Method for preparing polyol from waste grease and application thereof
A technology of waste oil and polyol, which is applied in the preparation of carboxylic acid esters, chemical instruments and methods, and the preparation of organic compounds. It can solve the problems of waste catering oil pollution, difficulty in sanitation work, blockage of sewage pipe network, etc., and achieves a wide range of uses. , avoid cumbersome post-processing, and reduce the cost of raw materials
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Embodiment 1
[0022]A method for preparing polyols from waste oils and fats of the present embodiment comprises the following steps:
[0023] Step 1 Preparation of solid acid with both sulfonic and carboxylic acid groups with large hydrophobic surface
[0024] Dissolve acrylic acid, styrenesulfonic acid and divinylbenzene in ethyl acetate, the solution solubility is 35%, and the mass ratio of unsaturated carboxylic acid, unsaturated sulfonic acid and divinylbenzene is 0.1:0.3: 1. Under the initiation of azobisisobutyronitrile initiator, carry out mixed solvothermal copolymerization for 5 hours. The amount of initiator is 0.3% of the total mass of reactants. The temperature of solvothermal polymerization is 100°C. Cool, filter, wash and dry. A solid acid catalyst with large hydrophobic surface and sulfonic acid groups and carboxylic acid groups is obtained.
[0025] Step 2 Pretreatment process of waste oil
[0026] After heating the swill oil to 60°C, filter it with a sand core to remove i...
Embodiment 2
[0035] A method for preparing polyols from waste oils and fats of the present embodiment comprises the following steps:
[0036] Step 1 Preparation of solid acid with both sulfonic and carboxylic acid groups with large hydrophobic surface
[0037] Dissolve maleic acid, vinylsulfonic acid and divinylbenzene in n-butanol, the solution solubility is 40%, and the mass ratio of unsaturated carboxylic acid, unsaturated sulfonic acid and divinylbenzene is 0.12:0.2 : 1, under the initiation of azobisisobutyronitrile initiator, carry out mixed solvothermal copolymerization for 8 hours, the amount of initiator is 0.5% of the total mass of reactants, the temperature of solvothermal polymerization is 120 ℃, cooling, filtering, washing and drying A solid acid catalyst with large hydrophobic surface and sulfonic acid groups and carboxylic acid groups is obtained.
[0038] Step 2 Pretreatment process of waste oil
[0039] After heating the waste frying oil to 60°C, filter it with a san...
Embodiment 3
[0048] A method for preparing polyols from waste oils and fats of the present embodiment comprises the following steps:
[0049] Step 1 Preparation of solid acid with both sulfonic and carboxylic acid groups with large hydrophobic surface
[0050] Dissolve crotonic acid, propylene sulfonic acid and divinylbenzene in isopropanol, the solution solubility is 40%, and the mass ratio of unsaturated carboxylic acid, unsaturated sulfonic acid and divinylbenzene is 0.13:0.25 : 1, under the initiation of azobisisobutyronitrile initiator, carry out mixed solvothermal copolymerization for 5 h, the amount of initiator is 0.6% of the total mass of reactants, the temperature of solvothermal polymerization is 120 ℃, cooling, filtering, washing and drying That is, a solid acid catalyst with large hydrophobic surface and sulfonic acid groups and carboxylic acid groups is obtained.
[0051] Step 2 Pretreatment process of waste oil
[0052] After heating the waste oil to 60°C, filter it wi...
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