CN115139613A - PE wood-plastic wallboard and preparation method thereof - Google Patents
PE wood-plastic wallboard and preparation method thereof Download PDFInfo
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- CN115139613A CN115139613A CN202210847018.XA CN202210847018A CN115139613A CN 115139613 A CN115139613 A CN 115139613A CN 202210847018 A CN202210847018 A CN 202210847018A CN 115139613 A CN115139613 A CN 115139613A
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- 229920003023 plastic Polymers 0.000 title claims abstract description 54
- 239000004033 plastic Substances 0.000 title claims abstract description 54
- 238000002360 preparation method Methods 0.000 title claims abstract description 24
- 239000000463 material Substances 0.000 claims abstract description 82
- 239000004698 Polyethylene Substances 0.000 claims abstract description 55
- 239000010410 layer Substances 0.000 claims abstract description 39
- 239000002994 raw material Substances 0.000 claims abstract description 32
- 239000002344 surface layer Substances 0.000 claims abstract description 32
- 230000001070 adhesive effect Effects 0.000 claims abstract description 20
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims abstract description 19
- 239000000853 adhesive Substances 0.000 claims abstract description 19
- 239000003963 antioxidant agent Substances 0.000 claims abstract description 15
- 230000003078 antioxidant effect Effects 0.000 claims abstract description 15
- KPUWHANPEXNPJT-UHFFFAOYSA-N disiloxane Chemical class [SiH3]O[SiH3] KPUWHANPEXNPJT-UHFFFAOYSA-N 0.000 claims abstract description 13
- 229920005989 resin Polymers 0.000 claims abstract description 10
- 239000011347 resin Substances 0.000 claims abstract description 10
- 229920001684 low density polyethylene Polymers 0.000 claims abstract description 9
- 239000004702 low-density polyethylene Substances 0.000 claims abstract description 9
- 239000003208 petroleum Substances 0.000 claims abstract description 9
- 239000012790 adhesive layer Substances 0.000 claims abstract description 8
- 229920001577 copolymer Polymers 0.000 claims abstract description 7
- 238000002156 mixing Methods 0.000 claims description 23
- 238000001125 extrusion Methods 0.000 claims description 18
- 239000003795 chemical substances by application Substances 0.000 claims description 17
- -1 polyethylene Polymers 0.000 claims description 17
- 239000002023 wood Substances 0.000 claims description 16
- 239000004743 Polypropylene Substances 0.000 claims description 15
- 239000000155 melt Substances 0.000 claims description 13
- 238000000034 method Methods 0.000 claims description 13
- 229920001155 polypropylene Polymers 0.000 claims description 13
- 229920001903 high density polyethylene Polymers 0.000 claims description 12
- 239000004700 high-density polyethylene Substances 0.000 claims description 12
- 238000002844 melting Methods 0.000 claims description 12
- 230000008018 melting Effects 0.000 claims description 12
- 229920006225 ethylene-methyl acrylate Polymers 0.000 claims description 11
- 238000001816 cooling Methods 0.000 claims description 10
- 230000003678 scratch resistant effect Effects 0.000 claims description 8
- BGYHLZZASRKEJE-UHFFFAOYSA-N [3-[3-(3,5-ditert-butyl-4-hydroxyphenyl)propanoyloxy]-2,2-bis[3-(3,5-ditert-butyl-4-hydroxyphenyl)propanoyloxymethyl]propyl] 3-(3,5-ditert-butyl-4-hydroxyphenyl)propanoate Chemical compound CC(C)(C)C1=C(O)C(C(C)(C)C)=CC(CCC(=O)OCC(COC(=O)CCC=2C=C(C(O)=C(C=2)C(C)(C)C)C(C)(C)C)(COC(=O)CCC=2C=C(C(O)=C(C=2)C(C)(C)C)C(C)(C)C)COC(=O)CCC=2C=C(C(O)=C(C=2)C(C)(C)C)C(C)(C)C)=C1 BGYHLZZASRKEJE-UHFFFAOYSA-N 0.000 claims description 7
- BAPJBEWLBFYGME-UHFFFAOYSA-N Methyl acrylate Chemical compound COC(=O)C=C BAPJBEWLBFYGME-UHFFFAOYSA-N 0.000 claims description 6
- JKIJEFPNVSHHEI-UHFFFAOYSA-N Phenol, 2,4-bis(1,1-dimethylethyl)-, phosphite (3:1) Chemical compound CC(C)(C)C1=CC(C(C)(C)C)=CC=C1OP(OC=1C(=CC(=CC=1)C(C)(C)C)C(C)(C)C)OC1=CC=C(C(C)(C)C)C=C1C(C)(C)C JKIJEFPNVSHHEI-UHFFFAOYSA-N 0.000 claims description 6
- 239000003999 initiator Substances 0.000 claims description 6
- 238000010521 absorption reaction Methods 0.000 claims description 5
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- 239000004952 Polyamide Substances 0.000 claims description 4
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- 229920000573 polyethylene Polymers 0.000 claims description 4
- 239000000843 powder Substances 0.000 claims description 4
- 239000000758 substrate Substances 0.000 claims description 4
- 239000003921 oil Substances 0.000 claims description 3
- 229920001296 polysiloxane Polymers 0.000 claims description 3
- 238000006748 scratching Methods 0.000 claims description 3
- 238000004519 manufacturing process Methods 0.000 claims description 2
- 230000002745 absorbent Effects 0.000 claims 1
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- 238000003825 pressing Methods 0.000 claims 1
- 238000007873 sieving Methods 0.000 claims 1
- 239000011230 binding agent Substances 0.000 description 36
- 239000000047 product Substances 0.000 description 22
- 230000000052 comparative effect Effects 0.000 description 17
- 239000000203 mixture Substances 0.000 description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
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- 238000001035 drying Methods 0.000 description 6
- 238000012360 testing method Methods 0.000 description 6
- DQXBYHZEEUGOBF-UHFFFAOYSA-N but-3-enoic acid;ethene Chemical compound C=C.OC(=O)CC=C DQXBYHZEEUGOBF-UHFFFAOYSA-N 0.000 description 5
- 239000002131 composite material Substances 0.000 description 5
- 238000005520 cutting process Methods 0.000 description 5
- 239000005038 ethylene vinyl acetate Substances 0.000 description 5
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- 239000012792 core layer Substances 0.000 description 4
- 239000002184 metal Substances 0.000 description 4
