KR102168260B1 - Photocatalytic composite activated carbon material introduced TiOF2 and manufacturing method thereof - Google Patents
Photocatalytic composite activated carbon material introduced TiOF2 and manufacturing method thereof Download PDFInfo
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- KR102168260B1 KR102168260B1 KR1020180151433A KR20180151433A KR102168260B1 KR 102168260 B1 KR102168260 B1 KR 102168260B1 KR 1020180151433 A KR1020180151433 A KR 1020180151433A KR 20180151433 A KR20180151433 A KR 20180151433A KR 102168260 B1 KR102168260 B1 KR 102168260B1
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- carbon material
- activated carbon
- titanium
- photocatalytic composite
- difluorooxide
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- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 102
- 239000000463 material Substances 0.000 title claims abstract description 45
- 239000002131 composite material Substances 0.000 title claims abstract description 32
- 230000001699 photocatalysis Effects 0.000 title claims abstract description 30
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 27
- 229910010273 TiOF2 Inorganic materials 0.000 title 1
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims abstract description 92
- 239000004408 titanium dioxide Substances 0.000 claims abstract description 46
- 238000000034 method Methods 0.000 claims abstract description 44
- 125000001153 fluoro group Chemical group F* 0.000 claims abstract description 27
- USEGOPGXFRQEMV-UHFFFAOYSA-N fluoro hypofluorite titanium Chemical compound [Ti].FOF USEGOPGXFRQEMV-UHFFFAOYSA-N 0.000 claims abstract description 27
- 239000003575 carbonaceous material Substances 0.000 claims abstract description 26
- YOBCTIIWHLYFII-UHFFFAOYSA-L difluorotitanium Chemical compound F[Ti]F YOBCTIIWHLYFII-UHFFFAOYSA-L 0.000 claims abstract description 23
- 230000008569 process Effects 0.000 claims abstract description 19
- 239000002243 precursor Substances 0.000 claims description 23
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 claims description 19
- 239000011737 fluorine Substances 0.000 claims description 19
- 229910052731 fluorine Inorganic materials 0.000 claims description 19
- 239000007789 gas Substances 0.000 claims description 19
- 239000000203 mixture Substances 0.000 claims description 17
- 238000002156 mixing Methods 0.000 claims description 13
- 238000004381 surface treatment Methods 0.000 claims description 11
- 229920000049 Carbon (fiber) Polymers 0.000 claims description 9
- 239000002904 solvent Substances 0.000 claims description 9
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 8
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims description 8
- 239000010936 titanium Substances 0.000 claims description 8
- 229910052719 titanium Inorganic materials 0.000 claims description 8
- 238000010336 energy treatment Methods 0.000 claims description 6
- 239000011261 inert gas Substances 0.000 claims description 6
- 238000001035 drying Methods 0.000 claims description 4
- 239000012153 distilled water Substances 0.000 claims description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 3
- -1 titanium difluorocarbon Chemical compound 0.000 claims description 2
- IKHGUXGNUITLKF-UHFFFAOYSA-N Acetaldehyde Chemical compound CC=O IKHGUXGNUITLKF-UHFFFAOYSA-N 0.000 abstract description 30
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 abstract description 22
- 239000000126 substance Substances 0.000 abstract description 12
- 238000013032 photocatalytic reaction Methods 0.000 abstract description 3
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical class C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 20
- 230000000052 comparative effect Effects 0.000 description 16
- 238000001179 sorption measurement Methods 0.000 description 15
- 239000000243 solution Substances 0.000 description 10
- 239000011148 porous material Substances 0.000 description 9
- VXUYXOFXAQZZMF-UHFFFAOYSA-N titanium(IV) isopropoxide Chemical compound CC(C)O[Ti](OC(C)C)(OC(C)C)OC(C)C VXUYXOFXAQZZMF-UHFFFAOYSA-N 0.000 description 8
- 238000004458 analytical method Methods 0.000 description 7
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 6
- 238000003682 fluorination reaction Methods 0.000 description 6
- 239000002245 particle Substances 0.000 description 6
- 238000002441 X-ray diffraction Methods 0.000 description 5
- 238000011282 treatment Methods 0.000 description 5
- 238000004833 X-ray photoelectron spectroscopy Methods 0.000 description 4
- 239000003054 catalyst Substances 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 4
- 235000019441 ethanol Nutrition 0.000 description 4
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 239000004566 building material Substances 0.000 description 3
- 238000011161 development Methods 0.000 description 3
- 208000008842 sick building syndrome Diseases 0.000 description 3
- 238000001291 vacuum drying Methods 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 description 2
- 230000000903 blocking effect Effects 0.000 description 2
- 239000013078 crystal Substances 0.000 description 2
- 230000001678 irradiating effect Effects 0.000 description 2
- PHTQWCKDNZKARW-UHFFFAOYSA-N isoamylol Chemical compound CC(C)CCO PHTQWCKDNZKARW-UHFFFAOYSA-N 0.000 description 2
- ZXEKIIBDNHEJCQ-UHFFFAOYSA-N isobutanol Chemical compound CC(C)CO ZXEKIIBDNHEJCQ-UHFFFAOYSA-N 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 238000009832 plasma treatment Methods 0.000 description 2
- 238000004626 scanning electron microscopy Methods 0.000 description 2
- 238000007086 side reaction Methods 0.000 description 2
- JMXKSZRRTHPKDL-UHFFFAOYSA-N titanium ethoxide Chemical compound [Ti+4].CC[O-].CC[O-].CC[O-].CC[O-] JMXKSZRRTHPKDL-UHFFFAOYSA-N 0.000 description 2
- XJDNKRIXUMDJCW-UHFFFAOYSA-J titanium tetrachloride Chemical compound Cl[Ti](Cl)(Cl)Cl XJDNKRIXUMDJCW-UHFFFAOYSA-J 0.000 description 2
- 239000012855 volatile organic compound Substances 0.000 description 2
- 206010003645 Atopy Diseases 0.000 description 1
- 206010019233 Headaches Diseases 0.000 description 1
- 206010047700 Vomiting Diseases 0.000 description 1
- 229910021536 Zeolite Inorganic materials 0.000 description 1
- 238000010306 acid treatment Methods 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- YHWCPXVTRSHPNY-UHFFFAOYSA-N butan-1-olate;titanium(4+) Chemical compound [Ti+4].CCCC[O-].CCCC[O-].CCCC[O-].CCCC[O-] YHWCPXVTRSHPNY-UHFFFAOYSA-N 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000011247 coating layer Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000002542 deteriorative effect Effects 0.000 description 1
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 1
- 201000010099 disease Diseases 0.000 description 1
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 1
- 208000002173 dizziness Diseases 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000000921 elemental analysis Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000004817 gas chromatography Methods 0.000 description 1
- 238000001879 gelation Methods 0.000 description 1
