KR101712813B1 - Method for preparing filter - Google Patents
Method for preparing filter Download PDFInfo
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- KR101712813B1 KR101712813B1 KR1020160177073A KR20160177073A KR101712813B1 KR 101712813 B1 KR101712813 B1 KR 101712813B1 KR 1020160177073 A KR1020160177073 A KR 1020160177073A KR 20160177073 A KR20160177073 A KR 20160177073A KR 101712813 B1 KR101712813 B1 KR 101712813B1
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- glass fiber
- fiber
- reinforced plastic
- sewage
- firing
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- 238000000034 method Methods 0.000 title claims description 16
- 229920002430 Fibre-reinforced plastic Polymers 0.000 claims abstract description 27
- 239000011151 fibre-reinforced plastic Substances 0.000 claims abstract description 27
- 239000010865 sewage Substances 0.000 claims abstract description 18
- 238000004519 manufacturing process Methods 0.000 claims abstract description 14
- 239000000654 additive Substances 0.000 claims abstract description 11
- 230000000996 additive effect Effects 0.000 claims abstract description 8
- 239000002245 particle Substances 0.000 claims abstract description 5
- 239000003365 glass fiber Substances 0.000 claims description 47
- 238000010304 firing Methods 0.000 claims description 22
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical group [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 claims description 11
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 10
- 239000011230 binding agent Substances 0.000 claims description 9
- 238000002156 mixing Methods 0.000 claims description 6
- 229910000019 calcium carbonate Inorganic materials 0.000 claims description 5
- 238000004140 cleaning Methods 0.000 claims description 3
- 239000005011 phenolic resin Substances 0.000 claims description 3
- 239000011259 mixed solution Substances 0.000 claims 1
- 239000002351 wastewater Substances 0.000 abstract description 6
- 239000011152 fibreglass Substances 0.000 abstract description 5
- 238000005245 sintering Methods 0.000 abstract 2
- 239000007822 coupling agent Substances 0.000 abstract 1
- 238000010298 pulverizing process Methods 0.000 abstract 1
- 239000000463 material Substances 0.000 description 23
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 10
- 239000011148 porous material Substances 0.000 description 9
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 6
- 239000000203 mixture Substances 0.000 description 6
- 238000006243 chemical reaction Methods 0.000 description 5
- 239000000126 substance Substances 0.000 description 5
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- 238000007667 floating Methods 0.000 description 4
- 238000003756 stirring Methods 0.000 description 4
- 239000011248 coating agent Substances 0.000 description 3
- 238000000576 coating method Methods 0.000 description 3
- 239000000428 dust Substances 0.000 description 3
- 239000011347 resin Substances 0.000 description 3
- 229920005989 resin Polymers 0.000 description 3
- 238000001179 sorption measurement Methods 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- 239000001569 carbon dioxide Substances 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 239000000356 contaminant Substances 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 238000000197 pyrolysis Methods 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 239000002990 reinforced plastic Substances 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- XDLMVUHYZWKMMD-UHFFFAOYSA-N 3-trimethoxysilylpropyl 2-methylprop-2-enoate Chemical compound CO[Si](OC)(OC)CCCOC(=O)C(C)=C XDLMVUHYZWKMMD-UHFFFAOYSA-N 0.000 description 1
- 101000878595 Arabidopsis thaliana Squalene synthase 1 Proteins 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 1
- 229920000877 Melamine resin Polymers 0.000 description 1
- 239000000020 Nitrocellulose Substances 0.000 description 1
- 239000004677 Nylon Substances 0.000 description 1
- FJWGYAHXMCUOOM-QHOUIDNNSA-N [(2s,3r,4s,5r,6r)-2-[(2r,3r,4s,5r,6s)-4,5-dinitrooxy-2-(nitrooxymethyl)-6-[(2r,3r,4s,5r,6s)-4,5,6-trinitrooxy-2-(nitrooxymethyl)oxan-3-yl]oxyoxan-3-yl]oxy-3,5-dinitrooxy-6-(nitrooxymethyl)oxan-4-yl] nitrate Chemical compound O([C@@H]1O[C@@H]([C@H]([C@H](O[N+]([O-])=O)[C@H]1O[N+]([O-])=O)O[C@H]1[C@@H]([C@@H](O[N+]([O-])=O)[C@H](O[N+]([O-])=O)[C@@H](CO[N+]([O-])=O)O1)O[N+]([O-])=O)CO[N+](=O)[O-])[C@@H]1[C@@H](CO[N+]([O-])=O)O[C@@H](O[N+]([O-])=O)[C@H](O[N+]([O-])=O)[C@H]1O[N+]([O-])=O FJWGYAHXMCUOOM-QHOUIDNNSA-N 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 239000003463 adsorbent Substances 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 239000012298 atmosphere Substances 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 229920002301 cellulose acetate Polymers 0.000 description 1
