KR20010060509A - Producing method of the folding filter with excellent antibacterial property for liquid purification - Google Patents
Producing method of the folding filter with excellent antibacterial property for liquid purification Download PDFInfo
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- KR20010060509A KR20010060509A KR1019990062904A KR19990062904A KR20010060509A KR 20010060509 A KR20010060509 A KR 20010060509A KR 1019990062904 A KR1019990062904 A KR 1019990062904A KR 19990062904 A KR19990062904 A KR 19990062904A KR 20010060509 A KR20010060509 A KR 20010060509A
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- filter
- glass fiber
- media
- average pore
- medium
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- 239000007788 liquid Substances 0.000 title claims abstract description 22
- 238000000034 method Methods 0.000 title claims description 35
- 238000000746 purification Methods 0.000 title claims description 4
- 230000000844 anti-bacterial effect Effects 0.000 title abstract description 10
- 239000003365 glass fiber Substances 0.000 claims abstract description 42
- 239000011148 porous material Substances 0.000 claims abstract description 26
- 239000004743 Polypropylene Substances 0.000 claims abstract description 23
- 239000004745 nonwoven fabric Substances 0.000 claims abstract description 22
- -1 polypropylene Polymers 0.000 claims abstract description 21
- 229920001155 polypropylene Polymers 0.000 claims abstract description 21
- 238000004519 manufacturing process Methods 0.000 claims abstract description 19
- 238000005452 bending Methods 0.000 claims abstract description 15
- 239000000835 fiber Substances 0.000 claims abstract description 12
- 239000011347 resin Substances 0.000 claims abstract description 8
- 229920005989 resin Polymers 0.000 claims abstract description 8
- 239000003242 anti bacterial agent Substances 0.000 claims abstract description 6
- AVIVHHYKMKWECD-UHFFFAOYSA-N 1-(10h-phenoxazin-1-yloxy)-10h-phenoxazine Chemical class O1C2=CC=CC=C2NC2=C1C=CC=C2OC1=C2NC3=CC=CC=C3OC2=CC=C1 AVIVHHYKMKWECD-UHFFFAOYSA-N 0.000 claims abstract description 5
- 239000004594 Masterbatch (MB) Substances 0.000 claims abstract description 5
- 238000002074 melt spinning Methods 0.000 claims abstract description 4
- 238000005520 cutting process Methods 0.000 claims abstract description 3
- 239000012528 membrane Substances 0.000 claims description 11
- 230000000845 anti-microbial effect Effects 0.000 claims description 10
- 239000004599 antimicrobial Substances 0.000 claims description 8
- 238000007670 refining Methods 0.000 claims description 6
- 230000015572 biosynthetic process Effects 0.000 claims description 3
- 238000004898 kneading Methods 0.000 claims description 2
- 238000005304 joining Methods 0.000 claims 1
- 239000000463 material Substances 0.000 abstract description 4
- 239000012535 impurity Substances 0.000 abstract description 2
- 238000005253 cladding Methods 0.000 abstract 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 9
- 230000000052 comparative effect Effects 0.000 description 7
- 239000002245 particle Substances 0.000 description 6
- 239000000843 powder Substances 0.000 description 6
- JXHIAXWBYMIWPS-UHFFFAOYSA-N 10-phenoxazin-10-yloxyphenoxazine Chemical compound C12=CC=CC=C2OC2=CC=CC=C2N1ON1C2=CC=CC=C2OC2=CC=CC=C21 JXHIAXWBYMIWPS-UHFFFAOYSA-N 0.000 description 4
- 241000894006 Bacteria Species 0.000 description 4
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 4
- 239000008103 glucose Substances 0.000 description 4
- 230000000704 physical effect Effects 0.000 description 4
- 229930091371 Fructose Natural products 0.000 description 3
- RFSUNEUAIZKAJO-ARQDHWQXSA-N Fructose Chemical compound OC[C@H]1O[C@](O)(CO)[C@@H](O)[C@@H]1O RFSUNEUAIZKAJO-ARQDHWQXSA-N 0.000 description 3
- 239000005715 Fructose Substances 0.000 description 3
- WQZGKKKJIJFFOK-VFUOTHLCSA-N beta-D-glucose Chemical compound OC[C@H]1O[C@@H](O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-VFUOTHLCSA-N 0.000 description 3
- 238000001914 filtration Methods 0.000 description 3
- 235000011194 food seasoning agent Nutrition 0.000 description 3
- 239000000155 melt Substances 0.000 description 3
- 239000004750 melt-blown nonwoven Substances 0.000 description 3
- 239000010865 sewage Substances 0.000 description 3
- 229910010413 TiO 2 Inorganic materials 0.000 description 2
- 238000004378 air conditioning Methods 0.000 description 2
- 230000035622 drinking Effects 0.000 description 2
- 239000004744 fabric Substances 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 238000011144 upstream manufacturing Methods 0.000 description 2
