低浓度甲烷甲醇深度氧化Ag/La0.6Sr0.4MnO3催化剂

Ag-modified La0.6Sr0.4MnO3 catalysts were prepared and their catalytic performance for deep oxidation of CH4 and CH3OH at low concentrations were investigated. The results showed that the La0.6Sr0.4MnO3 host catalyst with the perovskite-type nano-crystallite structure displayed considerably high catalytic activity for deep oxidation of CH4 and CH3OH at low concentrations. Ag modification to the La0.6Sr0.4MnO3 host catalyst resulted in significant enhancement of the catalyst activity, making the T95 (the reaction temperature needed for conversion of 95%of CH4 or CH3OH) lowered down to 735K (for CH4) and 421K (for CH3OH) from 813 and 465 K over the Ag-free system under the reaction conditions:0.1MPa,CH4/O2/N2=2/12/86(molar ratio),GHSV=45000 h-1 and CH3OH/O2/N2= 0.2/1.0/98.8 (molar ratio),GHSV=58000 h-1,respectively.The carbon containing product was almost CO2 and the contents of HCHO and CO in the reaction exit gas were both under GC detectable limit in both cases.
The results of spectroscopic characterization indicated that modification by proper amount of Ag-dopant did not change the perovskite structure of the La0.6Sr0.4MnO3 host catalyst as a whole. Interaction of Ag-dopant with the surface of the host catalyst,La0.6Sr0.4MnO3,was in favor of high dispersion of the Ag component at the catalyst surface and led to the oxidation of part of the Mn3+species to Mn4+,resulting in an increase of amounts of the reducible Mnn+ species and a decrease of their reduction temperature. On the other hand, this interaction led also to enhancement of adsorption ability of the catalyst toward O2 at relatively low temperature. High activity of the Ag modified La0.6Sr0.4MnO3 catalyst for CH4 and CH3OH complete oxidation was closely related to high redox-activity of the catalyst and its prominent adsorption-activation ability to O2 at relatively low temperatures.     

甲烷在流态化催化剂床裂解生长多壁碳纳米管

甲烷在流态化催化剂床裂解生长多壁碳纳米管;多壁碳纳米管;Ni-Mg-O催化剂;甲烷;流化床;催化化学蒸汽沉积法     

Ag/La_(0.6)Sr_(0.4)MnO_3基催化剂上CH_3OH和CO的完全氧化

合成了Ag/La0 6 Sr0 4 MnO3和Ag/La0 6 Sr0 4 MnO3/γ -Al2 O3两系列催化剂 ;发现钙钛矿型La0 6 Sr0 4 MnO3对低浓度CH3OH或CO的完全氧化显示出相当高的催化活性 ,适量Ag对钙钛矿型La0 6 Sr0 4 MnO3基质的修饰使其对CH3OH或CO完全氧化催化活性获明显提高 ;在 6%Ag/2 0 %La0 6 Sr0 4 MnO3/γ -Al2 O3催化剂上 ,CH3OH完全氧化的T95温度可低至 4 1 3K ,反应尾气中CH3OH氧化中间产物HCHO和CO的含量在检测极限以下 ;而在相同反应条件下在 1 %Pd/γ -Al2 O3和 1 %Pt/γ -Al2 O3催化剂上 ,CH3OH完全氧化的T95温度分别为 5 1 2和 4 68K ,相应反应尾气中HCHO含量分别为 2 0 0× 1 0 -6 和 63 0× 1 0 -6 ;对比考察了这些催化剂的耐热性能和操作稳定性 ,并结合XRD、XPS和H2 -TPR的表征结果 ,讨论了Ag的促进使用本质     

氢气在碳纳米管基材料上的吸附-脱附特性

利用高压容积法测定多壁碳纳米管(MWCNTs)及钾盐修饰的相应体系(K＋-MWCNTs)的储氢容量,并用程序升温脱附(TPD)方法表征研究氢气在MWCNTs基材料上的吸附-脱附特性.结果表明,在经纯化MWCNTs上,室温、9.0 MPa实验条件下氢的储量可达1.51％（质量分数）;K＋盐对MWCNTs的修饰对增加其储氢容量并无促进效应,但相应化学吸附氢物种的脱附温度有所升高;K＋的修饰也改变了MWCNTs表面原有的疏水性质.在低于723 K的温度下,H2/MWCNTs体系的脱附产物几乎全为氢气;773 K以上高温脱附产物不仅含H2,也含有CH4、C2H4、C2H2等C1/C2烃混合物;H2/K＋-MWCNTs储氢试样的脱附产物除占主体量的H2及少量C1/C2烃混合物外,还含水汽,其量与吸附质H2源水汽含量密切相关.H2在碳纳米管基材料上吸附兼具非解离 (即分子态) 和解离(即原子态)两种形式.     

