用不同类型的分子筛催化剂催化转化生物油制烯烃

研究了用一系列不同类型的分子筛催化剂催化转化制取低碳烯烃的过程,测试的催化剂包括HZSM-5、MCM-41、SAPO- 34和Y型分子筛．按照低碳烯烃的绝对收率和选择性,催化剂的活性排序为：HZSM-5>SAPO-34>MCM-41>Y型分子筛．研究表明,使用HZSM-5分子筛催化剂,获得的生物油最大低碳烯烃收率约为0.22 kg/(kg生物油),低碳烯烃的选择性约为50%,且生物油几乎实现完全转化．同时还研究了反应条件对生物油制低碳烯烃的影响．为了弄清催化剂结构与和低碳烯烃形成之间的关系,对相关催化剂进行了详细表征,对生物油热裂解和催化裂解过程进行了详细比较．     

在Ni/HZSM-5催化剂上低温水蒸汽重整生物油制氢

利用浸渍方法制备的Ni/HZSM-5催化剂在生物油低温水蒸汽重整合成中表现了较高的催化活性． 探讨了催化剂的组成、重整温度、水碳比例对重整过程的影响．在电催化重整研究中,发现催化剂上通过的电流可以显著地促进生物油水蒸汽重整．通过对不同负载量的Ni/HZSM-5催化剂和Ni₂₀/Al₂O₃催化剂的催化活性的比较,NiO在催化剂中负载量为20%(Ni₂₀/ZSM)时表现出了最高的催化活性; 即使在450 oC时, 在Ni₂₀/ZSM催化剂上也可以达到碳转化率接近完全, 氢气产率约为90%的效果． 利用XRD、ICP/AES、H₂-TPR、BET等表征手段对Ni/HZSM-5催化剂的形态和结构进行了表征.     

生物油制备生物质氢气和生物质燃料

研究了一种以生物质裂解油为原料制备氢气和生物燃料的催化转化过程。该过程包括生物油催化裂解制备氢气和生物合成气,合成气的调变,烯烃聚合和费脱合成耦合制备生物燃料。在优化反应条件下,氢气产率达到120.9 g H₂/（kg bio-oil）,烯烃聚合-费脱合成耦合反应形成的生物燃料产率达到526.1 g/（kg bio-syngas）。基于产物分析和催化剂特性表征,探讨了生物燃料合成过程中的反应路径和化学反应过程.     

超低密度SiO2气凝胶的制备及成型研究

 以正硅酸乙酯(TEOS)为硅源，采用酸碱二步催化溶胶-凝胶法，结合超临界干燥技术制备了超低密度SiO₂气凝胶,最低密度为3.4 mg/cm³；进一步结合成型工艺，在解决了模具设计和脱模技术后制备了具有不同密度的柱状和微型套筒样品，密度10～50 mg/cm³。研究了水、催化剂、稀释剂对二步溶胶-凝胶过程的影响，获得了制备低密度SiO₂气凝胶的最佳条件。利用扫描电镜、孔径分布及比表面积测试仪等对SiO₂气凝胶微结构进行了研究。结果表明，获得的超低密度SiO₂气凝胶具有较好的纳米网络，平均孔径18.9 nm，还具有高比表面积898 9 m²/g。     

利用生物质气化合成气在FeCuZnAlK催化剂上高效制备清洁生物燃料

研究了生物质气化合成气在Fe_1.5Cu₁Zn₁Al₁K_0.117催化剂上高效转化为清洁生物燃料的合成过程. 利用生物质气化合成气合成的生物燃料最大产率为1.59 kg/(kgcatal·h), 其中醇占0.57 kg/(kgcatal·h), 液体烃占1.02 kg/(kgcatal·h). 在生物燃料中, 醇类产物主要为C2⁺醇(主要为C2-C6高碳醇), 其含量占总醇的7     

Cu/HMOR催化二甲醚羰基化合成乙酸甲酯: 催化剂制备方法的影响 (cited: 2)

采用氨蒸发法、尿素水解法、离子交换法及浸渍法制备HMOR负载的Cu催化剂, 考察其催化二甲醚(DME)羰基化合成乙酸甲酯(MA)性能. 结果表明离子交换法制得Cu/HMOR催化剂在Cu的金属中心和酸性分子筛载体的共同作用下具有较好催化反应活性. 在210 oC、1.5 MPa、空速4883 h^-1,DME转化率为95.3%,MA选择性为94.9%. 对催化剂进行N2物理吸附、X射线衍射、NH₃程序升温脱附和CO程序升温脱附等表征发现,离子交换法制得Cu/HMOR催化剂具有较高比表面、大量弱酸及一定中强酸、适中的CO吸附强度,提高了CO插入DME羰基化反应活性.     

