Method for Separating and Enriching Quercetin Using Metal-Organic Framework@Mesoporous Silicon Composite Material-Matrix Solid Phase Dispersion Technology
A metal-organic framework and composite material technology, applied in the field of separation and enrichment of quercetin, can solve the problems of low extraction rate, complicated operation process, and large consumption of organic solvents, and achieve simple separation process, increased adsorption capacity, and reduced experimental Effect of Time and Solvent Usage
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specific Embodiment approach 1
[0016] Specific embodiment 1: This embodiment is a method for separating and enriching quercetin by using a metal organic framework@ mesoporous silicon composite material-matrix solid phase dispersion technology, which is specifically completed according to the following steps:
[0017] 1. Preparation of metal organic framework@ mesoporous silicon composite material: ① Dissolve terephthalic acid in N,N dimethylformamide solution ultrasonically to obtain a solution containing terephthalic acid; The mass ratio of the N,N dimethylformamide solution to the volume ratio of 1g:(12~34)mL; ②, ultrasonically dissolve ferric chloride in the N,N dimethylformamide solution to obtain iron ion Solution; The mass ratio of the ferric chloride to the volume of the N,N dimethylformamide solution is 1g: (63~88) mL; ③, the solution containing terephthalic acid is added dropwise to the solution of iron ions , Then add MCM-41, ultrasonic treatment for 20min~35min, to obtain a yellow suspension; transf...
specific Embodiment approach 2
[0022] Specific embodiment two: the difference between this embodiment and the specific embodiment one is: the MCM-41 described in step one (3) is prepared according to the following steps:
[0023] Add CTAB and ammonia to deionized water, then stir at the oil bath temperature of 55~75℃ until CTAB is completely dissolved, then add TEOS dropwise, continue to stir and react for 5h~8h, then proceed to room temperature crystallization, filtration, washing and After drying, the solid product is obtained. The solid product is washed with hydrochloric acid ethanol solution until the washing liquid is neutral, and the washed product is vacuum dried to obtain white solid mesoporous silica, namely MCM-41; the quality of the CTAB is equal to The volume ratio of deionized water is (0.8~2.0)g:(90~120)mL; the volume ratio of the ammonia water and deionized water is (60~80):(90~120); the mass of the TEOS is The volume ratio of deionized water is (4.4-5.8) g: (90-120) mL; the mass fraction of hy...
specific Embodiment approach 3
[0025] Specific embodiment three: this embodiment is different from specific embodiment one or two in that the rotating speed of the centrifuge during centrifugal washing in step one (4) is 4000 r / min to 5500 r / min. Others are the same as the first or second embodiment.
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