CuO-Bi2O3/SiO2-MgO催化剂的制备及炔化性能

采用浸渍法、沉积-沉淀法、共沉淀法制备了CuO-Bi2O3/SiO2-MgO催化剂,利用低温N2物理吸-脱附、透射电镜(TEM)、X射线衍射(XRD)、H2程序升温还原(H2-TPR)、傅里叶红外(FT-IR)等技术对其进行了表征,并考察了催化剂在甲醛乙炔化合成1,4-丁炔二醇反应中的催化性能.结果表明,制备方法对催化剂中活性组分分散度及还原性能有较大影响,进而在甲醛乙炔化合成1,4-丁炔二醇反应中表现出不同的催化活性.采用共沉淀法制备的催化剂中活性物种CuO具有高的分散度与较好的还原能力,经活化后可生成数量较多的炔铜配合物活性中心,表现出最佳的炔化反应活性与丁炔二醇选择性.     

制备条件对Cu2O结构及甲醛乙炔化性能的影响

以Cu（NO₃）₂·3H₂O为铜源,在液相还原过程中,调变沉淀剂NaOH、还原剂L-抗坏血酸钠的加入顺序制备了Cu₂O,借助X射线粉末衍射（XRD）、傅里叶变换红外光谱（FT-IR）、拉曼光谱（Raman）、俄歇电子能谱（XAES）和H₂程序升温还原（H₂-TPR）等手段研究了制备条件对Cu₂O结构及催化甲醛乙炔化性能的影响.结果表明,调变NaOH及L-抗坏血酸钠的添加方式改变了Cu₂O的结晶度与粒径尺寸,从而使Cu₂O表现出不同的炔化性能.先加入NaOH,后加入抗坏血酸钠,Cu₂O结晶度高,粒径大,难以转化为活性物种炔化亚铜;先加入抗坏血酸钠,后加入NaOH,Cu₂O被过度还原为非活性的金属Cu,两者均造成催化剂活性较低.而NaOH和抗坏血酸钠混合后添加的方式制备出表面Cu₂O结晶完整而体相Cu₂O分散度高的样品,这使得Cu₂O高效转化为炔化亚铜活性物种,表现出最优的炔化性能,在适宜的反应条件下,1,4-丁炔二醇收率达到71.7%,经6次循环后,仍保持在56.5%.     

Ni-M/SiO2催化1,4-丁炔二醇加氢的金属助剂效应

以SiO₂气凝胶为载体,采用等体积浸渍法制备了Ni/SiO₂及不同金属助剂改性的Ni-M/SiO₂（M=Fe、Co、Cu）催化剂,利用ICP、BET、XRD、H₂-TPR、H₂-TPD等手段对催化剂进行了表征,考察了不同第二金属对催化剂结构与1,4-丁炔二醇加氢性能的影响.结果表明,第二金属与Ni物种具有不同程度的双金属协同效应,其中Cu的加入不仅能够提高Ni活性物种的分散度,而且Ni-Cu双金属间的相互作用改善了NiO物种的还原性能及氢活化能力,有利于氢和1,4-丁炔二醇在活性位点的快速转化.在反应温度50℃,氢压1 MPa,反应时间3 h的加氢评价条件下,15Ni5Cu/SiO₂催化剂不仅可以实现1,4-丁炔二醇的完全转化,而且能够有效降低难分离副产物2-羟基四氢呋喃的含量,具有最优的加氢活性和对1,4-丁烯二醇的选择性.     

