Valério Rita, Brazinha Carla, Crespo João G
LAQV-Requimte, Department of Chemistry, NOVA School of Science and Technology, NOVA University of Lisbon, 2829-516 Caparica, Portugal.
UCIBIO-Applied Molecular Biosciences Unit, Department of Chemistry, School of Science and Technology, NOVA University Lisbon, 2819-516 Caparica, Portugal.
Membranes (Basel). 2022 Aug 19;12(8):801. doi: 10.3390/membranes12080801.
The increasing demand for natural products has led to biotechnological vanillin production, which requires the recovery of vanillin (and vanillyl alcohol at trace concentrations, as in botanical vanillin) from the bioconversion broth, free from potential contaminants: the substrate and metabolites of bioconversion. This work discusses the recovery and fractionation of bio-vanillin, from a bioconversion broth, by pervaporation and by vacuum distillation, coupled with fractionated condensation. The objective was to recover vanillin free of potential contaminants, with maximised fluxes and selectivity for vanillin against water and minimised energy consumption per mass of vanillin recovered. In vacuum distillation fractionated condensation, adding several consecutive water pulses to the feed increased the percentage of recovered vanillin. In pervaporation-fractionated condensation and vacuum distillation-fractionated condensation processes, it was possible to recover vanillin and traces of vanillyl alcohol without the presence of potential contaminants. Vacuum distillation-experiments presented higher vanillin fluxes than pervaporation fractionated condensation experiments, 2.7 ± 0.1 g·m h and 1.19 ± 0.01 g·m h, respectively. However, pervaporation fractionated condensation assures a selectivity of vanillin against water of 4.5 on the pervaporation step (acting as a preconcentration step) and vacuum distillation fractionated condensation requires a higher energy consumption per mass of vanillin recovered when compared with pervaporation- fractionated condensation, 2727 KWh kg at 85 °C and 1361 KWh kg at 75 °C, respectively.
对天然产物需求的不断增加促使了生物技术法生产香草醛,这需要从生物转化 broth 中回收香草醛(以及痕量浓度的香草醇,如植物香草醛中的情况),且要去除潜在污染物:生物转化的底物和代谢产物。这项工作讨论了通过渗透蒸发和真空蒸馏结合分馏冷凝从生物转化 broth 中回收和分离生物香草醛的方法。目标是回收不含潜在污染物的香草醛,使通量最大化,香草醛对水的选择性最大化,且每回收单位质量香草醛的能耗最小化。在真空蒸馏分馏冷凝中,向进料中添加几个连续的水脉冲可提高回收香草醛的百分比。在渗透蒸发 - 分馏冷凝和真空蒸馏 - 分馏冷凝过程中,有可能在不存在潜在污染物的情况下回收香草醛和痕量香草醇。真空蒸馏实验的香草醛通量高于渗透蒸发分馏冷凝实验,分别为 2.7±0.1 g·m²·h⁻¹ 和 1.19±0.01 g·m²·h⁻¹。然而,渗透蒸发分馏冷凝在渗透蒸发步骤(作为预浓缩步骤)中确保香草醛对水的选择性为 4.5,与渗透蒸发 - 分馏冷凝相比,真空蒸馏分馏冷凝每回收单位质量香草醛需要更高的能耗,在 85°C 时为 2727 KWh·kg⁻¹,在 75°C 时为 1361 KWh·kg⁻¹。