Method for catalytic production of trimethylolpropane oleate by using solid superacid and application of method
A technology for trimethylolpropane oleate and methylolpropane oleate, which is applied in the field of solid super acid catalyzed production of trimethylolpropane oleate, can solve the problems of easy foaming of products, difficulty in separation and purification, etc. , to achieve the effect of improving production efficiency and solving the problem of easy foaming and difficult purification
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Embodiment 1
[0015] Get trimethylolpropane 100kg, oleic acid 630kg mixes, powdery solid superacid 0.73kg, solid superacid is SO 4 2- / ZrO 2 -Al 2 o 3 , under 500Pa vacuum degree, react at 180°C for 6 hours, filter the obtained product with a 600-mesh filter cloth, filter out the solid superacid, and distill the filtered reaction product under reduced pressure at 200°C and 200Pa vacuum degree for 1 hour to remove untreated The reactant was reacted to obtain trimethylolpropane oleate, and the esterification rate was 93.5%.
Embodiment 2
[0017] Get trimethylolpropane 100kg, oleic acid 630kg mixes, powdery solid superacid 0.73kg, solid superacid is SO 4 2- / ZrO 2 , under 500Pa vacuum degree, react at 180°C for 7 hours, filter the obtained product with a 600-mesh filter cloth, filter out the solid superacid, and distill the filtered reaction product under reduced pressure at 200°C and 200Pa vacuum degree for 1 hour to remove untreated The reactant was reacted to obtain trimethylolpropane oleate, and the esterification rate was 91.3%.
Embodiment 3
[0019] Get trimethylolpropane 100kg, oleic acid 420kg mixes, powdery solid superacid 20.8kg, solid superacid is SO 4 2- / TiO 2 -Al 2 o 3 -SiO 2 , under 400Pa vacuum degree, react at 190°C for 5 hours, filter the obtained product with a 500-mesh filter screen, filter out the solid superacid, and distill the filtered reaction product under reduced pressure at 220°C and 600Pa vacuum degree for 1.5 hours to remove residual The reactants were reacted to obtain trimethylolpropane oleate, and the esterification rate was 96.5%.
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