- 238000005498 polishing Methods 0.000 description 4
- XMNIXWIUMCBBBL-UHFFFAOYSA-N 2-(2-phenylpropan-2-ylperoxy)propan-2-ylbenzene Chemical compound C=1C=CC=CC=1C(C)(C)OOC(C)(C)C1=CC=CC=C1 XMNIXWIUMCBBBL-UHFFFAOYSA-N 0.000 description 3
- 229920002292 Nylon 6 Polymers 0.000 description 3
- 230000005587 bubbling Effects 0.000 description 3
- 238000005034 decoration Methods 0.000 description 3
- 230000032798 delamination Effects 0.000 description 3
- 235000013312 flour Nutrition 0.000 description 3
- 239000008187 granular material Substances 0.000 description 3
- FPYJFEHAWHCUMM-UHFFFAOYSA-N maleic anhydride Chemical compound O=C1OC(=O)C=C1 FPYJFEHAWHCUMM-UHFFFAOYSA-N 0.000 description 3
- 239000006097 ultraviolet radiation absorber Substances 0.000 description 3
- 238000007605 air drying Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000004049 embossing Methods 0.000 description 2
- 235000012438 extruded product Nutrition 0.000 description 2
- 239000000945 filler Substances 0.000 description 2
- 238000005469 granulation Methods 0.000 description 2
- 230000003179 granulation Effects 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000011265 semifinished product Substances 0.000 description 2
- 235000012239 silicon dioxide Nutrition 0.000 description 2
- 239000000377 silicon dioxide Substances 0.000 description 2
- 239000012257 stirred material Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 229940124543 ultraviolet light absorber Drugs 0.000 description 2
- DMWVYCCGCQPJEA-UHFFFAOYSA-N 2,5-bis(tert-butylperoxy)-2,5-dimethylhexane Chemical compound CC(C)(C)OOC(C)(C)CCC(C)(C)OOC(C)(C)C DMWVYCCGCQPJEA-UHFFFAOYSA-N 0.000 description 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- 239000004677 Nylon Substances 0.000 description 1
- DYAHQFWOVKZOOW-UHFFFAOYSA-N Sarin Chemical compound CC(C)OP(C)(F)=O DYAHQFWOVKZOOW-UHFFFAOYSA-N 0.000 description 1
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 1
- 229920001587 Wood-plastic composite Polymers 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- FWDBOZPQNFPOLF-UHFFFAOYSA-N ethenyl(triethoxy)silane Chemical compound CCO[Si](OCC)(OCC)C=C FWDBOZPQNFPOLF-UHFFFAOYSA-N 0.000 description 1
- NKSJNEHGWDZZQF-UHFFFAOYSA-N ethenyl(trimethoxy)silane Chemical compound CO[Si](OC)(OC)C=C NKSJNEHGWDZZQF-UHFFFAOYSA-N 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000011900 installation process Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 229920001778 nylon Polymers 0.000 description 1
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- 239000011780 sodium chloride Substances 0.000 description 1
- 230000008961 swelling Effects 0.000 description 1
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 1
- 229920002554 vinyl polymer Polymers 0.000 description 1
- 239000012856 weighed raw material Substances 0.000 description 1
- 239000011155 wood-plastic composite Substances 0.000 description 1
Images
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B27/00—Layered products comprising a layer of synthetic resin
- B32B27/32—Layered products comprising a layer of synthetic resin comprising polyolefins
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/001—Combinations of extrusion moulding with other shaping operations
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/16—Articles comprising two or more components, e.g. co-extruded layers
- B29C48/18—Articles comprising two or more components, e.g. co-extruded layers the components being layers
- B29C48/21—Articles comprising two or more components, e.g. co-extruded layers the components being layers the layers being joined at their surfaces
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B27/00—Layered products comprising a layer of synthetic resin
- B32B27/06—Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material
- B32B27/08—Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material of synthetic resin
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B27/00—Layered products comprising a layer of synthetic resin
- B32B27/18—Layered products comprising a layer of synthetic resin characterised by the use of special additives
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B7/00—Layered products characterised by the relation between layers; Layered products characterised by the relative orientation of features between layers, or by the relative values of a measurable parameter between layers, i.e. products comprising layers having different physical, chemical or physicochemical properties; Layered products characterised by the interconnection of layers
- B32B7/04—Interconnection of layers
- B32B7/12—Interconnection of layers using interposed adhesives or interposed materials with bonding properties
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
- C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
- C08L23/04—Homopolymers or copolymers of ethene
- C08L23/06—Polyethene
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L97/00—Compositions of lignin-containing materials
- C08L97/02—Lignocellulosic material, e.g. wood, straw or bagasse
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09J—ADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
- C09J11/00—Features of adhesives not provided for in group C09J9/00, e.g. additives
- C09J11/02—Non-macromolecular additives
- C09J11/04—Non-macromolecular additives inorganic
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09J—ADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
- C09J123/00—Adhesives based on homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Adhesives based on derivatives of such polymers
- C09J123/02—Adhesives based on homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Adhesives based on derivatives of such polymers not modified by chemical after-treatment
- C09J123/04—Homopolymers or copolymers of ethene
- C09J123/08—Copolymers of ethene
