Application of Brönsted acid ionic liquids as green catalyst in the synthesis of 2-propanol with reactive distillation

Five Br?nsted acidic ionic liquids (ILs) were prepared and characterized by FT-IR, 1H NMR and 13C NMR. Their cat-alytic activities for the synthesis of 2-propanol (IPOH) via transesterification of isopropyl acetate (IPAc) with methanol (MeOH) were investigated. Among al the tested ILs, [Ps-mim]HSO4 performed best and was used as catalyst for further studies. The reaction kinetics were carried out to correlate the parameters in a homogeneous second order kinetic model. It has been found that there is close agreement between the calculated and experi-mental values. The high-pressure batch reactive distillation experimental apparatus was set up in order to en-hance the conversion of IPAc. A high conversion of IPAc of 99.4%was obtained under the optimal reaction conditions. The catalyst [Ps-mim]HSO4 can be recycled easily by a rotary evaporator and reused without any fur-ther treatment. The catalyst had been repeatedly used for four times and no obvious changes in the structure of catalyst could be observed.     

用离子液体作催化剂和夹带剂时在反应萃取精馏塔中乙酸甲酯和正丁醇酯交换反应的模拟

A new reactive and extractive distillation process with ionic liquids as entrainer and catalyst (RED-IL) was proposed to produce methanol and n-butyl acetate by transesterification reaction of methyl acetate with n-butanol. The RED-IL process was simulated via a rigorous model, and high purity products of methanol and n-butyl acetate can be obtained in such a process. The effects of reflux ratio, feed mode, holdup, feed location, entrainer ratio and catalyst concentration on RED-IL process were investigated. The conversion of methyl acetate and purities of products increase with the holdup in column, entrainer ratio and catalyst content. An optimal reflux ratio exists in RED-IL process. Comparing to the mixed-feed mode, the segregated-feed mode is more effective, in which the optimal feed locations of reactants exist.     

矿物均相酸催化剂催化甲醇和乙酸酯化反应动力学(英文)

In this work, esterification of acetic acid and methanol to synthesize methyl acetate in a batch stirred reactor is studied in the temperature range of 305.15–333.15 K. Sulfuric acid is used as the homogeneous catalyst with concentrations ranging from 0.0633 mol·L?1 to 0.3268 mol·L?1. The feed molar ratio of acetic acid to methanol is varied from 1:1 to 1:4. The influences of temperature, catalyst concentration and reactant concentration on the reaction rate are investigated. A second order kinetic rate equation is used to correlate the experimental data. The forward and backward reaction rate constants and activation energies are determined from the Arrhenius plot. The developed kinetic model is compared with the models in literature. The developed kinetic equation is useful for the simulation of reactive distillation column for the synthesis of methyl acetate.     

Reaction kinetics for synthesis of sec-butyl alcohol catalyzed by acid-functionalized ionic liquid

The acid-functionalized ionic liquid ([HSO3Pmim]HSO4) was synthesized by a two-step method. Nuclear magnetic resonance (NMR) and Fourier transform infrared spectroscopy (FT-IR) show that the synthesis ...     

由合成气生产二甲醚过程反应协同作用的研究

Influence of reaction temperature, pressure and space velocity on the direct synthesis of dimethyl ether (DME) from syngas is studied in an isothermal fixed-bed reactor. The catalyst is a physical mixture of C30 copper-based methanol (MeOH) synthesis catalyst and ZSM-5 dehydration catalyst. The experimental results show that the chemical synergy between methanol synthesis reaction and methanol dehydration reaction is evident. The conversion of carbon monoxide is over 90%.     

离子液体催化的芳烃氯甲基化反应

Ionic liquids have been used as catalysts for Blanc reaction of toluene. The effects of reaction temperature, reaction time and dosage of the ionic liquid catalyst have been investigated, and the catalytic performance of different ionic liquid catalysts for toluene chloromethylation was also studied. The reaction was found to proceed under mild conditions with excellent conversion （up to 90%） in the absence of Lewis acids. The ionic liquids could be recycled and reused without loss of their catalytic activities.     