- 231100000869 headache Toxicity 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 229940035429 isobutyl alcohol Drugs 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- WVDDGKGOMKODPV-ZQBYOMGUSA-N phenyl(114C)methanol Chemical compound O[14CH2]C1=CC=CC=C1 WVDDGKGOMKODPV-ZQBYOMGUSA-N 0.000 description 1
- 239000011941 photocatalyst Substances 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- HKJYVRJHDIPMQB-UHFFFAOYSA-N propan-1-olate;titanium(4+) Chemical compound CCCO[Ti](OCCC)(OCCC)OCCC HKJYVRJHDIPMQB-UHFFFAOYSA-N 0.000 description 1
- 239000010453 quartz Substances 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000001878 scanning electron micrograph Methods 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- RCYJPSGNXVLIBO-UHFFFAOYSA-N sulfanylidenetitanium Chemical compound [S].[Ti] RCYJPSGNXVLIBO-UHFFFAOYSA-N 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 238000009210 therapy by ultrasound Methods 0.000 description 1
- UBZYKBZMAMTNKW-UHFFFAOYSA-J titanium tetrabromide Chemical compound Br[Ti](Br)(Br)Br UBZYKBZMAMTNKW-UHFFFAOYSA-J 0.000 description 1
- ZWYDDDAMNQQZHD-UHFFFAOYSA-L titanium(ii) chloride Chemical compound [Cl-].[Cl-].[Ti+2] ZWYDDDAMNQQZHD-UHFFFAOYSA-L 0.000 description 1
- YONPGGFAJWQGJC-UHFFFAOYSA-K titanium(iii) chloride Chemical compound Cl[Ti](Cl)Cl YONPGGFAJWQGJC-UHFFFAOYSA-K 0.000 description 1
- 239000003440 toxic substance Substances 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
- 230000008673 vomiting Effects 0.000 description 1
- 239000010457 zeolite Substances 0.000 description 1
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/30—Processes for preparing, regenerating, or reactivating
- B01J20/32—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
- B01J20/3231—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the coating or impregnating layer
- B01J20/3234—Inorganic material layers
- B01J20/3236—Inorganic material layers containing metal, other than zeolites, e.g. oxides, hydroxides, sulphides or salts
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/20—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising free carbon; comprising carbon obtained by carbonising processes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/30—Processes for preparing, regenerating, or reactivating
- B01J20/32—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
- B01J20/3214—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the method for obtaining this coating or impregnating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
- B01J27/06—Halogens; Compounds thereof
- B01J27/08—Halides
- B01J27/12—Fluorides
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/002—Catalysts characterised by their physical properties
- B01J35/004—Photocatalysts
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- B01J35/39—
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B32/00—Carbon; Compounds thereof
- C01B32/30—Active carbon
- C01B32/354—After-treatment
- C01B32/372—Coating; Grafting; Microencapsulation
Abstract
본 발명은 이불소산화티탄이 도입된 광촉매 복합 활성탄소재 및 그 제조방법을 제공한다. 이러한 이불소산화티탄이 도입된 광촉매 복합 활성탄소재는 불소 관능기의 도입으로 인하여 가시광의 광원으로도 광촉매 반응이 진행될 수 있어 포름알데히드, 아세트알데히드 등의 유해물질을 상온 및 가시광에서 획기적으로 제거할 수 있게 된다. 또한 본 발명의 제조방법은 비교적 단순한 공정일 뿐만 아니라, 활성탄소재를 기반으로 이불소산화티탄을 도입하였다는 점과 표면에 불소 관능기가 도입된 탄소재를 제조하여 보다 효과적으로 이산화티탄을 도입함으로써 결과적으로 활성탄소재에 상온 및 가시광에서 반응할 수 있는 이불소산화티탄을 도입하였다는 점에 그 특징이 있다. The present invention provides a photocatalytic composite activated carbon material into which titanium difluoride oxide is introduced and a method of manufacturing the same. The photocatalytic composite activated carbon material into which titanium difluorooxide is introduced can undergo a photocatalytic reaction even with a visible light source due to the introduction of a fluorine functional group, so that harmful substances such as formaldehyde and acetaldehyde can be drastically removed from room temperature and visible light. do. In addition, the manufacturing method of the present invention is not only a relatively simple process, but also the fact that titanium difluoride was introduced based on an activated carbon material, and a carbon material having a fluorine functional group introduced on the surface was prepared, thereby introducing titanium dioxide more effectively. Its characteristic is that titanium difluoride, which can react at room temperature and visible light, is introduced into the activated carbon material.
Description
본 발명은 이불소산화티탄(TiOF2)이 도입된 광촉매 복합 활성탄소재 및 그 제조방법에 관한 것으로서, 보다 상세하게는 표면에 불소 관능기가 도입된 탄소재를 이산화티탄 전구체 용액과 혼합하고, 에너지를 처리함으로써 이불소산화티탄을 도입한 광촉매 복합 활성탄소재 및 그 제조방법에 관한 것이다.The present invention relates to a photocatalytic composite activated carbon material into which titanium difluorooxide (TiOF 2 ) is introduced and a method for manufacturing the same, and more particularly, a carbon material into which a fluorine functional group is introduced on the surface is mixed with a titanium dioxide precursor solution, and energy is It relates to a photocatalytic composite activated carbon material in which titanium difluoride is introduced by treatment, and a method of manufacturing the same.
본 발명은 이불소산화티탄을 높은 함량으로 도입할 수 있는 새로운 제조방법을 제공하는 것이다.The present invention is to provide a new manufacturing method capable of introducing titanium difluoride oxide in a high content.
또한, 본 발명은 포름알데히드, 아세트알데히드 등의 유해물질을 상온 및 가시광에서 획기적으로 제거할 수 있도록 하는 새로운 복합 활성탄소재의 제조방법을 제공하는 것이다.In addition, the present invention is to provide a new method for manufacturing a composite activated carbon material capable of remarkably removing harmful substances such as formaldehyde and acetaldehyde at room temperature and visible light.
산업의 발전에 따라 기능성과 편리성을 충족하는 다양한 건축자재의 개발이 유도되어 왔으며, 이에 따라 각종 화학물질 및 복합재료로 구성된 건축자재의 개발과 사용이 증가되어 왔다. 그러나 이러한 건축자재는 포름알데히드(HCHO)나 휘발성유기화합물(Volatiile Organic Compounds; VOCs)과 같은 각종 유해물질을 배출하여 실내공기의 오염을 초래하며 인체에 노출 되었을 시 거주자에게 두통, 구토, 현기증, 아토피 질환 등을 유발하는 이른바 새집증후군(Sick House Syndrome)의 원인이 된다. With the development of the industry, the development of various building materials that satisfies functionality and convenience has been induced, and accordingly, the development and use of building materials composed of various chemical substances and composite materials has increased. However, these building materials emit various harmful substances such as formaldehyde (HCHO) and volatile organic compounds (VOCs), causing contamination of the indoor air. When exposed to the human body, residents may suffer from headache, vomiting, dizziness, and atopy. It is the cause of so-called sick house syndrome (Sick House Syndrome) that causes diseases.
최근 신축 건물이 날로 증가함에 따라 실내오염도에 대한 관심이 높아지고 있으며, 새집증후군의 원인이 되는 유해물질 중의 포름알데히드나 아세트알데히드 가스를 처리하기 위하여 제올라이트, 활성탄소, 활성탄소섬유 등의 재료를 사용하여 흡착하는 방법이 많이 사용되고 있다. 하지만 이러한 재료를 통한 단순한 기공에 의한 물리적 흡착만으로는 완벽한 제거가 어렵기 때문에, 이를 개선하기 위해 위와 같은 재료에 대한 다양한 표면처리가 연구되고 있다. As new buildings increase day by day, interest in indoor pollution is increasing, and materials such as zeolite, activated carbon, and activated carbon fiber are used to treat formaldehyde or acetaldehyde gas among harmful substances that cause sick house syndrome. Adsorption method is widely used. However, since it is difficult to completely remove only by physical adsorption by simple pores through these materials, various surface treatments for the above materials have been studied to improve this.
