WO2012074230A2 - Method for preparing artificial wood using natural vegetable fibroid material - Google Patents

Method for preparing artificial wood using natural vegetable fibroid material Download PDF

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WO2012074230A2
WO2012074230A2 PCT/KR2011/008823 KR2011008823W WO2012074230A2 WO 2012074230 A2 WO2012074230 A2 WO 2012074230A2 KR 2011008823 W KR2011008823 W KR 2011008823W WO 2012074230 A2 WO2012074230 A2 WO 2012074230A2
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Prior art keywords
natural vegetable
artificial wood
vegetable fiber
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synthetic resin
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PCT/KR2011/008823
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French (fr)
Korean (ko)
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WO2012074230A3 (en
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김완식
김용태
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Kim Wan Sik
Kim Yong Tae
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Publication of WO2012074230A2 publication Critical patent/WO2012074230A2/en
Publication of WO2012074230A3 publication Critical patent/WO2012074230A3/en

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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • C08L23/02Compositions 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
    • C08L23/10Homopolymers or copolymers of propene
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B27WORKING OR PRESERVING WOOD OR SIMILAR MATERIAL; NAILING OR STAPLING MACHINES IN GENERAL
    • B27NMANUFACTURE BY DRY PROCESSES OF ARTICLES, WITH OR WITHOUT ORGANIC BINDING AGENTS, MADE FROM PARTICLES OR FIBRES CONSISTING OF WOOD OR OTHER LIGNOCELLULOSIC OR LIKE ORGANIC MATERIAL
    • B27N3/00Manufacture of substantially flat articles, e.g. boards, from particles or fibres
    • B27N3/007Manufacture of substantially flat articles, e.g. boards, from particles or fibres and at least partly composed of recycled material
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • C08L23/02Compositions 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
    • C08L23/04Homopolymers or copolymers of ethene
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • C08L23/02Compositions 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
    • C08L23/04Homopolymers or copolymers of ethene
    • C08L23/08Copolymers of ethene
    • C08L23/0807Copolymers of ethene with unsaturated hydrocarbons only containing more than three carbon atoms
    • C08L23/0815Copolymers of ethene with aliphatic 1-olefins
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • C08L23/02Compositions 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
    • C08L23/04Homopolymers or copolymers of ethene
    • C08L23/08Copolymers of ethene
    • C08L23/0846Copolymers of ethene with unsaturated hydrocarbons containing other atoms than carbon or hydrogen atoms
    • C08L23/0853Vinylacetate

Definitions

  • the present invention relates to a method for manufacturing artificial wood using natural vegetable fiber, and more particularly, by reducing the amount of synthetic resin, the gas generation rate is reduced in the event of a fire, and natural vegetable fiber contains a large amount of natural wood, but light weight natural wood It relates to a method for manufacturing artificial wood using natural vegetable fiber having the same texture.
  • natural wood is economical, has a relatively small specific gravity, and is easy to process, and is used for various purposes throughout the industry.
  • natural wood has the disadvantages of poor moisture resistance, pollution resistance and corrosion resistance.
  • artificial wood mixed with sawdust or wood chips and synthetic resin In order to solve this problem, it was intended to manufacture artificial wood mixed with sawdust or wood chips and synthetic resin.
  • artificial wood containing the sawdust or wood chips should include more than 60% by weight of synthetic resin to maintain the same properties as natural wood.
  • synthetic wood containing more than 60% by weight of synthetic resin is heavy weight, high resin content, and also disadvantageous price competitiveness, there is a risk that can release a large amount of harmful gas in the event of fire.
  • the present invention for solving the above problems is to provide a method for manufacturing artificial wood using natural vegetable fiber that can maintain the strength (physical properties) similar to natural wood even significantly reducing the content of synthetic resin.
  • the present invention provides a preferred embodiment, selected from polypropylene (MAPP), titanate and zirconate based on maleate treated synthetic resin mixed with polypropylene or high density polyethylene, ethylene vinyl acetate or linear low density polyethylene.
  • the drying step is the first drying step of drying so that the moisture content of the natural vegetable fiber powder at 80 ⁇ 100 °C less than 5% by weight; It provides a method for producing artificial wood using natural vegetable fiber comprising; and a second drying step of drying so that the water content of the natural vegetable fiber powder is less than 1% by weight at 100 ⁇ 130 °C.
  • the synthetic resin in the binder coating step comprises 13 to 29 parts by weight of polypropylene or high density polyethylene and 3 to 11 parts by weight of ethylene vinyl acetate or linear low density polyethylene based on a total of 100 parts by weight of artificial wood It provides a method for producing artificial wood using natural vegetable fiber.
  • the polypropylene in the binder coating step provides a method of manufacturing artificial wood using natural vegetable fibers of homopoly or impact polypropylene having a melt index of 7 to 15.
  • the high-density polyethylene in the binder coating step provides an artificial wood manufacturing method using natural vegetable fibers having a melt index of 2 ⁇ 10.
  • the linear low-density polyethylene in the binder coating step provides an artificial wood manufacturing method using natural vegetable fibers having a melt index of 1-4.
  • the binder coating step is to mix 16 to 40 parts by weight of synthetic resin, 0.8 to 3 parts by weight of binder and 0.2 to 0.5 parts by weight of silicone oil based on 100 parts by weight of artificial wood
  • a method for preparing artificial wood using vegetable fiber is to mix 16 to 40 parts by weight of synthetic resin, 0.8 to 3 parts by weight of binder and 0.2 to 0.5 parts by weight of silicone oil based on 100 parts by weight of artificial wood.
  • the method of manufacturing artificial wood in the first kneading step, 16 to 40 parts by weight of the synthetic resin coated with a binder and 50 to 75 parts by weight of the natural vegetable fiber powder dried in the drying step are added to 100 parts by weight of the artificial wood. It provides a method for producing artificial wood using natural vegetable fiber.
  • the first kneading step provides a method for manufacturing artificial wood using natural vegetable fiber that is kneaded at 80 ⁇ 110 °C for 7 to 15 minutes.
  • the content of the additive added in the second kneading step provides an artificial wood manufacturing method using natural vegetable fiber which is 2 to 6 parts by weight based on 100 parts by weight of the total artificial wood.
  • the additive added in the second kneading step is 0.2 to 1 parts by weight of lubricant, 0.1 to 0.3 parts by weight of antioxidant, 0.2 to 0.6 parts by weight of UV based on 100 parts by weight of artificial wood It may include a stabilizer, 0.3 to 0.7 parts by weight of nucleating agent, 1 to 3 parts by weight of filler, 0.2 to 0.4 parts by weight of inorganic pigment.
  • the second kneading step provides a method of manufacturing artificial wood using natural vegetable fiber, which is kneaded at 110 to 140 ° C. for 10 to 20 minutes.
  • the molding step provides an artificial wood manufacturing method using natural vegetable fibers that are molded by an extrusion molding machine heated to 180 ⁇ 230 °C.
  • the artificial wood manufacturing method between the second kneading step and the molding step using a pellet molding machine with a vacuum device heated to 170 ⁇ 200 °C gelled raw material through the second kneading step It provides a method for producing artificial wood using natural vegetable fiber, characterized in that it further comprises a; pelletizing step of producing a pellet of 2 ⁇ 3mm size.
  • FIG. 1 is a flow chart showing a method for manufacturing artificial wood using natural vegetable fiber according to an embodiment of the present invention.
  • a mixture of polypropylene (MAPP), titanate-based and zirconate-based silicone oil and silicone oil is mixed with a synthetic resin mixed with polypropylene or high-density polyethylene, ethylene vinyl acetate or linear low density polyethylene.
  • a binder coating step of coating the synthetic resin is
  • a second kneading step of kneading by adding one or more additives selected from the group consisting of a lubricant, an antioxidant, a UV stabilizer, a nucleating agent, a filler, and a pigment to the natural vegetable fiber powder which has undergone the first kneading step;
  • the step of adding an expanding agent and molding into an artificial wood product using an extrusion machine characterized in that it comprises a.
  • silicone oil is mixed with a binder selected from polypropylene (MAPP), titanate-based and zirconate-based maleates, in a synthetic resin containing polypropylene or high-density polyethylene, ethylene vinyl acetate or linear low density polyethylene.
  • a binder coating step of coating the synthetic resin the silicone oil not only makes the binder evenly coated on the synthetic resin, but also facilitates the kneading by improving the flow of the resin in the pelletization step or the molding step, thereby improving moldability and physical properties.
  • the content of the synthetic resin is less than the amount of natural vegetable fibrous powder in the above, when using the ethylene vinyl acetate or linear low-density polyethylene when processing in the pelletizing step or molding step to improve the flow of the mixture and facilitate uniform dispersion It is desirable to reduce the defective rate as well as to increase the physical properties (impact strength).
  • the synthetic resin is preferably 13 to 29 parts by weight of polypropylene or high density polyethylene and 3 to 11 parts by weight of ethylene vinyl acetate or linear low density polyethylene based on 100 parts by weight of artificial wood. More specifically, the synthetic resin is preferably a mixture of 20 to 70 parts by weight of ethylene vinyl acetate or linear low density polyethylene with respect to 100 parts by weight of polypropylene or high density polyethylene. In this case, it is preferable to use homo or impact polypropylene having a melt index of 7 to 15, and high density polyethylene preferably has a melt index of 2 to 10.
