丁二酸酯加氢动力学研究毕业论文
2022-04-05 19:51:59
论文总字数:17040字
摘 要
以生物质丁二酸二甲酯为原料,通过铜基催化剂加氢制备1,4-丁二醇、四氢呋喃以及γ-丁内酯三种重要产品。本论文采用Cu/SiO2催化剂,在连续流固定床反应器中进行,考察了不同的反应压力、氢酯摩尔比、反应温度、液时空速对加氢反应的影响。较佳的工艺条件为:反应压力为5 Mpa,氢酯摩尔比为150,反应温度为215 ℃,丁二酸二甲酯的液时空速为0.4 h-1。在这种条件下,丁二酸二甲酯的转化率高于90 %,1,4-丁二醇的选择性在70%以上。同时研究了丁二酸二甲酯气相加氢反应宏观动力学,建立了丁二酸二甲酯加氢体系的动力学模型,求取了动力学参数。模型验证结果表明:模型对实验数据的拟合是较好的。
关键词:丁二酸二甲酯 1,4-丁二醇 催化剂 加氢
Reaction kinetic of hydrogenation over dimethyl succinate
Abstract
With dimethyl succinate as raw materials,we used copper-based catalyst for the preparation of 1,4-butanediol, tetrahydrofuran and γ- butyrolactone three important products. In this study, Cu/SiO2 catalyst in a continuous flow tubular reactor. Experimental effects of reaction pressure, hydrogen carbonate molar ratio, reaction temperature, liquid hourly space velocity of the hydrogenation reaction. Preferred conditions are: a reaction pressure of 5Mpa, ester molar ratio of 150 hydrogen, the reaction temperature was 215 ℃, dimethyl succinate LHSV 0.4h-1. Under these conditions, dimethyl succinate conversion was greater than 90%, the selectivity of 1,4-butanediol is greater than 70% . Also studied the kinetic parameters of gas-phase hydrogenation of dimethyl succinate intrinsic kinetics, a dynamic model of dimethyl succinate hydrogenation system, the strike. Model validation results show that: the model fit the experimental data is valid
Key Words: Dimethyl succinate;1,4-Butanediol;Catalyst;Hydrogenation
目 录
摘要······························································I
ABSTRACT······················································II
第一章 文献综述················································ 1
1.1 前言·······················································1
1.2 加氢催化剂的研究进展·······································2
1.2.1 铜基催化剂············································2
1.2.2 钌基催化剂············································2
1.3 丁二酸酯及其加氢产物········································3
1.4 丁二酸酯加氢的反应设备······································4
1.4.1 釜式反应器············································5
1.4.2 固定床式反应器········································5
1.5 1,4-丁二醇的生产工艺········································6
1.5.1 Reppe法··············································6
1.5.2 丁二烯乙酰氧基化法····································6
1.5.3 环氧丙烷法············································7
1.5.4 顺酐法················································7
1.6 1,4-丁二醇生产现状·········································7
1.7 本课题的研究内容和意义······································8
1.7.1 研究内容··············································8
1.7.2 研究的意义············································8
第二章 实验部分·················································9
2.1 实验仪器、原料及试剂········································9
2.1.1 实验仪器··············································9
2.1.2 原料及试剂············································9
2.2 催化剂的制备···············································10
2.3 实验过程···················································10
2.3.1 实验原理·············································10
2.3.2 催化剂评价···········································10
2.3.3 气相分析条件·········································11
2.3.4 校正因子f的求算·····································12
第三章 结果与分析··············································14
3.1 反应压力的影响·············································14
3.2 氢酯比的影响···············································15
3.3 温度的影响·················································16
3.4 原料空速的影响·············································18
3.5 动力学模型的建立···········································19
3.5.1 动力学方程参数估算··································19
3.5.2 动力学模型验证·······································20
3.6 本章小结···················································21
第四章 结论与展望··············································22
参考文献···························································23
致谢·······························································25
第一章 文献综述
1.1 前言
近十年来,丁二醇及其下游产品构成的产业链是发展最快、产量增长最快、生产技术进步最快的行业之一,1,4-丁二醇的终端产品及衍生物的的需求大量增长推动着其不断发展。1,4-丁二醇的生产方法中,以生物质为原料的加氢生产工艺因其来源范围广、价格便宜、可再生的巨大优势成为主要研究方向。其中又以生物质丁二酸为主要研究材料之一。
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