- -1 cellulose and nylon Chemical compound 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000007598 dipping method Methods 0.000 description 1
- 239000012153 distilled water Substances 0.000 description 1
- 239000010840 domestic wastewater Substances 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- VOZRXNHHFUQHIL-UHFFFAOYSA-N glycidyl methacrylate Chemical compound CC(=C)C(=O)OCC1CO1 VOZRXNHHFUQHIL-UHFFFAOYSA-N 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 244000144972 livestock Species 0.000 description 1
- JDSHMPZPIAZGSV-UHFFFAOYSA-N melamine Chemical compound NC1=NC(N)=NC(N)=N1 JDSHMPZPIAZGSV-UHFFFAOYSA-N 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 229920001220 nitrocellulos Polymers 0.000 description 1
- 229920001778 nylon Polymers 0.000 description 1
- RVTZCBVAJQQJTK-UHFFFAOYSA-N oxygen(2-);zirconium(4+) Chemical compound [O-2].[O-2].[Zr+4] RVTZCBVAJQQJTK-UHFFFAOYSA-N 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920002647 polyamide Polymers 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 239000002861 polymer material Substances 0.000 description 1
- 239000002243 precursor Substances 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 239000010801 sewage sludge Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 238000004381 surface treatment Methods 0.000 description 1
- JMXKSZRRTHPKDL-UHFFFAOYSA-N titanium ethoxide Chemical compound [Ti+4].CC[O-].CC[O-].CC[O-].CC[O-] JMXKSZRRTHPKDL-UHFFFAOYSA-N 0.000 description 1
- 239000011800 void material Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
- 238000009941 weaving Methods 0.000 description 1
- 238000005303 weighing Methods 0.000 description 1
- 229910001928 zirconium oxide Inorganic materials 0.000 description 1
Images
Classifications
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- 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
- B29C67/00—Shaping techniques not covered by groups B29C39/00 - B29C65/00, B29C70/00 or B29C73/00
- B29C67/02—Moulding by agglomerating
- B29C67/04—Sintering
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D39/00—Filtering material for liquid or gaseous fluids
- B01D39/14—Other self-supporting filtering material ; Other filtering material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
-
- 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
- B29C70/00—Shaping composites, i.e. plastics material comprising reinforcements, fillers or preformed parts, e.g. inserts
- B29C70/02—Shaping composites, i.e. plastics material comprising reinforcements, fillers or preformed parts, e.g. inserts comprising combinations of reinforcements, e.g. non-specified reinforcements, fibrous reinforcing inserts and fillers, e.g. particulate fillers, incorporated in matrix material, forming one or more layers and with or without non-reinforced or non-filled layers
- B29C70/021—Combinations of fibrous reinforcement and non-fibrous material
- B29C70/023—Combinations of fibrous reinforcement and non-fibrous material with reinforcing inserts
-
- 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
- B29C70/00—Shaping composites, i.e. plastics material comprising reinforcements, fillers or preformed parts, e.g. inserts
- B29C70/02—Shaping composites, i.e. plastics material comprising reinforcements, fillers or preformed parts, e.g. inserts comprising combinations of reinforcements, e.g. non-specified reinforcements, fibrous reinforcing inserts and fillers, e.g. particulate fillers, incorporated in matrix material, forming one or more layers and with or without non-reinforced or non-filled layers
- B29C70/021—Combinations of fibrous reinforcement and non-fibrous material
- B29C70/025—Combinations of fibrous reinforcement and non-fibrous material with particular filler
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Mechanical Engineering (AREA)
- Composite Materials (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Environmental & Geological Engineering (AREA)
- Filtering Materials (AREA)
Abstract
Description
본 발명은 하수 및 오수 처리시설에 투입되는 여재 제조방법에 관한 것으로, 더욱 상세하게는 섬유강화플라스틱를 사용하여 여재를 제조하기 위한 방법에 관한 것이다.BACKGROUND OF THE INVENTION 1. Field of the Invention [0001] The present invention relates to a method for manufacturing a filter material to be introduced into a sewage and sewage treatment facility, and more particularly, to a method for manufacturing a filter material using a fiber reinforced plastic.
