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1.
在固定床反应器上,评价了不同温度下钙钛矿型复合氧化物SrTiO3和CaTiO3的组成变化对甲烷氧化偶联反应的影响.同时,利用XPS和CO2-TPD对催化剂的结构及其氧物种的反应特性进行了表征.结果表明:SrTiO3和少量Ca掺杂的CaxSrl-xTiO3有利于在较低温度(923K)下催化反应的活性和选择性,而CaTiO3体系则在高温(1073K)下表现出较好的活性和选择性.钙钛矿型复合氧化物SrTiO3和CaTiO3组成变化对不同温度下反应活性的影响与CO2-TPD的脱附谱图有很好的平行关系.  相似文献   

2.
研究了不同碱金属离子对CaO的促进作用,发现以Na~+的添加效果最好。在此基础上,研究了不同含钠化合物对CaO的促进作用,并用脉冲反应技术研究Na~+/CaO催化剂表面氧物种的特性及其作用。CaO表面上存在非选择性氧化的氧物种。Na~+对CaO的修饰作用是抑制非选择性氧化。当表面上的非选择性氧化的氧物种消耗后,体相的晶格氧会向表面迁移,以补充消耗掉的表面氧物种。消耗掉的表面氧物种也可由气相氧补充。CH_4脉冲和混合气脉冲说明仅靠[Na~+O~-]中心不足以使甲烷转化成C_2产物,必须有气相氧的参与才能使甲烷转化成C_2产物。  相似文献   

3.
Catalytic partial oxidation of methane to syngas using the lattice oxygen of La1-xSrxFeO3 perovskite oxide catalysts in place of molecular oxygen was studied. La1-xSrxFeO3 (x=0, 0.1, 0.2,0.5) perovskite oxides were prepared by the "auto-combustion method". XRD analysis showed that all La1-xSrxFeO3 samples have a single-phase perovskite-type oxide. The redox properties of the catalysts were investigated by temperature programmed reduction with hydrogen (H2-TPR). Reducibility of the catalysts increase with the increasing of the Sr2+ content. The oxygen species of the catalysts and their reaction with CH4 were studied by the temperature programmed surface reaction (CH4-TPSR). In the absence of gas phase oxygen, there exist two kinds of oxygen species on the catalysts. One kind of the oxygen species with strong oxidative ability is produced first, which can oxidize CH4 completely to CO2 and H2O.Then, the second oxygen species with weak oxidative ability is formed, which can oxidize CH4 partially to CO and H2 with high selectivity. The number of the oxygen species with strong oxidative ability in the CH4-TPSR tends to become zero at low x values (x≤0.1). Under suitable reaction conditions, switching alternatively the reactions of 11% O2-Ar and 11% CH4-He over a La0.sSr0.2FeO3 catalyst at 900 ℃ allows methane to be selectively converted to synthesis gas (CH4 conversion ~90%, CO selectivity >93%) using the lattice oxygen of the perovskite oxide catalyst in a redox mode.  相似文献   

4.
铈基氧化物催化剂上氧物种的EPR研究   总被引:2,自引:0,他引:2  
徐法强  杨廷录 《分子催化》1996,10(5):320-327
选择CeO2、20%(mol)Ce/Sr及SrCO33种甲烷氧化偶联催化剂,进行了吸附氧的EPR及骤冷EPR研究,对氧物种的形式、吸附方式及在反应中的作用进行了深入讨论.实验发现,氧化铈及复合催化剂很容易吸附氧分子产生O2-超氧离子,而碳酸锶表面不利于O-2的生成.O-2可以不同方式吸附于催化剂表面,不同方式吸附的O-2具有不同的氧化能力和稳定性.不同温度下骤冷可以在复合催化剂上得到几乎相同强度的O-2EPR信号,因此O-2可能不是甲烷的选择活化中心,而是在反应条件下转化成了O2-2或O-选择性物种.复合催化剂中的SrCO3,对CeO2中氧的流动性及产生氧中间体的能力起到了调节作用,抑制了过氧化.  相似文献   