  • the ethylene vinyl acetate preferably has an acetic acid content of 3 to 21% (w / w), and the linear low density polyethylene preferably has a melt index of 1 to 4.
  • the synthetic resin is coated by mixing with a silicone oil and a binder selected from maleated polypropylene, titanate-based or zirconate-based. At this time, it is preferable to mix 16 to 40 parts by weight of synthetic resin, 0.8 to 3 parts by weight of binder and 0.2 to 0.5 parts by weight of silicone oil based on 100 parts by weight of artificial wood.
  • the binder is used to increase the binding force between the synthetic resin and the natural vegetable fiber powder.
  • the natural vegetable fibrous powder has a hydrophilic polarity and the synthetic resin has a hydrophobic nonpolarity, so the binding strength of the two materials is weak.
  • the interaction of these natural vegetable fiber powders with the synthetic resin is greatly improved by the addition of a binder, resulting in a new chemical bond at the interface between the two materials.
  • the binder of the present invention can be evenly dispersed in a large amount of natural vegetable fiber powder and a medium amount of synthetic resin even in a very small amount, and first mixed with a synthetic resin and then mixed with a large amount of natural vegetable fiber powder to increase dispersibility to the maximum. Can be.
  • the binder may also increase the bending strength, modulus of elasticity, and the like as well as improve the bonding strength between the natural vegetable fiber powder and the synthetic resin, and may improve dimensional stability, impact strength, and the like.
  • the size of the natural plant fiber powder is preferably 80 ⁇ 150mesh.
  • the use of sawdust has the advantage that can be used to obtain an artificial wood with excellent physical properties because it can utilize a uniform amount of fiber with the same ingredients, unlike the fiber content is not constant depending on the species.
  • natural vegetable fiber powder has an advantage that can be more light weight because the specific gravity is about 0.85 but the wood powder is 1.37. At this time, the ratio of the diameter to the particle length of the natural vegetable fiber powder is preferably 3: 1 to 5: 1.
  • the prepared natural vegetable fiber powder is dried.
  • the fiber powder is preferably dried so that the moisture content is less than 1% by weight. If the moisture content of the natural vegetable fiber powder is high, there is a possibility that the problem of not evenly kneading with the synthetic resin to be described later. More specifically, since a large amount of natural vegetable fiber powder is mixed compared to synthetic resins, the volume of the natural vegetable fiber powder is large. However, when the water content of the powder is high, the volume of the powder becomes larger, which may prevent uniform mixing.
  • the moisture content when the moisture content is high, it may be difficult to continuously proceed the process due to the static electricity generated in the natural vegetable fiber powder in the first kneading step, the second kneading step or the pelletizing step. In this case, not only the physical properties of the manufactured synthetic wood are lowered, but also a problem that the defective rate is increased in the pelletizing step or the molding step occurs. More specifically, when the water content of the natural vegetable fiber powder is high, carbonization may occur in the pelletizing or forming step, resulting in deterioration of physical properties or inability to flow in the mold, resulting in unmolding. Depression or smoothness may occur.
  • Specific examples of the method for drying the content of the prepared natural vegetable fiber powder to be less than 1% by weight include the first drying step of drying the natural vegetable fiber powder to a water content of less than 5% by weight at a temperature of 80 ⁇ 100 °C and There is a method of going through a secondary drying step of drying so that the water content is less than 1% by weight at a temperature of 100 ⁇ 130 °C.
  • the first drying step is preferably performed on the tunnel-type closed conveyor belt of 80 ⁇ 100 °C
  • the second drying step is preferably carried out for 7 to 15 minutes in a blender of 100 ⁇ 130 °C. Do.
  • the reason for this two-step drying step is that the initial moisture content of the natural vegetable fiber powder is 12 to 15%.
  • Desirable drying equipment to be used in the secondary drying step is preferably a structure that can automatically control the heat from the outside as a blender having a heating function therein. This drying facility can be completely mixed with the impeller can uniformly dry the natural vegetable fiber powder on the outside and inside.
  • the binder is coated with the synthetic resin and the natural vegetable fiber powder dried in the drying step.
  • the binder-coated synthetic resin is 13 to 29 parts by weight of polypropylene or high density polyethylene, 3 to 11 parts by weight of ethylene vinyl acetate or linear low density ethylene, 0.8 to 2.5 parts by weight of maleated polypropylene based on 100 parts by weight of artificial wood It is preferable that a binder selected from titanate-based and zirconate-based and 0.2-0.5 parts by weight of silicone oil are mixed.
  • Synthetic resin coated with the binder is evenly mixed with the dried natural vegetable fiber powder while being flexible in a blender at 80-110 ° C., resulting in a gel with evenly distributed natural vegetable fiber powder.
  • the additive is preferably added in an amount of 2 to 6 parts by weight based on 100 parts by weight of artificial wood.
  • the blender at 110 ⁇ 140 °C It is preferable to make a gel-like synthetic raw material by kneading by pressing and heating for 10 to 20 minutes in the mixture.
  • the additive is an important factor for the performance and processability (mixing, extrusion) of the natural vegetable fiber powder.
  • Natural vegetable fibrous powder often causes problems such as warping, cracking, discoloration and coloring, and is used as a structural material, so the role of additives to increase mechanical strength is very important. It is also essential for smoothing the surface of the composite and increasing yield while reducing product defects in the extrusion process.
  • the additive increases stability, serves as a preservative, enables weight reduction, and improves mechanical properties.
  • the natural vegetable fiber powder subjected to the first kneading step includes 0.2 to 1 parts by weight of lubricant, 0.1 to 0.3 parts by weight of antioxidant, 0.2 to 0.6 parts by weight of UV stabilizer, based on 100 parts by weight of artificial wood, It is preferable to add an additive including 0.3 to 0.7 parts by weight of a nucleating agent, 1 to 3 parts by weight of a filler, and 0.2 to 0.4 parts by weight of an inorganic pigment.
  • the lubricant may be added to improve the surface properties of the product by increasing the dispersibility of the natural vegetable fiber powder during kneading and molding because the high viscosity of the synthetic resin at high temperatures.
  • the lubricant one selected from the group consisting of fatty acids, acid amides, fluoropolymers, and hydrocarbons may be used.
  • the antioxidant may be added to prevent the natural vegetable fiber powder from receiving oxygen from the air, phenolic antioxidants are mainly used.
  • UV stabilizers may be added to block ultraviolet rays, one selected from the group consisting of benzotrizole-based, benzophenone-based, triamine-based may be used.
  • the nucleating agent may be added to shorten the molding cycle by improving the crystallization temperature at the same time to improve the physical properties such as the stiffness, heat deformation temperature of the synthetic resin (PP or PE) to refine the crystals
  • One is selected from the group consisting of acid metal salts, sorbitol-based and phosphate ester metal salts.
  • the filler may be added to improve the long-term deformation due to impact strength, bending strength, heat deformation temperature and load, it may be selected from the group consisting of calcium carbonate, talc, mica.
  • inorganic pigments are added to impart color to the present invention, and are mainly colored and colored on synthetic resins.
  • the binder mixed with the synthetic resin in the binder mixing step is an additive for increasing the binding force between the synthetic resin and the natural vegetable fiber powder, without separating the kneading step.
  • the binder is combined with the synthetic resin or the natural vegetable fiber powder before the other various additives (additives in the second kneading step) are first combined with the synthetic resin or the natural vegetable fiber powder, the bonding strength is lowered and the physical properties are reduced and uniform. This is because the dispersion is not dispersed so that the extrusion amount change in the pelletizing step or the forming step is severe and may cause mass defects.
  • the reason for the pelletization step as described above is that the amount of natural vegetable fiber powder is higher than that of the compounded synthetic resin. This is because it is difficult to uniformly disperse the powders and additives, which may cause not only physical properties but also deterioration of product quality (surface state, depression, color, etc.).
  • the moisture content of the natural vegetable fiber powder is lowered to less than 1% during the drying step, so that when the kneaded raw material is brought back into the stock, a problem of having to go through the previous step again due to moisture impregnation may occur. have.
  • the synthetic resin is coated on the natural vegetable fiber powder after the pelletization step, even if brought to inventory can be minimized moisture impregnation.
  • the expansion agent in the gelled raw material or pelletized raw material After mixing the expansion agent in the gelled raw material or pelletized raw material through the second kneading step, and heat-melting at 180 ⁇ 230 °C and molding into an artificial wood product containing a natural vegetable fiber powder using an extruder. More specifically, in the forming step, the expansion agent 0.86phr (Parts perhundred parts of Rubber) ⁇ 2.04phr based on the gelled raw material or pelletized raw material is mixed, and the mixed raw material is extruded with a heated vacuum apparatus There is a method of putting into a molding machine.
  • Parts perhundred parts of Rubber Parts perhundred parts of Rubber
  • the heating conditions of the extruder is set to 180 ⁇ 230 °C and heated and melted, passed through a die to convert into a continuum having a cross-section of the desired shape (plate, mold release, etc.), cooled, solidified, wound or cut can be have.
