Method for recycling continuous alcoholysis of waste polyester material
The present invention is in related to a method for recycling a waste polyester material, more particularly to a method for recycling the waste polyester material through a chemical way to produce DMT. It belongs to the technical field of recycling and utilization of waste polyester materials. The present invention adopts the technology of continuous feeding and continuous alcoholysis, so that the material undergoes homogeneous alcoholysis in a melting state, and the required alcoholysis time is short. Two or more alcoholysis tanks are used in series for continuous alcoholysis. The product quality is stable. At the same time, due to the optimization of the amount of EG in the alcoholysis process, distillation and concentration are not required after the alcoholysis step is completed. The alcoholysis product is directly entered into the transesterification tank for the transesterification reaction, and pure DMT products can then be generated.
1. A method for recycling continuous alcoholysis of a waste polyester material comprising:
(a) material pretreatment: dewatering and deoxidizing the waste polyester material to make a reduction to below 300 ppm of the water content to obtain a raw waste polyester material;
(b) alcoholysis: after the step (a), the raw waste polyester material, an alcoholysis agent and an alcoholysis catalyst in a melting state being continuously and simultaneously fed into a first alcoholysis tank for a first alcoholysis in order to obtain a first melt, wherein the first melt is continuously fed to a second alcoholysis tank for a second alcoholysis, so as to obtain an alcoholysis product; and
(c) transesterification: the alcoholysis product, a transesterification agent, a transesterification catalyst in melting state being fed into a transesterification tank for a transesterification reaction in order to obtain crude dimethyl terephthalate(DMT) and crystallization, separation and purification of the crude DMT, wherein the first alcoholysis tank and the second alcoholysis tank are connected to each other in series.
2. The method for recycling the continuous alcoholysis of the waste polyester material according to claim 1 , wherein a step (al) between the step (a) and the step (b) is that of: proceeding a filter process to the raw waste polyester material.
3. The method for recycling the continuous alcoholysis of the waste polyester material according to claim 1 , wherein the alcoholysis agent is ethylene glycol, the weight ratio of the raw waste polyester material to the alcoholysis agent being 1.0:1.0˜2.0, the raw waste polyester material and the alcoholysis agent being continuously and simultaneously fed into the first alcoholysis tank.
4. The method for recycling the continuous alcoholysis of the waste polyester material according to claim 1 , wherein the alcoholysis catalyst is selected from the group consisting of: potassium carbonate and zinc acetate, an adding amount of the alcoholysis catalyst being 0.3 wt %˜3.0 wt % according to a weight of the waste polyester material as a standard.
5. The method for recycling the continuous alcoholysis of the waste polyester material according to claim 3 , wherein the alcoholysis catalyst is dissolved in the alcoholysis agent in order to obtain alcoholysis catalyst liquid, an adding amount of the alcoholysis catalyst being 10 wt %˜70 wt % according to a weight of the alcoholysis agent as a standard.
6. The method for recycling the continuous alcoholysis of the waste polyester material according to claim 5 , wherein reaction conditions of the first alcoholysis tank and the second alcoholysis tank are that of: an alcoholysis temperature range of 180° C.˜200° C. and an alcoholysis time range of 40 min˜90 min.
7. The method for recycling the continuous alcoholysis of the waste polyester material according to claim 1 , wherein the transesterification agent is methanol, a weight ratio of the raw waste polyester material to the transesterification agent is 1.0:1.0˜3.0.
8. The method for recycling the continuous alcoholysis of the waste polyester material according to claim 1 , wherein the transesterification catalyst is selected from the group consisting of: sodium hydroxide and potassium carbonate, an adding amount of the transesterification catalyst being 0.2 wt %˜5.0 wt % according to a weight of the waste polyester material as a standard.
9. The method for recycling the continuous alcoholysis of the waste polyester material according to claim 8 , wherein the adding amount of the transesterification catalyst is 0.3 wt %˜2.0 wt % according to the weight of the waste polyester material as a standard.
10. The method for recycling the continuous alcoholysis of the waste polyester material according to claim 7 , wherein reaction conditions of the transesterification are that of: a reaction temperature range of 60° C.˜80° C. and a reaction time range of 30 min˜90 min.
11. The method for recycling the continuous alcoholysis of the waste polyester material according to claim 4 , wherein the alcoholysis catalyst is dissolved in the alcoholysis agent in order to obtain alcoholysis catalyst liquid, an adding amount of the alcoholysis catalyst being 10 wt %˜70 wt % according to a weight of the alcoholysis agent as a standard.
12. The method for recycling the continuous alcoholysis of the waste polyester material according to claim 11 , wherein reaction conditions of the first alcoholysis tank and the second alcoholysis tank are that of: an alcoholysis temperature range of 180° C.˜200° C. and an alcoholysis time range of 40 min˜90 min.
13. The method for recycling the continuous alcoholysis of the waste polyester material according to claim 8 , wherein reaction conditions of the transesterification are that of: a reaction temperature range of 60° C.˜80° C. and a reaction time range of 30 min˜90 min.
14. The method for recycling the continuous alcoholysis of the waste polyester material according to claim 1 , wherein the raw waste polyester material is uniform waste polyester particles, and the waste polyester particles are fed into a screw extruder from a high-level storehouse through a rotary feeder for melting to form a molten material, and the waste polyester particles are filtered by a first filter program, and the conveying amount of the molten material is adjusted by the rotational speed of the screw extruder, and the rotary speed is controlled by the liquid level of the first alcoholysis tank.
15. The method for recycling the continuous alcoholysis of the waste polyester material according to claim 14 , wherein the material in the first alcoholysis tank is filtered by a second filter program and then is continuously fed into the second alcoholysis tank, and the rotary speed of the delivery pump is controlled by the liquid level of the second alcoholysis tank.
16. The method for recycling the continuous alcoholysis of the waste polyester material according to claim 15 , wherein the filter accuracy of the second filter program is more precise than the filter accuracy of the first filter program.