통상적으로 산 처리, 플라즈마 처리, 촉매 도입 등의 표면처리법이 사용되고 있으며, 그 중 촉매를 이용한 산화방법은 유해물질을 인체에 무해한 물질로 전환하여 제거할 수 있다는 장점이 있다. 하지만 촉매를 활성화시키기 위해서는 열 에너지나 빛 에너지와 같은 추가적인 에너지가 필요하다는 점에서 많은 제약이 따르고 있다. 따라서 공정이 단순하면서도 추가적인 에너지원 없이 가시광에서 작용하는 촉매를 제조하는 기술이 절실히 요구되고 있는 실정이다.Surface treatment methods such as acid treatment, plasma treatment, and catalyst introduction are generally used. Among them, the oxidation method using a catalyst has the advantage of converting and removing harmful substances into substances harmless to the human body. However, there are many restrictions in that additional energy such as thermal energy or light energy is required to activate the catalyst. Therefore, there is an urgent need for a technology for producing a catalyst that operates in visible light without an additional energy source while the process is simple.
본 발명의 목적은 이불소화티탄이 도입된 광촉매 복합 활성탄소재 및 이의 제조방법을 제공하는 것이다.It is an object of the present invention to provide a photocatalytic composite activated carbon material into which titanium difluoride is introduced and a method for manufacturing the same.
본 발명은 용이하게 상대적으로 높은 함량의 이불소화티탄을 도입한 광촉매 복합 활성탄소재 및 이의 제조방법을 제공하는 것이다.The present invention is to provide a photocatalytic composite activated carbon material in which a relatively high content of titanium difluoride is easily introduced, and a method for manufacturing the same.
본 발명의 다른 목적은 이불소산화티탄이 도입된 광촉매 복합 활성탄소재 및 이의 제조방법을 제공함으로써, 포름알데히드, 아세트알데히드 등의 유해물질을 상온 및 가시광에서 획기적으로 제거할 수 있도록 함에 있다Another object of the present invention is to provide a photocatalytic composite activated carbon material into which titanium difluoride oxide is introduced and a method for manufacturing the same, thereby enabling toxic substances such as formaldehyde and acetaldehyde to be drastically removed at room temperature and visible light.
상기 목적을 달성하기 위하여, 본 발명은In order to achieve the above object, the present invention
이불소산화티탄이 도입된 광촉매 복합 활성탄소재를 제공한다.It provides a photocatalytic composite activated carbon material in which titanium difluorooxide is introduced.
또한, 본 발명은In addition, the present invention
표면에 불소 관능기가 도입된 탄소재를 제조하는 단계;Preparing a carbon material having a fluorine functional group introduced thereto;
상기 불소 관능기가 도입된 탄소재와 이산화티탄 전구체 용액을 혼합하는 단계; 및Mixing the carbon material into which the fluorine functional group is introduced and a titanium dioxide precursor solution; And
상기 혼합물에 에너지를 처리하여 탄소재에 이불소산화티탄을 도입하는 단계; 를 포함하는 이불소산화티탄이 도입된 광촉매 복합 활성탄소재의 제조방법을 제공한다.Treating the mixture with energy to introduce titanium difluoride oxide into the carbon material; It provides a method of manufacturing a photocatalytic composite activated carbon material into which titanium difluorooxide is introduced.
본 발명에 의할 경우, 활성탄소재 기반에 이불소산화티탄을 도입함으로써, 이불소산화티탄이 도입된 광촉매 복합 활성탄소재를 제조할 수 있다. According to the present invention, a photocatalytic composite activated carbon material into which titanium difluorooxide is introduced can be prepared by introducing titanium difluorooxide into the activated carbon material base.
본 발명의 제조방법은 비교적 단순한 공정일뿐만 아니라 이러한 이불소산화티탄이 도입된 광촉매 복합 활성탄소재는 불소 관능기의 도입으로 인하여 가시광의 광원으로도 광촉매 반응이 진행될 수 있어 포름알데히드, 아세트알데히드 등의 유해물질을 상온 및 가시광에서 획기적으로 제거할 수 있게 된다.The manufacturing method of the present invention is not only a relatively simple process, but the photocatalytic composite activated carbon material into which titanium difluorooxide is introduced can undergo a photocatalytic reaction even with a light source of visible light due to the introduction of a fluorine functional group, thus harmful to formaldehyde and acetaldehyde Substances can be drastically removed at room temperature and visible light.
도 1은 실시예 1 내지 4 및 비교예 1, 2의 SEM 이미지를 나타낸 것이다.
도 2는 실시예 1 내지 4 및 비교예 1, 2의 XRD 분석 그래프이다1 shows SEM images of Examples 1 to 4 and Comparative Examples 1 and 2.
2 is an XRD analysis graph of Examples 1 to 4 and Comparative Examples 1 and 2
이하에서 본 발명에 대하여 구체적으로 설명한다. Hereinafter, the present invention will be described in detail.
본 명세서에서 사용되는 용어는 따로 정의하지 않는 경우 해당 분야에서 통상의 지식을 가진 자가 일반적으로 이해하는 내용으로 해석되어야 할 것이다. 본 명세서의 도면 및 실시예는 통상의 기술자가 본 발명을 쉽게 이해하고 실시하기 위한 것으로 도면 및 실시예에서 발명의 요지를 흐릴 수 있는 내용은 생략될 수 있으며, 본 발명이 도면 및 실시예로 한정되는 것은 아니다.Unless otherwise defined, terms used in this specification should be interpreted as generally understood by those of ordinary skill in the relevant field. The drawings and embodiments of the present specification are for a person skilled in the art to easily understand and implement the present invention, and contents that may obscure the gist of the invention in the drawings and examples may be omitted, and the present invention is limited to the drawings and examples. It does not become.
본 발명에서 사용되는 용어의 단수 형태는 특별한 지시가 없는 한 복수 형태도 포함하는 것으로 해석될 수 있다.The singular form of the terms used in the present invention may be interpreted as including the plural form unless otherwise indicated.
본 발명에서 특별한 언급 없이 불분명하게 사용된 %의 단위는 중량%를 의미한다.In the present invention, the unit of% used unclearly without special mention means% by weight.
본 발명은 상술한 기술적 과제의 해결을 위해 이불소산화티탄이 도입된 광촉매 복합 활성탄소재를 제공한다. 이는 유해물질의 단순한 기공에 의한 물리적 흡착뿐만 아니라 광촉매를 통한 효과적인 화학적 흡착 및 분해를 가능하게 하고, 기존의 이산화티탄이 도입된 활성탄소섬유와는 달리 상온 및 가시광에서 광촉매 반응이 진행되도록 함으로써 포름알데히드, 아세트알데히드 등의 유해물질을 상온 및 가시광에서도 효과적으로 제거할 수 있게 된다.The present invention provides a photocatalytic composite activated carbon material into which titanium difluorooxide is introduced to solve the above technical problem. This enables effective chemical adsorption and decomposition through photocatalyst as well as physical adsorption of harmful substances by simple pores, and unlike conventional activated carbon fibers into which titanium dioxide is introduced, formaldehyde reacts at room temperature and visible light by photocatalytic reaction. , It is possible to effectively remove harmful substances such as acetaldehyde at room temperature and visible light.
