共查询到19条相似文献,搜索用时 111 毫秒
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以α1-VOPO4相为催化剂, 在环己烷气相氧化脱氢反应中, 通过在原料中加入醋酸可控制反应产物的分布. 研究了不同醋酸量对目标产物选择性的影响, 醋酸在反应体系中优于环己烷吸附在α1-VOPO4催化剂的表面上, 使催化剂表面形成孤立的活性中心, 避免了产物环己烯的深度氧化. 反应温度为450 ℃, 醋酸与环己烷的摩尔比为12.9∶1时, 环己烷的转化率为6.9%, 环己烯的选择性为100%. 相似文献
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研究了超临界流体技术在共价有机骨架材料(COF)合成中的应用,以均苯三甲醛和对苯二胺为原料,N,N-二甲基甲酰胺为共溶剂,醋酸为催化剂,在超临界二氧化碳(scCO2)中合成了亚胺类共价有机骨架材料COF-LZU1.考察了共溶剂、反应温度、反应压力、反应时间、醋酸含量和反应物摩尔比对COF-LZU1材料的晶体结构和微观形貌的影响.实验结果表明,反应温度的升高有利于提高scCO2的传质速率及增加反应物在scCO2中的溶解度,从而促进反应的进行;反应时间的延长有利于晶体的成熟和结晶度的提高;醋酸不仅是反应催化剂,还具有形貌导向剂的作用,通过改变醋酸用量分别获得了球状、块状和棒状形貌的COF-LZU1;反应物中对苯二胺含量过高会干扰反应过程中醛基与氨基的有序结合,导致结晶度的降低以及形貌规整程度的下降.在反应温度为60℃,反应压力为20 MPa,反应时间为6 h,均苯三甲醛与对苯二胺摩尔比为1∶1.5,醋酸(3 mol/L)与N,N-二甲基甲酰胺体积比为1∶1的条件下,制备的COF-LZU1呈现截面直径为80 nm的纳米棒形貌,具有良好的结晶度和优异的热稳定性,热分解温度高达550℃.本文首次... 相似文献
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二醋酸纤维素接枝丙交酯共聚物的合成与表征 总被引:1,自引:0,他引:1
以二醋酸纤维素为接枝骨架,在辛酸亚锡的催化下,通过L-丙交酯的开环接枝聚合反应,合成了二醋酸纤维素和聚丙交酯接枝共聚物(CDA-g-PLA),并采用GPC、FTIR、1H-NMR和DSC对接枝共聚物进行表征.研究了原料质量比、催化剂用量、反应时间、反应温度对单体转化率(C%)、接枝率(G%)的影响.结果表明:反应温度150℃,单体丙交酯与二醋酸纤维素质量比为4:1,反应时间30min,催化剂辛酸亚锡与二醋酸纤维素的质量比为1%时,产物的接枝率较高. 相似文献
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以水杨酸和乙酸酐为原料,用SO■/SiO_2-TiO_2固体酸为催化合成乙酰水杨酸,考察了TiO_2与SiO_2质量比、硫酸浸渍量、浸渍时间、煅烧温度等因素对乙酰水杨酸产率影响,通过红外光谱、扫描电镜和激光粒度仪对催化剂或合成产物进行了表征。得到最佳反应条件:SiO_2:TiO_2质量比为0.4:1、硫酸浸渍量与TiO_2质量比为0.49:1、浸渍时间为26 h、煅烧温度为400℃,该条件下制备的固体酸催化合成乙酰水杨酸产率为65%。该催化剂具有易与反应体系分离,对设备腐蚀性小,可再生等优点。 相似文献
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以氯化铜、钼酸铵、苯酐、氯化铵、尿素和NaY分子筛为原料,采用苯酐-尿素法制备了酞菁铜/分子筛复合物CuPc/Y.采用等体积浸渍法将金属钯担载在CuPc/Y上制备了Pd-CuPc/Y催化剂,并在醋酸水溶液中考察了其催化甲烷选择氧化合成甲醇反应的性能,结果表明,催化性能与反应温度、溶剂中CH3COOH与H2O的混合比例、对苯醌用量、反应时间等因素有关,在0.5%Pd-0.5%CuPc/Y添加量0.5 g、CH3COOH与H2O体积比4∶1、对苯醌用量1 000 μmol、反应时间3 h、反应温度150 ℃的条件下,甲醇的最佳生成量为1 840 μmol.Pd-CuPc/Y催化剂可以多次循环使用,但由于催化剂流失和催化剂表面的钯粒子聚集的原因,循环使用后的催化剂催化活性有所下降.Pd-CuPc/Y在醋酸溶液中催化甲烷选择氧化合成甲醇是亲电取代反应和活性氧物种氧化共同作用的结果. 相似文献
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Fabiane Hamerski Giovana Gonçalves Dusi Julia Trancoso Fernandes dos Santos Vítor Renan da Silva Fernando Augusto Pedersen Voll Marcos Lúcio Corazza 《国际化学动力学杂志》2020,52(8):499-512
This study reports experimental data and kinetic modeling of acetic acid esterification with n-pentanol using sulfated zirconia as a catalyst. Reactions were carried out in an isothermal well-mixed batch reactor at different temperatures (50-80°C), n-pentanol to acid molar ratios (1:1-3:1), and catalyst loadings (5-10 wt% in relation to the total amount of acetic acid). The reaction mechanism regarding the heterogeneous catalysis was evaluated considering pseudo-homogeneous, Eley–Rideal, and Langmuir–Hinshelwood model approaches. The reaction mixture was considered a nonideal solution and the UNIQUAC thermodynamic model was used to take into account the nonidealities in the liquid phase. The results obtained indicated that increases in the temperature and catalyst loading increased the product formation, while changes in the n-pentanol to acetic acid molar ratio showed no significant effect. The estimated enthalpy of the reaction was −8.49 kJ mol−1, suggesting a slightly exothermic reaction. The Eley–Rideal model, with acetic acid adsorbed on the catalyst as the limiting step, was found to be the most significant reaction mechanism. 相似文献
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Selective Oxidation of Propane by Lattice Oxygen of Vanadium-Phosphorous Oxide in a Pulse Reactor 下载免费PDF全文
RusongZhao JianWang QunDong JianhongLiu 《天然气化学杂志》2005,14(2):88-94