- FKPUYTAEIPNGRM-UHFFFAOYSA-N 1-(diaminomethylidene)guanidine;hydron;chloride Chemical compound [Cl-].N\C([NH3+])=N/C(N)=N FKPUYTAEIPNGRM-UHFFFAOYSA-N 0.000 description 1
- HYZJCKYKOHLVJF-UHFFFAOYSA-N 1H-benzimidazole Chemical compound C1=CC=C2NC=NC2=C1 HYZJCKYKOHLVJF-UHFFFAOYSA-N 0.000 description 1
- 229920001817 Agar Polymers 0.000 description 1
- 239000004278 EU approved seasoning Substances 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- 241000191967 Staphylococcus aureus Species 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 239000008272 agar Substances 0.000 description 1
- 239000003570 air Substances 0.000 description 1
- 238000003915 air pollution Methods 0.000 description 1
- 230000001580 bacterial effect Effects 0.000 description 1
- 239000011324 bead Substances 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 239000003651 drinking water Substances 0.000 description 1
- 235000020188 drinking water Nutrition 0.000 description 1
- 230000009982 effect on human Effects 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 230000001747 exhibiting effect Effects 0.000 description 1
- 239000011152 fibreglass Substances 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 238000007306 functionalization reaction Methods 0.000 description 1
- 239000012760 heat stabilizer Substances 0.000 description 1
- 238000011081 inoculation Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 150000002978 peroxides Chemical class 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000008213 purified water Substances 0.000 description 1
- 238000012827 research and development Methods 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 238000001223 reverse osmosis Methods 0.000 description 1
- 239000004065 semiconductor Substances 0.000 description 1
- 238000003900 soil pollution Methods 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 239000004753 textile Substances 0.000 description 1
- 238000000108 ultra-filtration Methods 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 238000003911 water pollution Methods 0.000 description 1
Classifications
-
- 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
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/01—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with flat filtering elements
- B01D29/016—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with flat filtering elements with corrugated, folded or wound filtering elements
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D39/00—Filtering material for liquid or gaseous fluids
- B01D39/02—Loose filtering material, e.g. loose fibres
- B01D39/06—Inorganic material, e.g. asbestos fibres, glass beads or fibres
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
- B01D2239/04—Additives and treatments of the filtering material
- B01D2239/0442—Antimicrobial, antibacterial, antifungal additives
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
- B01D2239/06—Filter cloth, e.g. knitted, woven non-woven; self-supported material
- B01D2239/0604—Arrangement of the fibres in the filtering material
- B01D2239/0618—Non-woven
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
- B01D2239/10—Filtering material manufacturing
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
- B01D2239/12—Special parameters characterising the filtering material
- B01D2239/1216—Pore size
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
- B01D2239/12—Special parameters characterising the filtering material
- B01D2239/1291—Other parameters
Abstract
Description
본 발명은 유리섬유계 여재를 다층상으로 절곡후 필터를 제조하는 방법에 관한 것으로서, 특히 우수한 항균 성능을 보유하고 액체여과 특성 및 제거효율이 우수한 특성을 지닌 절곡필터의 제조방법에 관한 것이다.The present invention relates to a method for producing a filter after bending the glass fiber-based media in a multi-layered form, and more particularly, to a method for manufacturing a bending filter having excellent antibacterial performance and excellent characteristics of liquid filtration and removal efficiency.
최근들어 산업이 고도로 발달함에 따라 대기, 수질 및 토양 오염문제가 커다란 사회문제로 떠오르게 되었으며, 그중에서도 수질의 오염은 인간이 먹고 마시는데 직접적인 영향을 주게됨에 따라 그 문제성이 더 크게 부각되어왔다. 따라서 오염된 하수의 정화처리 방법과 일반수의 식수 또는 음료수의 사용을 위한 정수처리 방법이 다양하게 연구되어왔으며, 특히 역삼투막이나 한외여과막등의 막을 이용한 수질처리시스템이 활발히 연구되어지고 있다.In recent years, as the industry develops, the problem of air, water and soil pollution has emerged as a big social problem. Among them, the problem of water quality has been highlighted as it has a direct effect on human eating and drinking. Therefore, various methods of purifying polluted sewage and purified water for general drinking or drinking water have been studied. In particular, water treatment systems using membranes such as reverse osmosis membranes and ultrafiltration membranes have been actively studied.