섬유강화플라스틱(Fiber Reinforced Plastic)은 대부분 유리섬유와 수지로 이루어져 있다. 섬유강화플라스틱은 우수한 기계적, 내식성, 성형성을 갖으며, 건축, 토목, 항공 등 여러 가지 분야에 이용되고 있다.Fiber Reinforced Plastics are mostly made of glass fiber and resin. Fiber reinforced plastics have excellent mechanical, corrosion and moldability and are used in various fields such as construction, civil engineering, and aviation.
섬유강화플라스틱은 매트층 사이에 로빙층이 형성되어 있으며, 로빙층은 유리섬유가 촘촘하게 배치되어 있고, 로빙층의 상하에 형성된 매트층은 로빙층을 보호하도록 형성되어 있다. 로빙층의 두께는 매트층의 약 1/7의 두께를 갖는다. 이에 따라 로빙층을 쌓고 있는 매트층을 기계적으로 분리하기는 매우 어렵다. In the fiber-reinforced plastic, a roving layer is formed between matte layers, glass fibers are closely arranged in the roving layer, and a mat layer formed above and below the roving layer is formed to protect the roving layer. The thickness of the roving layer is about 1/7 of the thickness of the matte layer. Accordingly, it is very difficult to mechanically separate the mat layer for the roving layer.
섬유강화플라스틱을 재활용하기 위한 다른 방법으로서, 파쇄하는 방법이 있다. 파쇄방법은 파쇄기에 폐 섬유강화플라스틱을 넣고 잘게 커팅하게 되며, 이때 발생되는 유리섬유를 포함한 분진은 별도의 분진제거기로 제거한다.As another method for recycling fiber-reinforced plastic, there is a method of crushing. In the crushing method, the waste fiber reinforced plastic is put into the crusher and finely cut. The dust containing the glass fiber generated at this time is removed with a separate dust remover.
커팅된 섬유강화플라스틱은 그 속에 포함된 유리섬유는 씨실과 날실로 짜여져 있는 구조와 유사하여 오염물질을 제거하기에 적합하다. 다만 파쇄된 섬유강화플라스틱 속에 포함된 유리섬유의 공극의 크기를 조절하는 기계적 및 화학적 방법이 요구된다.The cut fiber-reinforced plastic is suitable for removing contaminants because the fiberglass contained therein is similar to a weft and warp-woven structure. However, there is a need for a mechanical and chemical method of regulating the size of the pores of the glass fibers contained in the shredded fiber-reinforced plastic.
한편, 공개특허공보 제10-2003-0050375호는 축산폐수, 정화조 오수, 산업폐수 및 생활하수의 고도처리에 사용되는 오, 폐수 처리용 부유성 여재에 관하여 기술하고 있는데, 탄산염, 산화지르코늄, 활성 알루미나, 및 점결제를 포함하는 여재를 건식 혼함한 후 물을 첨가하여 재혼합하고, 혼합된 여재를 성형기를 사용하여 구형으로 성형한다. 이어서 성형된 여재를 상온에서 건조시킨 다음, 고온 처리후 냉각시켜 여재를 제조하고 있다.On the other hand, Japanese Patent Application Laid-Open No. 10-2003-0050375 discloses a floating filter medium for treating wastewater used for advanced treatment of livestock wastewater, purified wastewater wastewater, industrial wastewater, and domestic wastewater, wherein carbonate, zirconium oxide, Alumina, and a binder are dry-blended, water is added to remultiplex, and the mixed filter material is formed into a sphere using a molding machine. Then, the formed filter material is dried at room temperature, and then treated at high temperature and cooled to produce a filter material.