改进型合成甲醇铜基催化剂NC208的低氢活化(英文)

用TPR、DTA和XRD方法研究了改进型合成甲醇铜基催化剂NC208,成功地建立了对该催化剂进行低氢活化的程序升温还原程序并把它用于工业生产,取得了很高的甲醇收率。     

强酸促进的W/HZSM-5基催化剂上甲烷非氧化脱氢芳构化

甲烷非氧化催化脱氢芳构化制芳烃是近年来甲烷优化利用的新研究方向之一"－'．迄今已报道的催化剂多为以HZSM－5分子筛为载体的过渡金属（如Pd、I't、Re和MO等）氧化物,其中以改进型的MO／HZSM－5基催化剂效果最佳［'－'j．按化学反应计量式6CH。--C6H。＋gH;进行热力学计算,结果表明：在773K温度下,甲烷平衡转化率（KC。。。,衡）仅为卫·8％;在叮3K和】023K时,xCH。平。分别为】1·3％和15·8％;若使Xo。。,Y＆达25％以上,则要求反应温度不低于1123K（在1123K和1173K时,XCH。,y＆分别为27·2％和33·196）·然…     

碳纳米管负载铑催化剂上丙烯氢甲酰化

Effect of carbon nanotubes, as a novel support material, on the performance of Rh-catalyst supported by them was studied. Catalysts based on carbon nanotubes, SiO2, carbon molecular sieves, active carbon, and GDX-l02(a copolymer of styrene with divinylbenzene),were prepared, and their catalytic behaviors for propene hydroformylation were investigated and compared. The results showed that, over the carbon nanotubes-supported Rh-catalyst, C3H6 conversion and regioselectivity of butyric aldehyde (represented by n/i, a ratio of n-butyric aldehyde to its isomer, i-butyric aldehyde, in the products) were pronouncedly improved: the average turnover frequency(TOF) for the catalytic hydroformylation of propene was 0.079 s-1 at 393K, which was 2.1 times faster than that over the Rh catalyst based on SiO2, and the n/i ratio of the aldehyde products reached to 11.6, which was 1.9 times higher than that over the catalyst based on SiO2. The roles of six-membered C-ring at the surface of the carbon-nanotubes on the stability of the catalytically active Rh-complexes and of the tubular nano-channel on the spatiospecific seletivity of reaction intermediate state and butyric aldehyde produced were discussed.     

Cr2O3在铜基甲醇合成催化剂中的作用

研究了三组份Cu－ZnO－Al_2O_3催化剂添加Cr_2O_3后．铬在催化剂中的存在形式，助催作用本质及其与甲醇含成催化活性的关联。结果表明：在ZnO－Cr_2O_3催化剂中，铬以Cr~(3 )和ZnCr_2O_4形式存在于ZnO晶格中，Cu-ZnO-Al_2O_3-Cr_2O_3催化剂的催化活性与CR~(3 )在ZnO晶格中诱导出来的正一价缺位和催化剂的其它顺磁性物种的ESR强度能很好地关联，在活性测试中，以含1％Cr（原子比）的Cu-ZnO-Al_2O_3-Cr_2O_3的催化活性最高。     

钌基和铁基催化剂上氨合成催化反应的氘反同位素效应

 氘反同位素效应是合理阐明过渡金属催化剂上氨合成催化反应机理的重要实验依据之一. 在 N2/H2 (或 D2) 体积比 1/3, 0.2 MPa, 633~733 K 和 GHSV = 24 000 或 12 000 h?1 的条件下, 检测到了 Ru 基 (纯 Ru, Ru/?-Al2O3, K-Ru/?-Al2O3, Ru/MgO, K-Ru/MgO 和 Ba-Ru/MgO) 和 Fe 基 (纯 Fe 和 A110-3) 催化剂上强的氘反同位素效应 (rD/rH ? 2), 其数值随催化剂和反应温度的变化而变化. 这可能是动力学同位素效应与热力学同位素效应二者相互强竞争的结果.     

碳纳米管负载/促进的Mo-Co加氢脱硫催化剂

 以多壁碳纳米管(CNT)为载体制备了负载型Mo-Co/CNT,并将其用于噻吩HDS反应. 结果表明,在n(C4H4S)/n(H2)= 2.3/97.7, GHSV=2200 ml/(g·h),p=0.1 MPa和T=623 K的条件下,在7.2%(Mo-Co)/CNT催化剂上,噻吩HDS的比反应速率可达到0.64·10-3s-1,分别是9.7%(Mo-Co)/γ-Al2O3和16.9%(Mo-Co)/AC催化剂上的1.68和2.28倍. 对比研究结果表明,用CNT代替γ-Al2O3或AC并不引起催化剂上噻吩HDS反应的表观活化能发生明显变化. 与Mo-Co/γ-Al2O3或Mo-Co/AC催化剂相比,一方面,Mo-Co/CNT催化剂更易在较低温度下还原活化,并导致工作态催化剂表层活性Mo物种(Mo4+)在总Mo量中所占比例明显提高; 另一方面,Mo-Co/CNT催化剂对H2具有更强的吸附和活化能力. 这两个因素对提高催化剂活性都有重要贡献.