이러한 수질처리시스템에 사용되는 필터는 그 종류가 다양하고 적용분야도 광범위한데, 예를 들어, 액체 정제용으로 부직포 및 다양한 종류의 막들을 이용해 절곡된 형태로 제조되는 액체필터가 미국, 일본 및 유럽 등지에서 개발되어 판매되고 있는 실정이다.The filters used in such water treatment systems are diverse and have a wide range of applications. For example, liquid filters manufactured in a bent form using non-woven fabrics and various kinds of membranes for liquid refining are available in the United States, Japan and Europe. The situation is developed and sold in places.
산업이 고도로 발전하게 됨에 따라 산업 장치들이 집적화, 정밀화되고 제조공정 뿐만 아니라 일반 사무실의 쾌적한 환경을 조성하기 위하여, 공조용 및 액체용 필터의 요구가 급속히 증대되었다. 그러나, 과거 공조용으로 사용되는 유리섬유 필터는 반도체 및 원자력발전소 등에서 유리섬유에 의한 2차 오염 뿐만 아니라, 폐기처리문제를 발생시키고, 필터제조공정 중의 조업시에 어려움이 발생하여 그 개선의 필요성이 대두되어 왔으며, 액체용으로 사용되고 있는 멜트블론(meltblown) 부직포의 경우는 짧은 수명과 낮은포집효율에 대한 개선이 요구되어왔다. 이에 따라 미국 및 일본을 중심으로 유리섬유의 대체 및 멜트블론 부직포의 고기능화를 위한 여재(media)개발이 중요한 문제로 여겨지게 되었으며, 특히 멜트블론 부직포의 경우, 생산량 및 다기능성이 매우 크게 증가되는 추세이며, 그에 따라 적용 범위도 점차 확대되고 있는 실정이다. 액체용 필터는 크게 수처리용과 오일처리용으로 나눌수 있으나 그 용도에 따라 세분화되어 각각의 용도에 따라 그 여재의 특성 또한 다양하게 요구되어 왔다.As the industry develops highly, the demands for air conditioning and liquid filters have rapidly increased in order to integrate and refine industrial devices and to create a pleasant environment for general offices as well as manufacturing processes. However, the glass fiber filters used for air conditioning in the past not only cause secondary pollution by glass fibers in semiconductors and nuclear power plants, but also cause disposal problems, and difficulties in operation during the filter manufacturing process have caused a need for improvement. In the case of meltblown nonwoven fabrics that have been emerging and used for liquids, improvements in short lifespan and low collection efficiency have been required. Accordingly, the development of media for the replacement of glass fiber and the high functionalization of meltblown nonwovens is considered to be an important problem, especially in the United States and Japan. Especially in the case of meltblown nonwoven fabrics, the production and versatility are greatly increased. As a result, the scope of application is gradually expanding. Liquid filters can be largely divided into water treatment and oil treatment, but they are subdivided according to their use, and various characteristics of the media have been required according to their respective uses.
특히 포도당 및 과당, 조미료 제조 공정액등의 고점도 액체를 정제하는 경우 유리섬유를 매체로 한 필터가 주로 사용되고 있으며, 이 경우 정제 공정중 유속 저항을 증가시키지 않고 이물 제거율이 높은 필터의 설계에 대한 요구가 계속되어져 왔다. 유리섬유를 매체로한 액체 여과용 필터의 경우 대한민국 특허출원 제 93- 702356 호에서는 수지-결합된 유리섬유 필터 매체를 이용하여 상향 및 하향면을 갖는 유리섬유 필터매체 및 필터 매체의 상향 및 하향면의 적어도 하나에 위치한 폴리머 메시를 함유하는 주름진 필터 요소를 포함하는 고점도 액체 여과용 필터제조에 관한 방법이 제시되어 있으나, 수지-결합된 유리섬유 필터 매체의 경우 고가의 문제점 및 포도당 및 과당, 조미료 제조 공정액등의 고점도 액체를 정제하는 필터에 적용하는 경우 제거효율은 우수한 반면 저유량의 문제점을 지닌다. 한편, 유리섬유 필터 매체를 이용한 포도당 및 과당, 조미료 제조 공정액등의 고점도 액체를 정제시 필터 외벽에 누적되는 글루코스 성분으로 인한 세균 번식의 문제점을 개선하기 위하여 필터지지체에 대하여 항균성을 부여하는 연구개발이 진행되어 왔는데, 예를 들어, 항균 기능을 부직포에 부여하는 방법으로 부직포를 제조하는 공정중 주로 스프레이법에 의해 후처리 공정에서 항균물질을 도포하는 방법이 사용되고 있으나, 공정 작업성의 어려움 및 마찰이나 세탁에 의한 내구성 저하, 의료용 부직포의 경우 인체에 대한 안전성등의 문제점을 지닌다. 또한 상기와 같은 문제점등을 개선하기 위한 방법으로 대한민국 특허출원 제 93-12277 호에서는 비다공성이면서 미립자에 의한 큰 표면적을 갖는 무기계 세라믹을 장섬유에 함유시켜 항균성을 갖는 PP 장섬유 부직포를 제조하는 방법이 제시되어 있고, 대한민국 특허출원 제 94-26076 호에서는 유기계 항균제로 벤즈 이미다졸 및 비구아니드 하이드로 클로라이드계 화합물을 투입하여 PP 장섬유 부직포를 제조하는 방법이 제시되어 있는데, 전자의 경우는 방사성등의 물성이 저하하는 문제점이 있고 후자의 경우는 항균성이 다소 미흡한 문제점이 있다.Especially in the case of refining high-viscosity liquids such as glucose, fructose and seasoning process liquids, filters based on fiberglass are mainly used.In this case, the demand for the design of filters with high foreign material removal rate without increasing the flow rate resistance during the refining process Has been going on. In the case of a filter for liquid filtration using glass fiber as a medium, Korean Patent Application No. 93-702356 discloses a glass fiber filter medium having an upward and a downward side using a resin-bonded glass fiber filter medium