Decolorization method for raffinose raffinate
A technology of raffinose and extract, which is applied in the production of sugar, oligosaccharides, sugars, etc., can solve problems such as simplification, and achieve the effects of simple operation, short production cycle and convenient operation
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Embodiment 1
[0042] Example 1: Preparation of Raffinose Extraction
[0043] Degreased cottonseed meal (wherein the mass percentage of raffinose is 3.9%) is sieved through a 1.8mm sieve, weighs 435 grams and puts it into a percolation column (Φ3.5cm×70cm), and its cumulative volume after filling is uniform About 560 milliliters, then add 350 milliliters of 75% ethanol aqueous solution to the percolation column, soak at 55°C for 30 minutes to fully swell the defatted cottonseed meal, open the outlet valve of the percolation column, and simultaneously Add extraction solvent continuously, control flow rate to be 168 milliliters / hour, until the volume that collects percolation extraction liquid is 1900 milliliters. The percolating liquid is analyzed, and solid content (solid content refers to the percentage that the quality when solution is dried to constant weight accounts for the percentage of solution mass before drying, the same below) is 4.2%; The mass percentage of raffinose is 38.2% bas...
Embodiment 2
[0045] Embodiment 2: the decolorization of raffinose extract
[0046] The degreased cottonseed meal ethanol extract (solid content 5%) prepared by the process of Example 1 was concentrated under reduced pressure to 1 / 10 of the original volume to obtain a concentrated solution, and deionized water with 4 times the volume of the concentrated solution was added to prepare an aqueous solution (solid content 10%), adding hydrochloric acid with a mass percent concentration of 5% to adjust the pH value of the solution to 5.
[0047] Put 230 grams of granular activated carbon into a fixed bed adsorption column with a size of Φ5.6cm×40cm, and the column bed volume BV is 980mL. Continuously feed the above-mentioned weakly acidic aqueous solution into the fixed-bed adsorption column at a flow rate of 1.0BV / h and collect the effluent at the outlet until about 10BV of decolorized liquid is collected. In the sample loading process, the color of the decolorized liquid flowing out is obvious...
Embodiment 3
[0049] Embodiment 3: the decolorization of raffinose extract
[0050] The degreased cottonseed meal ethanol extract (solid content 5%) prepared by the process of Example 1 was concentrated under reduced pressure to 1 / 10 of the original volume to obtain a concentrated solution, and deionized water with 4 times the volume of the concentrated solution was added to prepare an aqueous solution (solid content 10%), adding hydrochloric acid with a mass percent concentration of 5% to adjust the pH value of the solution to 4.
[0051] About 700 grams of macroporous adsorption resin HZ816 was loaded into an adsorption column with a size of Φ5.6cm×40cm, and the column bed volume BV was 980mL. Continuously feed the raffinose aqueous solution into the fixed-bed adsorption column at a flow rate of 1.0 BV / h and collect the effluent at the outlet until about 6 BV of decolorized liquid is collected. In the sample loading process, the color of the decolorized solution flowing out is obviously ...
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