稀土钙钛矿型催化剂对CO催化氧化活性及表面氧种的研究

研究了CO在不同催化剂La1 -xSrxMn1 -xBxO3(B =Fe、Ni、Cr)上的氧化反应活性 ,并利用程序升温热脱附(TPD)的方法对不同x值催化剂表面氧种及其含量的变化规律进行了考察 ,结合反应活性及表面吸附氧种随x值的变化规律 ,研究了催化剂对CO氧化反应的活性与表面活性氧种的关系。     

Ce掺杂改性Ni-Al-Ox催化剂CO-NO反应性能

通过尿素法制备了一系列Ce掺杂改性的Ni-Al-O_x复合氧化物催化剂,并研究了催化剂的CO-NO反应性能.活性测试结果表明,Ni-Al-Ce-O_x的催化活性明显优于Ni-Al-O_x,且活性随着Ce含量的增加而提高.当Ce的掺杂量为20%时,250℃条件下,NO转化率高达95%以上,同时催化剂具有良好的抗H₂O性能.XRD和Raman分析表明,Ce掺杂Ni-Al-O_x催化剂促进了氧空位产生.而XPS结果显示,氧空位随着Ce含量的增加而增加.H₂-TPR结果表明,Ce的掺杂使催化剂的氧化还原性能增强.结合NO-TPD和FTIR的表征结果,进一步发现Ce的加入使表面氧难以将NO氧化成硝酸盐,有利于NO在Ce的氧空位上分解为N₂或N₂O,促进CO-NO反应的进行.     

In situ adsorption-catalysis system for the removal of o-xylene over an activated carbon supported Pd catalyst

An activated carbon (AC) supported Pd catalyst was used to develop a highly efficient in situ adsorption-catalysis system for the removal of low concentrations of o-xylene. In this study, three kinds of Pd/AC catalysts were prepared and tested to investigate the synergistic efficiency between adsorption and catalysis for o-xylene removal. The Pd/AC catalyst was first used as an adsorbent to concentrate dilute o-xylene at low temperature. After saturated adsorption, the adsorbed o-xylene was oxidized to CO2 and H2O by raising the temperature of the catalyst bed. The results showed that more than 99% of the adsorbed o-xylene was completely oxidized to CO2 over a 5% Pd/AC catalyst at 140℃. Brunauer-Emmett-Teller (BET) analysis, scanning electron microscopy (SEM), temperature-programmed desorption (TPD), and temperature-programmed oxidation (TPO) were applied to investigate the physical properties of o-xylene adsorption-desorption and the in situ adsorption-catalysis activity of the AC support and Pd/AC catalyst. A synergistic relationship between the AC support and the active Pd species for the removal of low concentrations of o-xylene was established.     

Effect of CeO2 and Al2O3 on the activity of Pd/Co_3O_4/cordierite catalyst in the three-way catalysis reactions (CO/NO/CnHm)

The present article studies the effect of CeO₂ and Al₂O₃ on the activity of Pd/Co₃O₄/cordierite catalyst in conversion of NO, CO, C_nH_m. The catalysts were characterized by temperature programmed reduction with hydrogen, X-ray diffraction, X-ray photoelectron spectroscopy and transmission electron microscopy. It is shown that the effect of CeO₂ on the properties of Pd/Co₃O₄/cordierite catalyst depends on preparation method. The catalyst obtained by co-deposition of cerium and cobalt oxides has higher activity in CO oxidation (CO + O₂ and CO + NO) and total hexane oxidation (C₆H₁₄ + O₂). Such phenomenon is probably caused by more than stoichiometric amount of formed oxygen vacancies, an increase in both mobility of surface oxygen and dispersity of components in the catalytic composition. It is demonstrated that CeO₂ addition promotes the SO₂ resistance of Pd/Co₃O₄/cordierite. The second support decreases the activity of Pd/Co₃O₄/cordierite catalyst in the reactions of CO and C₆H₁₄ with oxygen because of CoAl₂O₄ formation.     