含Bi、Mg的硅酸铜催化剂的制备及其催化性能

以硝酸铋、硅酸钠和MgO-SiO₂复合微球为原料,分别采用共沉淀法和浸渍-沉淀法制备了含Bi、Mg的硅酸铜催化剂，其结构经SEM，低温N₂吸附-脱附、XRD和XPS表征。研究了催化剂在甲醛乙炔化合成1,4-丁炔二醇反应中的催化性能。结果表明：采用共沉淀法制备的催化剂具有高比表面积、孔径和孔体积，炔化反应活性高，1,4-丁炔二醇选择性大于96%。催化剂表面的活性组分主要为无定形硅酸铜，分散度与稳定性较好，活性组分Cu和Bi不易流失。     

高活性固体碱Na2O/Al2O3-MgO的合成与表征

过量NaOH易引起铝离子流失,造成以Al₂O₃-MgO为载体的催化剂性能不稳定,为此以NH₃为沉淀剂制备了Mg-Al共沉淀物,进而通过Na₂CO₃浸渍、老化、焙烧处置,制备了Na₂O/Al₂O₃-MgO催化剂,借助XRD、SEM、SEM-EDS、TG-DSC、N₂吸附-脱附等手段对其结构及形貌进行表征,以蒜头果油甲酯化率对其活性进行评价,结果表明：采用共沉淀-浸渍的处理方法可以获得类水滑石片层结构的催化剂前驱体,该前驱体主要分解温度在200~500℃之间,经高温煅烧处理后所得催化剂中有Na-Al及Na-Mg-Al氧化物形成。制备高活性Na₂O/Al₂O₃-MgO催化剂的条件为：镁铝离子比n_Mg/n_Al=3∶1~1∶3、老化时间12 h、焙烧温度550℃、焙烧时间5 h。以n_Mg/n_Al=1∶1时制备的催化剂进行验证实验发现,所得催化剂比表面积为30 m²·g^-1、平均孔径为8.8 nm,是一种介孔催化剂,该催化剂在蒜头果油甲酯化实验中表现出高的催化活性,蒜头果油甲酯化率最高达到96.4%。     

沉淀剂和Ag含量变化对甲醛降解性能的影响

采用不同沉淀剂制备CeO₂-Co₃O₄复合金属氧化物载体,通过浸渍负载不同含量Ag获得Ag/CeO₂-Co₃O₄催化剂.借助氮气物理吸附、XRD、Raman和H₂-TPR等手段研究了催化剂的物理化学性质.结果表明：当WHSV=30 000 mL·g^-1·h^-1时,催化剂能表现出良好的催化氧化甲醛性能,在≤ 90℃时实现甲醛的完全转化.草酸沉淀能有效降低Ce-Co氧化物的结晶度,使得Co²⁺含量增加,提供更多的氧空位,促进了氧分子的活化与迁移,从而提高了催化活性.随着Ag含量增加,使得由草酸沉淀制备的Ag/CeO₂-Co₃O₄催化剂的活性增强,且金属与载体间的相互作用也增强,当Ag负载量为1%（重量百分比）时活性最佳.     

超临界水中碳酸钠团簇成核与生长分子动力学模拟

应用分子动力学方法研究了碳酸钠颗粒在超临界水中的成核与生长过程. 计算了温度为700-1100 K、压力在23-30 MPa下碳酸钠的团聚过程, 计算时间为1 ns. 对体系结合能与径向分布函数的分析表明, 碳酸钠成核过程主要受静电作用的影响. 在超临界态下, 水分子与Na⁺和CO₃^2- 之间的静电作用降低, Na⁺与CO₃^2- 能够很容易碰撞形成Na₂CO₃小团簇. 在Na₂CO₃整个成核过程中, 单个离子的碰撞在前50 ps 内完成, 同时离子碰撞速率达到10³⁰ cm^-3·s^-1. 另外, 在成核阶段温度的影响比压力更加明显, 温度越高, 离子碰撞速率越快, 形成的初始团簇越多. 而压力对Na₂CO₃团簇的进一步生长影响较大.     