상기 활성탄소재의 일 예로 통상적으로 잘 알려져 있는 활성탄소, 활성탄소섬유 및 이들의 혼합물 중에서 선택될 수 있다. 다만 상대적으로 취급이 용이한 활성탄소섬유인 것이 바람직하나 반드시 이에 한정되는 것은 아니다.As an example of the activated carbon material, it may be selected from commonly known activated carbon, activated carbon fibers, and mixtures thereof. However, it is preferable that the activated carbon fiber is relatively easy to handle, but is not limited thereto.
상기 활성탄소재는 흡착용량과 장기간의 사용 등을 고려하여 비표면적이 1000㎡/g 이상인 것이 바람직하나, 반드시 이에 한정되는 것은 아니다.The activated carbon material preferably has a specific surface area of 1000 m 2 /g or more in consideration of adsorption capacity and long-term use, but is not limited thereto.
상기 활성탄소재는 상온 및 가시광에서 유해물질에 대한 효과적인 분해능을 담보하고 기공의 막힘 현상으로 흡착점이 감소되어 흡착효율이 저하되는 것을 방지하기 위하여 표면에 티탄이 10 내지 20%, 불소 관능기가 5 내지 15% 도입된 것이 바람직하나, 반드시 이에 한정되는 것은 아니다.The activated carbon material has 10 to 20% titanium and 5 to 15 fluorine functional groups on the surface in order to ensure effective resolution of harmful substances at room temperature and visible light, and to prevent a decrease in adsorption efficiency due to a decrease in adsorption point due to clogging of pores. % Is preferably introduced, but is not necessarily limited thereto.
또한, 본 발명은 이불소산화티탄이 도입된 탄소재를 제조하는 방법을 제공하는데, 그 제조방법은, 표면에 불소 관능기가 도입된 탄소재를 제조하는 단계; 상기 불소 관능기가 도입된 탄소재와 이산화티탄 전구체 용액을 혼합하는 단계; 및 상기 혼합물에 에너지를 처리하여 탄소재에 이불소산화티탄을 도입하는 단계; 를 포함하여 이루어진다.In addition, the present invention provides a method of manufacturing a carbon material into which titanium difluoride oxide is introduced, the method comprising: preparing a carbon material into which a fluorine functional group is introduced into the surface; Mixing the carbon material into which the fluorine functional group is introduced and a titanium dioxide precursor solution; And treating the mixture with energy to introduce titanium difluorooxide into the carbon material. It is made including.
이러한 제조방법은 비교적 단순한 공정일 뿐만 아니라, 활성탄소재를 기반으로 이불소산화티탄을 도입하였다는 점과 표면에 불소 관능기가 도입된 탄소재를 제조하여 보다 효과적으로 이산화티탄을 도입함으로써 결과적으로 활성탄소재에 상온 및 가시광에서 반응할 수 있는 이불소산화티탄을 도입하였다는 점에 그 특징이 있다. This manufacturing method is not only a relatively simple process, but also the fact that titanium difluoride was introduced based on the activated carbon material, and the carbon material with a fluorine functional group introduced on the surface was prepared to introduce titanium dioxide more effectively. It is characterized by the introduction of titanium difluoride, which can react at room temperature and visible light.
상기 제조방법에서의 탄소재는 다공성 탄소재로 알려진 어느 것을 사용하여도 무방하며, 일 예로 통상적으로 잘 알려져 있는 활성탄소, 활성탄소섬유 및 이들의 혼합물 중에서 선택될 수 있다. 다만 상대적으로 취급이 용이한 활성탄소섬유를 사용하는 것이 바람직하나, 반드시 이에 한정되는 것은 아니다.The carbon material in the above production method may be any known porous carbon material, and for example, it may be selected from commonly known activated carbon, activated carbon fibers, and mixtures thereof. However, it is preferable to use activated carbon fiber that is relatively easy to handle, but is not limited thereto.
상기 불소 관능기의 도입은 불소가스를 이용한 표면처리과정을 포함하는 공정을 통하여 이루어질 수 있다. 이는 후속단계에서 이산화티탄을 보다 효과적으로 도입하기 위한 과정이다. 상기 불소가스는 불소가 포함된 다양한 재료로부터 도입이 가능하며, 구체적으로 직접불소화법, 불소플라즈마 처리를 통해 도입이 가능하다. 일 예로 직접불소화법을 이용한 불소 관능기의 도입 과정은 비활성 가스를 주입하고 배기하는 과정을 3회 거친 후 불소가스와 반응시킴으로써 부반응을 최소화시키는 것이 바람직하다.The fluorine functional group may be introduced through a process including a surface treatment process using fluorine gas. This is a process for more effective introduction of titanium dioxide in a subsequent step. The fluorine gas can be introduced from various materials containing fluorine, and specifically, can be introduced through direct fluorination or fluorine plasma treatment. For example, in the process of introducing the fluorine functional group using the direct fluorination method, it is preferable to minimize side reactions by reacting with fluorine gas after injecting and evacuating an inert gas three times.
상기 불소가스를 이용한 표면처리과정은, 불소 관능기 도입의 미흡, 과반응으로 인한 기공의 구조 변형 및 이에 따른 흡착효율의 저하를 방지하기 위하여 25 내지 50℃의 온도에서 5 내지 15분 동안 이루어지는 것이 바람직하나, 반드시 이에 한정되는 것은 아니다.The surface treatment process using fluorine gas is preferably performed for 5 to 15 minutes at a temperature of 25 to 50° C. in order to prevent poor introduction of fluorine functional groups, structural deformation of pores due to overreaction, and decrease in adsorption efficiency accordingly. However, it is not necessarily limited thereto.
상기 불소가스를 이용한 표면처리과정은, 상술한 바와 같은 이유로 비활성가스 분위기에서 반응기 내 비활성가스 대비 불소가스 압력이 0.1 내지 0.3bar의 범위에서 이루어지는 것이 바람직하나, 반드시 이에 한정되는 것은 아니다.The surface treatment process using the fluorine gas is preferably performed in a range of 0.1 to 0.3 bar fluorine gas pressure relative to the inert gas in the reactor in an inert gas atmosphere for the same reason as described above, but is not limited thereto.
상기 불소 관능기가 도입된 탄소재는 불소 관능기 함량이 1 내지 10 중량비일 수 있다. 이는 상술한 바와 같이 탄소재에 불소 관능기가 적절한 함량으로 도입된 경우 후속단계에서 이산화티탄을 보다 효과적으로 도입할 수 있으며, 또한 티탄 및 불소 관능기가 과도하게 도입되어 기공을 막음으로써 흡착효율을 저하시키는 것을 방지할 수 있기 때문이다. 다만 반드시 이에 한정되는 것은 아니다.The carbon material into which the fluorine functional group is introduced may have a fluorine functional group content of 1 to 10 weight ratio. As described above, when the fluorine functional group is introduced in the carbon material in an appropriate amount, titanium dioxide can be more effectively introduced in the subsequent step, and the adsorption efficiency is reduced by blocking pores due to excessive introduction of titanium and fluorine functional groups. Because it can be prevented. However, it is not necessarily limited thereto.