Synergistic effect of F and triggered oxygen vacancies over F-TiO2 on enhancing NO ozonation

Oxidation-absorption technology is a key step for NO_x removal from low-temperature gas. Under the condition of low O₃ concentration (O₃/NO molar ratio = 0.6), F-TiO₂ (F-TiO₂), which is cheap and environmentally friendly, has been prepared as ozonation catalysts for NO oxidation. Catalytic activity tests performed at 120°C showed that the NO oxidation efficiency of F-TiO₂ samples was higher than that of TiO₂ (about 43.7%), and the NO oxidation efficiency of F-TiO₂-0.15 was the highest, which was 65.3%. Combined with physicochemical characteristics of catalysts and the analysis of active species, it was found that there was a synergistic effect between F sites and oxygen vacancies on F-TiO₂, which could accelerate the transformation of monomolecular O₃ into multi-molecule singlet oxygen (¹O₂), thus promoting the selective oxidation of NO to NO₂. The oxidation reaction of NO on F-TiO₂-0.15 follows the Eley-Rideal mechanism, that is, gaseous NO reacts with adsorbed O₃ and finally form NO₂.     

等离子体场内CeO2催化降解甲醇的表面活性氧物种来源与作用研究

利用水热法制备了3种不同形貌(纳米棒、纳米颗粒、纳米立方体)的CeO_2催化剂,并通过比表面积测试(BET)、扫描电子显微镜(SEM)、拉曼光谱分析(Raman)、O_2程序升温脱附(O_2-TPD)手段表征其物理化学性质,结果发现,CeO_2纳米棒的表面氧空位和氧物种最多.等离子体与催化协同降解甲醇性能评价实验结果显示,CeO_2纳米棒展现出最好的催化性能.进一步设计实验(甲醇-TPD、不同气氛常温催化、催化剂内后置比较、O_3催化氧化)推测在等离子体场内CeO_2表面活性氧物种来源及其作用.结果表明:①在等离子体场内参与CeO_2表面催化反应的活性氧物种有两个来源,一是催化剂本身存在的表面氧物种,二是等离子体区域产生的短寿命物种及长寿命物种(主要是O_3),其中,O_3分解产生的活性氧物种是提高催化性能的主要因素.②不同形貌CeO_2由于表面氧空位含量不同,导致O_3在催化剂上分解产生的活性氧物种的量不同,最终影响等离子体催化性能.     

Mn-Cu-O负载型催化剂上CO氧化性能的研究

研究了ＺｒＯ２或Ａｌ２Ｏ３负载Ｍｎ－Ｃｕ－Ｏ体系催化剂ＣＯ催化氧化活性，以及物相结构，表面氧性能与活性的关系。结果表明，锆基催化剂的氧化活性明显优于铝基催化剂，起燃温度Ｔ５０低达５０℃，ＺｒＯ２载 利于活性组份形成高活性物相，并促进表面吸附氧的脱附，表现出催化剂表面吸附氧的脱附温度高低次序与其氧化活性有一致的对应关系。     

A comparative investigation of NdSrCu_(1-x)Co_xO_(4-δ) and Sm_(1.8)Ce_(0.2)CU_(1-x)Co_xO_(4-δ) (x: 0-0.4) for NO decomposition

A series of single-phase T-structured NdSrCu_(1-x)Co_xO_(4-δ) with oxygen vacancies and T'-structured Sm_(1.8)Ce_(0.2)Cu_(1-x)Co_xO_(4-δ) (x:0-0.4) with oxygen excess were prepared using ultrasound-assisted citric acid complexing method, and characterized by means of techniques such as thermogravimetric analysis and NO temperature-progranuned desorption (NO-TPD). The catalytic activities of these materials were evaluated for the decomposition of NO. It was found that the NdSrCut_xCoxO4_b catalysts were of oxygen vacancies whereas the Sm_(1.8)Ce_(0.2)CU_(1-x)Co_xO_(4-δ) ones possessed excessive oxygen (i.e., over-stoichiometric oxygen); with a rise in Co doping level,the oxygen vacancy density of NdSrCu_(1-x)Co_xO_(4-δ) decreased while the over-stoichiometric oxygen amount of Sm_(1.8)Ce_(0.2)CU_(1-x)Co_xO_(4-δ)increased. The NO-TPD results revealed that NO could be activated much easier over the oxygen-deficient perovskite-like oxides than over the oxygen-excessive perovskite-like oxides, with the NdSrCuO_(3.702) catalyst showing the best efficiency in activating NO molecules. Under the conditions of 1.0% NO/helium, 2800 hr~(-1), and 600-900℃, the catalytic activity of NO decomposition followed the order of NdSrCuO_(3.702)> NdSrCu_(0.8)Co_(0.2)O_(3.736) > NdSrCu_(0.6)Co_(0.4)O_(3.789) > Sm_(1.8)Ce_(0.2)Cu_(0.6)Co_(0.4)O_(4.187)> Sm_(1.8)Ce_(0.2)Cu_(0.8)Co_(0.2)O_(4.104)> Sm_(1.8)Ce_(0.2)CuO_(4.045), in concord with the sequence of decreasing oxygen vacancy or oxygen excess density. Based on the results, we concluded that the higher oxygen vacancy density and the stronger Cu~(3+)/Cu~(2+) redox ability of NdSrCu_(1-x)Co_xO_(4-δ) account for the easier activation of NO and consequently improve the catalytic activity of NO decomposition over the catalysts.     