5.
碱土元素氧化物是一类具有较好催化活性和选择性的甲烷氧化偶联(OCM)催化剂[1,2]。Filkova[3]等研究了不同的碱土金属氧化物促进的Nd2O3催化剂的OCM催化性能,发现在所有碱土金属氧化物-Nd2O3催化剂中,SrO-Nd2O3催化剂具有最高的生成C2烃的选择性,这可能因为SrO较强的碱性以及Sr  相似文献   

6.
IntroductionThisprojectwassupportedbytheNationalNaturalScienceFoundationofChina.Becausemostofthecatalystsforoxidativecouplingofmethane(OCM)arecompositechides,thereactivitiesofdifferentkindsofoxygenspeciesareeXtensivelystudied.Generally,agoodOCMcatalystsho…  相似文献   

7.
在固体碱催化剂上甲烷氧化偶联反应的研究   总被引:2,自引:0,他引:2  
  相似文献   

8.
在催化剂甲烷氧化偶联反应性能研究的基础上,利用CO2-TPD技术考察了不同的碱金属化合物-La2O3/BaCo3催化剂的表面碱性。结果表明,BaCO3的协同作用,碱金属化合物的添加都增大了催化剂表面碱性的强度,也增加了碱性位的数量。  相似文献   

9.
Na2SnO3系催化剂表面吸附氧的EPR研究   总被引:1,自引:0,他引:1  
以Na_2SnO_3系甲烷氧化偶联催化剂中性能较好的5%Li_2SO_4-Na_2SnO_3样品为主要研究对象, 用电子顺磁共振(EPR)方法对表面吸附氧及其与甲烷的作用进行了研究, 实验表明: 样品在氧气氛中处理后,得到可归属为表面吸附超氧负离子O_2~-的顺磁信号, 在300 ℃以上温度条件下吸附氧后, 可产生这种表面氧物种, 该物种在室温、1.33×10~(-2) Pa真空条件下能稳定存在, 700 ℃与甲烷作用后顺磁信号显著减弱, 因而催化剂表面的O_2~-物种可能起着活化甲烷的作用.  相似文献   

10.
A series of perovskite type oxides La_(1-x)A_(x)MnO_3(x=0.1 for A=Li,Na,K;x=0.1~0.5 for A=Li)have been prepared by impregnation.Experimental results showed that the substitution of La~(3 ) by Li~ inLaMnO_(3 ?) greatly increased the selectivity to ethane and ethylene for theoxidative coupling of methane.Temperature-programmed desorption of oxygenproved the presence of oxygen vacancies in the oxide lattice.The higher Mn~(4 )/Mn_t ratio in oxide made the formation of oxygen vacancies easier on the oxidesurface.The general formula of the oxides is La_(1-x)Li_(x)Mn'V'_(y)O_(3-y),V=vacancy.  相似文献   

11.
Comparison of LaFeO3, La0.8Sr0.2FeO3, and La0.8Sr0.2Fe0.9Co0.1O3 perovskite oxides as oxygen cartier for partial oxidation of methane in the absence of gaseous oxygen was investigated by continuous flow reaction and sequential redox reaction. Methane was oxidized to syngas with high selectivity by oxygen species of perovskite oxides in the absence of gaseous oxygen. The sequential redox reaction revealed that the structural stability and continuous oxygen supply in redox re-action decreased over La0.8Sr0.2Fe0.9Co0.1O3 oxide, while LaFeO3 and Lao.sSro.2FeO3 exhibited excellent structural stability and continuous oxygen supply.  相似文献   

