首页> 外文期刊>Separation and Purification Technology >Buffering-out: Separation of tetrahydrofuran, 1,3-dioxolane, or 1,4-dioxane from their aqueous solutions using EPPS buffer at 298.15 K
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Buffering-out: Separation of tetrahydrofuran, 1,3-dioxolane, or 1,4-dioxane from their aqueous solutions using EPPS buffer at 298.15 K

机译:缓冲:使用298.15 K的EPPS缓冲液从水溶液中分离四氢呋喃,1,3-二氧戊环或1,4-二氧六环

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摘要

Buffering-out phase separation technique was performed to obtain 98.01 wt.% of tetrahydrofuran (THF), 96.63 wt.% of 1,3-dioxolane, and 94.85 wt.% of 1,4-dioxane from their aqueous solutions using a biological buffer. The phase separation was carried out at room temperature under atmospheric pressure; and the biological buffer is 3-[4-(2-hydroxyethyl)-l-piperazinyl]propanesulfonic acid (EPPS). The solid-liquid equilibrium (SLE), liquid-liquid equilibrium (LLE), and solid-liquid-liquid equilibrium (SLLE) data have been measured for EPPS + tetrahydrofuran + water, EPPS + 1,3-dioxolane + water, and EPPS + 1,4-dioxane + water systems. Phase diagrams were then constructed for these new phase separation systems. The solubility mass fractions were fitted to an empirical equation as a function of the cyclic ether and buffer concentrations. The effective excluded volume (EEV) model was applied to the solubility mass fractions as well in order to evaluate the phase-separation ability of the investigated cyclic ethers. The consistency of the LLE tie-line data was verified with the Othmer-Tobias correlation. For the process simulations purpose, these experimental tie-line data were also correlated satisfactorily with the NRTL activity coefficient model. The NRTL binary interaction parameters of the investigated systems were reported. By taking advantage of the buffering-out effect, a conceptual process flowsheet for recovery of the cyclic ethers from their aqueous solutions was proposed.
机译:进行缓冲相分离技术以使用生物缓冲剂从其水溶液中获得98.01 wt。%的四氢呋喃(THF),96.63 wt。%的1,3-二氧戊环和94.85 wt。%的1,4-二氧六环。相分离在室温下在大气压下进行。生物缓冲液为3- [4-(2-羟乙基)-1-哌嗪基]丙烷磺酸(EPPS)。对EPPS +四氢呋喃+水,EPPS + 1,3-二氧戊环+水和EPPS的固液平衡(SLE),液液平衡(LLE)和固液液平衡(SLLE)数据进行了测量+ 1,4-二恶烷+水系统。然后为这些新的相分离系统构建相图。将溶解度质量分数作为环醚和缓冲液浓度的函数拟合为经验公式。有效排除体积(EEV)模型也适用于溶解度质量分数,以评估所研究的环状醚的相分离能力。 LLE联系线数据的一致性通过Othmer-Tobias相关性进行了验证。出于过程仿真的目的,这些实验联系线数据也与NRTL活度系数模型令人满意地相关。报告了研究系统的NRTL二元相互作用参数。通过利用缓冲作用,提出了从其水溶液中回收环醚的概念性工艺流程图。

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