  • the swelling agent is to reduce the weight of the artificial wood product is to use a thermally expandable microspheres based on the acrylonitrile copolymer and containing a low boiling hydrocarbon.
  • This is a mechanical expansion method, not a chemical foaming agent or a gas foaming method that expands only to synthetic resins, and is an expansion method that has little relationship with the content of synthetic resins and is less affected by external conditions such as temperature and humidity.
  • Synthetic wood of the present invention according to the manufacturing method can be extruded according to the site in the form of a plate or a release shape, despite the synthetic resin contained 16 to 40% by weight, such as the strength (physical properties) and touch like natural wood Have

Abstract

The present invention relates to a method for preparing artificial wood using a natural vegetable fibroid material, and more specifically, to a preparation method of artificial wood comprising: the binder coating step of mixing a synthetic resin comprising polypropylene or high density polyethylene, and ethylene-vinyl acetate or linear low density polyethylene with a binder selected from maleated polypropylene (MAPP), a titanate-based binder and a zirconia-based binder and a silicone oil; the drying step of drying one or more natural vegetable fibroid powders selected from the group consisting of waste paper, rice straw, corn stalks, African millet stalks, hemp, coffee husks, coconut leaves, sugarcane dregs and green tea dregs; the first mixing step of mixing the binder-coated synthetic resin and the natural vegetable fibroid powders dried at the drying step; the second mixing step of adding one or more additives selected from the group consisting of a lubricant, an antioxidizing agent, a UV stabilizer, a nucleating agent, a filler and an inorganic pigment to the natural vegetable fibroid powders from the first mixing step to mix the mixture; and the molding step of adding a swelling agent and molding the mixture into synthetic wood using an extrusion molding machine. Artificial wood which is light and can maintain a strength (physical property) similar to that of natural wood by remarkably reducing the content of a synthetic resin which is heavy and has a high toxic gas production rate in case of a fire is provided, by employing the method for preparing artificial wood using a natural vegetable fibroid material of the present invention.

Description

천연 식물성 섬유질을 이용한 인조목재 제조방법Manufacturing method of artificial wood using natural vegetable fiber
본 발명은 천연 식물성 섬유질을 이용한 인조목재 제조방법에 관한 것으로, 보다 상세하게는 합성수지의 함량을 획기적으로 줄임으로써 화재발생시 유해한 가스발생률이 감소되고, 천연 식물성 섬유질이 다량 포함되어 무게가 가벼우면서도 천연목재와 같은 질감을 가지는 천연 식물성 섬유질을 이용한 인조목재 제조방법에 대한 것이다.The present invention relates to a method for manufacturing artificial wood using natural vegetable fiber, and more particularly, by reducing the amount of synthetic resin, the gas generation rate is reduced in the event of a fire, and natural vegetable fiber contains a large amount of natural wood, but light weight natural wood It relates to a method for manufacturing artificial wood using natural vegetable fiber having the same texture.
일반적으로 천연목재는 경제적이고, 비중이 비교적 작으며 가공하기가 용이하여 산업전반에 걸쳐 다양한 용도로 사용되고 있다. 하지만 천연목재는 내습성, 내오염성, 내부식성이 약한 단점이 있다. Generally, natural wood is economical, has a relatively small specific gravity, and is easy to process, and is used for various purposes throughout the industry. However, natural wood has the disadvantages of poor moisture resistance, pollution resistance and corrosion resistance.
이에 이를 해결하고자, 톱밥 또는 나무조각을 합성수지와 혼합시킨 인조목재를 제조하고자 하였다. 하지만 상기 톱밥 또는 나무조각을 포함하는 인조목재는 천연목재와 같은 물성을 유지하기 위해서는 60중량% 이상의 합성수지를 포함시켜야 한다. 그러나, 합성수지가 60중량% 이상 포함된 합성목재는 무게가 무겁고, 수지함량이 높기 때문에 가격 경쟁력에도 불리하며, 화재 발생시 유해가스를 대량 방출할 수 있는 위험이 있다. In order to solve this problem, it was intended to manufacture artificial wood mixed with sawdust or wood chips and synthetic resin. However, artificial wood containing the sawdust or wood chips should include more than 60% by weight of synthetic resin to maintain the same properties as natural wood. However, synthetic wood containing more than 60% by weight of synthetic resin is heavy weight, high resin content, and also disadvantageous price competitiveness, there is a risk that can release a large amount of harmful gas in the event of fire.
상기 문제점을 해결하기 위한 본 발명은 합성수지의 함량을 획기적으로 줄이고도 천연목재와 유사한 강도(물성)를 유지할 수 있는 천연 식물성 섬유질을 이용한 인조목재 제조방법을 제공하고자 한다. The present invention for solving the above problems is to provide a method for manufacturing artificial wood using natural vegetable fiber that can maintain the strength (physical properties) similar to natural wood even significantly reducing the content of synthetic resin.
이에 본 발명은 바람직한 제1구현예로서, 폴리프로필렌 또는 고밀도폴리에틸렌과, 에틸렌비닐아세테이트 또는 선형저밀도폴리에틸렌을 혼합한 합성수지에 말레이트 처리된 폴리프로필렌(MAPP), 티탄산염계 및 지르콘산염계 중에서 선택된 1종의 결합제와 실리콘오일을 혼합하여 상기 합성수지를 코팅하는 결합제 코팅단계; 폐지, 볏짚, 옥수수대, 수수대, 마, 커피껍질, 야자수잎, 사탕수수찌꺼기 및 녹차찌꺼기로 구성된 군으로부터 선택된 하나이상의 천연식물성 섬유질 분말을 건조하는 건조단계; 상기 결합제가 코팅된 합성수지와 상기 건조단계에서 건조된 천연식물성 섬유질 분말을 함께 혼련하는 제1혼련단계; 상기 제1혼련단계를 거친 혼합물에 윤활제, 항산화제, UV안정제, 조핵제, 충진제 및 무기안료로 구성된 군으로부터 선택된 하나 이상의 첨가제를 첨가하여 혼련하는 제2혼련단계; 및 팽창제를 첨가하고 압출성형기를 이용하여 인조목재 제품으로 성형하는 성형단계;를 포함하는 천연 식물성 섬유질을 이용한 인조목재 제조방법을 제공한다. Accordingly, the present invention provides a preferred embodiment, selected from polypropylene (MAPP), titanate and zirconate based on maleate treated synthetic resin mixed with polypropylene or high density polyethylene, ethylene vinyl acetate or linear low density polyethylene. A binder coating step of coating the synthetic resin by mixing a species of binder and silicon oil; A drying step of drying one or more natural vegetable fiber powders selected from the group consisting of waste paper, rice straw, corn stalks, sorghum, hemp, coffee bark, palm fronds, sugarcane grounds and green tea grounds; A first kneading step of kneading the binder-coated synthetic resin and the natural vegetable fiber powder dried in the drying step together; A second kneading step of kneading by adding one or more additives selected from the group consisting of a lubricant, an antioxidant, a UV stabilizer, a nucleating agent, a filler, and an inorganic pigment to the mixture that has passed through the first kneading step; It provides an artificial wood manufacturing method using natural vegetable fibers, including; forming step of adding an expanding agent and molding into an artificial wood product using an extrusion molding machine.
상기 구현예에 의한 인조목재 제조방법에서, 건조단계는 80~100℃에서 천연식물성 섬유질 분말의 함수율이 5중량% 미만이 되도록 건조하는 1차 건조단계; 및 100~130℃에서 천연식물성 섬유질 분말의 함수율이 1중량% 미만이 되도록 건조하는 2차 건조단계;를 포함하는 것인 천연 식물성 섬유질을 이용한 인조목재 제조방법을 제공한다. In the artificial wood manufacturing method according to the embodiment, the drying step is the first drying step of drying so that the moisture content of the natural vegetable fiber powder at 80 ~ 100 ℃ less than 5% by weight; It provides a method for producing artificial wood using natural vegetable fiber comprising; and a second drying step of drying so that the water content of the natural vegetable fiber powder is less than 1% by weight at 100 ~ 130 ℃.
상기 구현예에 의한 인조목재 제조방법에서, 결합제 코팅단계에서의 합성수지는 인조목재 총 100 중량부에 대하여 폴리프로필렌 또는 고밀도 폴리에틸렌 13~29 중량부 및 에틸렌비닐아세테이트 또는 선형저밀도 폴리에틸렌 3~11중량부를 포함하는 것인 천연 식물성 섬유질을 이용한 인조목재 제조방법을 제공한다. In the artificial wood manufacturing method according to the embodiment, the synthetic resin in the binder coating step comprises 13 to 29 parts by weight of polypropylene or high density polyethylene and 3 to 11 parts by weight of ethylene vinyl acetate or linear low density polyethylene based on a total of 100 parts by weight of artificial wood It provides a method for producing artificial wood using natural vegetable fiber.