상기 혼합하는 단계의 혼합비율은, 이산화티탄이 탄소재 표면에 제대로 도입되지 못하거나 반대로 이산화티탄이 과도하게 도입되어 기공을 막음으로써 흡착효율이 저하되는 것을 방지하기 위해 상기 이산화티탄 전구체 용액 100 중량부에 대해 상기 불소 관능기가 도입된 탄소재가 1.5 내지 3 중량부인 것이 바람직하나, 반드시 이에 한정되는 것은 아니다.The mixing ratio of the mixing step is 100 parts by weight of the titanium dioxide precursor solution in order to prevent the adsorption efficiency from deteriorating by preventing the titanium dioxide from being properly introduced to the surface of the carbon material, or by blocking the pores due to excessive introduction of titanium dioxide. The carbon material into which the fluorine functional group is introduced is preferably 1.5 to 3 parts by weight, but is not necessarily limited thereto.
상기 이산화티탄 전구체 용액은 알코올 용매와 이산화티탄 전구체를 혼합하여 제조할 수 있다. The titanium dioxide precursor solution may be prepared by mixing an alcohol solvent and a titanium dioxide precursor.
이산화티탄 전구체와 혼합되는 용매는 통상의 졸-겔 반응에서 사용되는 모든 용매를 사용할 수 있는데, 일 예로 메틸알코올, 에틸알코올, 이소프로필알코올, 부틸알코올, 벤질알코올, 이소아밀알코올, 이소부틸알코올 및 이들의 혼합물로 이루어지는 군으로부터 선택될 수 있다.The solvent mixed with the titanium dioxide precursor may be any solvent used in a conventional sol-gel reaction, for example, methyl alcohol, ethyl alcohol, isopropyl alcohol, butyl alcohol, benzyl alcohol, isoamyl alcohol, isobutyl alcohol, and It may be selected from the group consisting of mixtures thereof.
이산화티탄 전구체는 티타늄을 포함하는 모든 화합물을 사용할 수 있는데, 일 예로 티타늄 에톡사이드, 티타늄 이소프로폭사이드, 티타늄 프로폭사이드, 티타늄 부톡사이드, 티타늄 테트라에톡사이드, 티타늄 테트라이소프로폭사이드, 티타늄 테트라부톡사이드, 티타늄 클로라이드, 티타늄 다이클로라이드, 티타늄 트리클로라이드, 티타늄 테트라클로라이드, 티타늄 브로마이드, 티타늄 설파이드 및 이들의 혼합물로 이루어진 군으로부터 선택될 수 있다.Titanium dioxide precursor may be used any compound containing titanium, for example, titanium ethoxide, titanium isopropoxide, titanium propoxide, titanium butoxide, titanium tetraethoxide, titanium tetraisopropoxide, titanium It can be selected from the group consisting of tetrabutoxide, titanium chloride, titanium dichloride, titanium trichloride, titanium tetrachloride, titanium bromide, titanium sulfide, and mixtures thereof.
상기 알코올 용매와 상기 이산화티탄 전구체의 혼합 비율은알코올 용매 100 중량부를 기준으로 이산화티탄 전구체가 8 내지 43 중량부일 수 있다. 이는 후속단계에서 탄소재에 이산화티탄을 적절하게 도입시키면서도 탄소재에 이산화티탄이 응집되어 도입되거나, 입자의 크기가 불균일하게 도입되는 것을 방지하기 위함이다. The mixing ratio of the alcohol solvent and the titanium dioxide precursor may be 8 to 43 parts by weight of the titanium dioxide precursor based on 100 parts by weight of the alcohol solvent. This is to prevent the introduction of agglomerated titanium dioxide into the carbon material while introducing titanium dioxide into the carbon material appropriately in the subsequent step, or introducing uneven particle size.
본 발명에 있어서, 상기 혼합하는 단계 후 혼합물을 겔화하는 단계를 더 포함할 수 있다. 이는 상기 탄소재에 이산화티탄 및 이불소산화티탄을 보다 효과적으로 도입할 수 있도록 하며, 다공성 물질이 얇은 형태로 만들어지는 경우 갖게 되는 높은 표면적과 작은 기공 사이즈를 기대할 수 있도록 한다.In the present invention, it may further include gelling the mixture after the mixing step. This makes it possible to more effectively introduce titanium dioxide and titanium difluoride oxide into the carbon material, and it is possible to expect a high surface area and a small pore size to have when the porous material is made in a thin form.
상기 겔화하는 단계는 승온 조건에서 티타늄 전구체 코팅층이 졸상태에서 겔상태로 전이되면서 이산화티탄 및/또는 이불소산화티탄의 형태가 형성되는 단계를 의미한다.The step of gelling refers to a step in which the titanium precursor coating layer transitions from a sol state to a gel state under elevated temperature conditions to form a form of titanium dioxide and/or titanium difluoride oxide.
상기 겔화하는단계는, 반응을 진행시키면서도 굳는 현상을 방지하기 위하여 25 내지 30℃의 온도범위에서 12 내지 24시간 이루어지는 것이 바람직하나, 반드시 이에 한정되는 것은 아니다.The gelling step is preferably performed for 12 to 24 hours at a temperature range of 25 to 30° C. in order to prevent hardening while proceeding the reaction, but is not limited thereto.
본 발명에 있어서, 혼합물을 겔화하는 단계 후 겔화 혼합물을 추가적으로 건조시키는 단계를 더 포함할 수 있다. 이는 이산화티탄 전구체 용액의 남은 용매를 제거함으로써 보다 효과적으로 후속단계를 진행시키기 위함이다.In the present invention, after the step of gelling the mixture, a step of additionally drying the gelled mixture may be further included. This is to more effectively proceed to the next step by removing the remaining solvent of the titanium dioxide precursor solution.
상기 에너지 처리는, 초음파를 이용한 에너지 처리 과정을 포함할 수 있다. 상기 초음파를 이용한 에너지 처리 과정은 상기 혼합물을 증류수에 투입하고, 10 내지 50kHz 진동수범위에서 30 내지 60분 동안 이루어지는 것이 바람직하다. 이는 적절한 에너지 공급 및 부반응의 발생을 방지하기 위함이며, 반드시 이에 한정되는 것은 아니다.The energy treatment may include an energy treatment process using ultrasonic waves. The energy treatment process using ultrasonic waves is preferably carried out for 30 to 60 minutes in a frequency range of 10 to 50 kHz by adding the mixture to distilled water. This is to prevent occurrence of appropriate energy supply and side reactions, but is not necessarily limited thereto.
이하 실시예를 통해 본 발명을 더욱 상세하게 설명한다.The present invention will be described in more detail through the following examples.
이하 본 발명의 실시예 및 비교예에 따른 분석방법은 하기와 같다.Hereinafter, analysis methods according to Examples and Comparative Examples of the present invention are as follows.