- C09J123/0846—Copolymers of ethene with unsaturated hydrocarbons containing other atoms than carbon or hydrogen atoms
- C09J123/0869—Acids or derivatives thereof
-
- E—FIXED CONSTRUCTIONS
- E04—BUILDING
- E04F—FINISHING WORK ON BUILDINGS, e.g. STAIRS, FLOORS
- E04F13/00—Coverings or linings, e.g. for walls or ceilings
- E04F13/07—Coverings or linings, e.g. for walls or ceilings composed of covering or lining elements; Sub-structures therefor; Fastening means therefor
- E04F13/08—Coverings or linings, e.g. for walls or ceilings composed of covering or lining elements; Sub-structures therefor; Fastening means therefor composed of a plurality of similar covering or lining elements
- E04F13/0866—Coverings or linings, e.g. for walls or ceilings composed of covering or lining elements; Sub-structures therefor; Fastening means therefor composed of a plurality of similar covering or lining elements composed of several layers, e.g. sandwich panels or layered panels
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29L—INDEXING SCHEME ASSOCIATED WITH SUBCLASS B29C, RELATING TO PARTICULAR ARTICLES
- B29L2007/00—Flat articles, e.g. films or sheets
- B29L2007/002—Panels; Plates; Sheets
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2250/00—Layers arrangement
- B32B2250/24—All layers being polymeric
- B32B2250/242—All polymers belonging to those covered by group B32B27/32
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2307/00—Properties of the layers or laminate
- B32B2307/70—Other properties
- B32B2307/712—Weather resistant
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2607/00—Walls, panels
- B32B2607/02—Wall papers, wall coverings
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2207/00—Properties characterising the ingredient of the composition
- C08L2207/06—Properties of polyethylene
- C08L2207/062—HDPE
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Mechanical Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Architecture (AREA)
- Inorganic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Wood Science & Technology (AREA)
- Materials Engineering (AREA)
- Civil Engineering (AREA)
- Structural Engineering (AREA)
- Extrusion Moulding Of Plastics Or The Like (AREA)
Abstract
The invention provides a PE wood-plastic wallboard and a preparation method thereof, and relates to the technical field of surface layer materials of wood-plastic products. The PE wood-plastic wallboard comprises a base material layer, a bonding layer and a surface layer which are sequentially stacked; the adhesive layer is made of an adhesive, and the adhesive is prepared from the following raw materials in parts by weight: 50-87 parts of polyethylene-methyl acrylate copolymer, 1-3 parts of low-density polyethylene, 5-15 parts of petroleum resin, 0-28 parts of diatomite and 0.1-1 part of antioxidant; the surface layer is made of a surface material containing siloxane. The bonding layer in the PE wood-plastic wallboard enables the base material layer and the surface layer to be tightly bonded, and improves the stability and the weather resistance of the product.
Description
Technical Field
The invention relates to the technical field of wood-plastic products, in particular to a PE wood-plastic wallboard and a preparation method thereof.
Background
The PE (polyethylene) wood-plastic wallboard is a product integrating functions and decoration, can decorate a building entity, improves the quality of an application environment, can endow the building with good application functions and various choices, and fully shows the decoration aesthetic effect of wood-plastic materials and the building. Therefore, the application of the PE wood-plastic wallboard in the field of outdoor wall decoration is rapidly raised.
When the PE wood-plastic wallboard is used on an outer wall facade, a scaffold needs to be lapped in the installation process, and if the quality of a product is poor, a large amount of manpower and material resources need to be consumed in the maintenance process. The existing PE wood-plastic wallboard is generally formed by bonding a surface layer and a core layer, but the bonding property of a co-extrusion surface layer material and a core layer material is poor, the phenomena of bubbling, delaminating and the like (as shown in figure 1) easily occur in the outdoor use process of the product, and the appearance of the product is seriously influenced. The bonding property of the surface layer and the core layer of the PE wood-plastic wallboard needs to be improved.
At present, the method for solving the problems is mainly to add the binder into the surface layer material in a melt blending mode, for example, ester and maleic anhydride grafting compatilizers are introduced to improve the bonding strength of the wood-plastic composite co-extrusion surface layer composite material and the core layer material, but the method has high requirements on the material mixing process, if the materials are not uniformly mixed, the phenomenon of local debonding can be caused, in addition, in order to achieve an ideal bonding effect, the using amount of the binder can be increased during blending modification, and the product cost is improved.
The problems of uneven flow and unstable discharge (as shown in figure 2) are very easy to occur in a complex co-extrusion flow channel in a commercially available hot melt adhesive product such as an EVA hot melt adhesive or an EAA hot melt adhesive, so that no report that the adhesion is increased by using the hot melt adhesive as a co-extrusion material exists at present, and the adhesion problem is still improved by mainly adopting a surface material blending modification mode in the prior art.
Disclosure of Invention
In view of the above, there is a need to provide a PE wood-plastic wallboard, in which the bonding layer tightly bonds the substrate layer and the surface layer, and improves the stability and weather resistance of the product.