상기 구현예에 의한 인조목재 제조방법에서, 결합제 코팅단계에서의 폴리프로필렌은 용융지수가 7~15인 호모 또는 충격 폴리프로필렌인 천연 식물성 섬유질을 이용한 인조목재 제조방법을 제공한다. In the method of manufacturing artificial wood according to the above embodiment, the polypropylene in the binder coating step provides a method of manufacturing artificial wood using natural vegetable fibers of homopoly or impact polypropylene having a melt index of 7 to 15.
상기 구현예에 의한 인조목재 제조방법에서, 결합제 코팅단계에서의 고밀도 폴리에틸렌은 용융지수가 2~10인 천연 식물성 섬유질을 이용한 인조목재 제조방법을 제공한다. In the artificial wood manufacturing method according to the embodiment, the high-density polyethylene in the binder coating step provides an artificial wood manufacturing method using natural vegetable fibers having a melt index of 2 ~ 10.
상기 구현예에 의한 인조목재 제조방법에서, 결합제 코팅단계에서의 선형저밀도 폴리에틸렌은 용융지수가 1~4인 천연 식물성 섬유질을 이용한 인조목재 제조방법을 제공한다. In the artificial wood manufacturing method according to the embodiment, the linear low-density polyethylene in the binder coating step provides an artificial wood manufacturing method using natural vegetable fibers having a melt index of 1-4.
상기 구현예에 의한 인조목재 제조방법에서, 상기 결합제 코팅단계에서는 인조목재 총 100 중량부에 대하여 합성수지 16~40 중량부, 결합제 0.8~3 중량부 및 실리콘오일 0.2~0.5중량부를 혼합하는 것인 천연 식물성 섬유질을 이용한 인조목재 제조방법을 제공한다. In the artificial wood manufacturing method according to the embodiment, the binder coating step is to mix 16 to 40 parts by weight of synthetic resin, 0.8 to 3 parts by weight of binder and 0.2 to 0.5 parts by weight of silicone oil based on 100 parts by weight of artificial wood Provided is a method for preparing artificial wood using vegetable fiber.
상기 구현예에 의한 인조목재 제조방법에서, 제1혼련단계에서는 인조목재 총 100 중량부에 대하여 결합제가 코팅된 합성수지 16~40 중량부 및 건조단계에서 건조된 천연식물성 섬유질 분말 50~75 중량부를 배합하는 것인 천연 식물성 섬유질을 이용한 인조목재 제조방법을 제공한다. In the method of manufacturing artificial wood according to the embodiment, in the first kneading step, 16 to 40 parts by weight of the synthetic resin coated with a binder and 50 to 75 parts by weight of the natural vegetable fiber powder dried in the drying step are added to 100 parts by weight of the artificial wood. It provides a method for producing artificial wood using natural vegetable fiber.
상기 구현예에 의한 인조목재 제조방법에서, 제1혼련단계는 80~110℃에서 7~15분간 혼련하는 것인 천연 식물성 섬유질을 이용한 인조목재 제조방법을 제공한다. In the artificial wood manufacturing method according to the embodiment, the first kneading step provides a method for manufacturing artificial wood using natural vegetable fiber that is kneaded at 80 ~ 110 ℃ for 7 to 15 minutes.
상기 구현예에 의한 인조목재 제조방법에서, 제2혼련단계에서 첨가되는 첨가제의 함량은 인조목재 총 100 중량부에 대하여 2~6중량부인 천연 식물성 섬유질을 이용한 인조목재 제조방법을 제공한다. In the artificial wood manufacturing method according to the embodiment, the content of the additive added in the second kneading step provides an artificial wood manufacturing method using natural vegetable fiber which is 2 to 6 parts by weight based on 100 parts by weight of the total artificial wood.
상기 구현예에 의한 인조목재 제조방법에서, 상기 제2혼련단계에서 첨가되는 첨가제는 인조목재 총 100 중량부에 대하여 0.2~1 중량부의 윤활제, 0.1~0.3 중량부의 항산화제, 0.2~0.6 중량부의 UV안정제, 0.3~0.7 중량부의 조핵제, 1~3 중량부의 충진제, 0.2~0.4 중량부의 무기안료를 포함하는 것일 수 있다. In the artificial wood manufacturing method according to the embodiment, the additive added in the second kneading step is 0.2 to 1 parts by weight of lubricant, 0.1 to 0.3 parts by weight of antioxidant, 0.2 to 0.6 parts by weight of UV based on 100 parts by weight of artificial wood It may include a stabilizer, 0.3 to 0.7 parts by weight of nucleating agent, 1 to 3 parts by weight of filler, 0.2 to 0.4 parts by weight of inorganic pigment.
상기 구현예에 의한 인조목재 제조방법에서, 제2혼련단계는 110~140℃에서 10~20분간 혼련하는 것인 천연 식물성 섬유질을 이용한 인조목재 제조방법을 제공한다. In the method of manufacturing artificial wood according to the embodiment, the second kneading step provides a method of manufacturing artificial wood using natural vegetable fiber, which is kneaded at 110 to 140 ° C. for 10 to 20 minutes.
상기 구현예에 의한 인조목재 제조방법에서, 성형단계에서는 180~230℃로 가열된 압출성형기로 성형하는 것인 천연 식물성 섬유질을 이용한 인조목재 제조방법을 제공한다. In the artificial wood manufacturing method according to the embodiment, the molding step provides an artificial wood manufacturing method using natural vegetable fibers that are molded by an extrusion molding machine heated to 180 ~ 230 ℃.
상기 구현예에 의한 인조목재 제조방법에서, 제2혼련단계와 성형단계의 사이에 상기 제2혼련단계를 통하여 겔화된 원료를 170~200℃로 가열된 진공장치가 부착된 펠렛용 성형기를 이용하여 2~3mm 크기의 펠렛으로 제조하는 펠렛화 단계;를 더 포함하는 것을 특징으로 하는 천연 식물성 섬유질을 이용한 인조목재 제조방법을 제공한다. In the artificial wood manufacturing method according to the embodiment, between the second kneading step and the molding step using a pellet molding machine with a vacuum device heated to 170 ~ 200 ℃ gelled raw material through the second kneading step It provides a method for producing artificial wood using natural vegetable fiber, characterized in that it further comprises a; pelletizing step of producing a pellet of 2 ~ 3mm size.
본 발명의 제조방법에 의하면 무게가 무겁고 화재발생시 유해한 가스발생률이 높은 합성수지의 함량을 획기적으로 줄여 가벼우면서도 천연목재와 유사한 강도(물성)를 유지할 수 있는 천연 식물성 섬유질을 이용한 합성목재를 제공할 수 있다. According to the production method of the present invention, it is possible to provide a synthetic wood using natural vegetable fiber that can maintain the strength (physical properties) similar to natural wood, while lightly reducing the content of synthetic resin, which is heavy in weight and has a high rate of harmful gases during fire. .
도 1은 본 발명의 일 실시예에 따른 천연 식물성 섬유질을 이용한 인조목재 제조방법을 나타내는 흐름도이다. 1 is a flow chart showing a method for manufacturing artificial wood using natural vegetable fiber according to an embodiment of the present invention.
본 발명에 따른 천연 식물성 섬유질로 제조된 합성목재의 제조방법은, Method for producing a synthetic wood made from natural vegetable fibers according to the present invention,
1. 폴리프로필렌 또는 고밀도폴리에틸렌과, 에틸렌비닐아세테이트 또는 선형저밀도폴리에틸렌을 혼합한 합성수지에 말레이트 처리된 폴리프로필렌(MAPP), 티탄산염계 및 지르콘산염계 중에서 선택된 1종의 결합제와 실리콘오일을 혼합하여 상기 합성수지를 코팅하는 결합제 코팅단계; 1. A mixture of polypropylene (MAPP), titanate-based and zirconate-based silicone oil and silicone oil is mixed with a synthetic resin mixed with polypropylene or high-density polyethylene, ethylene vinyl acetate or linear low density polyethylene. A binder coating step of coating the synthetic resin;
2. 폐지, 볏짚, 옥수수대, 수수대, 마, 커피껍질, 야자수잎, 사탕수수찌꺼기 및 녹차찌꺼기로 구성된 군으로부터 선택된 하나 이상의 천연식물성 섬유질 분말을 건조하는 건조단계; 2. Drying step of drying at least one natural vegetable fibrous powder selected from the group consisting of waste paper, rice straw, corn stalks, sorghum, hemp, coffee skin, palm fronds, sugar cane grounds and green tea grounds;
3. 상기 결합제가 코팅된 합성수지와 상기 건조단계에서 건조된 천연식물성 섬유질 분말을 함께 혼련하는 제1혼련단계; 3. a first kneading step of kneading the binder-coated synthetic resin and the natural vegetable fiber powder dried in the drying step together;
4. 상기 제1혼련단계를 거친 천연식물성 섬유질 분말에 윤활제, 항산화제, UV안정제, 조핵제, 충진제 및 안료로 구성된 군으로부터 선택된 하나 이상의 첨가제를 첨가하여 혼련하는 제2혼련단계; 및 4. a second kneading step of kneading by adding one or more additives selected from the group consisting of a lubricant, an antioxidant, a UV stabilizer, a nucleating agent, a filler, and a pigment to the natural vegetable fiber powder which has undergone the first kneading step; And
5. 팽창제를 첨가하고 압출성형기를 이용하여 인조목재 제품으로 성형하는 성형단계;를 포함하는 것을 특징으로 한다. 5. The step of adding an expanding agent and molding into an artificial wood product using an extrusion machine; characterized in that it comprises a.