and an upward and downward side of a filter medium. A method for the manufacture of a filter for high viscosity liquid filtration comprising a pleated filter element containing a polymer mesh located on at least one of the elements has been proposed, but expensive problems with resin-bonded glass fiber filter media and the preparation of glucose, fructose and seasonings When applied to a filter for refining high-viscosity liquids, such as process liquids, the removal efficiency is excellent while having a low flow rate problem. Meanwhile, in order to improve the problem of bacterial propagation due to the glucose component accumulated on the filter outer wall when refining high viscosity liquids such as glucose, fructose, and seasoning process liquids using glass fiber filter media, research and development is given to the filter support. This has been progressed, for example, the method of applying the antimicrobial material in the post-treatment process mainly by the spray method in the process of manufacturing the nonwoven fabric by applying the antimicrobial function to the nonwoven fabric, but the difficulty of process workability and friction Durability deterioration due to washing, medical non-woven fabrics have problems such as safety to the human body. In addition, as a method for improving the above problems, Korean Patent Application No. 93-12277 discloses a method for producing a PP long fiber nonwoven fabric having antimicrobial properties by containing an inorganic ceramic having a large surface area by fine particles in a long fiber. In this case, Korean Patent Application No. 94-26076 discloses a method for preparing PP long fiber nonwoven fabric by adding benzimidazole and biguanide hydrochloride-based compound as an organic antimicrobial agent. There is a problem in that the physical properties of the latter, the latter has a problem that the antimicrobial properties are somewhat insufficient.
본 발명은 상기와 같은 유기섬유계 절곡필터의 문제점을 해결하기 위해 안출된 것으로서, 특히 부직포로 사용되는 폴리프로필렌 수지의 기본 물성을 저하시키지 않으면서도 항균성이 우수한 특성을 나타내는 액체 정제용 절곡필터의 제조방법을 제공하는 것을 목적으로 한 것이다.The present invention has been made to solve the problems of the organic fiber-based bending filter as described above, in particular, the production of a bending filter for liquid tablets exhibiting excellent antibacterial properties without reducing the basic physical properties of the polypropylene resin used as a nonwoven fabric The purpose is to provide a method.
본 발명은 상기 목적을 달성하기 위한 일 방법으로 폴리프로필렌 장섬유 부직포 제조시 유기계 항균제로 옥시비스 페녹사진계 유기계 항균제를 첨가하여 제조한 폴리프로필렌 장섬유 부직포를 지지체로 하고 유리섬유계 여재를 다층상으로 절곡하여 제조하는 것을 특징으로 한 절곡필터의 제조방법을 개시한다.The present invention is a polypropylene long fiber nonwoven fabric prepared by adding an oxybis phenoxazine-based organic antimicrobial agent as an organic antimicrobial agent when manufacturing a polypropylene long fiber nonwoven fabric as a method for achieving the above object as a support, and the glass fiber media in a multi-layer Disclosed is a method of manufacturing a bending filter, characterized by bending and manufacturing.
이하에서 본 발명을 구체적으로 설명한다.Hereinafter, the present invention will be described in detail.
본 발명에서는 폴리프로필렌 장섬유 부직포를 범용 폴리프로필렌 수지와 옥시비스 페녹사진계 항균제를 첨가하여 마스터 배치를 제조한 후 부직포 용도의 범용 폴리프로필렌 수지와 혼련하고 용융 방사 및 웹형성, 열접착 공정과 같은 주지의 부직포 제조공정을 거쳐 제조하며, 이렇게하여 얻어진 폴리프로필렌 장섬유 부직포를 상향 및 하향면의 지지체로 하고 유리섬유 여재를 다층상으로 절곡, 절단, 초음파 및 열접합공정 등을 거쳐 절곡필터를 제조한다.In the present invention, a polypropylene long fiber nonwoven fabric is prepared by adding a general polypropylene resin and an oxybis phenoxazine-based antimicrobial agent to prepare a master batch, and then kneading it with a general purpose polypropylene resin for nonwoven fabrics, such as melt spinning, web forming, and heat bonding processes. The polypropylene long fiber nonwoven fabric thus obtained is used as a support for the up and down surfaces, and the glass fiber media is folded, cut, ultrasonically and thermally bonded to produce a bending filter. .