A PE wood-plastic wallboard comprises a base material layer, a bonding layer and a surface layer which are sequentially stacked; the adhesive layer is made of an adhesive, and the adhesive is prepared from the following raw materials in parts by weight: 50-87 parts of polyethylene-methyl acrylate copolymer, 1-3 parts of low-density polyethylene, 5-15 parts of petroleum resin, 0-28 parts of diatomite and 0.1-1 part of antioxidant; the surface layer is made of a surface material containing siloxane.
In the PE wood-plastic wallboard, the adhesive takes the EMA as the base material, and the EMA has low viscosity to metal compared with EVA, EAA and other hot melt adhesives, so that the processability of the adhesive in a co-extruder can be improved, and the adhesive can stably flow in a complex co-extrusion flow channel; meanwhile, the diatomite filler is added into the binder, and the diatomite has strong water absorption performance, can absorb water entering the binder, prevents the water from breaking the structure of the binder, and maintains the use performance of the binder; furthermore, the surface material for preparing the surface layer contains siloxane components, and the diatomite in the binder contains components such as silicon dioxide, so that the bonding strength between the bonding layer and the surface layer can be improved, and the influence of blending modification of the surface material by adding the binder on the performance of the surface material can be avoided.
In one embodiment, the diatomite is used in 6-16 parts.
In one embodiment, the polyethylene-methyl acrylate copolymer is used in an amount of 71 to 81 parts.
In one embodiment, the content of the methyl acrylate in the ethylene methyl acrylate copolymer is 28-32%, and the melt flow index of the ethylene methyl acrylate copolymer is 2.8-3.2 g/10min.
In one embodiment, the low density polyethylene has a melt flow index of 3 to 8g/10min.
In one embodiment, the petroleum resin is a C5 petroleum resin.
In one embodiment, the residue of the 300-mesh sieve analyzed by the diatomite is less than or equal to 17.6 percent, and the oil absorption is 105-190 g/100g.
In one embodiment, the antioxidant is selected from: one or two of antioxidant 1010 and antioxidant 168.
In one embodiment, the preparation method of the adhesive comprises the following steps: uniformly mixing the polyethylene-methyl acrylate copolymer, the low-density polyethylene, the petroleum resin and the antioxidant, blending, melting, extruding and cooling to obtain the polyethylene-methyl acrylate copolymer.
In one embodiment, the blending melt extrusion is performed using a parallel twin screw extruder.
In one embodiment, the temperatures in each stage from the hopper to the die are: 80-100 ℃, 130-150 ℃, 140-160 ℃, 160-180 ℃, 170-190 ℃.
In one embodiment, the screw speed of the main machine is 200-350 r/min, and the screw speed of the feeding screw is 10-30 r/min.
In one embodiment, the substrate layer is made of a base material containing wood flour and polyethylene.
The base material in the invention is selected from materials which are commonly available in the market and can be used for preparing wood powder and polyethylene composite boards (such as wood powder/low density polyethylene composite boards, wood powder/high density polyethylene composite boards and the like).
In one embodiment, the surface layer material is prepared from the following raw materials in parts by weight: 50 to 80 portions of high-density polyethylene, 10 to 25 portions of polyamide, 5 to 15 portions of scratch resistance agent, 4 to 12 portions of compatilizer, 0.1 to 1 portion of antioxidant and 0.1 to 1 portion of ultraviolet absorber; the scratch resistant agent is silicone grafted polypropylene.
The surface material adopts the scratch-resistant agent of grafted siloxane on a polypropylene molecular chain, even if a large amount of scratch-resistant agent is added into the surface material, the scratch-resistant agent cannot be separated out on the surface of the product, meanwhile, the scratch resistance of the surface material can be improved, the phenomenon that the surface of the product is whitened after polishing is improved, and the color and the texture are natural and soft; and the scratch resistant agent adopts PP as a main material, so that the toughness of the surface material can be reduced, the phenomenon of burrs after polishing can be effectively improved, and the appearance of the product can be improved.
In one embodiment, the high density polyethylene is used in an amount of 55 to 72 parts. Preferably, the high density polyethylene is used in an amount of 55 to 62 parts.
In one embodiment, the polyamide is used in an amount of 18 to 25 parts.
In one embodiment, the anti-scratch agent is used in an amount of 12 to 15 parts.
In one embodiment, the high density polyethylene has a melt flow index of 0.8 to 1.2g/10min.
In one embodiment, the polyamide is polyamide 6 (i.e., nylon 6), and the relative viscosity of the polyamide 6 is 2.85 ± 0.03.
In one embodiment, the compatilizer is maleic anhydride grafted high-density polyethylene, the grafting ratio is 0.8-1.2%, and the melt flow index is 3-5 g/10min.
In one embodiment, the antioxidant is selected from: one or two of antioxidant 1010 and antioxidant 168.
In one embodiment, the ultraviolet light absorber is selected from: one or two of UV-531 and UV-327.
In one embodiment, the anti-scratching agent is prepared from the following raw materials in parts by weight: 90 to 95 portions of polypropylene, 1 to 4 portions of siloxane, 0.1 to 0.3 portion of initiator and 0.1 to 0.5 portion of antioxidant.
In one embodiment, the polypropylene is homopolymerized polypropylene, and the melt flow index is 10-14 g/10min.
In one embodiment, the silicone is selected from: one or two of vinyltrimethoxysilane and vinyltriethoxysilane.
In one embodiment, the initiator is selected from: dicumyl peroxide, 2,5-dimethyl-2,5-bis (t-butylperoxy) hexane, or both.
In one embodiment, the antioxidant is selected from: one or two of antioxidant 1010 and antioxidant 168.