改进液相还原法制备的Pd/C催化剂对甲酸氧化的电能

用液相还原法制备炭载Pd(Pd/C)催化剂时,先用Na₂CO₃调节溶液pH值至8～9,然后加入还原剂还原PdCl₂,由于PdCl₂能与Na₂CO₃形成配合物,降低了得到的Pd粒子聚集倾向,使制得的Pd/C催化剂中Pd粒子的平均粒径和相对结晶度都较小,分别为3.57 nm和1.37。而没有加Na₂CO₃制得的Pd/C催化剂中Pd粒子的     

孔雀石催化合成1,4-丁炔二醇的研究

研究了自制的孔雀石催化剂对甲醛乙炔化反应的催化性能,并对该催化剂进行了XRD表征,结果表明该催化剂对醛炔化反应具有很好的催化活性,1,4-丁炔二醇产率约95.05%,该催化剂的晶相主要是碱式碳酸铜。     

原子层沉积构筑Pd/TiO2限域催化剂及其在1,4-丁炔二醇加氢的应用

利用ALD制备了TiO₂限域的Pd催化剂, 研究了限域空间内Pd纳米颗粒与TiO₂的界面作用对1,4-丁炔二醇(BYD)加氢性能的影响. 相比于管外负载型催化剂, 限域催化剂在催化1,4-丁炔二醇选择性加氢反应中体现出非常高的催化活性和1,4-丁烯二醇的选择性. HR-TEM、 EDX-Mapping、 XRD、 XPS和H₂-TPR表征说明, 限域体系中Pd-TiO₂的界面相互作用强于传统TiO₂表面负载型Pd催化剂, 这种强界面作用不仅能够提高BYD的加氢活性, 也可抑制半加氢产物1,4-丁烯二醇的异构化和深度加氢, 提高1,4-丁烯二醇的选择性, 而且限域结构也可阻止管内壁Pd纳米颗粒的脱落, 提高催化剂的稳定性.     

Walter Reppe Revival – Identification and Genesis of Copper Acetylides Cu2C2 as Active Species in Ethynylation Reactions

More than six decades after proposing copper acetylide, Cu₂C₂, as catalytically active species in ethynylation reactions by Walter Reppe, the explosive species have been experimentally identified and investigated during catalysis in detail now. Taking into account specific safety precautions, unequivocal qualitative characterization was achieved by Raman spectroscopy and X-ray powder diffraction of supported copper catalysts Cu/Bi/SiO₂ during and after activation and catalysis in comparison to bulk Cu₂C₂ materials. Quantification of Cu₂C₂ succeeded by thermal analysis and Raman spectroscopy. Its formation in aqueous suspension is studied starting from copper(II) oxide catalysts including dissolution, reduction and precipitation steps. Copper acetylide formation can be correlated with catalytic performance in the ethynylation of formaldehyde to 1,4-butynediol.     

Characterization and Activity of Cu‐MnOx/γ‐Al2O3 Catalyst for Hydrogenation of Carbon Dioxide

The effect of manganese on the dispersion, reduction behavior and active states of surface of supported copper oxide catalysts have been investigated by XRD, temperature‐programmed reduction and XPS. The activity of methanol synthesis from CO₂/H₂ was also investigated. The catalytic activity over CuO‐MnO_x/γ‐Al₂O₃ catalyst for CO₂ hydrogenation is higher than that of CuO/γ‐Al₂O₃. The adding of manganese is beneficial in enhancing the dispersion of the supported copper oxide and make the TPR peak of the CuO‐MnK_x/γ‐Al₂O₃ catalyst different from the individual supported copper and manganese oxide catalysts, which indicates that there exists strong interaction between the copper and manganese oxide. For the CuO/γ‐Al₂O₃ catalyst there are two reducible copper oxide species; α and β peaks are attributed to the reduction of highly dispersed copper oxide species and bulk CuO species, respectively. For the CuO‐MnO_x/γ‐Al₂O₃ catalyst, four reduction peaks are observed, α peak is attributed to the dispersed copper oxide species; β peak is ascribed to the bulk CuO; γ peak is attributed to the reduction of high dispersed CuO interacting with manganese; δ peak may be the reduction of the manganese oxide interacting with copper oxide. XPS results show that Cu⁺ mostly existed on the working surface of the Cu‐Mn/γ‐Al₂O₃ catalysts. The activity was promoted by Cu with positive charge which was formed by means of long path exchange function between Cu? O? Mn. These results indicate that there is synergistic interaction between the copper and manganese oxide, which is responsible for the high activity of CO₂ hydrogenation.     

