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Microwave-assisted synthesis of malic acid involving hydrochloric acid as catalyst

机译:微波辅助合成氯酸作为催化剂的苹果酸

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The competing acid catalyzed reactions of fumaric acid (F) isomerization to form maleic acid (Mx) (reaction R1), and the hydration of F to malic acid (M) (reaction R2) were investigated under microwave heating. The kinetic experiments were performed in a sealed microwave-irradiated batch reactor operated at pressures between 615 and 1715 kPa, in the temperature range from 433 to 478 K, and for reaction times up to 21,600 s. Hydrochloric acid at three different concentrations (C (H) = 0.65, 1.30 and 1.94 M) was used as the catalyst. The concentrations of F, Mx and M were periodically determined by HPLC analyses. The Arrhenius parameters for the forward rate constants of the reactions R1 and R2 were tuned on the experimental data of species concentrations (k (10) = 5.63 +/- 0.04 M-1 s(-1), E (a1)/R = 4837 +/- 121 K, k (20) = (6.9 +/- 0.3) x 10(7) M-2 s(-1), E (a2)/R = 13,532 +/- 212 K). The tuning procedure involved the Simplex method of optimization, and a kinetic model represented by a system of four ordinary differential equations from material balances on species F, Mx, M and HCl. The model was able to reproduce the variation in species concentrations with time for all experimental conditions investigated, just with a partial set of the currently obtained data used to adjust the model parameters (C (H) = 0.65 M and 1.94 M). The current results at C (H) of 1.30 M and analogous data from the literature under quite different reaction conditions (e.g.; C (H) = 0.97 M, non-isothermal reactor externally heated with glycerol) confirm the reliability of the modeling approach. The catalyst concentration had the expected significant effect on the reaction rates, but the influence of microwave irradiation on the kinetics of the conversion of F and on the selectivity of M was small.
机译:在微波加热下研究了富马酸(F)异构化对富马酸(MX)(反应R1)的竞争酸催化反应(反应R1),以及F至苹果酸(M)(反应R2)的水合。在密封的微波照射分批反应器中进行动力学实验,在615-1715kPa的压力下操作,温度范围为433-478k,并反应时间高达21,600秒。用三种不同浓度(C(H)= 0.65,1.30和1.94m)用盐酸作为催化剂。通过HPLC分析定期确定F,MX和M的浓度。对物种浓度的实验数据调节反应R1和R2的前向速率常数的Arrhenius参数(K(10)= 5.63 +/- 0.04 m-1 s(-1),E(a1)/ r = 4837 +/- 121 k,K(20)=(6.9 +/- 0.3)×10(7)m-2 s(-1),E(a2)/ r = 13,532 +/- 212 k)。调谐过程涉及单纯x优化方法,以及由物种F,MX,M和HCl上的材料余额的四个常微分方程系统表示的动力学模型。该模型能够在研究所有实验条件的时间内再现物种浓度的变化,只需使用用于调整模型参数的部分集合(C(h)= 0.65 m和1.94 m)。当前结果在1.30米的C(h)和来自文献中的类似数据在相当不同的反应条件下(例如; c(h)=0.97μm,用甘油外部加热的非等温反应器)证实了建模方法的可靠性。催化剂浓度对反应速率的预期显着影响,但微波辐射对F的转化率和M的选择性的影响小。

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