In one embodiment, the preparation method of the anti-scratch agent comprises the following steps: uniformly mixing siloxane and an initiator to obtain a mixture A; mixing polypropylene and a second antioxidant to obtain a mixture B; and blending the mixture A and the mixture B, melting, extruding and cooling to obtain the scratch-resistant agent. .
In one embodiment, the scratch-resistant agent is prepared by adopting a parallel double-screw extruder, a mixture of siloxane and an initiator is placed in a side feeding tank, polypropylene is placed in a main feeding hopper, the rotating speed of a screw of a main machine is 200-350 r/min, and the rotating speed of a feeding screw of the main feeding hopper is 10-30 r/min; the mixed melt is added into a double-screw extruder in a side feeding mode to be mixed with the polypropylene melt, and the flow rate of the mixed melt is 0.5-0.8 kg/h.
In one embodiment, the temperatures in each stage from the hopper to the die are: 100-130 ℃, 150-170 ℃, 160-180 ℃, 170-190 ℃, 180-200 ℃, 190-200 ℃ and 200-210 ℃.
In one embodiment, the preparation method of the surface material comprises the following steps: and uniformly mixing the raw materials, melting, extruding, cooling and granulating to obtain the composite material.
In one embodiment, the melt extrusion step is specifically: and (3) placing the mixed raw materials into a feeding hopper of a parallel double-screw extruder, and blending, melting and extruding the raw materials.
In one embodiment, the temperatures in each stage from the hopper to the die are: 100-130 ℃, 150-180 ℃, 180-200 ℃, 190-210 ℃, 190-220 ℃, 200-230 ℃ and 200-230 ℃.
In one embodiment, the screw speed of the main machine is 200-350 r/min, and the screw speed of the main feeding hopper is 10-30 r/min.
The invention also provides a preparation method of the PE wood-plastic wallboard, and the PE wood-plastic wallboard is manufactured by adopting a three-layer co-extrusion method.
Compared with the method of adding the adhesive into the surface material for blending modification, the method for preparing the PE wood-plastic wallboard by adopting the three-layer co-extrusion mode can ensure that the adhesive property of the adhesive is not interfered by other layer materials, and the basic property of the surface material can not be influenced by the adhesive.
The co-extrusion is carried out by adopting an extruder, the channel of the extruder is made of metal, the viscosity of the binder in the PE wood-plastic wall is not high to metal, the binder can stably flow in the channel, and the processability is good.
In one embodiment, the raw materials of the base material layer, the bonding layer and the surface layer are respectively melt-extruded, sequentially stacked, pressed and shaped to obtain the PE wood-plastic wallboard.
In one embodiment, the raw material of the base material layer is melted and extruded in a conical double-screw extruder, the temperatures of sections from a hopper to a confluence core are respectively 190-210 ℃, 170-190 ℃, 170-150 ℃, 160-140 ℃ and 150-130 ℃, the temperatures of an upper area, a lower area, a left area and a right area of a front section of a die are respectively 150-170 ℃, 150-170 ℃ and 150-170 ℃, the temperatures of a post-die Duan Shangou, a lower area, a left area and a right area are respectively 190-220 ℃, 190-220 ℃ and 190-220 ℃, the screw rotating speed of a main machine is 10-15 r/min, and the rotating speed of a feeding screw of a main feeding hopper is 18-25 r/min.
In one embodiment, the melting extrusion of the raw materials of the adhesive layer is carried out in a first single-screw co-extruder, the temperature of each section from the hopper to the confluence core is 110-130 ℃, 140-170 ℃, 180-200 ℃ and the screw rotation speed of the main machine is 5-8 r/min.
In one embodiment, the surface layer raw material is melted and extruded in a second single-screw co-extruder, the temperature of each section from the hopper to the confluence core is respectively 110-130 ℃, 160-180 ℃, 180-200 ℃, 200-220 ℃, and the rotating speed of a main machine screw is 9-14 r/min.
Compared with the prior art, the invention has the following beneficial effects:
according to the PE wood-plastic wallboard, the adhesive takes the EMA as the base material, and the EMA has low viscosity to metal compared with hot melt adhesives such as EVA (ethylene vinyl acetate) and EAA (EAA), so that the processability of the adhesive in a co-extruder can be improved, and the adhesive can stably flow in a complex co-extrusion flow channel; meanwhile, the diatomite filler is added into the binder, and the diatomite has strong water absorption performance, can absorb water entering the binder, prevents the water from breaking the structure of the binder, and maintains the use performance of the binder; furthermore, the surface material for preparing the surface layer contains siloxane components, and the diatomite in the binder contains components such as silicon dioxide, so that the bonding strength between the bonding layer and the surface layer can be improved, and the influence of blending modification of the surface material by adding the binder on the performance of the surface material can be avoided.
Drawings
Fig. 1 is a schematic diagram of delamination and bubbling phenomena after the prior PE wood plastic product mentioned in the background art is used.
FIG. 2 is a schematic view of the product obtained by the non-uniform extrusion of the hot melt adhesive as mentioned in the background of the invention.
FIG. 3 is an appearance of the product of example 2 after weather resistance testing.
Detailed Description
To facilitate an understanding of the invention, a more complete description of the invention will be given below in terms of preferred embodiments. This invention may, however, be embodied in many different forms and should not be construed as limited to the embodiments set forth herein. Rather, these embodiments are provided so that this disclosure will be thorough and complete.
Unless defined otherwise, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this invention belongs. The terminology used in the description of the invention herein is for the purpose of describing particular embodiments only and is not intended to be limiting of the invention.
In the following examples and comparative examples, unless otherwise specified, reagents, materials, equipment were commercially available and the experimental procedures were those routine in the art. The following parts are all parts by weight.