液相合成甲醇催化剂活性的研究

The effects of reduction procedure, reaction temperature and composition of feed gas on the activity of a CuO-ZnO-Al2O3 catalyst for liquid phase methanol synthesis were studied. An optimized procedure different from conventional ones was developed to obtain higher activity and better stability of the catalyst. Both CO and CO2 in the feed gas were found to be necessary to maintain the activity of catalyst in the synthesis process. Reaction temperature was limited up to 523K, otherwise the catalyst will be deactivated rapidly. Experimental results show that the catalyst deactivation is caused by sintering and fouling, and the effects of CO and CO2 on the catalyst activity are also investigated. The experimental results indicate that the formation of water in the methanol synthesis is negligible when the feed gas contains both CO and CO2. The mechanism for liquid-phase methanol synthesis was discussed and it differed slightly from that for gas-phase synthesis.     

Kinetics study of the N-formylation of aniline with DMF catalyzed by temperature-controlled Brùnsted ionic liquids

A series of SO₃-functional Br?nsted acidic ionic liquids(SBAILs) were prepared to catalyze the Nformylation of aniline with DMF.The reaction conditions such as ionic liquid type,reaction temperature.catalyst loading and molar ratio of reactants were investigated.To the best of our knowledge,kinetic model for the N-formylation of aniline with DMF using SBAIL was firstly built and simulated.The studies on the reaction order of the reaction were evaluated by initial concentration method,...     

Solventless ketalization of glycerol to solketal with acetone over the ionic liquid[P(C4H9)3C14H29][TsO]

The ketalization of glycerol with acetone was conducted over an ionic liquid [P(C_4H_9)_3C_(14)H_(29)][Ts O](TTPT) in a batch reactor. A scheme to obtain the purified product using TTPT as a homogeneous catalyst is proposed and a maximum solketal yield of 86% is achieved at acetone/glycerol molar ratio of 6/1, reaction time of 0.5 h, reaction temperature of 303 K, catalyst amount of 5 wt% of glycerol. TTPT was recycled and reused for ten times without obvious losses in terms of quantity and activity. Furthermore, effects of various experimental parameters(stirring speed, catalyst loadings, temperature and reactant composition) on the reaction kinetics are investigated. In terms of kinetics modeling, Kγis fitted by reactant composition at the temperature range 298 K–323 K, which was a concise strategy that showed good precision in the kinetics fitting. The activation energy for this ketalization reaction was evaluated to be 28.2 k J·mol~(-1). In addition, the kinetics of the reaction at a temperature exceeding the boiling point of acetone were also studied. We believe that all the results are important for further development of a technology for the continuous synthesis of solketal.     

内部部分润湿催化剂的动力学行为

The global reaction rate of benzene hydrogenation to cyclohexane accompanied by partial internal wetting of catalyst pellets was measured by a new method, which investigated both adsorption and chemical reaction. The adsorption investigation was used to establish a relationship between the extent of liquid filling of the catalyst and the bulk conditions while the chemical reaction investigation was to study the effect of partial internal wetting of the catalyst on the global reaction rate. It was shown that the extent of liquid filling in the catalyst interior showed a significant effect on the global rate, and the current state of the catalyst depended on the history, i.e. whether it was a liquid evaporation process or a vapor condensation process, and two steady states were found under certain circumstances. A mathematical model was developed, which took multicomponent diffusion, chemical reaction, pore size distribution of the catalyst and capillary condensation of condensable components in the catalyst pellet into consideration. The predicted values were in good agreement with the experimental data.     

Synthesis and kinetics of 2,5-dicyanofuran in the presence of hydroxylamine ionic liquid salts

2,5-Dicyanofuran (DCF) is an important biomass-derived platform compound primarily used to prepare bio-based adiponitrile, which is the key precursor for the synthesis of nylon 66 and 1,6-hexanediisocyanate (HDI). In this study, one-pot, green and safe synthesis of DCF from 2,5-diformylfuran (DFF) and hydroxylamine ionic liquid salts was proposed. Eco-friendly hydroxylamine ionic liquid salts were used as the nitrogen source. Ionic liquid exhibited three-fold function of cosolvent, catalysis and phase separation. The conversion of DFF and yield of DCF reached 100% under the following optimum reaction conditions: temperature of 120 ℃ for 70 min, volume ratio of paraxylene: [HSO₃-b-Py]·HSO₄ of 2:1, and molar ratio of DFF:(NH₂OH)₂·[HSO₃-b-Py]·HSO₄ of 1:1.5. The reaction mechanism for the synthesis of DCF was proposed, and the kinetic model was established. The reaction order with respect to DFF and intermediate product 2,5-diformylfuran dioxime (DFFD) was 1.06 and 0.16, and the reaction activation energy was 64.07 kJ·mol^-1 and 59.37 kJ·mol^-1 respectively. After the reaction, the ionic liquid was easy to separate, recover and recycle.     

