Summary of the invention
The objective of the invention is to overcome the deficiencies in the prior art, a kind of paper plastic glue-free composite bidirectional stretching polypropylene film and preparation method thereof is provided, it is characterized in that: it comprises the top layer that setting in turn and coextru-lamination form, sandwich layer and can be directly and paper wood, preprint paper wood or contain the compound functional layer of film of this layer, it is characterized in that: described functional layer is an ethylene-butene copolymer, ethylene-octene copolymer, ethene-butylene-octene copolymer, the modified by maleic acid anhydride graft thing of ethylene-butene copolymer, the modified by maleic acid anhydride graft thing of ethylene-octene copolymer, the modified by maleic acid anhydride graft thing of ethene-butylene-octene copolymer or above copolymer, modifier, any composition of blend respectively with the blend again of hydrogenated petroleum resin, and its feature is as follows: (i) content of butylene is 10~30% in the ethylene-butene copolymer, and the content of octene is 5~20% in the ethylene-octene copolymer; The content of butylene is 1~30% in ethene-butylene-octene copolymer, the content of octene is 1~20%; The percent grafting of the modified by maleic acid anhydride graft thing of the modified by maleic acid anhydride graft thing of ethylene-butene copolymer, the modified by maleic acid anhydride graft thing of ethylene-octene copolymer, ethene-butylene-octene copolymer is 0.5~10%; The weight ratio that (ii) described functional layer accounts for film is 10~50%.
Be provided with top layer last time between described top layer and the sandwich layer, be provided with next top layer between sandwich layer and the functional layer.
Described top layer is polypropylene, polyethylene or both blend that contains antiblocking agent.
Described sandwich layer contains 60~100% isotactic polypropylene or for by one or more mixtures formed among 60~100% isotactic polypropylene and hydrogenated petroleum resin, antistatic additive, the slipping agent, next top layer and last time the top layer contain 60~100% isotactic polypropylene or be by one or more mixtures formed among 60~100% isotactic polypropylene and hydrogenated petroleum resin, antistatic additive, the slipping agent.
In described next top layer, sandwich layer and the last time top layer one or more layers contains titanium dioxide.
Described next top layer, sandwich layer and last time the top layer all contain calcium carbonate and/or polybutylene terephthalate (PBT).
The weight ratio that described hydrogenated petroleum resin accounts for functional layer is 1~30%.
The preparation method of paper plastic glue-free composite bidirectional stretching polypropylene film of the present invention is:
To press the component design premix through main material, modified materials, the additive masterbatch of screening, stir, resin after metering, send into the melt that extruder is processed into plasticizing, homogenizing, melt filters by pipeline transmission, filter, be assigned to die head through runner, become sheet by curtain coating casting sheet Quench, sheet is drawn into film through two-way (earlier vertically more laterally or in length and breadth to synchronously).The thickness of film adopts automatic measuring thickness device control, and film is through sided corona treatment or flame treatment, and through the female film of traction harvest, parent roll cuts into finished film at last through Ageing Treatment with the film after handling.
Adopt paper plastic glue-free composite bidirectional stretching polypropylene film of said structure and preparation method thereof, its advantage is:
Bidirectional stretching polypropylene film of the present invention, it comprises base layer and functional skin layer, base layer and the functional skin layer that constitutes by the described material of the technical program wherein, after coextru-lamination and stretching, functional layer can be directly and paper wood, preprint paper wood or contain the film of this layer compound, realized the no gel that paper is compound, save the coating process of glue method, simplified combination process, and, compound tense can not produce toxic gas, environmental protection, safety, health.Simultaneously, with the bidirectional stretching polypropylene film that this structure, composition manufacturing form, it is simple in structure, and heat seal strength is big, with paper wood, preprint paper wood or contain the product that the film of this functional layer is composited, and the peel strength height, the manufacturing that is beneficial to product is promoted.
The specific embodiment
The invention will be further described below in conjunction with accompanying drawing.