助剂对Ni-Al合金和Raney-Ni催化剂结构及1,4-丁烯二醇加氢性能的影响

采用等体积浸渍法将助剂(MgO、CuO、Co2O3)引入商品Ni-Al合金粉,经10%(w/w)NaOH溶液浸取制备Raney-Ni催化剂。通过能量色散X射线(EDX)、X射线衍射(XRD)、N2吸附-脱附测试、透射电镜(TEM)、NH3程序升温脱附(NH3-TPD)、X射线光电子能谱(XPS)等方法表征和评价实验,考察了金属助剂对Ni-Al合金粉及Raney-Ni催化剂元素组成、晶相结构、孔结构特征、表面形貌、表面酸碱性的影响。表征分析显示,不同助剂催化剂的元素含量、比表面积及表面形貌均表现出明显的差异。其中,添加助剂Cu的催化剂表面检测到较多的活性组分Ni,接近90%(w/w),该催化剂平均孔径最小(3.87 nm)、活性组分Ni颗粒分散性好。评价结果表明,该催化剂具有较佳的加氢性能,其1,4-丁烯二醇(BED)转化率为100%,1,4-丁二醇(BDO)选择性和收率分别为59.62%和59.62%,这与该催化剂较大的活性组分Ni负载量、酸强度和适中的酸量及存在的Cu对Ni分散性的提高进一步防止了Ni的严重烧结(即"限域效应")等有较大关联。     

超声改性的CuO/Al2O3-MgO催化剂结构 及其超低浓度甲烷催化燃烧性能

采用普通浸渍和超声改性的方法分别制备了CuO/Al₂O₃-MgO催化剂,用于超低浓度甲烷的催化燃烧,并利用SEM、XRD、XPS、H₂-TPR等技术对催化剂进行表征,研究了超声改性作用对催化剂的结构和性能的影响.结果表明,与普通浸渍法制备的催化剂相比,在超声改性的CuO/Al₂O₃-MgO催化剂上,甲烷的转化率得到提高,燃烧特征温度降低.随着超声时间的延长和超声功率的增加,催化剂的催化活性均呈现先增大后减小的趋势;催化剂制备的最佳超声工况为功率150 W、时间20 min.超声改性可使催化剂的比表面积和孔容积增大,表面催化活性较高的Cu⁺浓度增加,活性组分CuO由晶相向非晶相转变、分散度增大,晶粒粒径变小、分布更均匀;这使得甲烷催化燃烧的表观活化能下降、催化剂活性得到增强.     

Efficient oxidative degradation of 2-chlorophenol and 4-chlorophenol over supported CuO-based catalysts

A series of metal oxide catalysts for catalytic oxidative degradation of 2-chlorophenol (2-CP) and 4-chlorophenol (4-CP) were prepared, and the supported CuO catalysts were studied particularly. The supported CuO catalysts were characterized by XRD and NH3-TPD techniques, in which CuO/γ-Al2O3 exhibited high degradation activity. The addition of Na2O or K2O into CuO/γ-Al2O3 improved the oxidative degradation of CPs remarkably, in which Na2O was more efficient than K2O. Over CuO/γ-Al2O3-Na2O, CPs were completely converted and the liberation of the inorganic chloride from 2-CP or 4-CP reached 97% or 100% respectively at 30 ?C for 2 h. The supported CuO catalysts with good dispersion of CuO particles and less acid sites were favorable for the efficient oxidative degradation of CPs. In addition, the initial pH of the reaction solution was found to be an important factor which influenced the catalytic oxidative degradation of CPs and the initial pH of 11.2 and 9.8 was preferred for the oxidative degradation of 2-CP and 4-CP respectively over CuO/γ-Al2O3 catalyst.     

