Method for separating and extracting 1,3-propylene glycol from fermentation liquor
A fermented liquid and propylene glycol technology, applied in the field of chemical engineering, can solve the problems of difficult desalination, low yield, high cost, etc., and achieve the effect of high separation yield, high purity, and short process
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Embodiment 1
[0036] The composition of the fermented liquid after removal of bacteria: 1,3-propanediol 70g / L, 2,3-butanediol 17.5g / L, glycerin 2g / L, soluble protein 0.5g / L, salt concentration 1.7%, pH 6.8 .
[0037] (1) 1000L / h of fermentation liquid, 250L / h left after concentrated by three-effect evaporation, concentrated 4 times.
[0038] (2) Add 170kg / h of glycerol to the fermented liquid concentrated in step (1).
[0039] (3) The material of step (2) enters rectifying tower 1 and carries out rectification under vacuum, and pressure 5kPa, reflux ratio 0.5 obtain cut 253kg / h from tower top, tower bottom cut 189.5kg / h.
[0040] (4) the overhead fraction of step (3) enters rectifying tower 2 and carries out rectification under vacuum, pressure 10kPa, reflux ratio 15, extract 2 from side line, 3-butanediol product 17.0kg / h, purity 99.8%; Tower 69.5 kg / h of 1,3-propanediol product was produced from the still, and after decolorization, 67.0 kg / h of 1,3-propanediol product was obtained with ...
Embodiment 2
[0043] The composition of the fermented liquid after removal of bacteria: 1,3-propanediol 58.5g / L, 2,3-butanediol 14.6g / L, glycerin 5g / L, soluble protein 0.7g / L, salt concentration 1.2%, pH6. 8.
[0044] (1) The fermented liquid is 2000L / h, after three-effect evaporation and concentration, 361L / h remains, which is 5.54 times concentrated.
[0045] (2) Add the glycerol of 192kg / h in the concentrated fermented liquid of step (1).
[0046] (3) The material of step (2) enters rectifying tower 1 and carries out rectification under vacuum, pressure 6kPa, reflux ratio 1.0, obtain cut 357.6kg / h from tower top, tower bottom cut 227.4kg / h.
[0047] (4) the overhead fraction of step (3) enters rectifying tower 2 and carries out rectification under vacuum, pressure 5kPa, reflux ratio 20, extract 2,3-butanediol product 28.1kg / h from side line, purity 99.92%; Tower 115kg / h of 1,3-propanediol product was produced from the still, and after decolorization, 112.5kg / h of 1,3-propanediol produc...
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