본 발명에서 사용되는 옥시비스페녹사진계 유기 항균제의 투입 범위는 전체 부직포에 사용되는 폴리프로필렌 수지 총 중량의 0.5~2.0중량%로서, 0.5중량% 미만으로 사용하면 항균성이 미흡하고 2.0중량% 초과 사용하면 정제효율이 나빠지는 등의 문제점을 지닌다.The range of the oxybisphenoxazine-based organic antimicrobial agent used in the present invention is 0.5 to 2.0% by weight of the total weight of the polypropylene resin used in the entire nonwoven fabric, and when used in less than 0.5% by weight, the antimicrobial activity is insufficient and more than 2.0% by weight is used. There is a problem such as poor purification efficiency.
또한 필터여재로 사용되는 유리섬유 여재는 다층상으로 제작시 유리섬유 제1매체의 경우는 두께를 대략 0.1~3.0㎜, 평균기공 크기를 2~10㎛로 하고 유리섬유제2매체의 경우는 두께를 0.2~5.0㎜, 평균기공 크기를 1~10㎛ 범위로 하는 것이 좋으며, 또 필터 제조시 유효막 면적은 0.4~0.9㎡가 바람직하다.In addition, the glass fiber media used as the filter media should have a thickness of approximately 0.1 to 3.0 mm for the first glass fiber medium, an average pore size of 2 to 10 μm for the first glass fiber medium, and a thickness for the second glass fiber medium. It is preferable that the average pore size is in the range of 0.2 to 5.0 mm, and the range of 1 to 10 m, and the effective membrane area is 0.4 to 0.9 m 2 in the filter production.
이하에서 실시예 및 비교실시예를 들어 본 발명을 좀 더 구체적으로 설명한다. 이때 측정되는 물성은 하기와 같은 방법으로 측정한다.Hereinafter, the present invention will be described in more detail with reference to Examples and Comparative Examples. The physical properties measured at this time are measured in the following manner.
- 유량(flow rate : 순수 탱크에 18megaΩ의 순수를 넣고, 초기압력에 따른 처리유량을 유량계로 평가한다.-Flow rate: Into the pure water tank, 18megaΩ of pure water and the flow rate according to the initial pressure are evaluated by the flow meter.
- 제거효율(removal efficiency) : 오수 탱크에 폴리스티렌 비드를 넣고 일정비율로 순수와 섞어서 기어펌프를 통하여 투여시킨후, upstream 센서를 통하여 필터 통과전의 입자 수를 입자크기별로 측정한후, 필터를 통과한 유체를 downstream 센서를 통하여 유체의 입자수를 측정하여 입자개수의 변화로 측정한다.-Removal efficiency: Put polystyrene beads in the sewage tank, mix them with pure water at a certain ratio and administer them through the gear pump, measure the number of particles before passing the filter by particle size by the upstream sensor, and then pass through the filter. The fluid is measured by changing the particle count by measuring the particle number of the fluid through the downstream sensor.
- 포집능력(dirt holding capacity) : 오수 탱크에 입자를 넣고, downstream과 upstream의 차압이 35psi가 될 때가지 순환시킨 후, 필터의 무게변화를 측정하여 평가한다.Dirt holding capacity: The particles are placed in a sewage tank, circulated until the downstream and upstream differential pressure reaches 35 psi, and then measured by measuring the weight change of the filter.
- 항균성 : 일본섬유제품위생가공협회 평가규격인 쉐이크 플라스크(Shake Flask)법에 의하여 다층여재 상태에서의 항균성능을 평가한다. 즉, 황색 포도 상구균을 한천 배지에 접종하여 37℃에서 27시간 배양한 균을 접종원으로 하여 시험편에 접종한후 일정량의 액체를 가하여 시험편으로부터 세균을 액중에 추출시킨뒤 처리포와 미처리포의 액중에 잔존하는 세균의 수를 측정하여 항균제에 의한 세균의 감소 백분율을 계산한다.-Antimicrobial: The antimicrobial performance is evaluated in the state of multilayer media by the Shake Flask method, an evaluation standard of the Japan Textile Products Sanitary Processing Association. In other words, Staphylococcus aureus was inoculated into agar medium and inoculated into a specimen by inoculation with a bacterium cultured at 37 ° C. for 27 hours, and then a certain amount of liquid was added to extract bacteria from the specimen. The percentage of bacteria remaining by the antimicrobial agent is calculated by measuring the number of bacteria remaining.