According to illustrated in figures 1 and 2, paper plastic glue-free composite bidirectional stretching polypropylene film of the present invention, it comprises in turn the top layer 5 that is provided with, sandwich layer 3 and can be directly and paper wood, preprint paper wood or contain the compound functional layer 1 of film of this layer, when making this film, top layer 5, sandwich layer 3 and functional layer 1 are the coextru-lamination structure, constituted the most basic three layers structure of film of the present invention with these three layers, as shown in Figure 1.In addition, be to improve the performance of film, be provided with top layer 4 last time between top layer 5 and the sandwich layer 3, be provided with next top layer 2 between sandwich layer 3 and the functional layer 1.The film that forms with this five-layer structure has constituted another embodiment of the present invention, as shown in Figure 2.Top layer 5 is for containing polypropylene, polyethylene or both blends of antiblocking agent.According to different manufacturing requirements, next time top layer 2, sandwich layer 3 and last time the top layer 4 can be following three kinds of modes: first, sandwich layer 3 contains 60~100% isotactic polypropylene or for by one or more mixtures formed among 60~100% isotactic polypropylene and hydrogenated petroleum resin, antistatic additive, the slipping agent, next top layer 2 and last time top layer 4 contain 60~100% isotactic polypropylene or be by one or more mixtures formed among 60~100% isotactic polypropylene and hydrogenated petroleum resin, antistatic additive, the slipping agent; The second, one or more layers in next top layer 2, sandwich layer 3 and the last time top layer 4 contains titanium dioxide; The 3rd, one or more layers in next top layer 2, sandwich layer 3 and the last time top layer 4 contains calcium carbonate and/or polybutylene terephthalate (PBT).Functional layer 1 is an ethylene-butene copolymer, ethylene-octene copolymer, ethene-butylene-octene copolymer, the modified by maleic acid anhydride graft thing of ethylene-butene copolymer, the modified by maleic acid anhydride graft thing of ethylene-octene copolymer, the modified by maleic acid anhydride graft thing of ethene-butylene-octene copolymer or above copolymer, modifier, any composition of blend respectively with the blend again of hydrogenated petroleum resin, wherein, butene content in the ethylene-butene copolymer is 10~30%, octene content in the ethylene-octene copolymer is 5~20%, butene content is 1~30% in ethene-butylene-octene copolymer, octene content is 1~20%, the modified by maleic acid anhydride graft thing of ethylene-butene copolymer, the percent grafting of the modified by maleic acid anhydride graft thing of ethylene-octene copolymer and the modified by maleic acid anhydride graft thing of ethene-butylene-octene copolymer is 0.5~10%.
The weight ratio that hydrogenated petroleum resin in the functional layer (1) accounts for this layer is 1~30%.
As shown in Figure 3, method for manufacturing thin film of the present invention, its technological process is:
Among the figure: A is raw material (comprising main material, modified materials, additive masterbatch), and B is a melt, and C is a sheet, D is a film, and E is a finished product, and F is that extruder is extruded operation, G is that die head, curtain coating are cast the sheet chilling device to the melt forming operation, and H is the biaxial tension operation, and I is Ageing Treatment, branch cutting process.
To press the component design premix through the raw material A (comprising main material, modified materials, additive masterbatch) of screening, stir, resin after metering, send into the melt B that extruder processing F becomes plasticizing, homogenizing, melt filters by pipeline transmission, filter, be assigned to die head through runner, G becomes sheet C by curtain coating casting sheet, and sheet becomes film D through two-way (earlier vertically more laterally or in length and breadth to synchronously) stretching H.The thickness of film D adopts automatic measuring thickness device control, and to improve surface tension, through the female film of traction harvest, cut I at last and become finished film E through Ageing Treatment with the film after handling by parent roll through sided corona treatment or flame treatment for film.Wherein:
The extruder that described method is used, the temperature of die head are controlled at 220~270 ℃, curtain coating casting sheet temperature is at 15~40 ℃, surface treatment intensity is 35~45mN/m, in drawing process, can select two-step stretch or synchro-draw operation for use according to the condition of production equipment, in the two-step stretch operation, the longitudinal stretching cell temperature is controlled at 50~150 ℃, and the cross directional stretch cell temperature is controlled at 80~180 ℃, is respectively 4.5~6.5 and 7~10 to draw ratio in length and breadth.