The substrate layers in the following examples and comparative examples were prepared from commercially available wood flour and high density polyethylene granules, wherein the mass ratio of the wood flour to the high density polyethylene was about 65:35.
example 1
A PE wood-plastic wallboard comprises a base material layer, a bonding layer and a surface layer which are sequentially stacked. The adhesive layer was prepared using a binder of the raw material composition shown in table 1, and the surface layer was prepared using a surface material. The preparation method of the PE wood-plastic wallboard comprises the following steps of, wherein the dosage weight ratio of the surface layer material to the binder is 93:7.
(1) Preparation of the Binder
The raw materials of the binder were added to a blender and stirred for 15 minutes and then added to the feed hopper of a parallel twin-screw extruder. The temperature of each section from the hopper to the die head of the extruder is respectively set as follows: 80 ℃,130 ℃,150 ℃,160 ℃,160 ℃,160 ℃,180 ℃,180 ℃,190 ℃. The rotating speed of the screw of the main machine is 230r/min, and the rotating speed of the feeding screw of the main feeding hopper is 12r/min. And then the materials are blended, melted and extruded by an extruder. And cooling the extruded strips through a water tank, air-drying, and then cutting the extruded strips into particles in a granulator to obtain the bonding layer material.
(2) Preparation of the surface Material
The surface layer material is prepared from the following raw materials in parts by weight: 72 parts of high-density polyethylene with the melt flow index of 1g/10min, 6 parts of nylon with the relative viscosity of 2.85 +/-0.03, 5 parts of maleic anhydride grafted high-density polyethylene with the grafting rate of 1 percent and the melt flow index of 4g/10min, 5 parts of anti-scratch agent, 0.5 part of antioxidant 1010, 0.5 part of antioxidant 168, and 0.5 part of ultraviolet light absorber UV-531. The anti-scratch agent is prepared from the following raw materials in parts by weight: 99 parts of polypropylene (homopolymerized polypropylene with the melt flow index of 12g/10 min), 1 part of vinyl trimethoxy siloxane, 0.1 part of dicumyl peroxide and 0.3 part of antioxidant.
The preparation method of the anti-scratching agent comprises the following steps: adding vinyltrimethoxysiloxane and dicumyl peroxide into a liquid stirrer, stirring for 15 minutes, then adding the uniformly stirred materials into a side feeding tank of a parallel double-screw extruder, and adding polypropylene into a main feeding hopper. The temperature of each section from the hopper to the die head of the extruder is respectively set as follows: 100 ℃,150 ℃,180 ℃,190 ℃,200 ℃,200 ℃,200 ℃,200 ℃,210 ℃. The screw rotating speed of the main machine is 250r/min, and the rotating speed of the feeding screw of the main feeding hopper is 18r/min. The siloxane and initiator mixed liquid is added into a double-screw extruder by a melt pump in a side feeding mode, and the set flow rate is 0.6kg/h. And (3) blending, melting and extruding the materials through an extruder. And the extruded strips are cooled by air through a conveying belt and then enter a granulator for granulation, and are sealed and stored.
The preparation method of the surface material comprises the following steps: (i) Adding the weighed raw materials into a stirrer, stirring for 15 minutes, and then adding the uniformly stirred materials into a feeding hopper of a parallel double-screw extruder. (ii) The temperature of each section from the hopper to the die head of the extruder is set as follows: 110 deg.C, 180 deg.C, 200 deg.C, 210 deg.C, 220 deg.C, 230 deg.C. The screw rotating speed of the main machine is 200r/min, and the rotating speed of the feeding screw of the main feeding hopper is 15r/min. And (3) blending, melting and extruding the materials through an extruder. (iii) And cooling the extruded strips through a water tank, air-drying, and then feeding into a granulator for granulation to obtain the finished product.
(3) Three-layer coextrusion
S1, adding the granules for preparing the base material layer into a material hopper of a conical double-screw extruder.
S2, adding the binder into a material hopper of the single-screw co-extruder 1, turning on a material drying switch, setting the temperature to be 80 ℃, and drying the material for 2 hours. Adding the surface material into a material hopper of the single-screw co-extruder 2, opening a material drying switch, setting the temperature at 80 ℃, and drying the material for 2 hours.
S3, setting the temperatures of all sections of the conical double-screw extruder from the hopper to the confluence core to be 200 ℃,170 ℃,160 ℃,150 ℃ and 145 ℃ respectively; the temperatures of four areas (upper, lower, left and right) at the front section of the die are respectively 150 ℃,150 ℃,150 ℃ and 150 ℃; the temperatures of four zones (upper, lower, left and right) at the rear section of the die are 220 ℃,220 ℃,220 ℃ and 220 ℃. The screw rotating speed of the main machine is 12r/min, and the rotating speed of the feeding screw of the main feeding hopper is 18r/min.
S4, setting the temperatures of all sections of the single-screw co-extruder 1 from the hopper to the confluence core to be 110 ℃,160 ℃,200 ℃ and 200 ℃, and setting the screw rotation speed of the main machine to be 6r/min.
S5, setting the temperatures of all sections of the single-screw co-extruder 2 from the hopper to the confluence core to be 130 ℃,180 ℃,200 ℃,210 ℃ and the rotating speed of the main machine screw to be 11r/min.
And S6, opening the conical double-screw extruder, the single-screw co-extruder 1 and the single-screw co-extruder 2 to perform three-layer co-extrusion. And cutting and carrying the extruded product to a cooling and shaping vehicle after an online deep embossing process, naturally cooling and shaping to obtain a semi-finished product of the PE wood-plastic co-extruded wallboard, and polishing and cutting at a fixed length to obtain a finished product of the PE wood-plastic wallboard.