铜纳米阵列高效电解水产氧催化剂的制备

本文报道了一种利用简单的两步牺牲模板法,在泡沫铜基底表面完成了三维氧化铜纳米晶阵列的生长. 氧化铜纳米晶阵列具有良好的导电性,稳定性,在碱性溶液中有着优秀的电解水产氧催化性能. 氧化铜纳米晶阵列催化水的电化学氧化只需400 mV的过电势即可达到100 mA/cm²的电流密度,与其它铜基电解水产氧催化剂以及贵金属IrO₂相比都有着明显的优势. 氧化铜纳米晶阵列在270 mA/cm²左右的工作电流下连续工作10 h依然可以保持良好的稳定性,是相同的工作电压下IrO₂工作电流的10倍(约25 mA/cm²).     

焙烧温度对SiO2负载的Co3O4纳米粒子表面氧缺陷浓度和CO氧化催化性能的影响

以传统的浸渍法,在不同焙烧温度下制备了用于CO氧化反应的Co₃O₄/SiO₂催化剂．通过激光拉曼光谱(Raman)、X射线光电子能谱(XPS)、X射线衍射(XRD)、程序升温还原(TPR)和X射线吸收精细结构谱(XAFS)表征了该系列催化剂的结构．在所有的催化剂中,XRD和Raman光谱都只检测到了Co₃O₄晶相的存在．与Co₃O₄体相相比,XPS结果表明在200 oC焙烧的(Co₃O₄(200)/SiO₂)催化剂中Co₃O₄表面上存在着过量的Co²⁺．与XPS的结果一致,TPR结果表明Co₃O₄(200)/SiO₂催化剂中Co₃O₄表面上存在氧缺陷, 并且XAFS结果也表明Co₃O₄(200)/SiO₂催化剂中Co₃O₄具有更多的Co²⁺．提高焙烧温度使得过量的Co²⁺进一步氧化为Co³⁺,同时降低了表面氧缺陷浓度,从而得到计量比的Co₃O₄4/SiO₂催化剂．在所有的负载催化剂中Co₃O₄(200)/SiO₂催化剂表现出了最好的CO氧化催化性能,表明过量Co²⁺和表面氧缺陷的存在能够促进Co₃O₄催化CO氧化反应的活性.     

合成Pb(OH)2/rGO催化剂用于催化转化糖为乳酸

Pb²⁺离子可以作为高效的催化剂用于降解糖为乳酸, 但是为了降低暴露Pb²⁺离子于环境中的风险,最好的办法是把铅固定在一个固体催化剂上．报道了一个简单的制备Pb(PbO₂)/石墨烯复合固体催化剂的方法,可以得到石墨烯负载的纳米铅催化剂,铅颗粒的尺寸在2～5 nm．获得的催化剂可以在水中用于降解葡萄糖、果糖甚至纤维素,产物主要为乳酸．对于果糖、乳酸的产率为58.7% (433 K,2.5 MPa N₂);当直接使用纤维素为原料,无额外酸、碱催化剂时,乳酸的产率可以达到31.7%.     

利用双段床反应器从生物油重整合成气合成甲醇

一种组合了合成气在线调整和甲醇合成的双段床反应器,成功应用于由生物油重整得到的富CO₂合成气的高效合成甲醇．在前段催化床反应器内,富含CO2的原始生物质合成气在CuZnAlZr催化剂的催化作用下可以有效地转化为含CO的合成气．经过450 oC的合成气在线调整之后,CO₂/CO的比率由6.3大幅降至1.2．经过调整后的生物质基合成气在后段催化床反应器内由工业CuZnAl催化剂催化合成甲醇,当反应条件为260 oC 和5.5 MPa时得到每小时每kg催化剂的最大甲醇     