이하 본 발명을 상세히 설명한다. Hereinafter, the present invention will be described in detail.
1. 결합제 코팅단계1. Binder Coating Step
먼저, 폴리프로필렌 또는 고밀도폴리에틸렌과, 에틸렌비닐아세테이트 또는 선형저밀도폴리에틸렌을 혼합한 합성수지에 말레이트 처리된 폴리프로필렌(MAPP), 티탄산염계 및 지르콘산염계 중에서 선택된 1종의 결합제와 실리콘오일을 혼합하여 상기 합성수지를 코팅하는 결합제 코팅단계이다. 이때, 실리콘 오일은 합성수지에 결합제가 골고루 코팅되게 할 뿐 아니라 펠렛화 단계 또는 성형단계에서 수지의 흐름을 좋게 하여 혼련을 용이하게 하므로 성형성 및 물성을 양호하게 하는 효과가 있다. First, silicone oil is mixed with a binder selected from polypropylene (MAPP), titanate-based and zirconate-based maleates, in a synthetic resin containing polypropylene or high-density polyethylene, ethylene vinyl acetate or linear low density polyethylene. A binder coating step of coating the synthetic resin. In this case, the silicone oil not only makes the binder evenly coated on the synthetic resin, but also facilitates the kneading by improving the flow of the resin in the pelletization step or the molding step, thereby improving moldability and physical properties.
또한, 상기에서 다량의 천연식물성 섬유질 분말에 비해 혼합되는 합성수지의 함량은 적은데 펠렛화 단계 또는 성형단계에서 가공시 에틸렌비닐아세테이트 또는 선형저밀도 폴리에틸렌을 사용하는 경우 혼합물의 흐름을 좋게하고 균일한 분산을 용이하게 하여 불량률을 줄일 수 있을 뿐 아니라 물성(충격강도)을 높일 수 있어 바람직하다. In addition, the content of the synthetic resin is less than the amount of natural vegetable fibrous powder in the above, when using the ethylene vinyl acetate or linear low-density polyethylene when processing in the pelletizing step or molding step to improve the flow of the mixture and facilitate uniform dispersion It is desirable to reduce the defective rate as well as to increase the physical properties (impact strength).
상기에서, 합성수지는 인조목재 총 100 중량부에 대하여 폴리프로필렌 또는 고밀도 폴리에틸렌 13~29중량부 및 에틸렌비닐아세테이트 또는 선형저밀도 폴리에틸렌 3~11중량부를 혼합한 것이 바람직하다. 보다 구체적으로는 합성수지는 폴리프로필렌 또는 고밀도 폴리에틸렌 100 중량부에 대하여 20~70중량부의 에틸렌비닐아세테이트 또는 선형저밀도 폴리에틸렌을 혼합한 것이 바람직하다. 이때, 폴리프로필렌은 용융지수가 7~15인 호모 또는 충격 폴리프로필렌을 사용하는 것이 바람직하고, 고밀도 폴리에틸렌은 용융지수가 2~10인 것이 바람직하다. 또한, 에틸렌비닐아세테이트는 초산 함량이 3~21%(w/w)인 것이 바람직하고, 선형저밀도 폴리에틸렌은 용융지수가 1~4인 것이 바람직하다. In the above, the synthetic resin is preferably 13 to 29 parts by weight of polypropylene or high density polyethylene and 3 to 11 parts by weight of ethylene vinyl acetate or linear low density polyethylene based on 100 parts by weight of artificial wood. More specifically, the synthetic resin is preferably a mixture of 20 to 70 parts by weight of ethylene vinyl acetate or linear low density polyethylene with respect to 100 parts by weight of polypropylene or high density polyethylene. In this case, it is preferable to use homo or impact polypropylene having a melt index of 7 to 15, and high density polyethylene preferably has a melt index of 2 to 10. In addition, the ethylene vinyl acetate preferably has an acetic acid content of 3 to 21% (w / w), and the linear low density polyethylene preferably has a melt index of 1 to 4.
상기 합성수지는 말레이트 처리된 폴리프로필렌, 티탄산염계 또는 지르콘산염계 중에서 선택된 결합제 및 실리콘 오일과 혼합하여 코팅된다. 이때, 인조목재 총 100 중량부에 대하여 16~40 중량부의 합성수지, 0.8~3 중량부의 결합제 및 0.2~0.5 중량부의 실리콘오일을 혼합하는 것이 바람직하다. The synthetic resin is coated by mixing with a silicone oil and a binder selected from maleated polypropylene, titanate-based or zirconate-based. At this time, it is preferable to mix 16 to 40 parts by weight of synthetic resin, 0.8 to 3 parts by weight of binder and 0.2 to 0.5 parts by weight of silicone oil based on 100 parts by weight of artificial wood.
상기 결합제는 합성수지와 천연 식물성 섬유질 분말의 결합력을 높이기 위해서 사용하는 것이다. 원칙적으로 천연 식물성 섬유질 분말은 친수성인 극성을 나타내고 합성수지는 소수성인 비극성을 나타내므로 두 물질의 결합력은 약하다. 이러한 천연 식물성 섬유질 분말과 합성수지의 상호작용은 결합제의 첨가에 의해 두 물질 사이의 계면에서 새로운 화학적 결합을 일으켜 크게 개선된다. 또한, 본 발명의 결합제는 극소량으로도 다량의 천연 식물성 섬유질 분말과 중간량의 합성수지에 골고루 분산이 가능한 것으로, 합성 수지와 먼저 혼합한 후 다량의 천연 식물성 섬유질 분말을 혼합하여 분산성을 최대한으로 높일 수 있다. 상기 결합제는 또한, 천연 식물성 섬유질 분말과 합성 수지간의 결합력 개선뿐만 아니라 굽힘강도, 탄성계수 등을 증가시키고, 치수안정성, 충격강도 등을 향상시킬 수 있다. The binder is used to increase the binding force between the synthetic resin and the natural vegetable fiber powder. In principle, the natural vegetable fibrous powder has a hydrophilic polarity and the synthetic resin has a hydrophobic nonpolarity, so the binding strength of the two materials is weak. The interaction of these natural vegetable fiber powders with the synthetic resin is greatly improved by the addition of a binder, resulting in a new chemical bond at the interface between the two materials. In addition, the binder of the present invention can be evenly dispersed in a large amount of natural vegetable fiber powder and a medium amount of synthetic resin even in a very small amount, and first mixed with a synthetic resin and then mixed with a large amount of natural vegetable fiber powder to increase dispersibility to the maximum. Can be. The binder may also increase the bending strength, modulus of elasticity, and the like as well as improve the bonding strength between the natural vegetable fiber powder and the synthetic resin, and may improve dimensional stability, impact strength, and the like.
2. 건조단계2. Drying Step
폐지, 볏짚, 옥수수대, 수수대, 마, 커피껍질, 야자수잎, 사탕수수찌꺼기 및 녹차찌꺼기 등으로 구성된 군에서 선택된 하나 이상의 천연식물성 섬유질 분말을 준비한다. 상기 천연식물성 섬유질 분말의 크기는 80~150mesh인 것이 바람직하다. 천연식물성 섬유질 분말을 사용하는 경우, 톱밥을 사용하면 수종에 따라서 섬유질의 함량이 일정하지 않은 것과는 달리 동일한 성분으로 균일한 함량의 섬유질을 활용할 수 있어 물성이 우수한 인조목재를 얻을 수 있다는 장점이 있다. 또한 천연식물성 섬유질 분말은 진비중이 0.85 정도이나 목분은 1.37이므로 보다 경량화가 가능한 장점이 있다. 이때, 천연 식물성 섬유질 분말의 파티클 길이 대비 직경의 비는 3:1 ~ 5:1인 것이 바람직하다. Prepare at least one natural plant fiber powder selected from the group consisting of waste paper, rice straw, corn stalks, sorghum, hemp, coffee skin, palm fronds, sugar cane waste and green tea dregs. The size of the natural plant fiber powder is preferably 80 ~ 150mesh. In the case of using the natural vegetable fiber powder, the use of sawdust has the advantage that can be used to obtain an artificial wood with excellent physical properties because it can utilize a uniform amount of fiber with the same ingredients, unlike the fiber content is not constant depending on the species. In addition, natural vegetable fiber powder has an advantage that can be more light weight because the specific gravity is about 0.85 but the wood powder is 1.37. At this time, the ratio of the diameter to the particle length of the natural vegetable fiber powder is preferably 3: 1 to 5: 1.