LaBO3钙钛矿催化剂的VOCs催化燃烧特性

采用共沉淀法制备了LaBO3(B=Cr、Fe、Mn、Co、Ni)钙钛矿催化剂,并用XRD、BET、H2-TPR、O2-TPD等手段对其进行了表征,考察了催化剂对苯、甲苯、乙酸乙酯和丙酮的催化燃烧性能.结果表明,Cr、Fe钙钛矿晶相中存在少量的La2CrO6和La2O3杂晶相,破坏了其活性结构.Mn、Co、Ni则能与La形成完善的钙钛矿晶相,且表现出优良的催化性能,其中LaMnO3为阳离子缺陷结构,存在较丰富的晶格氧,更适合催化燃烧C—H键键能较高和难以活化的有机分子(如苯);LaCoO3、LaNiO3属于阴离子缺陷钙钛矿结构,存在更丰富的表面氧,更适合催化燃烧易在低温下活化的含氧类有机分子(如乙酸乙酯、丙酮).     

Study on catalysts for combustion of lean CH_4

ＳｔｕｄｙｏｎｃａｔａｌｙｓｔｓｆｏｒｃｏｍｂｕｓｔｉｏｎｏｆｌｅａｎＣＨ＿４ＺｈｏｕＺｅｘｉｎｇ，ＹｉｎＬｉｎｇ，ＸｕＪｉｎｇＫｅｓｅａｒｃｈＣｅｎｔｅｒｆｏｒＥｃｏ－ＦｎｖｉｒｏｎｍｅｎｔａｌＳｃｉｅｎｃｅｓ，ＣｈｉｎｅｓｅＡｃａｄｅｍｙｏｆＳｃ...     

N-doped CoAl oxides from hydrotalcites with enhanced oxygen vacancies for excellent low-temperature propane oxidation

A series of nitrogen-doped CoAlO (N-CoAlO) were constructed by a hydrothermal route combined with a controllable NH₃ treatment strategy. The effects of NH₃ treatment on the physico-chemical properties and oxidation activities of N-CoAlO catalysts were investigated. In comparison to CoAlO, a smallest content decrease in surface Co³⁺ (serving as active sites) while a largest increased amount of surface Co²⁺ (contributing to oxygen species) are obtained over N-CoAlO/4h among the N-CoAlO catalysts. Meanwhile, a maximum N doping is found over N-CoAlO/4h. As a result, N-CoAlO/4h (under NH₃ treatment at 400°C for 4 hr) with rich oxygen vacancies shows optimal catalytic activity, with a T₉₀ (the temperature required to reach a 90% conversion of propane) at 266°C. The more oxygen vacancies are caused by the co-operative effects of N doping and suitable reduction of Co³⁺ for N-CoAlO/4h, leading to an enhanced oxygen mobility, which in turn promotes C₃H₈ total oxidation activity dominated by Langmuir-Hinshelwood mechanism. Moreover, in situ diffuse reflectance infrared Fourier transform spectroscopy (DRIFTs) analysis shows that N doping facilities the decomposition of intermediate species (propylene and formate) into CO₂ over the catalyst surface of N-CoAlO/4h more easily. Our reported design in this work will provide a promising way to develop abundant oxygen vacancies of Co-based catalysts derived from hydrotalcites by a simple NH₃ treatment.     