Ultrasound assisted co-precipitation of nanostructured CuO–ZnO–Al2O3 over HZSM-5: Effect of precursor and irradiation power on nanocatalyst properties and catalytic performance for direct syngas to DME

Nanostructured CuO–ZnO–Al₂O₃/HZSM-5 was synthesized from nitrate and acetate precursors using ultrasound assisted co-precipitation method under different irradiation powers. The CuO–ZnO–Al₂O₃/HZSM-5 nanocatalysts were characterized using XRD, FESEM, BET, FTIR and EDX Dot-mapping analyses. The results indicated precursor type and irradiation power have significant influences on phase structure, morphology, surface area and functional groups. It was observed that the acetate formulated CuO–ZnO–Al₂O₃/HZSM-5 nanocatalyst have smaller CuO crystals with better dispersion and stronger interaction between components in comparison to nitrate based nanocatalysts. Ultrasound assisted co-precipitation synthesis method resulted in nanocatalyst with more uniform morphology compared to conventional method and increasing irradiation power yields smaller particles with better dispersion and higher surface area. Additionally the crystallinity of CuO is lower at high irradiation powers leading to stronger interaction between metal oxides. The nanocatalysts performance were tested at 200–300 °C, 10–40 bar and space velocity of 18,000–36,000 cm³/g h with the inlet gas composition of H₂/CO = 2/1 in a stainless steel autoclave reactor. The acetate based nanocatalysts irradiated with higher levels of power exhibited better reactivity in terms of CO conversion and DME yield. While there is an optimal temperature for CO conversion and DME yield in direct synthesis of DME, CO conversion and DME yield both increase with the pressure increase. Furthermore ultrasound assisted co-precipitation method yields more stable CuO–ZnO–Al₂O₃/HZSM-5 nanocatalyst while conventional precipitated nanocatalyst lost their activity ca. 18% and 58% in terms of CO conversion and DME yield respectively in 24 h time on stream test.     

粗生物油催化裂解制取低碳轻烯烃

利用La/HZSM-5催化剂,研究了催化裂解粗生物油及其模型化合物(包括甲醇、乙醇、乙酸、丙酮和苯酚)制取轻烯烃的过程. 获得的最大轻烯烃产率为0.19 kg/kg粗生物油. 研究表明,温度、重时空速和镧对HZSM-5分子筛的改性等因素可用来调制烯烃产率和选择性. 分子筛中添加镧,可适当的调节催化剂酸度和强弱酸位比例,从而提高烯烃选择性、产率和催化剂稳定性. 生物油制备轻烯烃的效率与原料的化学成分和氢碳有效比(H/Ce? )密切相关. 此外,比较了粗生物油催化裂解和热裂解过程,同时利用模型化合物研究了生物油转化为轻烯烃的相关反应历程和机理.     

Physicochemical characteristics of ZSM-5/SAPO-34 composite catalyst for MTO reaction

SAPO-34 and ZSM-5 are the most well-known catalyst for MTO reaction. A combination of ZSM-5 and SAPO-34 might give rise to optimal catalyst to meet a change of market demand for ethylene, propylene and butadiene. In this study, we have developed ZSM-5/SAPO-34 composite catalysts to control the composition of light olefins in MTO reaction. ZSM-5/SAPO-34 composite catalysts showed very different physicochemical and catalytic properties with respect to ZSM-5 and SAPO-34 synthetic procedure. The physicochemical properties of the composite catalysts have been compared by XRD, SEM, N₂ isotherm, FT-IR and NH₃-TPD. Their catalytic performances were also evaluated for MTO reaction. The series composite catalyst synthesized by successive crystallization of SAPO-34 synthetic gel after ZSM-5 crystallization exhibited relatively high catalytic performance.     

A novel DME steam-reforming catalyst designed with fact database on-demand

Novel catalysts for dimethyl ether (DME) steam reforming (SR) were designed based on catalysis database on-demand. A catalyst library consisting of precious metals loaded on various metal oxides was tested for DME SR and its elemental reactions of DME hydrolysis and MeOH SR. Platinum loaded on alumina, Pt/Al₂O₃, shows high activity for DME SR as reported previously. The drawback of the catalyst was also confirmed; the formation of methane leading to the reduction of hydrogen formation. From the fact database for DME hydrolysis and MeOH SR built up with high-throughput experimentation tools, the high activity of Pt/Al₂O₃ for DME SR is owing to its high activity on DME hydrolysis because its activity on MeOH steam reforming is not remarkable. Based on these facts, novel catalysts were designed and achieved by physical mixing of Pt/Al₂O₃ which reveals high activity on DME hydrolysis with an active catalyst on MeOH steam reforming. By mixing of Pt/Al₂O₃ with Pd/Al₂O₃, methane formation was suppressed without loss of hydrogen production activity.     