건조된 활성탄소섬유 (평균 직경 10μm, BET 1500㎡/g)를 반응기에 투입하고 기상 불소 표면처리를 통해 오직 불소 관능기만을 도입하기 위하여 반응기 내부를 비활성 상태로 유지하였다. 반응기 내부를 진공감압으로 배기하고 질소의 비활성가스를 주입하는 과정을 3회 반복하였다. 이후 상기 반응기에 불소가스 압력이 0.1bar가 되도록 주입하고 상온에서 10분 동안 반응시켜 상기 활성탄소섬유 표면에 불소 관능기를 도입하였다.The dried activated carbon fiber (
상기 불소 관능기를 도입한 후, 이산화티탄 전구체(티타늄 이소프로폭사이드(titanium isopropoxide, TTIP, 97.0%, Aldrich, USA)) 이소프로필 알코올 용액을 0.5M이 되도록 제조하였다. 상기 기상 불소 표면처리된 활성탄소섬유 3g과 상기 이산화티탄 전구체 용액 200ml를 혼합하여 약 12시간 교반하고, 겔화 및 건조하였다.After introducing the fluorine functional group, a titanium dioxide precursor (titanium isopropoxide, TTIP, 97.0%, Aldrich, USA) was prepared so that an isopropyl alcohol solution of 0.5M. The gas phase fluorine surface-treated activated carbon fiber 3g and 200ml of the titanium dioxide precursor solution were mixed, stirred for about 12 hours, gelled and dried.
상기 겔화한 후 건조된 활성탄소섬유를 증류수에 넣고 40분 동안 초음파처리를 실시하여 활성탄소섬유 표면에 이불소산화티탄의 전환을 완료하여 도입하였다.After the gelation, the dried activated carbon fiber was added to distilled water and subjected to ultrasonic treatment for 40 minutes to complete the conversion of titanium difluoride on the surface of the activated carbon fiber and introduced.
상기 제조된 광촉매 복합 활성탄소섬유 원소함량을 X-선 광전자 분광기(X-ray photoelectron spectroscopy; XPS), Thermo Fisher Scientific사의 VG Multilab 2000모델을 사용하여 측정하였으며, 그 함량을 표 1에 기재하였다.The prepared photocatalytic composite activated carbon fiber element content was measured using an X-ray photoelectron spectroscopy (XPS), Thermo Fisher Scientific's VG Multilab 2000 model, and the content is shown in Table 1.
또한, 이불소산화티탄의 도입정도를 주사전자현미경 (Scanning electron microscopey; SEM) (Hitachi사의 S-4800)을 이용하여 5000배로 확대하여 관찰한 것을 도 1에 수록하였다.In addition, the degree of introduction of titanium difluoride oxide was observed by magnifying 5000 times using a scanning electron microscope (SEM) (Hitachi's S-4800) and observed in FIG. 1.
또한, PANalytical사의 X'Pert PRO모델을 사용하여 XRD(X-ray diffraction)를 측정하였으며 도 2에 기재하였다. 시료는 진공 건조 오븐으로 수분을 건조시켜 사용했으며, 상온에서 Cu KαX-선을 조사하여 분석을 진행하였다.In addition, XRD (X-ray diffraction) was measured using PANalytical's X'Pert PRO model, and it is described in FIG. 2. The sample was used after drying moisture in a vacuum drying oven, and the analysis was conducted by irradiating Cu KαX-rays at room temperature.
또한, 아세트알데히드의 흡착특성 평가 결과를 표 2에 기재하였다.In addition, the evaluation results of the adsorption properties of acetaldehyde are shown in Table 2.
상기 실시예 1에서 이산화티탄 전구체 용액의 농도가 0.8M이 되도록 수행한 것을 제외하고 상기 실시예 1과 동일하게 수행하여 활성탄소섬유 표면에 이불소산화티탄을 도입하였다.In the same manner as in Example 1, except that the concentration of the titanium dioxide precursor solution was 0.8 M in Example 1, titanium difluoride was introduced into the surface of the activated carbon fiber.
상기 실시예 1에서 반응기에 주입되는 불소가스 압력이 0.2bar가 되도록 주입한 것을 제외하고 상기 실시예 1과 동일하게 수행하여 활성탄소섬유 표면에 이불소산화티탄을 도입하였다.In Example 1, titanium difluoride was introduced on the surface of the activated carbon fiber in the same manner as in Example 1, except that the pressure of fluorine gas injected into the reactor was 0.2 bar.
상기 실시예 1에서 반응기에 주입되는 불소가스 압력이 0.2bar가 되도록 주입하고, 이산화티탄 전구체 용액의 농도를 0.8M이 되도록 수행한 것을 제외하고 상기 실시예 1과 동일하게 수행하여 활성탄소섬유 표면에 이불소산화티탄을 도입하였다.In the same manner as in Example 1, except that the pressure of fluorine gas injected into the reactor in Example 1 was 0.2 bar, and the concentration of the titanium dioxide precursor solution was 0.8 M, the activated carbon fiber surface was Titanium difluorooxide was introduced.
<비교예 1><Comparative Example 1>
아무런 처리를 하지 않은 실시예 1의 활성탄소섬유이다.It is the activated carbon fiber of Example 1 without any treatment.
<비교예 2><Comparative Example 2>
실시예 1의 기상 불소 표면처리 과정을 생략한 것을 제외하고 상기 실시예 1과 동일하게 수행하여 활성탄소섬유 표면에 이산화티탄을 도입하였다.Titanium dioxide was introduced to the surface of the activated carbon fiber in the same manner as in Example 1, except that the gas phase fluorine surface treatment process of Example 1 was omitted.
물성측정결과Property measurement result
원소함량 분석Element content analysis
X-선 광전자 분광기(X-ray photoelectron spectroscopy; XPS), Thermo Fisher Scientific사의 VG Multilab 2000모델을 사용하여 측정하였으며 시료는 진공 건조 오븐으로 수분을 건조시켜 사용하였다.X-ray photoelectron spectroscopy (XPS) was measured using a Thermo Fisher Scientific VG Multilab 2000 model, and the sample was dried in a vacuum drying oven.
본 발명의 실시예 1 내지 4 및 비교예 2의 활성탄소섬유 표면에 도입된 티탄 및 불소 관능기의 함량을 측정하여 표 1에 나타내었다.The contents of the titanium and fluorine functional groups introduced on the surfaces of the activated carbon fibers of Examples 1 to 4 and Comparative Example 2 of the present invention were measured and shown in Table 1.
활성탄소섬유 표면 형태 분석Analysis of surface morphology of activated carbon fiber
주사전자현미경 분석(Scanning electron microscopy; SEM)Scanning electron microscopy (SEM)
Hitachi사의 S-4800 모델을 이용하여 측정하였다. 시료는 5000배로 확대하여 표면변화를 측정하였다.It was measured using Hitachi's S-4800 model. The sample was magnified by 5000 times to measure the surface change.
본 발명의 실시예 1 내지 4 및 비교예 1, 2의 표면 형상을 확인하기 위하여 SEM 분석을 실시하였고, 그 이미지를 도 1에 나타내었다. 도 1에서 알 수 있듯이, 비교예 1의 표면은 매끄러운 반면, 2는 매우 작은 이산화티탄 입자들이 도입됨을 확인할 수 있다.SEM analysis was performed to confirm the surface shape of Examples 1 to 4 and Comparative Examples 1 and 2 of the present invention, and the images are shown in FIG. 1. As can be seen from FIG. 1, it can be seen that the surface of Comparative Example 1 is smooth, whereas in 2, very small titanium dioxide particles are introduced.