그리고, 상기 준비된 천연식물성 섬유질 분말을 건조한다. 이때, 상기 섬유질 분말은 함수율이 1중량% 미만이 되도록 건조하는 것이 바람직하다. 천연식물성 섬유분말의 함수율이 높으면 후술할 합성수지와 고르게 혼련되지 못하는 문제가 발생할 우려가 있다. 보다 구체적으로는 합성수지에 비해 다량의 천연식물성 섬유 분말을 혼합하기 때문에 천연식물성 섬유 분말의 부피가 큰데, 분말의 함수율이 높으면 분말의 부피가 더 커져 균일하게 섞이지 못할 우려가 있다. 또한, 함수율이 높으면 제1혼련단계, 제2혼련단계 또는 펠렛화 단계에서 천연식물성 섬유분말에서 발생하는 정전기로 인해 공정을 연속적으로 진행하기에 어려움이 발생할 수 있다. 이와 같은 경우 제조되는 합성목재의 물성이 저하될 뿐 아니라 펠렛화 단계 또는 성형단계에서 불량률이 높아지는 문제가 발생한다. 더욱 구체적으로는 천연식물성 섬유질 분말의 함수율이 높을 경우 펠렛화 단계 또는 성형단계에서 탄화현상이 발생하여 물성저하가 발생하거나 금형에서 흐름이 원활하지 못하여 미성형이 되는 현상이 발생할 수 있고 완제품의 표면이 함몰되거나 매끄럽지 못하게 되는 현상이 발생할 수 있다. Then, the prepared natural vegetable fiber powder is dried. At this time, the fiber powder is preferably dried so that the moisture content is less than 1% by weight. If the moisture content of the natural vegetable fiber powder is high, there is a possibility that the problem of not evenly kneading with the synthetic resin to be described later. More specifically, since a large amount of natural vegetable fiber powder is mixed compared to synthetic resins, the volume of the natural vegetable fiber powder is large. However, when the water content of the powder is high, the volume of the powder becomes larger, which may prevent uniform mixing. In addition, when the moisture content is high, it may be difficult to continuously proceed the process due to the static electricity generated in the natural vegetable fiber powder in the first kneading step, the second kneading step or the pelletizing step. In this case, not only the physical properties of the manufactured synthetic wood are lowered, but also a problem that the defective rate is increased in the pelletizing step or the molding step occurs. More specifically, when the water content of the natural vegetable fiber powder is high, carbonization may occur in the pelletizing or forming step, resulting in deterioration of physical properties or inability to flow in the mold, resulting in unmolding. Depression or smoothness may occur.
상기 준비된 천연식물성 섬유질 분말의 함량이 1중량% 미만이 되도록 건조하는 방법의 구체적 일례로는 천연식물성 섬유질 분말을 80~100℃의 온도에서 함수율이 5중량% 미만이 되도록 건조하는 1차 건조단계 및 100~130℃의 온도에서 함수율이 1중량% 미만이 되도록 건조하는 2차 건조단계를 거치는 방법이 있다. 여기서, 특별히 제한되지는 않으나 1차 건조단계는 80~100℃의 터널형 밀폐 콘베이어 벨트 위에서 수행되는 것이 바람직하고, 2차 건조단계는 100~130℃의 배합기에서 7~15분 동안 수행되는 것이 바람직하다. 이와 같이 건조단계를 2단계를 거치는 이유는 천연 식물성 섬유질 분말의 초기 함수율이 12~15%인데, 터널형 밀폐 콘베이어 벨트식 건조기에서 한번에 1%까지 함수율을 낮추는 것은 불가능할 뿐만 아니라 아무리 밀봉을 잘했다 하더라도 습기가 침투하기 때문이다. 상기 2차 건조단계에서 사용되기에 바람직한 건조설비는 내부에 가열기능이 있는 배합기로서 외부에서열을 자동으로 조절할 수 있는 구조인 것이 바람직하다. 이러한 건조설비는 임펠라로 완전히 혼합하는 것이 가능하므로 바깥과 속의 천연식물성 섬유질 분말을 균일하게 건조할 수 있다. Specific examples of the method for drying the content of the prepared natural vegetable fiber powder to be less than 1% by weight include the first drying step of drying the natural vegetable fiber powder to a water content of less than 5% by weight at a temperature of 80 ~ 100 ℃ and There is a method of going through a secondary drying step of drying so that the water content is less than 1% by weight at a temperature of 100 ~ 130 ℃. Here, although not particularly limited, the first drying step is preferably performed on the tunnel-type closed conveyor belt of 80 ~ 100 ℃, the second drying step is preferably carried out for 7 to 15 minutes in a blender of 100 ~ 130 ℃. Do. The reason for this two-step drying step is that the initial moisture content of the natural vegetable fiber powder is 12 to 15%. In a tunnel-type closed conveyor belt dryer, it is not only possible to lower the moisture content to 1% at a time, but even if it is well sealed Because it penetrates. Desirable drying equipment to be used in the secondary drying step is preferably a structure that can automatically control the heat from the outside as a blender having a heating function therein. This drying facility can be completely mixed with the impeller can uniformly dry the natural vegetable fiber powder on the outside and inside.
3. 제1혼련단계3. First kneading stage
상기 결합제가 코팅된 합성수지와 상기 건조단계에서 건조된 천연식물성 섬유질 분말을 혼련하는 단계이다. 이때, 인조목재 총 100 중량부에 대하여 결합제가 코팅된 합성수지 16~40 중량부 및 건조단계에서 건조된 천연식물성 섬유질 분말 50~75중량부를 배합하는 것이 바람직하다. 보다 구체적으로는 인조목재 총 100 중량부에 대하여 상기 결합제가 혼합된 합성수지 16~40중량부를 상기 건조단계에서 건조된 천연식물성 섬유분말 50~75중량부와 함께 80~110℃의 수퍼 배합기에서 7~15분간 가압 및 가열하여 혼련하는 것이 바람직하다. The binder is coated with the synthetic resin and the natural vegetable fiber powder dried in the drying step. At this time, it is preferable to combine 16 to 40 parts by weight of the synthetic resin coated with a binder and 50 to 75 parts by weight of the natural vegetable fiber powder dried in the drying step based on 100 parts by weight of the artificial wood. More specifically, 16 to 40 parts by weight of the synthetic resin in which the binder is mixed with respect to 100 parts by weight of artificial wood, together with 50 to 75 parts by weight of the natural vegetable fiber powder dried in the drying step, 7 ~ 7 ~ in a super blender at 80 ~ 110 ℃ It is preferable to knead | mix and pressurize and heat for 15 minutes.
상기 결합제가 코팅된 합성수지는 인조목재 총 100 중량부에 대하여 13~29중량부의 폴리프로필렌 또는 고밀도폴리에틸렌, 3~11중량부의 에틸렌비닐아세테이트 또는 선형저밀도에틸렌, 0.8~2.5중량부의 말레이트 처리된 폴리프로필렌, 티탄산염계 및 지르콘산염계 중에서 선택된 결합제 및 0.2~0.5중량부의 실리콘 오일이 혼합된 것이 바람직하다. The binder-coated synthetic resin is 13 to 29 parts by weight of polypropylene or high density polyethylene, 3 to 11 parts by weight of ethylene vinyl acetate or linear low density ethylene, 0.8 to 2.5 parts by weight of maleated polypropylene based on 100 parts by weight of artificial wood It is preferable that a binder selected from titanate-based and zirconate-based and 0.2-0.5 parts by weight of silicone oil are mixed.
상기 결합제가 코팅된 합성수지는 80~110℃의 배합기에서 유연해지면서 건조된 천연식물성 섬유분말과 함께 고르게 섞여지며, 그 결과 천연식물성 섬유분말이 고르게 분포된 겔이 만들어진다. Synthetic resin coated with the binder is evenly mixed with the dried natural vegetable fiber powder while being flexible in a blender at 80-110 ° C., resulting in a gel with evenly distributed natural vegetable fiber powder.
4. 제2혼련단계4. The second kneading stage
제1혼련단계를 거친 천연식물성 섬유질 분말에 윤활제, 항산화제, UV안정제, 조핵제, 충진제, 안료로 구성된 군으로부터 선택된 하나 이상의 첨가제를 첨가하여 혼련하는 단계이다. 이때, 첨가제는 인조목재 총 100 중량부에 대하여 2~6중량부의 양으로 첨가되는 것이 바람직하다. 보다 구체적으로는 인조목재 총 100 중량부에 대하여 2~6중량부의 윤활제, 항산화제, UV안정제, 조핵제, 충진제, 안료로 구성된 군으로부터 선택된 하나 이상의 첨가제를 첨가한 후, 110~140℃의 배합기에서 10~20분간 가압 및 가열하여 혼련함으로써 겔상의 합성원료를 만드는 것이 바람직하다. It is a step of kneading by adding one or more additives selected from the group consisting of a lubricant, an antioxidant, a UV stabilizer, a nucleating agent, a filler, and a pigment to the natural vegetable fiber powder which has undergone the first kneading step. At this time, the additive is preferably added in an amount of 2 to 6 parts by weight based on 100 parts by weight of artificial wood. More specifically, after adding at least one additive selected from the group consisting of 2-6 parts by weight of lubricant, antioxidant, UV stabilizer, nucleating agent, filler, pigment based on 100 parts by weight of artificial wood, the blender at 110 ~ 140 ℃ It is preferable to make a gel-like synthetic raw material by kneading by pressing and heating for 10 to 20 minutes in the mixture.