An investigation on catalytic performance and reaction mechanisms of Fe/OMS-2 for the oxidation of carbon monoxide, ethyl acetate, and toluene

The octahedral molecular sieve（OMS-2）-supported Fe（ xFe/OMS-2: x = 1, 3, 5, and 10） catalysts were prepared using the pre-incorporation method. Physicochemical properties of the as-synthesized materials were characterized by means of various techniques, and their catalytic activities for CO, ethyl acetate, and toluene oxidation were evaluated. Among all of the samples, performed the best, with the reaction temperature required to achieve 90% conversion（ T 90%） being 160 °C for CO oxidation, 210 ...     

不同合成法对Ce-MnOx选择性催化氧化NH3性能的影响

分别采用水热法和浸渍法2种合成方法制备了Ce-MnO_x催化剂,应用于氨的选择性催化氧化。实验结果表明:水热法制备的Ce-MnO_x具有更高的催化氧化NH₃活性,其中,在反应温度为200℃时,Ce(5)-MnO_x(HY)具有98%的NH₃转化率及91%的N₂选择性。XRD、BET、Raman、XPS、SEM、H₂-TPR等方法对催化剂的表征结果表明,水热法合成的Ce-MnO_x具有更大的比表面积(94.37 m2/g),其优异的催化活性归因于表面丰富的Mn4+和Ce3+、大量的化学吸附氧、丰富的活性位点、Mn和Ce间的相互作用等。In-situ DRIFTS分析表明,催化剂表面吸附态的NH₃经过脱氢作用生成—NH₂、—NH中间体,其中,—NH与原子氧结合生成的—HNO能被O₂快速氧化形成NO,NO再与—NH₂继续反应生成N₂和H₂O。研究可为锰基催化剂在低温氨氧化及选择性方面的研究提供重要参考。     

铈钴复合氧化物催化剂催化CO-SCR反应机理研究

利用共沉淀法制备了一系列Ce-Co-O_x复合氧化物催化剂,并对其CO-SCR反应性能进行了研究.考察了Co和Ce比例对CO-SCR反应活性的影响,确定最佳的Ce和Co复合比例为3：7,最高转化率为84%（250℃）.经表征分析发现,Ce（0.3）-Co（0.7）-O_x上发生CO-SCR的主活性位点是Co.掺杂Ce提升催化性能主要有两方面原因：一是催化剂比表面积增大,提高了表面的吸附位数量;二是Ce-Co-O_x催化剂形成的固溶体提升了氧迁移率.反应机理可能是气态或者弱吸附状态的CO与NO的吸附物种（主要是桥接二齿亚硝酸盐物种和螯合式双齿硝酸盐物种）反应.     

Reduction of NO by CO using Pd-CeTb and Pd-CeZr catalysts supported on SiO2 and La2O3-Al2O3

The catalytic activity of Pd catalysts supported on Ce_0.73Tb_0.27O_x/SiO₂, Ce_0.6Zr_0.4O_x/SiO₂, Ce_0.73Tb_0.27O_x/La₂O₃-Al₂O₃ and Ce_0.6Zr_0.4O_x/La₂O₃-Al₂O₃ was studied using the reduction of NO by CO. The catalysts were characterized by X-ray fluorescence, surface area, X-ray diffraction, temperature-programmed reduction, CO chemisorption and oxygen storage capacity. Temperature-programmed reduction results indicated that Tb or Zr incorporation improves the reducibility and oxygen storage capacity. CO chemisorption data suggested the presence of large PdO particles due to the low CO/Pd ratio. No significant differences were obtained in light off temperatures (T_{Light off}) for all Pd catalysts and the most active was 1.5%Pd/Ce_0.6Zr_0.4O_x/SiO₂.     

Co- or Ni-modified Sn-MnOx low-dimensional multi-oxides for high-efficient NH3-SCR De-NOx: Performance optimization and reaction mechanism

NH₃-SCR performances were explored to the relationship between structure morphology and physio-chemical properties over low-dimensional ternary Mn-based catalysts prepared by one-step synthesis method.Due to its strong oxidation performance,Sn-MnOx was prone to side reactions between NO,NH₃ and O₂,resulting in the generation of more NO₂ and N₂ O,here most of N₂ O was driven from the non-selective oxidation of NH₃,while ...     

