NOVELTY - Forming glyceride and product rich in glycerol involves taking 5-10 parts by mass of pre-treated weak polarity macroporous absorbent resin, 10-20 parts by mass Tris-HCl buffer solution and free lipase LipaseT1, stirring, filtering and drying to form hydrophobic resin immobilized lipase LipaseT1; taking 10 parts of plant oil raw material, adding 4 parts of glycerol, passing through packed column of immobilized lipase LipaseT1; separating by centrifugal separation to form upper oil phase of grease-rich glycerides, and separating to form monoglyceride and product rich in glycerol.    USE - For preparation of glyceride and product rich in glycerol (claimed), where glyceride is used as food additive and as an important agent in food, pharmacy, cosmetic industry and so on.    ADVANTAGE - The method does not generate by-product, has high partial glyceride product content, allows immobilized enzyme to be used repeatedly, and has good application prospect. The method exhibits high efficiency, is economical and environment-friendly. The lipase LipaseT1 used exhibits high thermal stability, has low moisture content. The method avoids the occurrence of hydrolysis side reaction, and simplifies recovery and subsequent separation process. The method exhibits high reaction efficiency, does not use free fatty acid, and does not generate by-product.    DETAILED DESCRIPTION - Preparation of glyceride and product rich in glycerol involves taking 5-10 parts by mass of pre-treated weak polarity macroporous absorbent resin, 10-20 parts by mass Tris-HCl buffer solution and free lipase LipaseT1, stirring and absorbing at a temperature of 25-35 degrees C for 2 hours, then filtering and drying till the water content is not more than 1% to obtain hydrophobic resin immobilized lipase LipaseT1; taking 10 parts plant oil raw material, adding 4 parts of glycerol, adding to tank, uniformly stirring and continuously passing through a packed column of immobilized lipase LipaseT1 and recycling the raw material in whole reaction system at 1-500 MPa, where vacuum in system is lower than 75, reacting at 5 degrees C for 2 hours to obtain product mixture; separating the product mixture by centrifugal separation to obtain upper oil phase that is grease-rich glycerides, and then separating to obtain monoglyceride and product rich in glycerol.