상기 첨가제는 천연식물성 섬유질 분말의 성능과 가공성(배합, 압출)에 중요한 인자이다. 천연식물성 섬유질 분말은 종종 뒤틀림, 갈라짐, 변색, 착색 등의 문제가 발생하고, 구조재로서 이용되므로 기계적인 강도를 증가시키는 첨가제의 역할은 매우 중요하다. 또한, 압출공정에서 제품의 불량을 감소시키면서 복합재의 표면을 매끄럽게 만들고 생산량을 증대시키는데 필수적이다. 본 발명에서 상기 첨가제는 안정성을 높이고, 보존제 역할을 하며 경량화를 가능하게 하고 기계적 성질을 개선하는 역할 등을 한다. The additive is an important factor for the performance and processability (mixing, extrusion) of the natural vegetable fiber powder. Natural vegetable fibrous powder often causes problems such as warping, cracking, discoloration and coloring, and is used as a structural material, so the role of additives to increase mechanical strength is very important. It is also essential for smoothing the surface of the composite and increasing yield while reducing product defects in the extrusion process. In the present invention, the additive increases stability, serves as a preservative, enables weight reduction, and improves mechanical properties.
본 발명의 바람직한 구체적 일례로서, 제1혼련단계를 거친 천연식물성 섬유분말에는 인조목재 총 100 중량부에 대하여 0.2~1중량부의 윤활제, 0.1~0.3중량부의 항산화제, 0.2~0.6중량부의 UV안정제, 0.3~0.7중량부의 조핵제, 1~3중량부의 충진제, 0.2~0.4중량부의 무기안료를 포함하는 첨가제가 첨가되는 것이 바람직하다. As a specific specific example of the present invention, the natural vegetable fiber powder subjected to the first kneading step includes 0.2 to 1 parts by weight of lubricant, 0.1 to 0.3 parts by weight of antioxidant, 0.2 to 0.6 parts by weight of UV stabilizer, based on 100 parts by weight of artificial wood, It is preferable to add an additive including 0.3 to 0.7 parts by weight of a nucleating agent, 1 to 3 parts by weight of a filler, and 0.2 to 0.4 parts by weight of an inorganic pigment.
구체적으로, 상기에서 윤활제는 합성수지가 높은 온도에서 점성이 높기 때문에 혼련 및 성형 중에 천연식물성 섬유분말의 분산성을 높여 제품의 표면성질을 개선하기 위해서 첨가할 수 있다. 상기 윤활제로는 Fatty acids계, acid amide계, fluoropolymer계, hydrocarbon계로 구성된 군으로부터 하나가 선택되어 사용될 수 있다. Specifically, the lubricant may be added to improve the surface properties of the product by increasing the dispersibility of the natural vegetable fiber powder during kneading and molding because the high viscosity of the synthetic resin at high temperatures. As the lubricant, one selected from the group consisting of fatty acids, acid amides, fluoropolymers, and hydrocarbons may be used.
상기에서 항산화제는 천연식물성 섬유분말이 공기로부터 산소를 공급받는 것을 막기 위해 첨가될 수 있으며, 페놀계 항산화제가 주로 사용된다. The antioxidant may be added to prevent the natural vegetable fiber powder from receiving oxygen from the air, phenolic antioxidants are mainly used.
상기에서 UV안정제는 자외선을 차단하기 위해 첨가될 수 있으며, benzotrizole계, benzophenone계, triamine계로 구성된 군으로부터 선택된 하나가 사용될 수 있다. In the above UV stabilizers may be added to block ultraviolet rays, one selected from the group consisting of benzotrizole-based, benzophenone-based, triamine-based may be used.
또한, 상기에서 조핵제는 합성수지(PP 또는 PE)의 결정을 미세화하는 것으로 합성수지의 강성, 열변형온도 등의 물성을 개량함과 동시에 결정화 온도를 향상시킴으로서 성형 사이클을 단축시키기 위해 첨가될 수 있으며 카본산금속염류, sorbitol계, 인산에스테르금속염으로 구성된 군으로부터 하나가 선택되어 사용된다. In addition, the nucleating agent may be added to shorten the molding cycle by improving the crystallization temperature at the same time to improve the physical properties such as the stiffness, heat deformation temperature of the synthetic resin (PP or PE) to refine the crystals One is selected from the group consisting of acid metal salts, sorbitol-based and phosphate ester metal salts.
상기에서 충진제는 충격강도, 굽힘강도, 열변형온도 및 하중에 의한 장기적인 변형을 개선하기 위하여 첨가할 수 있으며, 탄산칼슘, 활석, 운모로 구성된 군으로부터 하나가 선택되어 사용될 수 있다. The filler may be added to improve the long-term deformation due to impact strength, bending strength, heat deformation temperature and load, it may be selected from the group consisting of calcium carbonate, talc, mica.
상기에서 무기안료는 본 발명에 색을 부여하기 위하여 첨가되며, 주로 합성수지에 착색되어 발색된다. In the above, inorganic pigments are added to impart color to the present invention, and are mainly colored and colored on synthetic resins.
혼련단계를 제1혼련단계와 제2혼련단계의 두 단계로 분리한 이유는 결합제 혼합단계에서 합성수지와 혼합된 결합제는 합성수지와 천연식물성 섬유질 분말의 결합력을 높이기 위한 첨가제인데, 혼련단계를 분리하지 않고 한꺼번에 배합하여 혼련하는 경우에 결합제가 합성수지 또는 천연식물성 섬유질 분말과 결합하기 전에 다른 다양한 첨가제(제2혼련단계의 첨가제)가 먼저 합성수지 또는 천연식물성 섬유질 분말과 결합하는 경우 결합력이 저하되어 물성 저하 및 균일한 분산이 되지 않아 펠렛화 단계 또는 성형 단계에서의 압출량 변화가 심하게 되고 대량 불량의 원인이 될 수 있기 때문이다. The reason why the kneading step is separated into two stages of the first kneading step and the second kneading step is that the binder mixed with the synthetic resin in the binder mixing step is an additive for increasing the binding force between the synthetic resin and the natural vegetable fiber powder, without separating the kneading step. In the case of mixing and kneading at the same time, when the binder is combined with the synthetic resin or the natural vegetable fiber powder before the other various additives (additives in the second kneading step) are first combined with the synthetic resin or the natural vegetable fiber powder, the bonding strength is lowered and the physical properties are reduced and uniform. This is because the dispersion is not dispersed so that the extrusion amount change in the pelletizing step or the forming step is severe and may cause mass defects.
5. 펠렛화 단계5. Pelletizing Step
제2혼련단계를 통하여 겔화된 원료를 170~200℃로 가열된 진공장치가 부착된 펠렛용 성형기에 의해서 2~3mm의 펠렛으로 펠렛화하는 단계이며, 상기 진공장치(펠렛용 성형기)를 통해 건조 단계, 혼련 단계 등을 거치면서 다시 함침된 잔여 수분을 제거할 수 있다. Pelletizing the gelled material through a second kneading step into pellets of 2 to 3 mm by means of a pellet molding machine with a vacuum apparatus heated to 170 to 200 ° C., and drying through the vacuum apparatus (pellet molding machine). During the step, kneading step, etc., it is possible to remove the remaining water impregnated again.
이는 본 발명의 성형전에 겔화된 원료를 펠렛으로 만듦으로써, 완제품제조 전에 저장이 용이하며 펠렛화 단계를 통해 원료의 구성요소들이 더욱 균일하게 분포될 수 있게 한다. 본 발명의 인조목재 제조방법에서 펠렛화 단계는 경우에 따라서 생략이 가능하다. This makes the gelled raw material into pellets prior to molding of the present invention, which allows for easy storage prior to manufacture of the finished product and allows the components of the raw material to be more evenly distributed through the pelletization step. Pelletizing step in the artificial wood manufacturing method of the present invention can be omitted in some cases.
보다 구체적으로, 상기와 같이 펠렛화 단계를 거치는 이유는 배합되는 합성수지에 비해 천연 식물성 섬유질 분말이 다량이므로 혼련단계를 거친 후 바로 성형단계로 가면 합성수지 또는 첨가제의 기능을 극대화한다 해도 합성수지, 천연식물성 섬유질 분말 및 첨가제가 균일하게 분산되기가 어렵워 물성뿐 아니라 제품의 품질(표면상태, 함몰, 색상 등)의 저하 등을 초래할 우려가 있기 때문이다. More specifically, the reason for the pelletization step as described above is that the amount of natural vegetable fiber powder is higher than that of the compounded synthetic resin. This is because it is difficult to uniformly disperse the powders and additives, which may cause not only physical properties but also deterioration of product quality (surface state, depression, color, etc.).
또한, 펠렛화 단계를 거치지 않는 경우 건조단계를 거치면서 천연식물성 섬유질 분말의 함수율을 1% 미만으로 낮추었기 때문에 혼련된 원료를 재고로 가져가면 수분 함침으로 인해 전단계 공정을 다시 거쳐야 하는 문제가 발생할 수 있다. 한편, 펠렛화 단계를 거치면 천연 식물성 섬유질 분말에 합성수지가 코팅되어 있으므로 재고로 가져가더라도 수분 함침이 최소화될 수 있다. In addition, when the pelletization step is not carried out, the moisture content of the natural vegetable fiber powder is lowered to less than 1% during the drying step, so that when the kneaded raw material is brought back into the stock, a problem of having to go through the previous step again due to moisture impregnation may occur. have. On the other hand, since the synthetic resin is coated on the natural vegetable fiber powder after the pelletization step, even if brought to inventory can be minimized moisture impregnation.
