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Highly pure 1,3‐propanediol: Separation and purification from crude glycerol‐based fermentation
Author(s) -
Wang Shizhen,
Qiu Longhui,
Dai Hongfei,
Zeng Xiaofei,
Fang Baishan
Publication year - 2015
Publication title -
engineering in life sciences
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 0.547
H-Index - 57
eISSN - 1618-2863
pISSN - 1618-0240
DOI - 10.1002/elsc.201500004
Subject(s) - adsorption , chromatography , volumetric flow rate , yield (engineering) , elution , glycerol , chemistry , distillation , 1,3 propanediol , column chromatography , vacuum distillation , activated carbon , fermentation , ethanol , materials science , organic chemistry , thermodynamics , physics , metallurgy
A new separation and purification process was developed for recovering 1,3‐propanediol (1,3‐PD) from crude glycerol‐based fermentation broth with high purity. The downstream process integrated chitosan flocculation, activated carbon decolorization, fixed bed cation exchange resin adsorption, and vacuum distillation. Breakthrough curves were measured considering the effect of sample concentration, flow rate, temperature, and resin stack height. Yoon–Nelson model was proposed to fit the fixed bed adsorption. The characteristic column parameters were calculated. Optimal condition for adsorption was 1,3‐PD, 30.0 g/L; flow rate, 1.00 mL/min; stacking height, 30.0 cm; and temperature, 298 K. Ethanol‐water (75%, 1 mL/min) was used as eluent to separate 1,3‐PD and glycerol with 95.3% 1,3‐PD elution rate. After vacuum distillation, the overall purity and yield of 1,3‐PD were 99.2% and 80.8% in the purification process, respectively. This is a simple and efficient downstream strategy for 1,3‐PD purification.

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