酸性离子液体[SO_3H-Bmim]HSO_4作电解质的甲醇燃料电池性能研究

采用两步法合成了1-磺酸丁基-3甲基咪唑硫酸氢盐([SO_3H-Bmim]HSO_4)酸性离子液体,对其红外光谱结构和电导率进行表征;同时采用不锈钢材料制作了燃料电池的壳体,并制备了阳极和阴极材料,与[SO_3H-Bmim]HSO_4电解质一起组装成燃料单电池。以甲醇为燃料、空气为氧源在80℃采用伏安法测定了燃料电池的性能,其功率密度达到0.19 m W·cm~(-2),有望为甲醇燃料电池实际利用开辟新途径。     

稀土催化苯乙烯配位聚合制备富含间规聚苯乙烯

由稀土羧酸盐(RE)、烷基铝(AL)与含氯活化剂(CL)组成的催化体系用于苯乙烯(St)定向聚合,研究了催化剂配比及反应条件对苯乙烯聚合反应动力学和产物结构的影响,采用凝胶渗透色谱仪(GPC)、核磁共振波谱仪(¹³C NMR)、偏光显微镜(POM)及差示扫描量热仪(DSC)等分析测试手段表征聚苯乙烯(PS)的分子量及其分布、立构规整度、结晶性及热性能。实验结果表明:含氯活化剂为氯代羧酸酯(CE)时,聚合速率对单体浓度均呈现一级动力学关系, 表观增长活化能为34.4 kJ·mol^-1,可得到数均分子量(M_n)为2.8×10⁵～6.8×10⁵ g·mol^-1、熔点为160～260℃的可结晶聚苯乙烯。对于CE与卤代烃(RX)复合的催化体系,可明显提高催化活性,当聚合温度为50、60、70℃时,表观增长速率常数可分别提高3.9倍、5.6倍及9.2倍,分子量降低(M_n为0.5×10⁴～5.0×10⁵ g·mol^-1),并可得到间规度[rrrr]约为60%的可结晶聚苯乙烯,熔点为170～240℃。     

Kinetics of xylose dehydration into furfural in acetic acid

In this paper kinetics of xylose dehydration into furfural using acetic acid as catalyst was studied comprehensively and systematical y. The reaction order of both furfural and xylose dehydration was determined and the reaction activation energy was obtalned by nonlinear regression. The effect of acetic acid concentration was also investi-gated. Reaction rate constants were galned. Reaction rate constant of xylose dehydration is k1 ? 4:189 . 1010 ?A.0:1676 exp ?108:6.1000RT . ., reaction rate constant of furfural degradation is k2 ? 1:271 . 104?A.0:1375 exp?63:413.1000RT . and reaction rate constant of condensation reaction is k3 ? 3:4051 . 1010?A.0:1676 exp?104:99.1000RT .. Based on this, the kinetics equation of xylose dehydration into furfural in acetic acid was set up according to theory of Dunlop and Furfural generating rate equation is dd?F.t ? k1?X.0e?k1t?k2?F.?k3?X.0e?k1t?F.. ? 2015 The Chemical Industry and Engineering Society of China, and Chemical Industry Press. Al rights reserved.     