6. 성형 단계6. Molding Step
제2혼련단계를 통하여 겔화된 원료 또는 펠렛화된 원료에 팽창제를 혼합하고 180~230℃로 가열용융한 후 압출성 형기를 이용하여 천연식물성 섬유분말을 포함하는 인조목재 제품으로 성형하는 단계이다. 더욱 구체적인 일례로는, 성형단계에서 상기 겔화된 원료 또는 펠렛화된 원료를 기준으로 팽창제 0.86phr(Parts perhundred parts of Rubber)~2.04phr를 혼합하고, 혼합된 원료를 가열된 진공장치가 부착된 압출 성형기에 투입하는 방법이 있다. 그리고, 압출성형기의 가열조건을 180~230℃로 하고 가열용융한 뒤, 다이를 통과시켜 소비자가 원하는 형상(판상, 이형 등)의 단면을 가진 연속체로 변환시키고 냉각, 고화하여 권취 또는 절단할 수 있다. After mixing the expansion agent in the gelled raw material or pelletized raw material through the second kneading step, and heat-melting at 180 ~ 230 ℃ and molding into an artificial wood product containing a natural vegetable fiber powder using an extruder. More specifically, in the forming step, the expansion agent 0.86phr (Parts perhundred parts of Rubber) ~ 2.04phr based on the gelled raw material or pelletized raw material is mixed, and the mixed raw material is extruded with a heated vacuum apparatus There is a method of putting into a molding machine. Then, the heating conditions of the extruder is set to 180 ~ 230 ℃ and heated and melted, passed through a die to convert into a continuum having a cross-section of the desired shape (plate, mold release, etc.), cooled, solidified, wound or cut can be have.
상기에서, 팽창제는 상기 인조목재 제품의 경량화를 위한 것으로 아크릴로니트릴 공중합체를 기재로 하고 저비점 탄화수소를 내포하는 열팽창성 미소구체(Micropheres)를 이용하는 것이다. 이때, 팽창을 위해서는 팽창제와 겔화된 원료 또는 펠렛화된 원료를 가열용융한 후 180~230℃의 분위기에서 1~4분가량 열을 가하여 30~70%까지 팽창시키는 것이 바람직하다. 이는 합성수지에 한하여 팽창시키는 화학발포제나 가스발포방식이 아닌 기계팽창 방식이며, 합성수지의 함량과 관계가 적고 온도, 습도 등의 외부조건에 의한 영향을 적게 받는 팽창방식이다. 화학발포나 가스발포 방식은 합성수지를 대상으로 팽창시키는 것이기 때문에 중(中)량의 합성수지를 팽창시키는데는 한계가 있을 뿐만 아니라 외부조건(수분, 온도 등)에 따라 민감하게 반응하기 때문에 많은 경량화가 어렵다. 특히 가스발포방식은 외부에서 가스를 주입해야 하기 때문에 위험성이나 설비투자가 많이 필요하다. In the above, the swelling agent is to reduce the weight of the artificial wood product is to use a thermally expandable microspheres based on the acrylonitrile copolymer and containing a low boiling hydrocarbon. At this time, it is preferable to inflate the expansion agent and the gelled or pelletized raw material by heat-melting, and then expand it by 30 to 70% by adding about 1 to 4 minutes of heat in an atmosphere of 180 to 230 ° C. This is a mechanical expansion method, not a chemical foaming agent or a gas foaming method that expands only to synthetic resins, and is an expansion method that has little relationship with the content of synthetic resins and is less affected by external conditions such as temperature and humidity. Since chemical foaming or gas foaming is intended to expand synthetic resins, it is difficult to expand medium weight synthetic resins and reacts sensitively to external conditions (moisture, temperature, etc.). . In particular, the gas foaming method requires a lot of risk or facility investment because the gas must be injected from the outside.
상기 제조방법에 따른 본 발명의 합성목재는 판상 또는 이형의 형상으로 현장에 맞게 압출성형될 수 있으며, 합성수지가 16~40중량%가 함유됨에도 불구하고 천연목재와 같은 강도(물성) 및 촉감 등을 가진다. Synthetic wood of the present invention according to the manufacturing method can be extruded according to the site in the form of a plate or a release shape, despite the synthetic resin contained 16 to 40% by weight, such as the strength (physical properties) and touch like natural wood Have
명세서에서 최적의 실시예들이 개시되었다. 여기서, 특정한 용어들이 사용되었으나, 이는 단지 본 발명을 설명하기 위한 목적에서 사용된 것이지 의미한정이나 특허청구범위에 기재된 본 발명의 범위를 제한하기 위하여 사용된 것은 아니다. 그러므로, 본 기술 분야의 통상의 지식을 가진 자라면, 이로부터 다양한 변형 및 균등한 타실시예가 가능하다는 점을 이해할 것이다. 따라서, 본 발명의 진정한 기술적 보호범위는 첨부된 특허청구범위의 기술적 사상에 의해 정해져야 할 것이다. Optimal embodiments have been disclosed in the specification. Herein, specific terms have been used, but they are used only for the purpose of illustrating the present invention and are not intended to limit the scope of the present invention as defined in the claims or the claims. Therefore, those skilled in the art will understand that various modifications and equivalent other embodiments are possible from this. Therefore, the true technical protection scope of the present invention will be defined by the technical spirit of the appended claims.

Claims (14)

  1. 폴리프로필렌 또는 고밀도폴리에틸렌과, 에틸렌비닐아세테이트 또는 선형저밀도폴리에틸렌을 혼합한 합성수지에 말레이트 처리된 폴리프로필렌(MAPP), 티탄산염계 및 지르콘산염계 중에서 선택된 1종의 결합제와 실리콘오일을 혼합하여 상기 합성수지를 코팅하는 결합제 코팅단계;The synthetic resin is mixed with a silicone oil of at least one binder selected from polypropylene (MAPP), titanate-based and zirconate-based polypropylene (MAPP), titanate-based and zirconate-based synthetic resins mixed with polypropylene or high-density polyethylene, ethylene vinyl acetate or linear low-density polyethylene Binder coating step of coating;
    폐지, 볏짚, 옥수수대, 수수대, 마, 커피껍질, 야자수잎, 사탕수수찌꺼기 및 녹차찌꺼기로 구성된 군으로부터 선택된 하나 이상의 천연식물성 섬유질 분말을 건조하는 건조단계;A drying step of drying one or more natural vegetable fiber powders selected from the group consisting of waste paper, rice straw, corn stalks, sorghum, hemp, coffee bark, palm fronds, sugar cane grounds and green tea grounds;
    상기 결합제가 혼합된 합성수지와 상기 건조단계에서 건조된 천연식물성 섬유질 분말을 함께 혼련하는 제1혼련단계;A first kneading step of kneading the synthetic resin mixed with the binder and the natural vegetable fiber powder dried in the drying step together;
    상기 제1혼련단계를 거친 혼합물에 윤활제, 항산화제, UV안정제, 조핵제, 충진제 및 무기안료로 구성된 군으로 부터 선택된 하나 이상의 첨가제를 첨가하여 혼련하는 제2혼련단계; 및A second kneading step of kneading by adding one or more additives selected from the group consisting of a lubricant, an antioxidant, a UV stabilizer, a nucleating agent, a filler, and an inorganic pigment to the mixture that has passed through the first kneading step; And
    팽창제를 첨가하고 압출성형기를 이용하여 인조목재 제품으로 성형하는 성형단계;를 포함하는 천연 식물성 섬유질을 이용한 인조목재 제조방법.Adding a swelling agent and the molding step of molding into an artificial wood product using an extrusion molding machine; artificial wood manufacturing method using natural vegetable fiber comprising a.
  2. 제1항에 있어서, 건조단계는The method of claim 1, wherein the drying step
    80~100℃에서 천연식물성 섬유질 분말의 함수율이 5중량% 미만이 되도록 건조하는 1차 건조단계; 및A primary drying step of drying at 80 to 100 ° C. such that the water content of the natural vegetable fiber powder is less than 5 wt%; And
    100~130℃에서 천연식물성 섬유질 분말의 함수율이 1중량% 미만이 되도록 건조하는 2차 건조단계;를 포함하는 것인 천연 식물성 섬유질을 이용한 인조목재 제조방법.A method of manufacturing artificial wood using natural vegetable fiber, comprising; a second drying step of drying so that the water content of the natural vegetable fiber powder is less than 1% by weight at 100 ~ 130 ℃.
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PCT/KR2011/008823 2010-12-02 2011-11-18 Method for preparing artificial wood using natural vegetable fibroid material WO2012074230A2 (en)

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KR102413191B1 (en) * 2021-12-30 2022-06-27 (주)지케이우드 Synthetic wood from recycled coffee grounds and manufacturing method therefor
KR102413193B1 (en) * 2021-12-30 2022-06-27 (주)지케이우드 Synthetic wood from recycled waste media and manufacturing method therefor

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