실시예 1 내지 4의 표면은 비교적 큰 크기의 이산화티탄 및 이불소산화티탄 입자들이 도입되었음을 확인하였다. 불소화 전처리 공정이 없이 이산화티탄을 도입한 샘플보다, 불소화 전처리 후 이산화티탄을 도입한 샘플이 더욱 많은 양의 입자가 표면에 도입되었음을 확인할 수 있다. The surfaces of Examples 1 to 4 confirmed that titanium dioxide and titanium difluorooxide particles having a relatively large size were introduced. It can be seen that a larger amount of particles was introduced into the surface of the sample to which titanium dioxide was introduced after the pre-fluorination treatment than the sample to which titanium dioxide was introduced without the pre-fluorination process.
이산화티탄 및 이불소산화티탄이 도입된 활성탄소섬유 결정 구조 분석Crystal structure analysis of activated carbon fiber with titanium dioxide and titanium difluoride introduced
X선 회절법(X-ray diffraction; XRD)X-ray diffraction (XRD)
PANalytical사의 X'Pert PRO모델을 사용하여 측정하였다. 시료는 진공 건조 오븐으로 수분을 건조시켜 사용했으며, 상온에서 Cu KαX-선을 조사하여 분석을 진행하였다.It was measured using PANalytical's X'Pert PRO model. The sample was used after drying moisture in a vacuum drying oven, and the analysis was conducted by irradiating Cu KαX-rays at room temperature.
본 발명의 실시예 1 내지 4 및 비교예 2에 의하여 활성탄소섬유 표면에 도입된 이산화티탄 및 이불소산화티탄의 결정구조를 확인하기 위하여 XRD 분석을 실시하였다. 도 2의 그래프에서 X축은 2θ값, Y축은 피크의 강도를 의미한다. 활성탄소섬유에 불소화 전처리 없이 이산화티탄을 도입한 결과, 도 2에서 알 수 있듯이, 도입된 이산화티탄의 함량이 적고, 결정성이 크지 않아 피크가 거의 관찰되지 않았다. 반면 불소화 전처리를 실시한 후 이산화티탄을 도입한 경우에는, 이불소산화티탄 피크가 명확하게 나타나는 것을 확인하였다. XRD analysis was performed to confirm the crystal structures of titanium dioxide and titanium difluoride introduced on the surface of activated carbon fibers according to Examples 1 to 4 and Comparative Example 2 of the present invention. In the graph of FIG. 2, the X-axis represents the 2θ value and the Y-axis represents the intensity of the peak. As a result of introducing titanium dioxide into the activated carbon fiber without pre-fluorination treatment, as can be seen from FIG. 2, the amount of the introduced titanium dioxide was small and crystallinity was not large, so that a peak was hardly observed. On the other hand, when titanium dioxide was introduced after performing the pre-fluorination treatment, it was confirmed that the titanium difluorooxide peak appeared clearly.
이산화티탄 및 이불소산화티탄이 도입된 활성탄소섬유의 아세트알데히드 흡착특성 분석Analysis of Acetaldehyde Adsorption Characteristics of Activated Carbon Fibers with Titanium Dioxide and Titanium Difluorooxide
아세트알데히드 흡착 실험은 주입장치, 반응장치 및 측정장치로 이루어진 gas chromatography (GC, Agilent HP-6890)를 사용하였다. 반응기는 내경 10mm, 외경 11mm, 높이 200mm의 석영관을 사용하였고, 아세트알데히드 흡착실험시 활성탄소섬유 0.02g을 투입하여 진행하였다. 반응기 내부로 주입되는 아세트알데히드 가스(농도 100ppm)는 질량유속 조절기(MFC, mass flow controller,Korea)를 사용하여 100sccm의 유속으로 일정하게 주입하였다. 파과(breakthrough)가 시작되며 배출되는 아세트알데히드의 농도를 GC 분석장치를 이용하여 일정 시간 간격으로 측정하여 파과곡선을 산출하였다. 이때 장착된 컬럼은 DB-5MS이며, 그 피크 측정 온도는 50 ℃로 설정하였다.Gas chromatography (GC, Agilent HP-6890) consisting of an injection device, a reaction device, and a measuring device was used for the acetaldehyde adsorption experiment. A quartz tube having an inner diameter of 10 mm, an outer diameter of 11 mm, and a height of 200 mm was used as the reactor, and 0.02 g of activated carbon fiber was added during the acetaldehyde adsorption test. Acetaldehyde gas (concentration 100 ppm) injected into the reactor was constantly injected at a flow rate of 100 sccm using a mass flow controller (MFC, Korea). Breakthrough started and the concentration of acetaldehyde discharged was measured at regular time intervals using a GC analyzer to calculate a breakthrough curve. At this time, the mounted column was DB-5MS, and the peak measurement temperature was set to 50 °C.
본 발명의 실시예 1 내지 4 및 비교예 1, 2의 활성탄소섬유의 아세트알데히드 제거특성을 GC 장비를 이용하여 분석하였고, 그 결과를 표 2에 나타내었다.The acetaldehyde removal characteristics of the activated carbon fibers of Examples 1 to 4 and Comparative Examples 1 and 2 of the present invention were analyzed using GC equipment, and the results are shown in Table 2.
아세트알데히드 감소량(%)100 minutes
Acetaldehyde reduction (%)
비교예 1의 경우 오직 활성탄소섬유 기공에 의한 흡착효과를 나타내며, 표 2로부터 알 수 있듯이 제거효율이 가장 낮다. 비교예 2는 이산화티탄 입자가 도입된 활성탄소섬유로 비교예 1보다 아세트알데히드 제거효율이 증가하였음을 확인할 수 있으며, 또한 이산화티탄 및 이불소산화티탄 입자가 도입된 실시예1 내지 4의 경우는 더욱 증가하였음을 확인할 수 있다.In the case of Comparative Example 1, only the adsorption effect by the pores of the activated carbon fiber is shown, and as can be seen from Table 2, the removal efficiency is the lowest. Comparative Example 2 is an activated carbon fiber into which titanium dioxide particles are introduced, and it can be confirmed that the acetaldehyde removal efficiency is increased compared to Comparative Example 1. In the case of Examples 1 to 4 in which titanium dioxide and titanium difluorooxide particles are introduced, It can be seen that it increased further.
Claims (18)
상기 활성탄소재는 활성탄소, 활성탄소섬유 및 이들의 혼합물 중에서 선택되는 어느 하나인 것을 특징으로 하는 이불소산화티탄을 도입한 광촉매 복합 활성탄소재.The method of claim 1,
The activated carbon material is a photocatalytic composite activated carbon material incorporating titanium difluorocarbon, characterized in that any one selected from activated carbon, activated carbon fibers, and mixtures thereof.
상기 활성탄소재의 비표면적은 1000㎡/g 이상인 것을 특징으로 하는 이불소산화티탄을 도입한 광촉매 복합 활성탄소재.The method of claim 1,
A photocatalytic composite activated carbon material incorporating titanium difluoride, characterized in that the specific surface area of the activated carbon material is 1000 m 2 /g or more.