<실시예 1><Example 1>
용융지수가 15이고 평균입경이 200㎛의 폴리프로필렌 파우더 92중량%, 항균제로서 10,10'-옥시비스 페녹사진 파우더 5중량%, TiO2분말 2.5중량%, 열안정제로서 이가녹스 1010(시바가이기사제품) 0.1중량%, 퍼록사이드(일본화약(주)제품) 0.4중량%로 구성된 마스터 배치 성분들을 혼합기에 넣고 혼합한후 트윈 스크류가 장착된 용융압출기를 이용하여 스크류 회전속도 200~250rpm, 용융온도 200~220℃의 조건에서 마스타배치 칩을 제조하였다. 제조된 칩을 진공 건조기에서 120℃ × 4시간 조건에서 건조한후 용융지수 35의 부직포용 폴리프로필렌 칩과 1:9로 혼련하여 210℃에서 용융 방사하고 웹형성 및 열접착 공정을 거쳐 항균 기능성을 보유하는 중량 60g/㎡ 폴리프로필렌 장섬유 부직포를 제조하여 상향 및 하향면의 다층여재의 지지체로 하고, 여기에 두께 0.35㎜, 평균기공 크기 3㎛인 유리섬유 제1매체와 두께 0.7㎜, 평균기공크기 2㎛인 유리섬유 제2매체를 4층여재로하여 유효 막면적 0.7㎡ 조건에서 통상의 방법으로 절곡, 절단, 초음파 및 열접합 공정을 거쳐 절곡 필터를 제조하였으며, 물성을 평가하여 그 결과를 표 1에 명기하였다.92 wt% of polypropylene powder with an average particle diameter of 200 μm with a melt index of 15 μm, 5 wt% of 10,10′-oxybisphenoxazine powder as an antibacterial agent, 2.5 wt% of TiO 2 powder, and Iganox 1010 (Shibagai as a heat stabilizer) Article)) 0.1% by weight, peroxide (0.4 kg) of master batch components into a mixer, mixed with a screw screw speed 200 ~ 250rpm, using a melt extruder equipped with a twin screw The master batch chip was manufactured under the conditions of the temperature of 200 ~ 220 ℃. The chips are dried in a vacuum dryer at 120 ℃ × 4 hours, kneaded with a polypropylene chip for nonwoven fabric of melt index 35 at 1: 9, melt spun at 210 ℃, and retained antibacterial function through web formation and heat bonding processes. A weight of 60 g / m 2 polypropylene long fiber nonwoven fabric was prepared and used as a support for the multilayer media of up and down surfaces, and the first glass fiber medium having a thickness of 0.35 mm and an average pore size of 3 μm and a thickness of 0.7 mm and an average pore size. Bending filter was prepared by bending, cutting, ultrasonic and thermal bonding process in the usual way under the effective film area of 0.7㎡ with 4μm glass fiber 2nd media with 2㎛, and evaluated the properties 1 is specified.
<실시예 2><Example 2>
실시예 1에 있어서 항균제 10,10'-옥시비스 페녹사진 파우더를 10중량%(항균제 투입농도 1.0%)로 변경한 것 이외에는 실시예 1과 동일한 조건 및 동일한 방법으로 실시하였으며, 그 결과를 표 1에 명기하였다.Except for changing the antimicrobial 10,10'-oxybis phenoxazine powder in Example 1 to 10% by weight (antibacterial concentration of 1.0%) was carried out under the same conditions and the same method as in Example 1, the results are shown in Table 1 It is specified in.
<실시예 3><Example 3>
실시예 1에 있어서 항균제 10,10'-옥시비스 페녹사진 파우더를 20중량%(항균제 투입농도 2.0%)로 변경한 것 이외에는 실시예 1과 동일한 조건 및 동일한 방법으로 실시하였으며, 그 결과를 표 1에 명기하였다.Except for changing the antimicrobial 10,10'-oxybis phenoxazine powder in Example 1 to 20% by weight (antibacterial concentration 2.0%) was carried out under the same conditions and the same method as in Example 1, the results are shown in Table 1 It is specified in.
<실시예 4><Example 4>
실시예 1에 있어서 유리섬유 제1매체의 두께 1.0㎜, 평균기공 크기 3㎛ 및 유리섬유 제2매체의 두께 1.0㎜, 평균기공 크기 2㎛로 변경한 것 이외에는 실시예 1과 동일한 조건 및 동일한 방법으로 실시하였으며, 그 결과를 표 1에 명기하였다.The same conditions and methods as in Example 1 were changed in Example 1 except that the thickness of the first glass fiber medium was 1.0 mm, the average pore size was 3 μm, and the thickness of the glass fiber second medium was 1.0 mm and the average pore size was 2 μm. It was carried out in, and the results are listed in Table 1.