본 발명은 상기한 문제점을 해소하기 위해 안출한 것으로서, 섬유강화플라스틱 속에 포함된 유리섬유 조직을 이용하여 오수 및 하수 속에 포함된 이물질을 제거할 수 있는 여재의 제조방법을 제공하려는 데 그 목적이 있다. SUMMARY OF THE INVENTION The present invention has been made to solve the above-mentioned problems, and an object of the present invention is to provide a manufacturing method of a filter material capable of removing foreign matters contained in sewage and sewage water using a glass fiber structure contained in a fiber- .
또한 오, 하수 중에 포함된 부유성 이물질을 제거하기 위하여 다공성을 가지며, 이물질 흡착력이 우수한 여재의 제조방법을 제공하려는 데 그 목적이 있다.It is also an object of the present invention to provide a method of manufacturing a filter material having porosity for removing floating foreign matter contained in sewage and having excellent foreign matter adsorption ability.
본 발명의 해결하고자 하는 과제는 언급한 과제로 제한되지 않는다. 언급하지 않은 다른 기술적 과제들은 이하의 기재로부터 본 발명이 속하는 기술분야에서 통상의 지식을 가진 자에게 명확하게 이해될 수 있을 것이다.The problems to be solved by the present invention are not limited to the above-mentioned problems. Other technical subjects not mentioned will be apparent to those skilled in the art from the following description.
본 발명에 따른 여재의 제조방법은 오수 및 하수에 투입되는 여재의 제조방법에 관한 것으로서, 오수 및 하수에 투입되는 여재의 제조방법이며, 섬유강화플라스틱을 소정의 입도 크기로 파쇄하는 단계와, 섬유강화플라스틱을 소성하여 유리섬유 럼프를 얻는 단계와, 결합제와 첨가제가 혼합된 용액에 유리섬유를 침지 및 소성시켜 유리섬유 성형체를 얻는 단계와, 유리섬유 성형체의 표면을 개질처리하는 단계를 포함한다.A method of manufacturing a filter material according to the present invention is a method of manufacturing a filter material to be introduced into sewage and sewage, comprising the steps of crushing a fiber reinforced plastic to a predetermined particle size, Obtaining a glass fiber lump by firing the reinforced plastic; and dipping and firing the glass fiber in a solution mixed with the binder and the additive to obtain a glass fiber compact, and a step of modifying the surface of the glass fiber compact.
추가적으로 상기 섬유강화플라스틱을 소성하여 유리섬유 럼프를 얻는 단계 이후에 세정하는 단계를 더욱 포함할 수 있다.Further comprising the step of firing the fiber-reinforced plastic to obtain a glass fiber lump followed by cleaning.
상기 유리섬유 성형체를 얻는 단계의 첨가제는 탄산칼슘이 사용된다.As the additive in the step of obtaining the glass fiber compact, calcium carbonate is used.
본 발명에 따른 여재의 제조방법은 폐 섬유강화플라스틱을 원재료로 사용할 수 있으므로, 폐기물의 재활용이라는 이점이 있다.The method of manufacturing a filter material according to the present invention has an advantage of recycling waste since waste plastic reinforced plastic can be used as a raw material.
또한 본 발명에 따른 여재는 흡착용제를 사용하여 코팅처리된 다공성 여재로서 오, 하수 중의 부유성 이물질을 쉽게 흡착할 수 있는 이점이 있다.Further, the filter material according to the present invention is a porous filter material coated with an adsorbing solvent and has an advantage of easily adsorbing floating foreign matter in sewage.
도 1은 본 발명에 따른 섬유강화플라스틱을 이용한 여재의 제조방법을 나타낸 것이다.1 shows a method of manufacturing a filter material using a fiber-reinforced plastic according to the present invention.
이하, 본 발명의 실시예를 첨부된 도면을 참조하여 상세히 설명한다. Hereinafter, embodiments of the present invention will be described in detail with reference to the accompanying drawings.
도 1은 본 발명에 따른 여재 제조방법을 나타낸 것이다.1 shows a method for manufacturing a filter material according to the present invention.