Theoretical study of the cracking mechanisms of linear α-olefins catalyzed by zeolites

The cracking reactions of linear C₄-C₁₀ α-olefins over zeolites have been studied by using density functional theory at the B3LYP/6-31G(d,p) level. The obtained results reveal that the β-scission processes of C₄-C₁₀ olefins have the same reaction mechanism. Every pathway only involves a transition state corresponding to the rupture of the C-C bond, while the intrinsic reaction coordinate analysis indicates that the protonated intermediate species is formed during the reaction process. Furthermore, it is found that this intermediate species is not usually highly stable alkoxy group but adsorbed short-lifetime carbocation. This phenomenon can well explain why the carbocations are seldom observed inside the zeolite's cavities. The calculated real activation energy for this pathway is lower than the experimental value for corresponding alkane cracking contrary to the previously reported pathway via an alkoxide intermediate. Therefore, the reaction pathway via a carbocation intermediate species is energetically much more favorable. In addition, the study also shows that the real activation energies of olefin cracking are nearly independent of the olefin chain length, which is in agreement with the existing experimental results of alkane cracking.     

Research on Si-Al based catalysts prepared by complete liquid-phase method for DME synthesis in a slurry reactor

A series of Si-Al based DME synthesis catalysts were prepared by complete liquid-phase method and characterized by in situ XPS, XRD, N₂ adsorption and NH₃-TPD analyses. Based on the results, the addition of Si could adjust the pore structure and surface acidity of catalyst, exhibiting a strong promoting effect on the CO conversion and DME selectivity. However, when Si/Al ratio is higher, Si would cover active sites and increase the amount of strong acidity sites, causing the reduction in catalytic activity. It was found from in situ XPS characterization that Cu⁰ is the active center of methanol synthesis in DME production, and the addition of Si changes the chemical surroundings of active components and weaken the interaction between Cu, Zn and Al, which maybe give rise to the decrease in catalyst stability.     

生物质催化转化制取芳香化合物

利用分子筛催化剂(NaZSM-5、HZSM-5、ReY和HY)研究了木屑上催化裂解制取芳香物(苯、甲苯、二甲苯)的反应过程,发现HZSM-5催化剂具有最高的生物质裂解制备芳香化合物的活性. 在450 oC、 载气流速为300 mL/min和催化剂/木屑比为2的优化反应条件下,芳香化合物的产率和选择性分别达到26.5%和62.5C-mol%.     

Promotion of surface SOx on the selective catalytic reduction of NO by hydrocarbons over Ag/Al2O3

The promotion of sulfur oxides on the selective catalytic reduction (SCR) of NO by hydrocarbons in the presence of a low concentration of sulfur oxides over Ag/Al₂O₃ has been investigated by a flow reaction test and in situ infrared spectroscopy. When the C₃H₆ (or C₁₀H₂₂) + NO + O₂ feed-flow reaction was tested, maximum NO reduction was below 30% over fresh Ag/Al₂O₃. After the addition of SO₂ to the feed flow, conversion increased slightly. Conversion increased further after SO₂ was cut-off from the feed flow. This demonstrated that the increase in NO reduction activity of the catalyst was related to SO_x adsorbed on the catalyst. SO_x adsorbed on the catalytic surface (1375 cm⁻¹) was detected by IR spectroscopy and was stable within the temperature range. NCO species, as an intermediate in NO reduction, on SO_x-adsorbed Ag/Al₂O₃ in a C₃H₆ + NO + O₂ feed flow was observed in in situ IR spectra during the elevation of the reaction temperature from 473 to 673 K, while it was only observed at 673 K on fresh Ag/Al₂O₃ under the same experimental conditions. We suggest that SO_x in low concentrations depressed the combustion of reductants by contaminating hydrocarbon combustion active sites on the catalyst, resulting in an increase in NO reduction efficiency of the reductants.