Porous polymer microsphere functionalized with benzimidazolium based ionic liquids as effective solid catalysts for esterification

To prepare polymer supported ionic liquids (PSILs) as effective catalysts for esterification, the free radical suspension copolymerization of vinylbenzyl chloride (VBC, monomer), styrene (St, monomer) and divinylbenzene (DVB, crosslinker) with the addition of n-heptane (porogen) was carried out for the fabrication of the porous polymer (PVD) microsphere as support, followed by the immobilization of sulfonic acid-functionalized ionic liquids by the successive treatment of benzimidazole (BIm), 1,3-propane sultone and sulfuric acid (H₂SO₄) or trifluoromethanesulfonic acid (CF₃SO₃H). The effects of the compositions of DVB and n-heptane on the internal structure of the polymer supports were investigated, and it was found that the support with 40 wt% DVB and 60 wt% n-heptane (with relative to the monomer) could endow the final PSILs with the relatively optimal catalytic performance. The preliminary experiment in the batch reactor indicated that PSILs herein exhibited higher catalytic activities than commercial Amberlyst 46 resin for the esterification of propanoic acid (PROAc) with n-propanol (PROOH). Consequently, the optimal PSILs catalyst, PVD-[Bim-SO₃H]HSO₄, was selected for further study in the batch reactive distillation column because of low cost and its ease of preparation. The yield of propyl ropionate (PROPRO) could reach up to 97.78% at the optimized conditions of PROOH/PROAc molar ratio (2:1) and catalyst dosage (2.0 wt%). The investigation of the reaction kinetic manifested that the calculated results of second order pseudo-homogeneous kinetic model were in good agreement with experimental values. The pre-exponential factor and activation energy were 4.12×10⁷ L·mol^-1·min^-1 and 60.57 kJ·mol^-1, respectively. It is worth noting that the PSILs catalyst could be simply recovered and reused with relatively satisfactory decrease in the catalytic activity, which made it an environmental friendly and promising catalyst in the industrial application.     

离子液体反应萃取精馏合成乙酸乙酯

采用离子液体1-磺酸丁基-3-甲基咪唑硫酸氢盐([HSO₃bmim][HSO₄])和1-丁基-3-甲基咪唑双三氟甲磺酰亚胺盐([BMIM][Tf₂N])分别作为催化剂和萃取剂,对乙酸甲酯与乙醇合成乙酸乙酯和甲醇的反应萃取精馏(RED)过程进行了模拟计算。在反应动力学和汽液相平衡分析基础上建立了反应萃取精馏流程,研究了理论板数、回流比、持液量、进料位置、溶剂比(萃取剂进料与原料进料摩尔流量的比值)、催化剂进料流量等参数对反应萃取精馏过程的影响。在优化的操作条件下,甲醇纯度为0.9922,乙酸乙酯纯度为0.9905,乙酸甲酯转化率为0.9922。     

树脂催化重汽油烷基化硫转移的动力学研究

采用树脂催化剂,研究重汽油中噻吩类硫化物的烷基化硫转移性能,分析反应前后硫分布的变化,并对反应动力学进行研究。结果表明,在反应温度110℃和反应时间60 min条件下,烷基化硫转移率大于90%,其反应动力学为一级反应速率方程,反应活化能为20.32 kJ·mol~(-1),指前因子为1 364 h~(-1),噻吩类硫化物烷基化反应的动力学方程可表示为:r=1364exp(-2.445×10~3/T)c_T。     

反气相色谱法与汉森溶解度参数软件测定原煤的三维溶解度参数

采用反气相色谱法（IGC）研究原煤在温度433.15、443.15、453.15、463.15和473.15 K时的三维溶解度参数（HSP）,并使用外推法得到原煤室温（298.15 K）时HSP的色散力分量（δ_d）、极性力分量（δ_p）、氢键力分量（δ_h）以及校正溶解度参数（δ_t）分别为δ_d=20.83（J·cm^-3）^1/2,δ_p=11.95（J·cm^-3）^1/2,δ_h=11.08（J·cm^-3）^1/2,δ_t=26.44（J·cm^-3）^1/2。同时,采用汉森三维溶解度参数软件（HSPiP）模拟原煤在室温下的HSP,得到δ_d=19.92（J·cm^-3）^1/2,δ_p=11.18（J·cm^-3）^1/2,δ_h=11.47（J·cm^-3）^1/2,δ_t=25.56（J·cm^-3）^1/2。IGC与HSPiP得出的数据一致,研究结果为煤的热力学性质研究及其溶胀剂的选择等应用提供了参考。