Example 2
A PE wood plastic wallboard, having substantially the same structure and preparation method as in example 1, except that the binder was replaced with the binder of the present example of equal weight, and the composition of the binder raw material of the present example is shown in table 1.
Example 3
A PE wood plastic wallboard, having substantially the same structure and preparation method as example 1, except that the binder was replaced with the binder of the present example of equal weight, the composition of the binder raw material of the present example is shown in table 1.
Example 4
A PE wood plastic wallboard, having substantially the same structure and preparation method as example 1, except that the binder was replaced with the binder of the present example of equal weight, the composition of the binder raw material of the present example is shown in table 1.
Example 5
A PE wood plastic wallboard, having substantially the same structure and preparation method as in example 1, except that the binder was replaced with the binder of the present example of equal weight, and the composition of the binder raw material of the present example is shown in table 1.
Comparative example 1
A PE wood-plastic wallboard comprises a base material layer and a surface layer which are sequentially stacked, and does not contain an adhesive layer. The preparation method of the PE wood-plastic wallboard is as follows.
(1) Preparation of the surface Material
The skin material raw material and the preparation method were the same as in example 1.
(2) Double-layer coextrusion
S1, adding the granules for preparing the base material layer into a material hopper of a conical double-screw extruder.
S2, adding the surface material into a material hopper of the single-screw co-extruder, turning on a material drying switch, setting the temperature to be 80 ℃, and drying the material for 2 hours.
S3, setting the temperatures of all sections of the conical double-screw extruder from the hopper to the confluence core to be 200 ℃,170 ℃,160 ℃,150 ℃ and 145 ℃ respectively; the temperatures of four areas (upper, lower, left and right) at the front section of the die are respectively 150 ℃,150 ℃,150 ℃ and 150 ℃; the temperatures of four zones (upper, lower, left and right) at the rear section of the die are 220 ℃,220 ℃,220 ℃ and 220 ℃. The screw rotating speed of the main machine is 12r/min, and the rotating speed of the feeding screw of the main feeding hopper is 18r/min.
S4, setting the temperatures of all sections of the single-screw co-extruder from the hopper to the confluence core to be 130 ℃,180 ℃,200 ℃,210 ℃ and the rotating speed of the main machine screw to be 11r/min.
And S5, opening the conical double-screw extruder and the single-screw extruder to perform double-layer co-extrusion. And cutting and carrying the extruded product to a cooling and shaping vehicle after an online deep embossing process, naturally cooling and shaping to obtain a semi-finished product of the PE wood-plastic co-extruded wallboard, and polishing and cutting at a fixed length to obtain a finished product of the PE wood-plastic wallboard.
Comparative example 2
The PE wood-plastic wallboard is basically the same as the PE wood-plastic wallboard in the comparative example 1 in structure and preparation method, and is characterized in that a surface material in the comparative example 1 is replaced by a certain commercially available surface material, and the PE wood-plastic wallboard comprises the following raw material components: 48 parts of HDPE, 15 parts of PP, 30 parts of sarin resin, 7 parts of EVA, 0.6 part of antioxidant 1010 and 168.6 parts of antioxidant.
Comparative example 3
A PE wood plastic wallboard, the structure and method of manufacture of which is essentially the same as example 1, except that EMA in the binder is replaced with equal mass EAA. The binder layer is discharged unevenly in the extrusion process, and the product is unqualified.
Comparative example 4
A PE wood-plastic wallboard is basically the same as the structure and the preparation method of the PE wood-plastic wallboard in example 1, except that siloxane is not added into a surface material.
Comparative example 5
The PE wood-plastic wallboard comprises a base material layer and a surface layer which are sequentially stacked, and does not comprise an adhesive layer. The preparation method of the PE wood-plastic wallboard is as follows.
(1) Blending modification of surface layer material
The surface material in the example 1 and the adhesive in the example 1 are mixed in a mass ratio of 80:20 and mixing.
(2) Double-layer coextrusion
The double-layer co-extrusion method is basically the same as that of comparative example 1, except that the blending modified surface material is used for replacing the surface material in comparative example 1 in S2.
Table 1 examples raw material kinds and amounts of binders
Test items | Example 1 | Example 2 | Example 3 | Example 4 | Example 5 |
EMA | 81 | 75 | 71 | 65 | 59 |
LDPE | 3 | 3 | 3 | 3 | 3 |
C5 Petroleum resins | 10 | 10 | 10 | 10 | 10 |
Diatomite | 6 | 12 | 16 | 22 | 28 |
Antioxidant 1010 | 0.3 | 0.3 | 0.3 | 0.3 | 0.3 |
Antioxidant 168 | 0.3 | 0.3 | 0.3 | 0.3 | 0.3 |
Wherein the EMA contains 30 wt% of methyl acrylate, 3.0g/10min of melt flow index, 5g/10min of low density polyethylene, 16% of diatomite with 300-mesh sieve residue and 150g/100g of oil absorption.
Experimental example 1
The PE wood plastic wallboard of the above examples and comparative examples was subjected to a surface bonding strength test, and the results are shown in table 2.