<실시예 5>Example 5
실시예 1에 있어서 유리섬유 제1매체의 두께 2.0㎜, 평균기공 크기 3㎛ 및 유리섬유 제2매체의 두께 2.0㎜, 평균기공 크기 2㎛로 변경한 것 이외에는 실시예 1과 동일한 조건 및 동일한 방법으로 실시하였으며, 그 결과를 표 1에 명기하였다.The same conditions and the same method as in Example 1, except that the thickness of the glass fiber first medium was 2.0 mm, the average pore size was 3 μm, and the thickness of the glass fiber second medium was 2.0 mm, and the average pore size was 2 μm. It was carried out in, and the results are listed in Table 1.
<실시예 6><Example 6>
실시예 1에 있어서 유리섬유 제1매체의 두께 0.35㎜, 평균기공 크기 6㎛ 및 유리섬유 제2매체의 두께 0.7㎜, 평균기공 크기 6㎛로 변경한 것 이외에는 실시예 1과 동일한 조건 및 동일한 방법으로 실시하였으며, 그 결과를 표 1에 명기하였다.In Example 1, the same conditions and methods as in Example 1 were changed except that the thickness of the first glass fiber medium was 0.35 mm, the average pore size was 6 μm, and the thickness of the glass fiber second medium was 0.7 mm and the average pore size was 6 μm. It was carried out in, and the results are listed in Table 1.
<실시예 7><Example 7>
실시예 1에 있어서 두께 0.35㎜, 평균기공 크기 3㎛ 및 유리섬유 제1매체와 두께 0.7㎜, 평균기공 크기 2㎛인 유리섬유 제2매체를 4층여재로하고 유효 막면적을 0.4㎡ 조건으로 변경한 것 이외에는 실시예 1과 동일한 조건 및 동일한 방법으로 실시하였으며, 그 결과를 표 1에 명기하였다.In Example 1, four layers of 0.35 mm thick, 3 micron average pore size, glass fiber first medium, and a second glass fiber medium of 0.7 mm thickness and 2 μm average pore size were used, and the effective membrane area was 0.4 m 2. Except having changed, it carried out by the same conditions and the same method as Example 1, and the result was specified in Table 1.
<실시예 8><Example 8>
실시예 1에 있어서 두께 0.35㎜, 평균기공 크기 3㎛ 및 유리섬유 제1매체와 두께 0.7㎜, 평균기공 크기 2㎛인 유리섬유 제2매체를 4층여재로하고 유효 막면적을 0.9㎡ 조건으로 변경한 것 이외에는 실시예 1과 동일한 조건 및 동일한 방법으로 실시하였으며, 그 결과를 표 1에 명기하였다.In Example 1, four layers of 0.35 mm thick, average pore size 3 μm, glass fiber first medium, and 0.7 mm thick, average pore size 2 μm were used as four layer media, and the effective membrane area was 0.9 m 2. Except having changed, it carried out by the same conditions and the same method as Example 1, and the result was specified in Table 1.
<비교실시예 1>Comparative Example 1
용융지수 35의 부직포용 폴리프로필렌 칩과 TiO2마스타 배치(2.5중량%)를 9:1로 혼련하여 210℃에서 용융 방사하고 웹형성 및 열접착 공정을 거쳐 일반적인 폴리프로필렌 장섬유 부직포를 제조하여 상향 및 하향면의 다층여재의 지지체로 하고 여기에 두께 0.35㎜, 평균기공 크기 3㎛ 및 유리섬유 제1매체와 두께 0.7㎜, 평균기공 크기 2㎛인 유리섬유 제2매체를 4층여재로하고 유효 막면적을 0.7㎡ 조건에서 통상의 방법으로 절곡, 절단, 초음파 및 열접합 공정을 거쳐 절곡 필터를 제조하였으며, 물성을 평가하여 그 결과를 표 1에 명기하였다.Polypropylene chips for nonwoven fabrics with a melt index of 35 and TiO 2 master batches (2.5% by weight) were kneaded at 9: 1 for melt spinning at 210 ° C, followed by web formation and heat bonding to produce general polypropylene long fiber nonwoven fabrics. And a multi-layered support on the downward side, and having a thickness of 0.35 mm, an average pore size of 3 μm, and a glass fiber first medium and a thickness of 0.7 mm and an average pore size of 2 μm as four layer media. The membrane area was bent, cut, ultrasonically and thermally bonded in a conventional manner under the conditions of 0.7 m2 to produce a bent filter. The physical properties were evaluated and the results are shown in Table 1.
