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Liquid Phase Dehydration of 1-Butanol to Di-n-butyl ether Experimental Performance, Modeling and Simulation of Ion Exchange Resins as Catalysts

机译:1-丁醇液相脱水制二正丁基醚的实验性能,离子交换树脂催化性能的建模与模拟

摘要

[eng] Di-n-butyl ether (DNBE) is considered a very attractive oxygenate compound to reformulate diesel fuel. The research work performed along this thesis has clearly proven that sulfonic P(S-DVB) ion exchange resins are suitable catalysts for the synthesis of DNBE from the liquid phase dehydration of 1-butanol at the temperature range of 140-190 °C. A catalyst screening of acidic P(S-DVB) ion exchange resins showed that resins activity is enhanced with high acid capacities and with polymer matrices that are able to swell moderately allowing 1-butanol ready access to the active sites but without resulting in very large distance between the active centers. The resin Amberlyst 36 (oversulfonated, medium values of %DVB) proved to be the most active catalysts tested. However, in an industrial process a high selectivity to DNBE is extremely desirable from an environmental and economic standpoint, and resins that present a more elastic polymer matrix and higher ability to swell (gel type resins and Amberlyst 70) are the ones that present higher selectivities. Among all the tested resins, Amberlyst 70 was selected as the most suitable catalyst for industrial use given its excellent property balance: satisfactory activity, high selectivity to DNBE and thermal stability up to 463 K. The relatively large value found for the thermodynamic equilibrium constant of DNBE formation and the fact that the formation of the secondary product 1-butene was extremely slow assure high conversion levels in an industrial etherification process. DNBE formation proved to be a slightly exothermic reaction, almost athermic, whereas 1-butene formation was found to be an endothermic reaction. A comprehensive kinetic analysis enlightened that the reaction rate to form DNBE on Amberlyst 70 is highly influenced by the temperature and the presence of water. Two kinetic models that are able to predict the reaction rates of DNBE formation were identified. One of them stems from a Langmuir-Hinshelwood-Hougen-Watson (LHHW) formalism in which two adsorbed molecules of 1-butanol react to yield ether and water, being the reversible surface reaction the rate limiting step. The other one stems from a mechanism in which the rate limiting step is the desorption of water and where the adsorption of DNBE is negligible. Both models present several characteristics in common: in both water inhibition effect is correctly represented by a correction factor derived from a Freundlich adsorption isotherm; the number of free active sites is found to be negligible compared to the occupied ones; both present similar values of apparent activation energies (122 ± 2 kJ/mol). The study of the influence of typical 1-butanol impurities (isobutanol or ethanol and acetone, depending on the production process) demonstrated that isobutanol enhances the formation of branched ethers whereas ethanol leads to the formation of ethyl butyl ether and di- ethyl ether and acetone hardly reacts. In the second part of this thesis, it was demonstrated the suitability of molecular dynamics simulations in the understanding of the microscopic structure of P(S-DVB) ion-exchange resins and the prediction of their properties. Atomistic simulations of the structure of sulfonated P(S-DVB) resins reveled the decisive role that internal loops (closed polymer chains) play in defining the properties (i.e. density, porosity and structures) of highly cross-linked resins. Thus, although crosslinks ensure the local backbone structure, internal loops confer rigidity and loop architecture. It was also demonstrated that the developed atomistic model is able to predict the swelling behavior of ion-exchange resins in 1-butanol. From the swelling study performed by means of molecular dynamic simulation it was possible to characterize and quantify the structure of the swollen polymeric network at molecular level and to conclude that alcohol molecules tend to interact with the sulfonic groups of the resin.
机译:[eng]二正丁基醚(DNBE)被认为是重新配制柴油燃料的一种非常有吸引力的含氧化合物。沿着本论文进行的研究工作已经清楚地证明,磺酸P(S-DVB)离子交换树脂是从1-丁醇在140-190°C的温度范围内液相脱水合成DNBE的合适催化剂。酸性P(S-DVB)离子交换树脂的催化剂筛选表明,高酸容量和能够适度溶胀的聚合物基质可增强树脂活性,允许1-丁醇随时进入活性位点,但不会产生很大的活动中心之间的距离。树脂Amberlyst 36(过磺化,%DVB的中等值)被证明是测试中最具活性的催化剂。然而,在工业过程中,从环境和经济的角度来看,对DNBE的高选择性是非常需要的,呈现出更高弹性聚合物基体和更高溶胀能力的树脂(凝胶型树脂和Amberlyst 70)是呈现出更高选择性的树脂。 。在所有测试的树脂中,Amberlyst 70具有出色的性能平衡:令人满意的活性,对DNBE的高选择性以及高达463 K的热稳定性,因此被选为最适合工业用途的催化剂。 DNBE的形成以及副产物1-丁烯的形成非常缓慢的事实确保了工业醚化过程中的高转化率。 DNBE的形成被证明是一个轻微的放热反应,几乎是吸热的,而1-丁烯的形成被认为是一个吸热反应。全面的动力学分析表明,在Amberlyst 70上形成DNBE的反应速率受温度和水的存在影响很大。确定了两个能够预测DNBE形成反应速率的动力学模型。其中之一源于Langmuir-Hinshelwood-Hougen-Watson(LHHW)形式,其中两个被吸附的1-丁醇分子反应生成醚和水,这是限速步骤中可逆的表面反应。另一个源于一种机制,其中限速步骤是水的解吸,而DNBE的吸附可忽略不计。两种模型都具有一些共同的特征:在两种情况下,抑水作用均正确地由Freundlich吸附等温线得出的修正因子表示。发现自由活动场所的数量与被占用的场所相比可以忽略不计;两者都表现出相似的表观活化能值(122±2 kJ / mol)。对典型的1-丁醇杂质(异丁醇或乙醇和丙酮,取决于生产工艺)的影响的研究表明,异丁醇会增强支链醚的形成,而乙醇会导致乙基丁醚和二乙基醚和丙酮的形成几乎没有反应。在论文的第二部分,证明了分子动力学模拟在理解P(S-DVB)离子交换树脂的微观结构及其性能预测方面的适用性。磺化P(S-DVB)树脂结构的原子模拟揭示了内部环(封闭的聚合物链)在定义高度交联的树脂的性能(即密度,孔隙率和结构)方面起的决定性作用。因此,尽管交联确保了局部骨干结构,但内部环路赋予了刚性和环路架构。还证明了开发的原子模型能够预测1-丁醇中离子交换树脂的溶胀行为。通过借助分子动力学模拟进行的溶胀研究,可以在分子水平上表征和定量溶胀的聚合物网络的结构,并得出结论,醇分子倾向于与树脂的磺酸基相互作用。

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