TABLE 2 surface bond strength results
Item | Surface bond strength/MPa |
Test standard | GB/T 17657-2016 |
Example 1 | 1.16 |
Example 2 | 1.27 |
Example 3 | 1.13 |
Example 4 | 0.92 |
Example 5 | 0.82 |
Comparative example 1 | 0.56 |
Comparative example 2 | 0.75 |
Comparative example 3 | 1.02 |
Comparative example 4 | 0.95 |
Comparative example 5 | 1.06 |
Experimental example 2
The product of example 2 was subjected to a weather resistance test and boiled in 5wt% saline at 100 ℃ for 240 hours to observe whether the product had a poor phenomenon such as delamination and swelling of the surface layer structure. The tested product is shown in fig. 3, and the result shows that the product of example 2 has no debonding phenomenon, and no delamination or bubbling phenomenon after the weather resistance test.
All possible combinations of the technical features of the above embodiments may not be described for the sake of brevity, but should be considered as within the scope of the present disclosure as long as there is no contradiction between the combinations of the technical features.
The above-mentioned embodiments only express several embodiments of the present invention, and the description thereof is specific and detailed, but not to be understood as limiting the scope of the invention. It should be noted that, for a person skilled in the art, several variations and modifications can be made without departing from the inventive concept, which falls within the scope of the present invention. Therefore, the protection scope of the present patent shall be subject to the appended claims.
Claims (10)
1. The utility model provides a wallboard is moulded to PE wood which characterized in that: the adhesive comprises a base material layer, an adhesive layer and a surface layer which are sequentially stacked; the adhesive layer is made of an adhesive, and the adhesive is prepared from the following raw materials in parts by weight: 50-87 parts of polyethylene-methyl acrylate copolymer, 1-3 parts of low-density polyethylene, 5-15 parts of petroleum resin, 0-28 parts of diatomite and 0.1-1 part of antioxidant; the surface layer is made of a surface material containing siloxane.
2. The PE wood-plastic wallboard of claim 1, wherein: the weight content of methyl acrylate in the ethylene methyl acrylate copolymer is 28-32%, and the melt flow index of the ethylene methyl acrylate copolymer is 2.8-3.2 g/10min; the melt flow index of the low-density polyethylene is 3-8 g/10min; the petroleum resin is C5 petroleum resin; the residue of the 300-mesh sieve for sieving out the diatomite is less than or equal to 17.6 percent, and the oil absorption is 105-190 g/100g; the antioxidant is selected from: one or two of antioxidant 1010 and antioxidant 168; the dosage of the diatomite is 6 to 16 parts; the using amount of the polyethylene-methyl acrylate copolymer is 71-81 parts.
3. The PE wood-plastic wallboard according to claim 1 or 2, characterized in that: the preparation method of the adhesive comprises the following steps: mixing the raw materials uniformly, blending, melting, extruding and cooling to obtain the product.
4. The PE wood-plastic wallboard of claim 3, wherein: adopting a parallel double-screw extruder to perform blending, melting and extruding; the temperature of each section from the hopper to the die head is respectively as follows: 80-100 ℃, 130-150 ℃, 140-160 ℃, 160-180 ℃ and 170-190 ℃; the rotating speed of the screw of the main machine is 200-350 r/min, and the rotating speed of the feeding screw is 10-30 r/min.
5. The PE wood-plastic wallboard of claim 1, wherein: the substrate layer is made of base materials containing wood powder and polyethylene.
6. The PE wood-plastic wallboard of claim 1, wherein: the surface layer material is prepared from the following raw materials in parts by weight: 50 to 80 parts of high-density polyethylene, 10 to 25 parts of polyamide, 5 to 15 parts of scratch resistance agent, 4 to 12 parts of compatilizer, 0.1 to 1 part of antioxidant and 0.1 to 1 part of ultraviolet absorbent; the scratch resistant agent is silicone grafted polypropylene.
7. The PE wood-plastic wallboard of claim 6, wherein: the anti-scratching agent is prepared from the following raw materials in parts by weight: 90 to 95 portions of polypropylene, 1 to 4 portions of siloxane, 0.1 to 0.3 portion of initiator and 0.1 to 0.5 portion of antioxidant.
8. The method for preparing a PE wood plastic wallboard according to any of claims 1-7, characterized in that: the PE wood-plastic wallboard is manufactured by a three-layer co-extrusion method.
9. The method for producing according to claim 8, characterized in that: and respectively melting and extruding the raw material of the base material layer, the raw material of the bonding layer and the raw material of the surface layer, sequentially laminating, pressing and shaping to obtain the PE wood-plastic wallboard.
10. The method of claim 9, wherein: melting and extruding the raw materials of the base material layer in a conical double-screw extruder, wherein the temperatures of all sections from a hopper to a confluence core are respectively 190-210 ℃, 170-190 ℃, 170-150 ℃, 160-140 ℃ and 150-130 ℃, the temperatures of an upper zone, a lower zone, a left zone and a right zone of the front section of a die are respectively 150-170 ℃, 150-170 ℃ and 150-170 ℃, the temperatures of a Duan Shangou, a lower zone, a left zone and a right zone behind the die are respectively 190-220 ℃, 190-220 ℃ and 190-220 ℃, the screw rotating speed of a main machine is 10-15 r/min, and the rotating speed of a feeding screw of a main feeding hopper is 18-25 r/min;
melting and extruding the raw material of the bonding layer in a first single-screw co-extruder, wherein the temperature of each section from the hopper to the confluence core is respectively 110-130 ℃, 140-170 ℃, 180-200 ℃, and the screw rotating speed of the main machine is 5-8 r/min;
the surface layer raw material is melted and extruded in a second single-screw co-extruder, the temperature of each section from the hopper to the confluence core is respectively 110-130 ℃, 160-180 ℃, 180-200 ℃, 200-220 ℃, and the rotating speed of the main machine screw is 9-14 r/min.
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