<비교실시예 2>Comparative Example 2
실시예 1에 있어서 항균제로서 첨가제 1인 10,10'-옥시비스 페녹사진 파우더를 30중량%(항균제 투입농도 3.0%)로 변경한 것 이외에는 실시예 1과 동일한 조건 및 동일한 방법으로 실시하였으며, 그 결과를 표 1에 명기하였다.In Example 1, except that 10,10'-oxybis phenoxazine powder, which is additive 1, as an antibacterial agent was changed to 30% by weight (antibacterial concentration 3.0%), the same procedure and the same method as in Example 1 were carried out. The results are listed in Table 1.
<비교실시예 3>Comparative Example 3
실시예 1에 있어서 유리섬유 제1매체의 두께 4.0㎜, 평균기공 크기 5㎛ 및 유리섬유 제2매체의 두께 6.0㎜, 평균기공 크기 5㎛로 변경한 것 이외에는 실시예1과 동일한 조건 및 동일한 방법으로 실시하였으며, 그 결과를 표 1에 명기하였다.The same conditions and the same method as in Example 1, except that the thickness of the glass fiber first medium was changed to 4.0 mm, the average pore size of 5 μm, and the thickness of the glass fiber second medium was 6.0 mm, and the average pore size was 5 μm. It was carried out in, and the results are listed in Table 1.
<비교실시예 4>Comparative Example 4
실시예 1에 있어서 두께 0.35㎜, 평균기공 크기 3㎛ 및 유리섬유 제1매체와 두께 0.7㎜, 평균기공 크기 2㎛인 유리섬유 제2매체를 4층여재로하고 유효 막면적을 0.2㎡ 조건으로 변경한 것 이외에는 실시예 1과 동일한 조건 및 동일한 방법으로 실시하였으며, 그 결과를 표 1에 명기하였다.In Example 1, four layers of 0.35 mm thick, 3 μm average pore size and 1 glass fiber first medium, and a second glass fiber medium of 0.7 mm thickness and 2 μm average pore size were used, and the effective membrane area was 0.2 m 2. Except having changed, it carried out by the same conditions and the same method as Example 1, and the result was specified in Table 1.
<비교실시예 5>Comparative Example 5
실시예 1에 있어서 두께 0.35㎜, 평균기공 크기 3㎛ 및 유리섬유 제1매체와 두께 0.7㎜, 평균기공 크기 2㎛인 유리섬유 제2매체를 4층여재로하고 유효 막면적을 1.3㎡ 조건으로 변경한 것 이외에는 실시예 1과 동일한 조건 및 동일한 방법으로 실시하였으며, 그 결과를 표 1에 명기하였다.In Example 1, four layers of 0.35 mm thick, 3 μm average pore size and 1 glass fiber first medium, and a second glass fiber medium of 0.7 mm thickness and 2 μm average pore size were used, and the effective membrane area was 1.3 m 2. Except having changed, it carried out by the same conditions and the same method as Example 1, and the result was specified in Table 1.
상기 실시예 및 비교실시예에서도 확인되듯이, 본 발명에 따라 제조된 절곡필터의 경우 유량 및 불순물 제거효율이 우수하면서도 항균성이 우수하여 액체 정제용으로 사용시 매우 유용하다.As can be seen from the above examples and comparative examples, the bending filter manufactured according to the present invention has excellent flow rate and impurities removal efficiency, but also has excellent antibacterial properties, which is very useful when used for liquid purification.
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
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KR20020054879A (en) * | 2000-12-28 | 2002-07-08 | 한형수 | Method for manufacturing bended filter to purifying fluid |
WO2006057726A1 (en) * | 2004-10-26 | 2006-06-01 | Reemay, Inc. | Composite filtration media |
KR100809145B1 (en) * | 2002-02-15 | 2008-02-29 | 주식회사 새 한 | Manufacturing method of bending filter of Ultra Filtration membrane for liquid |
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JPS62247816A (en) * | 1986-04-18 | 1987-10-28 | Kureha Chem Ind Co Ltd | Filter for air conditioner consisting of antimicrobial fiber cloth |
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KR0137382B1 (en) * | 1994-09-27 | 1998-04-25 | 박흥기 | Preparation method of antibiotic flat membrane |
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Publication number | Priority date | Publication date | Assignee | Title |
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KR20020054879A (en) * | 2000-12-28 | 2002-07-08 | 한형수 | Method for manufacturing bended filter to purifying fluid |
KR100809145B1 (en) * | 2002-02-15 | 2008-02-29 | 주식회사 새 한 | Manufacturing method of bending filter of Ultra Filtration membrane for liquid |
WO2006057726A1 (en) * | 2004-10-26 | 2006-06-01 | Reemay, Inc. | Composite filtration media |
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