12.
在甲烷氧化偶联(OCM)反应条件下,用原位红外光谱研究SrO-La2O3/CaO催化剂,结果表明,晶格氧使甲深度氧化,La2O3和CaO具有活泼的晶格氧,SrO的晶格氧比较稳定,气相氧通过催化剂表面消耗掉的晶格氧,加速甲烷了深度氧化,另一方面,催化剂表面的碳酸根物种在氧气氛下分解,在La2O3和LC催化剂中,催化剂表面La2O2(CO3)的分解形成配位不饱和的晶格氧O^2-,并为气相氧吸附提供氧空  相似文献   

13.
Na-W-Mn/SiO2催化剂体系中Na对甲烷氧化偶联制乙烯的作用   总被引:4,自引:2,他引:4  
制备了一系列不同Na的含量的Na-W-Mn/SiO2催化剂,并进行了它们的甲烷氧化偶联制乙烯反应性能的评价和XPS,XRD表征。研究结果发现,由于Na的表面富集引起了W和Mn向表面迁移,从而在催化剂表面形成了活化和选择氧化甲烷的Na-O-Mn和Na-O-W活性中心,这表明Na是甲烷高转化率和乙烯高选择性必不可少的活性组分。  相似文献   

14.
The catalytic properties of complex oxide catalysts with ABO3 perovskite structure (A = Sr, Ba, La; B = Mn, Co, Ni) in the oxidative coupling of methane were studied with separate introduction of methane and oxygen onto the catalyst. The greatest catalytic activity was found for the nickel-containing oxides but these catalysts have much lower operational stability than Mn- and Co-containing catalysts. Modification of the oxide systems studied by partial replacement of the strontium or transition metal ions by alkali metal ions considerably improves their activity and selectivity.__________Translated from Teoreticheskaya i Eksperimental’naya Khimiya, Vol. 41, No. 2, pp. 110–114, March– April, 2005.  相似文献   

15.
The effect of the diffusion of oxygen from the volume of the catalyst to its surface on the dynamics of the oxidative coupling of methane was assessed on the basis of a mathematical model of the reaction of methane with the oxidized surface of KNaSrCoO3–x perovskite. It was shown that the possible values of the diffusion coefficient lie in the range of 10-18-10-16 cm2/s characteristic of the diffusion of oxygen in oxide catalysts.  相似文献   

16.
采用柠檬酸法制备了Ca,Sr共掺杂的CeO_2催化剂,发现共掺杂催化剂较单掺杂或未掺杂催化剂呈现出更好的催化甲烷氧化偶联(OCM)反应性能.通过表征可知,Ca,Sr共掺杂催化剂的物相为CeO_2和SrCO_3,Ca高度分散或掺杂于CeO_2之中;CeO_2的粒径明显变小;表面呈中等程度碱性;Ce基催化剂上的亲电氧物种数量随着碱土金属的掺杂而增大,亲电氧物种与晶格氧摩尔比(O_2-2+O-2)/O-2的大小顺序(CeSrCaCe SrCeO_2)与C2选择性一致;且SrCO_3相的存在有助于Ce基氧化物催化甲烷氧化偶联反应(OCM)性能的改善.  相似文献   