溶剂极性对微波辐射老化制备前驱体及CuO/ZnO/Al2O3催化剂结构的影响

在制备CuO/ZnO/Al2O3催化剂的老化过程中,采用微波辐射老化技术,着重研究了溶剂极性对前躯体物相组成,烧后CuO/ZnO/Al2O3催化剂结构及其在浆态床合成甲醇工艺中催化性能的影响。通过XRD、DTG、H2-TPR,FTIR、HR-TEM和XPS对前驱体及催化剂表征表明,沉淀母液在微波辐射条件下进行老化,溶剂的极性对前躯体物相组成及催化剂结构影响显著。随着溶剂极性的增大,Zn2+/Cu2+取代Cu2(CO3)(OH)2/Zn5(CO3)2(OH)6中Cu2+/Zn2+的取代反应增强,使得前躯体中(Cu,Zn)5(CO3)2(OH)6和(Cu,Zn)2(CO3)(OH)2物相的含量增多,结晶度提高,导致烧后CuO/ZnO/Al2O3催化剂中CuO-ZnO协同作用增强,且CuO晶粒减小,表面Cu含量增加,催化剂活性和稳定性提高。水溶剂的极性最大,制备的催化剂活性和稳定性最好,甲醇的时空收率(STY)和平均失活率分别为320 mg.g-1.h-1和0.11%.d-1。     

Study of CO2 Hydrogenation to Methanol over Cu-V/γ-Al2O3 Catalyst

The effect of vanadium addition to CU/γ-Al2O3 catalyst used in the hydrogenation of CO2 to produce methanol was studied. It was found that the catalytic performance of the Cu-based catalyst improved after V addition. The influence of reaction temperature, space velocity and the molar ratio of H2 to CO2 on the performance of 12%Cu-6%V/γ-Al2O3 catalyst were also studied. The results indicated that the best conditions for reaction were as follows: 240℃, 3600 h-1 and a molar ratio of H2 to CO2 of 3:1. The results of XRD and TPR characterization demonstrated that the addition of V enhanced the dispersion of the supported CuO species, which resulted in the enhanced catalytic performance of CU-V/γ-Al2O3 binary catalyst.     

沉淀方法对铜基甲醇合成催化剂前驱体及其性能的影响

 分别采用共沉淀法 (CP)、两步沉淀法 (TP) 和分步沉淀法 (FP) 制备了 Cu/ZnO/Al₂O₃ 甲醇合成催化剂. 结果发现, FP 催化剂上甲醇收率比 CP 催化剂上高 46.3%, 比 TP 催化剂上高 9.3%. 采用 X 射线衍射、微分热重分析、红外光谱、N₂ 吸附-脱附、程序升温还原及 N₂O 滴定等方法表征了催化剂. 结果表明, FP 催化剂前驱体中 (Cu,Zn)₂CO₃(OH)₂ 和 (Zn,Cu)₅(CO₃)₂(OH)₆ 两种高活性物相较多, 而 (Cu,Zn)₆Al₂(OH)₁₆CO₃•4H₂O 物相较少, 焙烧后形成了较多的 CuO-ZnO 固溶体, 同时形成了较多的碳酸盐, 因而催化活性更高.     

1,4-丁炔二醇与4,4′-二乙炔联苯共聚物的合成及表征研究

 本文用(Ph₃P)₂PdCl₂为催化剂,合成了1,4-丁炔二醇(BD)与4,4-二乙炔联苯(DEBP)共聚物。对用不同比例的两种单体得到的共聚物测定了比重(d₄²⁵、溶胀度(θ_D)、最良溶剂及相邻两交联点之间的平均分子量(M_c)。实验表明,在两种单体摩尔比中,DEBP用量越多,共聚物中泡状微孔越多,颜色越淡,溶胀度和比重越小,交联度越大;DEBP/BD(摩尔比)大于1/5时,共聚物的最良溶剂为苯,溶度参数为9.15卡^0.5·cm^-1.5,是1/10时,其最良溶剂为乙醇,溶度参数是12.7卡^0.5·cm^-1.5。对共聚物还做了红外光谱表征。