Method for reducing anisidine value of grease by adopting macroporous adsorption resin
A technology of anisidine value and pore adsorption, applied in the direction of fat oil/fat refining, fat production, etc., can solve the problem of reducing oil anisidine, etc., and achieve the effect of simple equipment, high efficiency, and low production and operation costs
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Embodiment 1
[0036]Prepare the anisidine value of 23.39 (GBT24304-2009 test method) linseed oil with n-hexane dilution concentration of 30%, to obtain the upper column liquid, the macroporous adsorption resin after the upper column activation treatment, keep the temperature of the resin column at 50 ° C, the flow rate When the test result is greater than 15, stop collecting the effluent, and rotate the collected liquid at 110°C to recover n-hexane to obtain the treated oil.
[0037] According to the GBT24304-2009 test method, the anisidine value of the treated oil was detected, the resin was effectively adsorbed for 48 hours, the anisidine value of the mixed solution was 10.20, and the anisidine value was reduced by 56%.
Embodiment 2
[0039] Prepare the anisidine value to be 25.42 (GBT24304-2009 test method) and the hemp oil is diluted with n-hexane and the concentration is 50%, to obtain the upper column liquid, and the macroporous adsorption resin after the upper column activation treatment, keep the temperature of the resin column at 50°C, and the flow rate When the test result is greater than 15, stop collecting the effluent, and rotate the collected liquid at 110°C to recover n-hexane to obtain the treated oil.
[0040] According to the GBT24304-2009 test method, the anisidine value of the treated oil was detected, the resin was effectively adsorbed for 36 hours, the anisidine value of the mixed solution was 11.28, and the anisidine value was reduced by 55.6%.
Embodiment 3
[0042] The used resin in Example 1 was regenerated. Regeneration method: first pass 2BV of n-hexane to replace the residual oil in the resin; then pass 2BV of ethanol and pass 1BV of desalted water. Soak the macroporous adsorption resin in desalinated water for more than 24 hours, put 7% v / v hydrochloric acid with 2BV volume of the resin on the column at a flow rate of 1BV / h, then wash with desalinated water until the pH of the effluent is > 3, and configure 5% hydrogen Put sodium oxide on the column with a flow rate of 1 BV / h and a total volume of 2BV, then wash with desalted water until the conductivity of the effluent water is less than 30us / cm, and finally use 95% ethanol on the column with a flow rate of 1BV / h and a total volume of 2BV, and then use n-hexane column, flow rate 1BV / h, total volume 2BV, standby
[0043] Configure 50% linseed oil with n-hexane (the anisidine value of the raw material is 27.53) to obtain the upper column liquid, the flow rate is 0.5BV / h, coll...
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