Selective oxidation of propane by lattice oxygen of vanadium-phosphorus oxide (VPO) catalysts was investigated with a pulse reactor in which the oxidation of propane and the re-oxidation of catalyst were implemented alternately in the presence of water vapor. The principal products are acrylic acid (AA),acetic acid (HAc), and carbon oxides. In addition, small amounts of C1 and C2 hydrocarbons were also found, molar ratio of AA to HAc is 1.4-2.2. The active oxygen species are those adsorbed on catalyst surface firmly and/or bound to catalyst lattice, i.e. lattice oxygen; the selective oxidation of propane on VPO catalysts can be carried out in a circulating fluidized bed (CFB) riser reactor. For propane oxidation over VPO catalysts, the effects of reaction temperature in a pulse reactor were found almost the same as in a steady-state flow reactor. That is, as the reaction temperature increases, propane conversion and the amount of C1 C2 hydrocarbons in the product increase steadily, while selectivity to acrylic acid and to acetic acid increase prior to 350℃ then begin to drop at temperatures higher than 350℃, and yields of acrylic acid and of acetic acid attained maximum at about 400℃. The maximum yields of acrylic acid and of acetic acid for a single-pass are 7.50% and 4.59% respectively, with 38.2% propane conversion. When theamount of propane pulsed decreases or the amount of catalyst loaded increases, the conversion increases but the selectivity decreases. Increasing the flow rate of carrier gases causes the conversion pass through a minimum but selectivity and yields pass through a maximum. In a fixed bed reactor, it is hard to obtainhigh selectivity at a high reaction conversion due to the further degradation of acrylic acid and acetic acid even though propane was oxidized by the lattice oxygen. The catalytic performance can be improved inthe presence of excess propane. Propylene can be oxidized by lattice oxygen of VPO catalyst at 250℃, nevertheless, selectivity to AA and to HAc are even lower, much more acetic acid was produced (molar ratio of AA to HAc is 0.19:1-0.83:1) though the oxidation products are the same as from propane. 相似文献
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Reverse atom transfer radical polymerization (RATRP) has been successfully applied in the synthesis of polyacrylonitrile (PAN) with FeCl3/acetic acid as catalyst in the presence of conventional initiator azobisisobutyronitrile (AIBN) at 65°C in N,N-dimethylformamide (DMF). A FeCl3 to acetic acid ratio of 1:2 not only gave better control on polymer's molecular weight and its distribution, but also provided a rapid polymerization rate compared with any other molar ratio of FeCl3 to acetic acid. The polymerization rate increased with increasing temperature and the apparent activation energy was calculated to be 80.6 kJ·mol?1. In comparison with dimethyl sulfoxide, acetonitrile, cyclohexanone and ethyl acetate, DMF was considered to be the best solvent of the polymerization for its polarity. Analysis of 1H-NMR further confirmed the living nature of the polymerization. 相似文献
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乙酸选择性加氢制乙醇反应性能研究 《燃料化学学报》2016,44(7):862-869
在固定床反应器上考察了反应温度、反应压力、乙酸(HAC)液体进料空速、H_2/HAC(总气体空速GHSV或H_2流量)对乙酸选择性加氢制乙醇反应的影响,研究了乙酸转化率、产物选择性、乙醇时空收率的变化规律,验证了自主开发催化剂的稳定性。结果表明,副产物的选择性受反应条件的影响,选择合适的反应条件可以抑制乙酸乙酯和丙酮的生成。原料与催化剂床层接触时间小于5s时,可以避免发生乙酸加氢分解脱羰反应生成甲烷气相产物,也避免了乙醇的进一步反应生成乙烷。在反应温度为280℃,反应压力为2.5 MPa,乙酸进料液时空速为0.72 h~(-1),H_2/HAC(mol ratio)为16的条件下,乙酸乙酯选择性为6%。900 h长周期实验表明,自主开发催化剂具有较好的工业应用前景。 相似文献
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Zhong-Lei Meng Ru-Si Wen Xiao-Rui Huang Rong-Xiu Qin Yi-Ming Hu Yong-Hong Zhou 《Molecules (Basel, Switzerland)》2022,27(3)
We report the use of five alpha-hydroxy acids (citric, tartaric, mandelic, lactic and glycolic acids) as catalysts in the synthesis of terpineol from alpha-pinene. The study found that the hydration rate of pinene was slow when only catalyzed by alpha-hydroxyl acids. Ternary composite catalysts, composed of AHAs, phosphoric acid, and acetic acid, had a good catalytic performance. The reaction step was hydrolysis of the intermediate terpinyl acetate, which yielded terpineol. The optimal reaction conditions were as follows: alpha-pinene, acetic acid, water, citric acid, and phosphoric acid, at a mass ratio of 1:2.5:1:(0.1–0.05):0.05, a reaction temperature of 70 °C, and a reaction time of 12–15 h. The conversion of alpha-pinene was 96%, the content of alpha-terpineol was 46.9%, and the selectivity of alpha-terpineol was 48.1%. In addition, the catalytic performance of monolayer graphene oxide and its composite catalyst with citric acid was studied, with acetic acid used as an additive. 相似文献