본 발명에 따른 여재는 원재료로서 일정 크기로 파쇄된 섬유강화플라스틱(fiber reinforced plastic)을 사용한다. 섬유강화플라스틱은 로빙층(roving layer)과 매트층(mat layer)으로 이루어져 있는데, 상기 로빙층은 2개의 매트층 사이에 형성된다. 상기 매트층은 수지 속에 유리 섬유가 드물게 형성되어 있고, 로빙층에는 수지 속에 유리섬유가 70%이상으로 짜여져 형성된다.The filter material according to the present invention uses fiber reinforced plastic which is crushed to a predetermined size as a raw material. The fiber-reinforced plastic comprises a roving layer and a mat layer, wherein the roving layer is formed between two matte layers. The mat layer is formed by rarely forming glass fibers in the resin, and the roving layer is formed by weaving 70% or more of glass fibers in the resin.
본 발명에 따른 여재의 제조방법은 섬유강화플라스틱을 소정의 입도 크기로 파쇄하는 단계와, 섬유강화플라스틱을 소성하여 유리섬유 럼프를 얻는 단계와, 결합제에 첨가제를 혼합한 혼합용액에 유리섬유 럼프를 침지시켜 유리섬유 성형체를 형성하는 단계와, 유리섬유 성형체의 표면을 개질처리하는 단계를 포함함한다.A method for manufacturing a filter material according to the present invention comprises the steps of crushing a fiber-reinforced plastic to a predetermined particle size, firing a fiber-reinforced plastic to obtain a glass fiber lump, and adding a glass fiber lump To form a glass fiber compact, and a step of modifying the surface of the glass fiber compact.
추가적으로, 상기 섬유강화플라스틱을 소성하여 유리섬유를 얻는 단계 이후에 황산으로 세정하는 단계를 더욱 포함할 수 있다.In addition, the step of firing the fiber-reinforced plastic to obtain the glass fiber may further include washing with sulfuric acid.
우선, 섬유강화플라스틱을 여재로 사용하기 위해 일정 크기로 파쇄한다. 섬유강화플라스틱은 소정의 두께를 갖는 판(plate) 형상으로 제공될 수 있다. 파쇄기에 판 형상의 섬유강화플라스틱을 소정의 크기로 파쇄한다. 상기 파쇄된 섬유강화플라스틱의 크기는 900mm3 ~ 3,000m3로 형성할 수 있다.First, the fiber-reinforced plastic is crushed to a certain size to use as a filter material. The fiber-reinforced plastic may be provided in the form of a plate having a predetermined thickness. The plate-shaped fiber-reinforced plastic is crushed to a predetermined size on the crusher. The size of the shredded fiber-reinforced plastic may be from 900 mm 3 to 3,000 m 3 .
한편, 본 발명에서는 로빙층과 매트층을 분리하지 않고 사용하는 것을 실시예로 하지만, 상기 로빙층의 외측에 형성되는 매트층은 유리섬유의 함량이 낮으므로 로빙층의 아래 위에 형성된 매트층을 제거하여 유리섬유가 대부분인 로빙층만을 사용할 수 있다.Meanwhile, in the present invention, the roving layer and the mat layer are not separated but the mat layer formed outside the roving layer has a low glass fiber content, so that the mat layer formed under the roving layer is removed Only the roving layer in which most of the glass fibers are present can be used.
소성하여 유리섬유 럼프를 얻는 단계에서 상기 소성온도는 600℃ 내지 900℃로 형성할 수 있으며, 파쇄된 섬유강화플라스틱의 입도에 따라 소성온도는 조절될 수 있다. 여기서 소성은 열분해를 말하는데, 열분해는 공기가 거의 없는 상태에서 가열하는 방식으로 고분자 물질을 저분자 물질로 분해하는 것을 말한다. 소성 과정 후 유리섬유 럼프에는 챠아(char)가 형성되어 덩어지게 되며, 이러한 유리섬유 럼프의 표면에는 소성과정에서 먼지 등 이물질이 묻어있게 된다. 이를 위해 추가적으로 소성 과정 후에는 세정과정이 이어질 수 있다. 상기 이물질은 묽은 황산에 침지시켜 교반하여 제거할 수 있다.In the step of obtaining a glass fiber lump by firing, the firing temperature may be set to 600 to 900 ° C, and the firing temperature may be controlled according to the particle size of the spun fiber-reinforced plastic. Here, firing means pyrolysis, and pyrolysis refers to decomposition of a polymer substance into a low-molecular substance by heating in the absence of air. After the firing process, a char is formed on the glass fiber lump, and the surface of the glass fiber lump is contaminated with dust or the like during the firing process. For this, the cleaning process may be continued after the firing process. The foreign substance can be removed by immersion in diluted sulfuric acid and stirring.