17.
A redox cycle process, in which CH4 and air are periodically brought into contact with a solid oxide packed in a fixed-bed reactor, combined with the water-gas shift (WGS) reaction, is proposed for hydrogen production. The sole oxidant for partial oxidation of methane (POM) is found to be lattice oxygen instead of gaseous oxygen. A perovskite-type LaFeO3 oxide was prepared by a sol-gel method and employed as an oxygen storage material in this process. The results indicate that, under appropriate reaction conditions, methane can be oxidized to CO and H2 by the lattice oxygen of LaFeO3 perovskite oxide with a selectivity higher than 95% and the consumed lattice oxygen can be replenished in a reoxidation procedure by a redox operation. It is suggested that the POM to H2/CO by using the lattice oxygen of the oxygen storage materials instead of gaseous oxygen should be possibly applicable. The LaFeO3 perovskite oxide maintained relatively high catalytic activity and structural stability, while the carbonaceous deposits, which come from the dissociation of CH4 in the pulse reaction, occurred due to the low migration rate of lattice oxygen from the bulk toward the surface. A new dissociation-oxidation mechanism for this POM without gaseous oxygen is proposed based on the transient responses of the products checked at different surface states via both pulse reaction and switch reaction over the LaFeO3 catalyst. In the absence of gaseous-phase oxygen, the rate-determining step of methane conversion is the migration rate of lattice oxygen, but the process can be carried out in optimized cycles. The product distribution for POM over LaFeO3 catalyst in the absence of gaseous oxygen was determined by the concentration of surface oxygen, which is relevant with the migration rate of lattice oxygen from the bulk toward the surface. This process of hydrogen production via selective oxidation of methane by lattice oxygen is better in avoiding the deep oxidation (to CO2) and enhancing the selectivity. Therefore, this new route is superior to general POM in stability (resistance to carbonaceous deposition), safety (effectively avoiding accidental explosion), ease of operation and optimization, and low cost (making use of air not oxygen).  相似文献   

18.
用原位FT-IR研究了甲烷和氧与纯CaO,La_2O_3和SrO氧化物以及LC和SLC催化剂的相互作用和反应.当不存在气相氧时,引入的甲烷与表面晶格氧反应生成碳酸盐物种。在室温或高温下,在这些氧化物和催化剂上不能检测到CH_4或O_2的吸附物类。但是,当CH_4和O_2同时存在时,在La_2O_3和LC催化剂上能检测到1118cm~-1的新谱带、这一谱带可能来自于表面碳酸盐在高温下氧气氛中的分解,并可归属为物种。甲烷与这一活性氧物种反应生成C_2H_4。但对SLC催化剂,在高温下不能检测到物种,而甲烷和氧在高温下反应也能产生表面碳酸盐并在气相中形成乙烯,这就表明,气相氧对这些催化剂也起着关键作用,但是在LC和SLC催化剂上甲烷氧化偶联反应可能有本质上的差别。  相似文献   

19.
甲烷在Ni/TiO2催化剂表面的活化   总被引:2,自引:0,他引:2  
考察了Ni/TiO2催化剂甲烷部分氧化和二氧化碳重整制合成气的反应活性,实验表明,以TiO2为载体的镍系催化剂对于甲烷部分氧化制合成气反应具有较好的活性,尤其对H2的选择性较高,对二氧化碳重整制合成气反应具有较好的低温反应活性.采用脉冲-质谱在线分析等技术,在无气相氧条件下向Ni/TiO2催化剂脉冲CH4,发现甲烷在催化剂表面的活化(转化)及其氧化产物的选择性与金属催化剂表面氧的浓度密切相关.CH4与Ni/TiO2催化剂作用过程中存在明显的氢溢流和氧溢流现象,可能是这种溢流效应使得Ni/TiO2催化剂具有良好的反应活性和抗积碳性能.  相似文献   

20.
The effects of surface acidity-basicity and surface oxidation reduction property of Li-La-Mn/TiO2 (I) and Li-La-Mn-W/TiO2 (II) catalysts on oxidative coupling of methane were studied by CO2-temperature programmed desorption (CO2-TPD) and temperature programmed reduction temperature programmed oxidation (TPR-TPO). The results show that there exist strong basic sites on catalysts I and II, but the quantity of these sites on catalyst II is more than that on catalyst I. Besides, the strength of basics site on catalyst II is stronger than that on catalyst I. The surface of catalyst II is easier to reduce and re-oxidize than that of catalyst I. The surface of catalyst II is easier to reduce and re-oxidize than of catalyst I, and the extent of reduction and reoxidation of catalyst II is more intensive than catalyst I, which results in a lowing of the reaction temperature and enhances the activity and C2 hydrocarbon yield as well as gas hourly space velocity(GHSV). Catalyst II is excellent for the oxidative coupling of methane (OCM).  相似文献   

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