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以羟基乙酸和正丁醇为原料,用新型固体超强酸SO2-4/ZrO2/La3+为催化剂,合成羟基乙酸正丁酯。其工艺简单,产物转化率高。最佳工艺条件为:n(羟基乙酸)∶n(正丁醇)=1∶3.5,回流反应4h,催化剂用量为醇酸总质量的2.35%,收率83.2%。 相似文献
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探讨了以AlCl3/NaHSO4为复合催化剂,冰醋酸、正丁醇为原料合成乙酸正丁酯。确定了反应的优化条件:当冰醋酸用量为0.1 mol时,反应物料的投料物质的量比n(冰醋酸)∶n(正丁酯)=1∶1.7,催化剂配料物质的量比为n(AlCl3)∶n(NaHSO4)=1∶1.5,催化剂用量2 g,15 mL环己烷作带水剂,回流温度下反应时间为120 min,其酯化率达97%。 相似文献
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SBA-15负载对甲苯磺酸催化合成乙酸正丁酯 总被引:2,自引:0,他引:2
采用后合成方法,将含有磺酸基的有机酸对甲苯磺酸负载在介孔分子筛SBA—15表面上,合成含有一定酸性的固体酸催化剂TsOH—SBA—15。用IR对乙酸正丁酯进行表征。结果表明,该催化剂对冰乙酸和正丁醇的酯化反应具有较高的催化活性。探讨了酸醇物质的量比、催化剂用量及反应时间对乙酸正丁酯合成产率的影响。通过正交试验优化酯化反应条件:n冰乙酸∶n正丁醇=1∶1.2,催化剂用量为5%(以冰醋酸质量计),反应时间80 min条件下,合成乙酸正丁酯产率在95%以上。 相似文献
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以固体超强酸S2O82-/TiO2为催化剂、冰乙酸和正丁醇为原料合成乙酸正丁酯,考察反应条件对酯化率的影响。结果表明,最佳反应条件n(醇)∶n(酸)=1.4∶1,催化剂用量0.5 g(冰乙酸用量0.2 mol),过硫酸铵浓度0.75 mol.L-1,115~117℃反应1.5 h,酯化率达99%以上。催化剂可重复使用,且对设备腐蚀程度较小。 相似文献
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以改性D001型阳离子交换树脂为催化剂,以乙酸和正丁醇为原料,在浆态鼓泡床多相反应器反应回流条件下催化酯化反应制备乙酸正丁酯,研究了反应器的技术优势及催化剂的特性和催化剂类型、用量对酯化反应的影响及其使用寿命. 结果表明,最佳反应条件为:正丁醇:乙酸=1.2:1(摩尔比),催化剂用量占乙酸量的40%(w),反应温度110℃,反应时间75 min,该条件下乙酸正丁酯产率达98%以上,纯度达99.5%,催化剂经洗涤活化、再生,可重复使用6次. 相似文献
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离子液体N-甲基咪唑对甲苯磺酸盐催化剂的制备及应用 总被引:1,自引:0,他引:1
采用一步法制备Brφnsted酸性离子液体N-甲基咪唑对甲苯磺酸盐催化剂([Hmjm]TsO),并对其进行了红外光谱、拉曼光谱等表征。将其应用于醋酸和正丁醇的酯化反应,详细考察了离子液体用量、反应时间、醇酸物料比、反应温度等因素对酯化反应的影响,并确定了较佳反应条件为:温度95~98℃,n(丁醇):n(醋酸):1.2:1,离子液体用量为反应物总质量的20.O%,反应时间6h,酯化率可达到85.0%。同时,[Hmim]TsO离子液体循环使用6次后,酯化率仍可达到78.2%。 相似文献
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用玻璃球负载纳米级SO42-/TiO2固体超强酸催化合成乙酸正丁酯,对催化剂的制备条件和乙酸正丁酯的合成条件进行了研究。在最佳反应条件下,乙酸的转化率为99.3%,催化剂重复使用8次后乙酸的转化率仍高达92.3%。该催化剂选择性好,未发现有副产物生成,看来具有较好的应用前景。 相似文献
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A novel cerium (III) salt of Dawson type tungstophosphoric acid (Ce2P2W18O62·16H2O) was prepared by doping cerous nitrate in H6P2W18O62·13H2O powder and characterized by thermogravimetry and differential thermal analyses (TG/DTA), Fourier transform infrared spectroscopy (FT-IR), X-ray powder diffraction (XRD), pyridine infrared spectroscopy (Py-IR) and scanning electron microscopy (SEM). Its catalytic activity was evaluated by the probe reaction of synthesis of n-butyl acetate with acetic acid and n-butanol. The effects of various parameters such as molar ratio of n-butanol to acetic acid, reaction temperature, reaction time, and catalyst amount have been studied by single factor experiment. The results show that Ce2P2W18O62·16H2O behaved as an excellent heterogeneous catalyst in the synthesis of n-butyl acetate. The optimum synthetic conditions were determined as follows:molar ratio of n-butanol to acetic acid at 2.0:1.0, mass of the catalyst being 1.44% of the total reaction mixture, reaction temperature of 120 ℃ and reaction time of 150 min. Under above conditions, the conversion of acetic acid was above 97.8%. The selectivity of n-butyl acetate based on acetic acid was, in all cases, nearly 100%. The catalysts could be recycled and still exhibited high catalytic activity with 90.4% conversion after five cycles of reaction. It was found by means of TG-DTA and Py-IR that the catalyst deactivation was due to the adsorption of a complex of by-product on the active sites on catalysts surface or the catalyst loss in its separation from the products. Compared with using sulfuric acid as catalyst, the present procedure with Ce2P2W18O62·16H2O is a green productive technology due to simple process, higher yield, catalyst recycling and no corrosion for the production facilities. 相似文献
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在连续搅拌和分水条件下,研究了复合硫酸盐(Fe2(SO4)3-K2SO4)催化乙酸与正丁醇的反应。通过正交实验考查了催化剂用量、反应物配比、反应时间等因素对反应的影响。结果表明,其最优条件是:固定乙酸用量0.10mol,催化剂用量1.50g,醇酸物质的量比1.8∶1,反应时间2h,乙酸正丁酯的酯化率可达98.4%;另外,该催化剂具有制备方便,催化活性好,环境污染小等优点。 相似文献
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Based on a previous investigation, a simulation model was used for optimization of coproduction of ethyl acetate and n-butyl acetate by reactive distil ation. An experimental setup was established to verify the simulated results. The effects of various operating variables, such as ethanol feed location, acetic acid feed location, feed stage of reaction mixture of acetic acid and n-butanol, reflux ratio of ethyl acetate reactive distillation column, and distil-late to feed ratio of n-butyl acetate column, on the ethanol/n-butanol conversions, ethyl acetate/n-butyl acetate purity, and energy consumption were investigated. The optimal results in the simulation study are as follows:ethanol feed location, 15th stage;acetic acid feed location, eighth stage;feed location of reaction mixture of acetic acid and n-butanol, eighth stage;reflux ratio of ethyl acetate reactive distillation column, 2.0;and distillate to feed ratio of n-butyl acetate, 0.6. 相似文献