Summary of the invention
The object of the invention is to provide a kind of TTR resin base high-speed coating special 4.2 microns of BOPET.
Technical scheme of the present invention is as follows:
A kind of TTR resin base BOPET, thickness is 4.2 microns, is formed by base-material and organosilicon master batch processing;
Described base-material is PET, i.e. polyethylene terephthalate;
Described organosilicon masterbatch is dimethyldichlorosilane(DMCS) (CH
3)
2siCl
2with the mixture of polyethylene terephthalate, wherein the content of dimethyldichlorosilane(DMCS) is 6000 ~ 8000ppm.
Described TTR resin base BOPET, by percentage to the quality, binder content is 35% ~ 65%.
Described TTR resin base BOPET, by percentage to the quality, binder content is 45%.
It should be noted that, for better preparing the BOPET of 4.2 microns, the relevant production units prepared on the production line of the BOPET of special 4.2 microns of TTR resin base high-speed coating of the present invention produced by Austrian An Deli thatch company, and the production unit introduced is at MDO(longitudinal stretching), TDO(cross directional stretch) region can better meet needed for production compared to domestic equipment.
The transitional product that the present invention uses compared to prior art, thermostability, separability, cleanliness factor and the surperficial adaptability to coating solvent have larger improvement, can meet the properties requirement of the special BOPET of TTR resin base high-speed coating preferably.
Embodiment
Below in conjunction with embodiment, explanation is described further to the present invention.
embodiment 1
Prepare by the mass ratio of base-material and organosilicon masterbatch=3.5:6.5, described base-material is PET, i.e. polyethylene terephthalate; Described organosilicon masterbatch is dimethyldichlorosilane(DMCS) (CH
3)
2siCl
2with the mixture of polyethylene terephthalate, wherein the content of dimethyldichlorosilane(DMCS) is 7000ppm.
By the raw material for preparing after mixing, drying, enter forcing machine and carry out raw materials melt at 280 DEG C of temperature, first by raw material after melting after 5 μm of high-precision filters filter, extrude at T-shaped die head and cool at chilling roller, after after the preheating of MDO 55 DEG C ~ 76 DEG C, carry out 3.65 times and vertical draw draw horizontal with 4.1 of TDO times, crystallisation by cooling process is carried out at the horizontal latter end that draws of TDO, and then through the operation such as trimming, rolling harvest work in-process, after cutting, packing, become the special 4.2 microns of BOPET finished products of TTR mixed base high-speed coating.
Cut BOPET finished product prepared by the present embodiment, the excellent rate of classification of product of finished product can reach 89%, and coating A level product rate can reach 72%.
As shown in the table to the main materialization index determining of the special 4.2 microns of BOPET finished products of TTR resin base high-speed coating prepared by the present embodiment:
embodiment 2
Preparation method is with embodiment 1, and only adjustment base-material and organosilicon masterbatch are prepared by the mass ratio of 4:6, and described base-material is PET, i.e. polyethylene terephthalate; Described organosilicon masterbatch is dimethyldichlorosilane(DMCS) (CH
3)
2siCl
2with the mixture of polyethylene terephthalate, wherein the content of dimethyldichlorosilane(DMCS) is 7000ppm.
Cut BOPET finished product prepared by the present embodiment, the excellent rate of classification of product of finished product can reach 91%, and coating A level product rate can reach 83%.
As shown in the table to the main materialization index determining of the special 4.2 microns of BOPET finished products of TTR resin base high-speed coating prepared by the present embodiment:
embodiment 3
Preparation method is with embodiment 1, and only adjustment base-material and organosilicon masterbatch are prepared by the mass ratio of 4.5:5.5, and described base-material is PET, i.e. polyethylene terephthalate; Described organosilicon masterbatch is dimethyldichlorosilane(DMCS) (CH
3)
2siCl
2with the mixture of polyethylene terephthalate, wherein the content of dimethyldichlorosilane(DMCS) is 7000ppm.
Cut BOPET finished product prepared by the present embodiment, the excellent rate of classification of product of finished product can reach 90%, and coating A level product rate can reach 87%.
As shown in the table to the main materialization index determining of the special 4.2 microns of BOPET finished products of TTR resin base high-speed coating prepared by the present embodiment:
embodiment 4
Preparation method is with embodiment 1, and only adjustment base-material and organosilicon masterbatch are prepared by the mass ratio of 5:5, and described base-material is PET, i.e. polyethylene terephthalate; Described organosilicon masterbatch is dimethyldichlorosilane(DMCS) (CH
3)
2siCl
2with the mixture of polyethylene terephthalate, wherein the content of dimethyldichlorosilane(DMCS) is 7000ppm.
Cut BOPET finished product prepared by the present embodiment, the excellent rate of classification of product of finished product can reach 84%, and coating A level product rate can reach 83%.
As shown in the table to the main materialization index determining of the special 4.2 microns of BOPET finished products of TTR resin base high-speed coating prepared by the present embodiment:
Above-described embodiment is preferred embodiment of the present invention, from the TTR resin base high-speed coating BOPET product performance prepared by above-described embodiment, BOPET product performance prepared by the mass ratio of embodiment 3 i.e. base-material and organosilicon masterbatch=4.5:5.5 are best, therefore embodiment 3 most preferred embodiment the most of the present invention.