Method for purifying, reclaiming and condensing sugar in lignocellulose prehydrolysis liquid
A technology of lignocellulose and pre-hydrolysate, which is applied in the production of sugar, sugar production, glucose production, etc., to achieve the effects of increasing concentration, easy industrialized continuous production, and simple operation
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Embodiment 1
[0018] Embodiment 1: a kind of method of purifying, reclaiming and concentrating sugar in lignocellulose prehydrolyzate comprises the steps:
[0019] (1) The lignocellulose prehydrolyzate obtained through dilute acid pretreatment (xylose 80g / L, glucose 20g / L, arabinose 10g / L, mannose 1g / L, galactose 1g / L, formic acid 5g / L , acetic acid 20g / L, levulinic acid 4g / L, furfural 40g / L, 5-hydroxymethylfurfural 5g / L, pH3.0) enter the microfiltration module through the feed pump to remove suspended impurities. The internal pressure of the microfiltration module is 0.1-0.2MPa, the temperature is 25°C, and the pore size is about 0.45 microns.
[0020] (2) The permeated liquid obtained in step (1) enters the feed liquid tank, and then pressurized by the feed pump to 26.5L.m -2 .h -1 The membrane flux passes through the flat polyamide nanofiltration membrane module with a molecular weight cut-off of 90Da. At the same time, deionized water is continuously added to the feed tank, and the wa...
Embodiment 2
[0021] Embodiment 2: a kind of method of purifying, reclaiming and concentrating the sugar in the lignocellulose prehydrolyzate comprises the steps:
[0022] (1) The lignocellulose prehydrolyzate obtained after steam explosion pretreatment (xylose 10g / L, glucose 50g / L, arabinose 1g / L, mannose 6g / L, galactose 3g / L, formic acid 1g / L L, acetic acid 10g / L, levulinic acid 8g / L, furfural 1g / L, 5-hydroxymethylfurfural 20g / L, pH3.0) enter the microfiltration module through the feed pump to remove suspended impurities. The internal pressure of the microfiltration module is 0.1-0.16MPa, the temperature is 25°C, and the pore size is about 0.45 microns.
[0023] (2) The permeated liquid obtained in step (1) enters the feed liquid tank, and then pressurized by the feed pump to 39.8L.m -2 .h -1 The membrane flux passes through the flat polyamide nanofiltration membrane module with a molecular weight cut-off of 150Da. At the same time, deionized water is continuously added to the feed tank...
Embodiment 3
[0024]Embodiment 3: a kind of method of purifying, reclaiming and concentrating sugar in lignocellulose prehydrolyzate comprises the steps:
[0025] (1) The lignocellulose prehydrolyzed solution (xylose 30g / L, glucose 15g / L, arabinose 0.3g / L, mannose 0.6g / L, galactose 0.3g / L) obtained by pretreatment with organic solvents such as alcohol , formic acid 0.3g / L, acetic acid 5g / L, levulinic acid 0.6g / L, furfural 4g / L, 5-hydroxymethylfurfural 0.7g / L, pH3.0) enter the microfiltration module through the feed pump to remove Suspended impurities. The internal pressure of the microfiltration module is 0.1-0.16MPa, the temperature is 25°C, and the pore size is about 0.45 microns.
[0026] (2) The permeated liquid obtained in step (1) enters the feed liquid tank, and then pressurized by the feed pump to 39.8L.m -2 .h -1 The membrane flux passes through the flat polyamide nanofiltration membrane module with a molecular weight cut-off of 150Da, until the volume of the retentate is concen...
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