유리섬유 럼프는 가열 및 가압에 의해 유리섬유의 강도가 현저하게 낮아지게 된다. 또한 유리섬유는 소성에 의해 결합력이 약화된 상태가 된다. 이와 같이 약화된 유리섬유 럼프의 기계적 강도, 온도변화에 따른 물성의 변화를 보완하기 위해 유리섬유 럼프에는 결합력을 증대시키기 위해 결합제를 침지시킨다. 결합제는 에탄올 100중량부에 대하여 페놀수지 60~80중량부를 교반혼합하여 제조한다. In the glass fiber lump, the strength of the glass fiber is remarkably lowered by heating and pressurization. In addition, the glass fiber is in a state where the bonding force is weakened by firing. To compensate for the mechanical strength of the weakened glass fiber lump and the change in physical properties due to the temperature change, the binder is immersed in the glass fiber lump in order to increase the bonding strength. The binder is prepared by stirring and mixing 60 to 80 parts by weight of a phenol resin with respect to 100 parts by weight of ethanol.
한편 유리섬유 성형체에 형성되는 공극은 오염물질을 포집하기에는 너무 작은 크기를 갖을 수 있다. 이에 따라 공극의 크기를 증대시키기 위해 결합제에 첨가제를 혼합한다. 상기 첨가제는 상기 에탄올 100중량부에 대하여 대략 3~5 중량부일 수 있다. 첨가제의 혼합비율을 높이면 기공의 수를 증가되며, 첨가제의 혼합비율을 낮추면 기공의 수가 감소된다. 적절한 참가제의 혼합으로 기공수를 조절할 수 있다.On the other hand, the voids formed in the glass fiber formed body may have a size too small to capture contaminants. The additive is then mixed with the binder to increase the size of the pores. The additive may be about 3 to 5 parts by weight based on 100 parts by weight of the ethanol. Increasing the mixing ratio of the additives increases the number of pores, and lowering the mixing ratio of the additives reduces the number of pores. The mixing of suitable entraining agents can control the number of pores.
본 발명에서는 첨가제로서 탄산칼슘(CaCO3)이 사용된다. 탄산칼슘은 소성에 의해 공극을 형성된다. 상기 소성온도는 300℃ 내지 500℃ 범위일 수 있다. 소성과정에서 공극의 크기를 증대시키기 위해 소성초기 저온에서 가압하고, 설정된 소성온도에 이르면 감압한다. 탄산칼슘은 소성에 의해 이산화탄소 가스가 발생되어 기공이 형성되는데, 이산화탄소의 가스가 생성되어 배출되면서 기공이 형성된다.In the present invention, calcium carbonate (CaCO 3 ) is used as an additive. Calcium carbonate forms a void by firing. The firing temperature may range from 300 ° C to 500 ° C. In order to increase the size of the pores in the firing process, pressurization is performed at a low temperature in the initial stage of firing, and the pressure is reduced when the firing temperature is reached. Calcium carbonate generates carbon dioxide gas by firing to form pores. The carbon dioxide gas is generated and discharged to form pores.
이와 같이 첨가제가 혼합된 결합제에 유리섬유 럼프를 침지시킨 후 상온에서 건조시킨 다음 소성하여 유리섬유 성형체를 얻는다. 상기 결합제에 의해 유리섬유는 쉽게 부서러지지 않고 형체를 유지할 수 있다.The glass fiber lump is immersed in the binder in which the additives are mixed, dried at room temperature, and then fired to obtain a glass fiber compact. By the binder, the glass fiber is not easily broken and can maintain the shape.
