980 K脱附出N₂气体, 其活化能分别是0.48 和2.5 eV. TiO₂表面经预覆氧处理后, N₂的脱附量降低. N₂的脱附量随NO气体暴露量增加而增加, 但当气体覆盖度超过一定值后, 脱附量趋于定值. 脱附峰值温度随气体暴露量的增加而降低.     

Performance and Kinetics Studies on Selective Catalytic Reduction of NOx with NH3 over MnOx-WO3/TiO2 Catalyst

The catalytic activities of MnOx-WO3/TiO2 for selective catalytic reduction(SCR) of NO with NH3 were investigated in a wide range of temperature and reaction condition.It yielded a NOx conversion of 80.3%-99.6% and a N2 product selectivity of 100%-98.7% during 100 °C to 350 °C at gas hourly space velocity(GHSV)=18900 h-1.In the presence of 0.01% SO2 and 6% H2O at 120 °C,the NOx conversion can maintain 98.5%.At 300 °C and with 0.07% SO2 in reactant stream,the NOx conversion stabilized at 99% as high as the commercial V-W/TiO2 catalyst's level.The steady-state kinetics study shows that O2 played a promoting role.In the presence of less than 1.5% O2,NOx conversion can increase sharply with the increase of O2 concentration.The reaction order was zero with respect to NH3 and first with respect to NO with excess O2 and H2O.The kinetics active energy(Ea) of Mn-W/TiO2 was calculated to be 6.24 kJ/mol according to the kinetic experiment at various temperatures,much lower than those of other catalysts reported in the literature.Mn-W/TiO2 is an excellent catalyst for SCR of NO with NH3 by now.