La-M-Co-O/堇青石催化剂的制备及催化氧化氯苯

采用柠檬酸络合法制备La-M-Co-O（M=Mn,Cr,Fe,Ni和Cu）/堇青石催化剂,运用BET,XRD,SEM,H₂-TPR和XPS技术对催化剂性能及微观结构进行表征分析,研究考察过渡金属掺杂,掺杂量以及焙烧温度等对催化剂催化氧化性能的影响.结果表明,随着催化剂焙烧温度升高至650℃时,催化剂表面所负载的活性氧化物颗粒最为分散,其氧化活性最佳,且当反应温度为350℃时,催化剂催化氧化氯苯转化率可达96.4%,究其原因是高温焙烧致使催化剂形成LaCoO₃钙钛矿型复合氧化物,其复合氧化物的晶体结构有利于催化剂催化氧化氯苯性能的提高.     

La-M-Co-O/堇青石催化剂的制备及催化氧化氯苯

采用柠檬酸络合法制备La-M-Co-O（M=Mn,Cr,Fe,Ni和Cu）/堇青石催化剂,运用BET,XRD,SEM,H₂-TPR和XPS技术对催化剂性能及微观结构进行表征分析,研究考察过渡金属掺杂,掺杂量以及焙烧温度等对催化剂催化氧化性能的影响.结果表明,随着催化剂焙烧温度升高至650℃时,催化剂表面所负载的活性氧化物颗粒最为分散,其氧化活性最佳,且当反应温度为350℃时,催化剂催化氧化氯苯转化率可达96.4%,究其原因是高温焙烧致使催化剂形成LaCoO₃钙钛矿型复合氧化物,其复合氧化物的晶体结构有利于催化剂催化氧化氯苯性能的提高.     

Fe2O3(1-12)作用下CO化学链燃烧反应机理研究

在化学链燃烧(CLC)过程中,载氧体表面的原子结构和电子特性决定了其化学反应活性.本文以Fe_2O_3为载氧体,探讨了其自然条件下主要裸露的高米勒数指表面(1-1 2)的结构性质,研究发现表面不同配位数的氧和铁原子(包括O2f、O3f、O4f、Fe4f和Fe5f)的键参数、电子态密度及电荷布居等存在明显差异.为探究这种差异对Fe_2O_3反应活性的影响,对比分析了CO在表面5种氧和铁原子位生成CO_2的吸附-反应机理.CO在表面低配位O原子O2f和O3f首先形成物理吸附,然后被晶格氧氧化生成CO_2,反应需要克服能垒分别为3.657 e V和3.401 e V;然而,CO在O4f位吸附时,首先克服1.864 e V能垒形成二齿形碳酸盐物种,之后克服1.097 e V的能垒形成CO_2.当CO在Fe4f和Fe5f位吸附时,CO与Fe原子成键,后经过活化与表面O原子成键,形成二齿形碳酸盐物种,能垒分别为0.416和0.219 e V,最终碳酸盐物种分别克服0.500和1.462e V的能垒生成CO_2.因此,可以推断表面高配位数的O4f、Fe4f和Fe5f原子,由于其较高的氧化态,在化学链燃烧过程中充当活性位的作用.本研究有助于了解铁基载氧体表面化学链燃烧反应的微观机理,并为载氧体表面结构性能调控制备提供理论借鉴.     

钯、铜、锰、铈三效催化剂性能研究

应用脉冲－火焰反应装置、ＸＲＤ、ＴＰＲ和氢氧滴定技术来研究Ｐｄ－Ｃｕ－Ｍｎ－Ｃｅ－Ｏ三效催化剂的性能。实验结果表明，不同的制备Ｐｄ－Ｃｕ－Ｍｎ－Ｃｅ－Ｏ催化剂的方法，则催化活性各不相同。在分层制备的催化剂中，催化性能主要以外层组分性能为主；以混合浸渍法制备的样品中，ＣｕＭｎ＿２Ｏ＿４相消失，Ｃｕ－Ｍｎ－Ｃｅ－Ｏ表面氧环境发生变化；表面活性剂的添加改变了Ｐｄ的分布，使催化剂表面易于还原；这些改变均对催化剂的三效性能发生影响。催化剂表面的有效贮氧量与三效活性没有明显的关系。