상기 활성탄소재는 표면에 티탄이 10 내지 20At%, 불소 관능기가 5 내지 15At% 도입된 것을 특징으로 하는 이불소산화티탄을 도입한 광촉매 복합 활성탄소재.The method of claim 1,
The activated carbon material is a photocatalytic composite activated carbon material incorporating titanium difluorooxide, characterized in that 10 to 20 At% of titanium and 5 to 15 At% of a fluorine functional group are introduced on the surface.
상기 불소 관능기가 도입된 탄소재와 이산화티탄 전구체 용액을 혼합하는 단계; 및
상기 혼합물에 에너지를 처리하여 탄소재에 이불소산화티탄을 도입하는 단계;를 포함하는 이불소산화티탄이 도입된 광촉매 복합 활성탄소재의 제조방법.Surface treatment of the carbon material using fluorine gas to prepare a carbon material into which a fluorine functional group is introduced;
Mixing the carbon material into which the fluorine functional group is introduced and a titanium dioxide precursor solution; And
The method of manufacturing a photocatalytic composite activated carbon material in which titanium difluorooxide is introduced, comprising: introducing titanium difluorooxide into a carbon material by treating energy in the mixture.
상기 탄소재는 활성탄소, 활성탄소섬유 및 이들의 혼합물 중에서 선택되는 어느 하나인 것을 특징으로 하는 이불소산화티탄이 도입된 광촉매 복합 활성탄소재의 제조방법.The method of claim 5,
The carbon material is a method for producing a photocatalytic composite activated carbon material into which titanium difluorooxide is introduced, characterized in that any one selected from activated carbon, activated carbon fibers, and mixtures thereof.
상기 불소가스를 이용한 표면처리과정은, 25 내지 50℃의 온도에서 5 내지 15분 동안 이루어지는 것을 특징으로 하는 이불소산화티탄이 도입된 광촉매 복합 활성탄소재의 제조방법.The method of claim 5,
The surface treatment process using fluorine gas is a method for producing a photocatalytic composite activated carbon material in which titanium difluoride is introduced, characterized in that the surface treatment is performed for 5 to 15 minutes at a temperature of 25 to 50°C.
상기 불소가스를 이용한 표면처리과정은, 비활성가스 분위기에서 반응기 내 비활성가스 대비 불소가스 압력이 0.1 내지 0.3bar의 범위에서 이루어지는 것을 특징으로 하는 이불소산화티탄이 도입된 광촉매 복합 활성탄소재의 제조방법.The method of claim 5,
The surface treatment process using the fluorine gas is a method for producing a photocatalytic composite activated carbon material in which titanium difluorooxide is introduced, characterized in that the pressure of the fluorine gas relative to the inert gas in the reactor is in a range of 0.1 to 0.3 bar in an inert gas atmosphere.
상기 활성탄소재는 표면에 티탄이 10 내지 20At%, 불소 관능기가 5 내지 15At% 도입된 것을 특징으로 하는 이불소산화티탄이 도입된 광촉매 복합 활성탄소재의 제조방법.The method of claim 5,
The activated carbon material is a method of manufacturing a photocatalytic composite activated carbon material in which titanium difluorooxide is introduced, characterized in that 10 to 20 At% of titanium and 5 to 15 At% of a fluorine functional group are introduced on the surface.
상기 혼합하는 단계의 혼합비율은, 상기 이산화티탄 전구체 용액 100 중량부에 대해 상기 불소 관능기가 도입된 탄소재가 1.5 내지 3 중량부인 것을 특징으로 하는 이불소산화티탄이 도입된 광촉매 복합 활성탄소재의 제조방법.The method of claim 5,
The mixing ratio of the mixing step is a method for producing a photocatalytic composite activated carbon material containing titanium difluorooxide, characterized in that 1.5 to 3 parts by weight of the carbon material into which the fluorine functional group is introduced per 100 parts by weight of the titanium dioxide precursor solution .
상기 이산화티탄 전구체 용액은 알코올 용매와 이산화티탄 전구체를 혼합하여 제조하는 것을 특징으로 하는 이불소산화티탄이 도입된 광촉매 복합 활성탄소재의 제조방법.The method of claim 5,
The titanium dioxide precursor solution is a method of manufacturing a photocatalytic composite activated carbon material into which titanium difluorooxide is introduced, characterized in that prepared by mixing an alcohol solvent and a titanium dioxide precursor.
상기 알코올 용매와 상기 이산화티탄 전구체의 혼합 비율은, 알코올 용매 100 중량부를 기준으로 이산화티탄 전구체가 8 내지 43 중량부인 것을 특징으로 하는 이불소산화티탄이 도입된 광촉매 복합 활성탄소재의 제조방법.The method of claim 12,
The mixing ratio of the alcohol solvent and the titanium dioxide precursor is 8 to 43 parts by weight of the titanium dioxide precursor based on 100 parts by weight of the alcohol solvent.
상기 혼합하는 단계 후, 혼합물을 겔화하는 단계를 더 포함하는 것을 특징으로 하는 이불소산화티탄이 도입된 광촉매 복합 활성탄소재의 제조방법.The method of claim 5,
After the step of mixing, the method for producing a photocatalytic composite activated carbon material into which titanium difluoride is introduced, further comprising gelling the mixture.
상기 겔화하는 단계는, 25 내지 30℃의 온도범위에서 12 내지 24시간 이루어지는 것을 특징으로 하는 이불소산화티탄이 도입된 광촉매 복합 활성탄소재의 제조방법.The method of claim 14,
The step of gelling is a method for producing a photocatalytic composite activated carbon material in which titanium difluorooxide is introduced, characterized in that it takes place for 12 to 24 hours at a temperature range of 25 to 30°C.
상기 겔화하는 단계 후, 겔화 혼합물을 추가적으로 건조시키는 단계를 더 포함하는 것을 특징으로 하는 이불소산화티탄이 도입된 광촉매 복합 활성탄소재의 제조방법.The method of claim 14,
After the step of gelling, the method of manufacturing a photocatalytic composite activated carbon material into which titanium difluorooxide is introduced, further comprising the step of additionally drying the gelling mixture.
상기 에너지 처리는, 초음파를 이용한 에너지 처리 과정을 포함하는 것을 특징으로 하는 이불소산화티탄이 도입된 광촉매 복합 활성탄소재의 제조방법.The method of claim 5,
The energy treatment is a method of manufacturing a photocatalytic composite activated carbon material into which titanium difluorooxide is introduced, characterized in that it includes an energy treatment process using ultrasonic waves.
상기 초음파를 이용한 에너지 처리 과정은, 상기 혼합물을 증류수에 투입하고, 10 내지 50kHz 진동수범위에서 30 내지 60분 동안 이루어지는 것을 특징으로 하는 이불소산화티탄이 도입된 광촉매 복합 활성탄소재의 제조방법.
The method of claim 17,
The energy treatment process using ultrasonic waves is a method of manufacturing a photocatalytic composite activated carbon material in which titanium difluorooxide is introduced, characterized in that the mixture is added to distilled water and is performed for 30 to 60 minutes in a frequency range of 10 to 50 kHz.
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