Functional layer 1 accounts for the weight ratio of film 10~50%.
Among the embodiment 1 shown in Figure 1:
Functional layer 1 is the modified by maleic acid anhydride graft thing 9015 that 70% ethylene-butene copolymer 4090S adds 30% ethylene-butene copolymer;
Sandwich layer 3 is that 98% isotactic polypropylene FS3011 adds 2% antistatic additive ASPA2446;
Top layer 5 is delustring material DUL3636DP17.
The gross thickness of prepared product is 20 μ m, functional layer 1 thick 8 μ m, delustring bed thickness 3 μ m.
The preparation method is: will press the component design premix through the raw material A (comprising main material, modified materials, additive masterbatch) of screening, stir, resin after metering, send into the melt B that extruder is processed into plasticizing, homogenizing F, melt filters by pipeline transmission, filter, be assigned to die head through runner, G becomes sheet C by curtain coating casting sheet, and sheet becomes film D through two-way (earlier vertically more laterally or in length and breadth to synchronously) stretching H.The thickness of film D adopts automatic measuring thickness device control, and to improve surface tension, through the female film of traction harvest, cut I at last and become finished film E through Ageing Treatment with the film after handling by parent roll through sided corona treatment or flame treatment for film.Wherein, equipment is the flat embrane method bidirectional stretching polypropylene film of German BRUECKNER production line, 235~265 ℃ of extrusion temperatures; The longitudinal stretching temperature: preheating, stretching and setting temperature 50-150 ℃, 5 times of draw ratios; The cross directional stretch temperature: 80~180 ℃ of preheating, stretching and setting temperatures, draw ratio is 9 times; Sided corona treatment power is 25wmin./m
2, the properties of product of manufacturing are as follows:
(1) thickness: 20 μ m (2) density (extinction type): 0.83g/cm
3(3) hot strength (vertically/laterally): 90MPa/130MPa (4) heat seal strength: 8.0N/15mm
(5) peel strength (film-paper wood): 3.5N/15mm
(6) glossiness: 8.5Gu (7) percent thermal shrinkage (vertically/laterally): 2.5%/1.5%
(8) surface tension: 40mN/m
In the enforcement 2 shown in Figure 2:
Functional layer 1 is that the modified by maleic acid anhydride graft thing 9015 that 50% ethylene-butene copolymer 4090S adds 20% ethylene-butene copolymer adds 30% hydrogenated petroleum resin (masterbatch such as PA609);
Top layer 4 was 98% isotactic polypropylene FS3011 and added 2% antistatic additive ASPA2446 next time top layer 2, sandwich layer 3, last time;
Top layer 5 is the antiblocking agent ABVT180 that 98% isotactic polypropylene FS3011 adds 2000PPM.
The gross thickness of prepared product is 18 μ m, functional layer 1 thick 7 μ m.
The preparation method is identical with embodiment 1, and the specific performance of product is:
(1) thickness: 18 μ m (2) density (brightening type): 0.9g/cm
3
(3) hot strength (vertically/laterally): 110MPa/200MPa (4) heat seal strength: 6.0N/15mm
(5) peel strength (film-paper wood or preprint paper wood): 3.2N/15mm
(6) mist degree: 1.2% (7) percent thermal shrinkage (vertically/laterally): 2.0%/1.2%
(8) surface tension: 40mN/m
By the bidirectional stretching polypropylene film that said structure, composition and preparation method produce, it is simple in structure, and heat seal strength is big, with paper wood, preprint paper wood or contain the product that the film of this functional layer is composited, and the peel strength height, the manufacturing that is beneficial to product is promoted.