Background technology
At present, on the market existing architectural shape have that timber is made, have plastics to make, and the former is unfavorable for forest conservation, and easily humidity, easy mould moth, do not have fireproof performance, the latter then is unfavorable for environmental protection, quality weight, is not easy to secondary operations.
Summary of the invention
Be to solve problems of the prior art, the invention provides that a kind of functional performance is good, environment-protecting asepsis and be convenient to the Green Environmental Protection Laminated Core Layer Foamed Profile Extrustion Die And Production Method of secondary operations.
For achieving the above object, the technical solution adopted in the present invention is: a kind of green environment-protecting co-squeezing core layer foaming special-shaped material, internal layer is that foaming layer, skin are the co-extrusion hard layer, and foaming layer is formulated by the component of following weight percentage: Corvic 63~67%, calcium carbonate 11~15%, haloflex 3~7%, auxiliary chemicals 12~19%; The co-extrusion hard layer is formulated by the component of following weight percentage: Corvic 42~46%, calcium carbonate 42~46%, haloflex 3.5~5%, auxiliary chemicals 7~9%.
Auxiliary chemicals in the described foaming layer component are made up of the component of following weight percentage: lead salt compound stabilizer 15~25%, dibutyl ester 5~15%, zinc oxide 0.5~5%, Tissuemat E 0.5~3%, Celogen Az 0.5~5%, PVC foaming control agent 45~65%, titanium dioxide 5~15%, stearic acid 0.5~3%; Auxiliary chemicals in the co-extrusion hard layer component are made up of the component of following weight percentage: titanium dioxide 40~42%, paraffin 1.6~1.8%, stearic acid 1.6~1.8%, lead salt compound stabilizer 20~24%, Celogen Az 31~36%.
Auxiliary chemicals in the described foaming layer component comprise that also percentage by weight is 0.1~0.4% fluorescent whitening agent; Auxiliary chemicals in the co-extrusion hard layer component comprise that also percentage by weight is 0.1~0.2% fluorescent whitening agent.
Production method of the present invention is: each component with foaming layer and co-extrusion hard layer ran up in mixer respectively 30~50 minutes by constant weight percentage earlier, again each component of mixed foaming layer is put in the barrel of double screw extruder, simultaneously mixed each component of co-extrusion hard layer is put in the barrel of single screw extrusion machine, then single screw extrusion machine is moved on to one side of double screw extruder, make the co-extrusion import of the discharging opening aligning extrusion die of single screw extrusion machine, open double screw extruder and single screw extrusion machine, each component is transmitted simultaneously by screw rod, in extrusion die, form blank, and extrude, through the stock mould plastotype, last inlet water tank cools off again.
Green environment-protecting co-squeezing core layer foaming special-shaped material of the present invention cannot not have agingly, environment-protecting asepsis, indeformable, hardness is high, will never fade, anticorrosive property strong, waterproof, fire-retardant, advantage such as can follow closely, can saw, can dig, precision and glossiness are up to more than 95%, and scientific structure, handsome in appearance, easy for installation, also recyclable in addition utilization greatly reduces cost of production.
The specific embodiment
The invention will be further described below by specific embodiment, but the present invention is not limited by following examples.
Table 1: the corresponding relation of each embodiment weight percentages of components of foaming layer
| Corvic % | Calcium carbonate % | Haloflex % | Auxiliary chemicals % |
Embodiment 1 | 63 | 12 | 6 | 19 |
Embodiment 2 | 64 | 11 | 7 | 18 |
Embodiment 3 | 65 | 13 | 5 | 17 |
Embodiment 4 | 66 | 15 | 7 | 12 |
Embodiment 5 | 67 | 14 | 3 | 16 |
Table 2: the corresponding relation of each embodiment weight percentages of components of co-extrusion hard layer
| Corvic % | Calcium carbonate % | Haloflex % | Auxiliary chemicals % |
Embodiment 1 | 42 | 46 | 5 | 7 |
Embodiment 2 | 43 | 44.5 | 3.5 | 9 |
Embodiment 3 | 44 | 44 | 4 | 8 |
Embodiment 4 | 45 | 42 | 4.5 | 8.5 |
Embodiment 5 | 46 | 43 | 3.5 | 7.5 |
Table 3: the percentage by weight corresponding relation of each embodiment component of auxiliary chemicals in the foaming layer
| Lead salt compound stabilizer % | Dibutyl ester % | Zinc oxide % | Tissuemat E % | Celogen Az % | PVC foaming control agent % | Titanium dioxide % | Stearic acid % | Fluorescent whitening agent % |
Embodiment 1 | 25 | 15 | 5 | 2 | 1 | 45 | 5 | 2 | 0 |
Embodiment 2 | 22 | 5 | 0.5 | 2.6 | 1.5 | 50 | 15 | 3 | 0.4 |
Embodiment 3 | 20 | 10 | 2 | 0.5 | 5 | 55 | 6.9 | 0.5 | 0.1 |
Embodiment 4 | 18 | 7 | 2 | 1 | 0.5 | 60 | 10 | 1.3 | 0.2 |
Embodiment 5 | 15 | 6 | 0.8 | 3 | 3 | 65 | 6 | 0.9 | 0.3 |
Table 4: the percentage by weight corresponding relation of each embodiment component of auxiliary chemicals in the co-extrusion hard layer
| Titanium dioxide % | Paraffin % | Stearic acid % | Lead salt compound stabilizer % | Celogen Az % | Fluorescent whitening agent % |
Embodiment 1 | 40 | 1.8 | 1.7 | 20.5 | 36 | 0 |
Embodiment 2 | 40.2 | 1.8 | 1.8 | 24 | 32 | 0.2 |
Embodiment 3 | 41 | 1.7 | 1.8 | 22 | 33.3 | 0.2 |
Embodiment 4 | 41.5 | 1.7 | 1.7 | 20 | 35 | 0.1 |
Embodiment 5 | 42 | 1.6 | 1.6 | 23.7 | 31 | 0.1 |
Table 5: the timetable that the component of each embodiment runs up in mixer
| Embodiment 1 | Embodiment 2 | Embodiment 3 | Embodiment 4 | Embodiment 5 |
Time (minute) | 30 | 35 | 40 | 45 | 50 |
More than the production method of each embodiment identical, the concrete operations step is as follows:
Each component with foaming layer and co-extrusion hard layer ran up in mixer respectively 30~50 minutes by constant weight percentage earlier, again each component of mixed foaming layer is put in the barrel of double screw extruder, simultaneously mixed each component of co-extrusion hard layer is put in the barrel of single screw extrusion machine, then single screw extrusion machine is moved on to one side of double screw extruder, make the co-extrusion import of the discharging opening aligning extrusion die of single screw extrusion machine, open double screw extruder and single screw extrusion machine, each component is transmitted simultaneously by screw rod, in extrusion die, form blank, and extrude, through the stock mould plastotype, last inlet water tank cools off again.
Product of the present invention is fit to be used in the building of restaurant, dwelling house, office, each public place.