유리섬유 성형체는 물과 친화력이 낮아 쉽게 오하수 속에 포함된 부유성 이물질을 흡착시키기가 어렵다. 본 발명에서는 유리섬유 성형체의 표면에 흡착용제에 의한 코팅처리가 수행된다. 코팅처리는 오하수와 접촉력이 강화되어 오하수에 포함된 물질의 흡착을 강화시킨다. 본 발명에 따른 흡착용재로서 셀룰로오스 아세테이트, 셀룰로오스 나이트레이트 등 셀룰로오스계 및 나일론 등 폴리아마이드계 고분자 물질을 사용할 수 있다.Since the affinity of the glass fiber formed body with water is low, it is difficult to easily adsorb floating foreign matters contained in the sewage water. In the present invention, the surface of the glass fiber compact is coated with an adsorption solvent. The coating treatment enhances the contact with the sewage and enhances the adsorption of the substances contained in the sewage. As the adsorbent material according to the present invention, polyamide-based polymer materials such as cellulose acetate and cellulose nitrate, such as cellulose and nylon, can be used.
〈실시예〉 <Examples>
섬유강화플라스틱을 입도 1,000mm3 크기로 자른 다음 800℃ 온도로 1시간동안 소성하여 유리섬유 럼프를 얻는다. 이 후, 유리섬유 럼프에 고착된 이물질을 제거하기 위기 위해 35% 농도의 묽은 황산에 침지시킨다. The fiber-reinforced plastic is cut to a size of 1,000 mm 3 and then fired at 800 ° C. for 1 hour to obtain a glass fiber lump. Thereafter, it is immersed in dilute sulfuric acid of 35% concentration to remove foreign matter adhering to the glass fiber lump.
이어서 에탄올 500ℓ에 페놀수지 370g과 탄산칼슘 20g을 혼합한 혼합액에 세정된 유리섬유 럼프를 넣고 교반한 다음 상온에서 건조 후 소성한다. 소성전 상온에서 500℃로 상승시키고 점차 압력을 증가시키고 30psi 분위기에서 감압하여 유리섬유 성형체를 얻는다.Then, the washed glass fiber lump is added to a mixture of 370 g of phenol resin and 20 g of calcium carbonate in 500 L of ethanol, stirred, and then dried at room temperature and then fired. The temperature of the sintered body is raised from room temperature to 500 ° C, the pressure is gradually increased, and the pressure is reduced in a 30 psi atmosphere to obtain a glass fiber compact.
플라스크에 에탄올 7g과 전구체로서 titaniumethoxide 0.7g을 넣고 상온에서 30분 동안 충분히 교반한 다음 3-Methacryloxypropyltrimethoxysilane 15g을 넣고 1시간 동안 교반하여 혼합액을 준비한다. 이 후 혼합액에 1mol 농도의 염산 5g을 첨가한 후 100℃에서 90분 동안 교반한 후 상온으로 될때까지 냉각시킨다. 이어서, 증류수를 첨가하여 pH 2.5가 되도록 교반한 다음, 접착제로서 Glycidyl Methacrylate 3g을 넣고 상온에서 1.5시간 동안 교반하여 코팅액을 준비한다.Add 7 g of ethanol and 0.7 g of titaniumethoxide as precursors to the flask and stir thoroughly at room temperature for 30 minutes. Add 15 g of 3-Methacryloxypropyltrimethoxysilane and stir for 1 hour to prepare a mixture. Thereafter, 5 g of hydrochloric acid having a concentration of 1 mol is added to the mixture, and the mixture is stirred at 100 ° C. for 90 minutes and then cooled to room temperature. Subsequently, distilled water was added to the mixture to adjust the pH to 2.5, and 3 g of Glycidyl Methacrylate was added as an adhesive. The mixture was stirred at room temperature for 1.5 hours to prepare a coating solution.
이와 같이 준비된 코팅액에 앞서 준비한 유리섬유 성형체를 넣고 교반하여 5시간동안 건조시킨다.The glass fiber preform thus prepared is put into the prepared coating solution, stirred and dried for 5 hours.
이와 같이 준비된 유리섬유 성형체를 여재로 하여 다음과 같이 시험하였다.The thus-prepared glass fiber formed body was tested as follows.
