Metal-enzyme preparation co-catalysis method for improving the leaching of solanesol in waste tobacco
A technology of solanesol and enzyme preparation, which is applied in the field of metal-enzyme preparation co-catalysis to improve the leaching of solanesol in waste tobacco, can solve the problem of increasing the difficulty of impurity removal, reducing the extraction rate of solanesol, and reducing production output and other issues to achieve the effect of shortening the service life of production equipment, reducing hidden dangers of production safety, and avoiding corrosion
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Embodiment 1
[0022] A kind of metal-enzyme co-catalysis method that improves the leaching of solanesol in waste tobacco The concrete steps are as follows:
[0023] (1) Raw material pretreatment
[0024] Wash 40g of discarded tobacco leaves, dry them, place them in an oven, bake them in an oven at 100°C for 30 minutes, take them out, crush them with a pulverizer, and then sieve them through a 60-mesh molecular sieve to obtain tobacco leaves with a particle size of less than 60 mesh. Pack in separate bags and set aside.
[0025] (2) Metal-enzyme co-catalyzed reaction
[0026]After the first (1) step is completed, the ratio of raw material quality (g) after the first step (1): catalyst quality (g): water volume (ml) ratio is 1: 0.035: 10, at ( 1) Add catalyst and water to the pretreated raw material, stir evenly, then use sulfuric acid or sodium hydroxide dilute solution to adjust the pH value of the system to 7, and then place the mixed solution after adjusting the pH value in a shaker , ...
Embodiment 2
[0032] A method for improving the metal-enzyme preparation co-catalysis method of solanesol leaching in waste tobacco, with embodiment 1, wherein:
[0033] In the step (1), the selected tobacco mesh is 20 mesh, the oven temperature is 85°C, and the drying time is 90 minutes.
[0034] In step (2), the ratio of mass (g) of tobacco solid waste: mass (g) of catalyst: volume (ml) of water is 1:0.0125:5. Hydrochloric acid solution was used to adjust the pH of the system to 4, and the temperature of the enzymatic hydrolysis water bath was 25°C. Enzymatically activate the tobacco base material for 8h. The metal-enzyme dosage ratio is metal catalyst (g): enzyme preparation (g) = 1:1.6; the enzyme activity ratio of the enzyme preparation is xylanase: cellulase: laccase = 2:47:51 complex enzyme.
[0035] In step (3), the mass of the pretreated tobacco solid waste: the volume ratio of the composite extractant solution is 1:8, and the volume ratio of the composite extractant ethanol:met...
Embodiment 3
[0038] A method for improving the metal-enzyme preparation co-catalysis method of solanesol leaching in waste tobacco, with embodiment 1, wherein:
[0039] In the step (1), the selected tobacco mesh is 120 mesh, the oven temperature is 110°C, and the drying time is 30 minutes.
[0040] In step (2), the ratio of mass (g) of tobacco solid waste: mass (g) of catalyst: volume (ml) of water is 1:0.075:15. A hydrochloric acid solution was used to adjust the pH of the system to 6, and the temperature of the water bath was 45°C. Enzymatically activate the tobacco base material for 4h. The metal-enzyme dosage ratio is metal catalyst (g): enzyme preparation (g) = 1:10; the enzyme activity ratio of the enzyme preparation is xylanase: cellulase: laccase = 2:34:64 compound enzyme.
[0041] In step (3), the mass of the pretreated tobacco solid waste: the volume ratio of the composite extractant solution is 1:12, and the volume ratio of the composite extractant ethanol:methanol is 1:9. T...
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