공장내 식당에서 배출되는 생활하수를 원수로 사용한다. 반응조는 1,000mm(W)×1,000mm(L)×500mm(H)이고, 여재를 반응조의 50% 비율(부피)로 충진한다. 반응조 내에 원수를 투입한다. 이 때 반응조 내의 ph6.5~7.5, DO 2.0~3.5, 원수 온도 20℃를 유지하였다.The raw sewage discharged from the restaurant in the factory is used as raw water. The reaction tank is 1,000 mm (W) x 1,000 mm (L) x 500 mm (H), and the filter material is filled with 50% (volume) of the reaction tank. The raw water is introduced into the reaction tank. At this time, pH 6.5 to 7.5, DO 2.0 to 3.5, and raw water temperature of 20 ° C were maintained in the reaction tank.
또한 저류조 내에 계량조를 설치하고 20ℓ/min용량의 에어리프트(AirLift)를 이용하여 일정량 반응조에 투입하였다. 반응조 내의 미생물의 활성을 위해서 종균제를 투입하고 일주일간 공폭기를 진행한 후 1개월 유지하였다. 이후, 활성화 여부를 체크하고 2개월간 수질분석을 진행하였다.In addition, a weighing tank was installed in the storage tank and was introduced into a constant amount of the reactor using an airlift having a capacity of 20 l / min. In order to activate the microorganisms in the reaction tank, the microorganism was added to the reactor, followed by air bombing for one week, and then maintained for 1 month. After that, the water quality was analyzed for 2 months.
1 ~ 2 weeks
89.1
86.2
3 ~ 4 weeks
90.1
91.1
5 ~ 6 weeks
92.7
93.3
7 ~ 8 weeks
93.5
92.3
상기 <표 1>의 유입수 처리효율을 살펴보면, 공극과 표면처리로부터 얻어진 여재는 오하수 처리를 위한 소재로서 사용가능하다는 것을 보여준다.The inflow water treatment efficiency of Table 1 shows that the filter material obtained from the pores and the surface treatment can be used as a material for sewage treatment.
이상, 본 발명을 구체적인 실시예를 통하여 상세하게 설명하였으나, 본 발명은 상기 실시예에 한정되지 않고, 본 발명의 기술적 사상의 범위내에서 통상의 지식을 가진 자에 의하여 여러 가지 변형이 가능하다.While the present invention has been particularly shown and described with reference to exemplary embodiments thereof, it is to be understood that the present invention is not limited to the disclosed exemplary embodiments, but various changes and modifications may be made by those skilled in the art without departing from the scope of the present invention.
Claims (3)
섬유강화플라스틱을 소정의 입도 크기로 파쇄하는 단계와,
섬유강화플라스틱을 소성하여 유리섬유 럼프를 얻는 단계와,
결합제에 첨가제를 혼합한 혼합용액에 유리섬유 럼프를 침지 및 소성시켜 유리섬유 성형체를 얻는 단계와,
유리섬유 성형체의 표면을 개질처리하는 단계를 포함하는 것을 특징으로 하는 여재의 제조방법.
As a method for producing filter media to be introduced into sewage and sewage,
Disrupting the fiber-reinforced plastic to a predetermined particle size;
Firing the fiber-reinforced plastic to obtain a glass fiber lump;
A step of obtaining a glass fiber formed body by immersing and firing a glass fiber lump in a mixed solution obtained by mixing an additive with a binder,
And a step of modifying the surface of the glass fiber compact.
상기 섬유강화플라스틱을 소성하여 유리섬유 럼프를 얻는 단계와 유리섬유 성형체를 얻는 단계 사이에 유리섬유 럼프를 세정하는 단계를 더욱 포함하는 것을 특징으로 하는 여재의 제조방법.
The method according to claim 1,
Further comprising the step of cleaning the glass fiber lump between the step of obtaining the glass fiber lump by firing the fiber-reinforced plastic and the step of obtaining the glass fiber molded product.
상기 결합제는 에탄올에 페놀수지를 혼합하여 제조하고, 상기 첨가제는 탄산칼슘인 것을 특징으로 하는 여재의 제조방법.
The method according to claim 1 or 2,
Wherein the binder is prepared by mixing phenol resin with ethanol, and the additive is calcium carbonate.
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