[go: up one dir, main page]

WO2018110852A1 - Alkali-based metal-treated activated carbon material for automotive filter, and preparation method therefor - Google Patents

Alkali-based metal-treated activated carbon material for automotive filter, and preparation method therefor Download PDF

Info

Publication number
WO2018110852A1
WO2018110852A1 PCT/KR2017/013400 KR2017013400W WO2018110852A1 WO 2018110852 A1 WO2018110852 A1 WO 2018110852A1 KR 2017013400 W KR2017013400 W KR 2017013400W WO 2018110852 A1 WO2018110852 A1 WO 2018110852A1
Authority
WO
WIPO (PCT)
Prior art keywords
activated carbon
potassium
barium
alkali metal
carbon material
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Ceased
Application number
PCT/KR2017/013400
Other languages
French (fr)
Korean (ko)
Inventor
배재영
윤태관
이종탁
이재영
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Industry Academic Cooperation Foundation of Keimyung University
Original Assignee
Industry Academic Cooperation Foundation of Keimyung University
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Industry Academic Cooperation Foundation of Keimyung University filed Critical Industry Academic Cooperation Foundation of Keimyung University
Publication of WO2018110852A1 publication Critical patent/WO2018110852A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B32/00Carbon; Compounds thereof
    • C01B32/30Active carbon
    • C01B32/354After-treatment
    • C01B32/372Coating; Grafting; Microencapsulation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D39/00Filtering material for liquid or gaseous fluids
    • B01D39/14Other self-supporting filtering material ; Other filtering material
    • B01D39/20Other self-supporting filtering material ; Other filtering material of inorganic material, e.g. asbestos paper, metallic filtering material of non-woven wires
    • B01D39/2055Carbonaceous material
    • B01D39/2058Carbonaceous material the material being particulate
    • B01D39/2062Bonded, e.g. activated carbon blocks
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2257/00Components to be removed
    • B01D2257/50Carbon oxides
    • B01D2257/504Carbon dioxide

Definitions

  • the present invention relates to an activated carbon material for automobile interior filters treated with an alkali-based metal which can increase carbon dioxide adsorption performance by treating an alkali metal to activated carbon used as an automobile interior filter, and a method of manufacturing the same.
  • the air filter used in the current vehicle interior it is limited to the function of removing fine substances and suppressing the propagation of bacteria, but in the case of the air filter used in the luxury vehicle, VOCs gas and nitrogen It has the function to trap oxides (NO ⁇ ) and sulfur oxides (SO ⁇ ).
  • CO 2 is classified as a global warming gas and is regulated.
  • CO 2 gas When CO 2 gas is accumulated inside a vehicle, it can be adsorbed and controlled as a dangerous gas that may cause drowsiness of the driver and lead to an accident.
  • An object of the present invention is to provide an activated carbon material for a vehicle interior filter and a method for manufacturing the same that can increase carbon dioxide adsorption performance by treating an alkali metal to activated carbon used as a vehicle interior filter.
  • the present invention provides an activated carbon material for automobile interior filters treated with alkali-based metal, the hydroxide of alkali metal or hydroxide of alkaline earth metal on the surface of the activated carbon.
  • the present invention comprises the steps of dissolving the activated carbon and alkali metal precursor or alkaline earth metal precursor in distilled water to prepare a mixed solution; Preparing a first stirring solution by stirring the mixed solution at room temperature; Adding an acid catalyst to the first stirring solution; Preparing a second stirring solution by stirring the first stirring solution added with the acid catalyst at room temperature; And filtering and drying the second stirring solution to produce an alkali metal oxide-activated carbon or an alkaline earth metal oxide-activated carbon.
  • Figure 2 is a flow chart showing a method for producing an activated carbon material for automobile interior filter treated with an alkali metal of the present invention
  • Example 3 is a view showing the carbon dioxide adsorption change amount of the activated carbon material treated with alkali metal and alkali-based metals prepared according to Example 1 and Comparative Example 1;
  • Example 4 is a view showing the carbon dioxide adsorption change amount of the activated carbon material treated with alkali metal and alkali-based metals prepared according to Example 1 and Comparative Example 2;
  • FIG. 5 is a view showing the carbon dioxide adsorption change amount of the activated carbon material treated with an alkali-based metal prepared according to Examples 1 to 3;
  • FIG. 6 is a view showing a specific surface area measurement result (a) of activated carbon not treated with an alkali metal and a specific surface area measurement result (b) with an activated carbon material treated with an alkali metal according to Example 1;
  • Example 8 is a view showing an EPMA analysis result of an activated carbon material treated with alkaline earth metals according to Example 1;
  • FIG. 10 is a view showing an EPMA analysis result of an activated carbon material treated with alkaline earth metals according to Comparative Example 2;
  • FIG. 11 is a view showing the EPMA analysis result after storing the activated carbon material treated with alkaline earth metal-based metal according to Example 1 for 30 days in an airtight container;
  • FIG. 12 is a view showing the results of EPMA analysis after storing the activated carbon material treated with alkaline earth metals according to Comparative Example 2 in a closed container for 30 days.
  • the inventors of the present invention have found that the adsorption amount of carbon dioxide can be increased by adding an acid catalyst to an activated carbon used as a filter material in a low temperature process to treat an alkali metal, thereby completing the present invention.
  • the present invention provides an activated carbon material for automobile interior filters treated with an alkali-based metal, on which an activated metal surface is loaded with an alkali metal hydroxide or an alkaline earth metal hydroxide.
  • the alkali metal may be any one selected from the group consisting of lithium (Li), sodium (Na), potassium (K), and rubidium (Rb), but is not limited thereto.
  • the alkaline earth metal may be any one selected from the group consisting of calcium, strontium, and barium, but is not limited thereto.
  • the present invention comprises the steps of dissolving the activated carbon and alkali metal precursor or alkaline earth metal precursor in distilled water to prepare a mixed solution; Preparing a first stirring solution by stirring the mixed solution at room temperature; Adding an acid catalyst to the first stirring solution; Preparing a second stirring solution by stirring the first stirring solution added with the acid catalyst at room temperature; And filtering and drying the second stirring solution to produce an alkali metal oxide-activated carbon or an alkaline earth metal oxide-activated carbon.
  • 1 is a view showing a carbon dioxide adsorption mechanism of alkali metals and alkaline earth metals.
  • the alkali metal precursors are potassium hydride, potassium hydroxide, potassium dioxide, potassium permanganate, potassium carbonate, potassium bicarbonate, potassium chloride (Potassium chloride), Potassium iodide, Potassium bromide, Potassium fluoride, Potassium cyanide, Potassium cyanate, Potassium cyanate Potassium thiocyanate, Potassium nitrate, Potassium nitrite, Potassium sulfate, Potassium bisulfate, Potassium sulfite, Potassium hexafluorophosphate Potassium triphosphate tribasic, Dibasic potassium phosphate, Potassium dihydrogen phosphate, Potassium dichromate, Cal chromate Potassium chromate, Potassium bromate, Potassium methoxide, Potassium ethoxide, Potassium acetate, Potassium thioacetate, Potassium formate formate, Potassium iodate
  • the alkaline earth metal precursors include barium nitrate, barium hydroxide, barium chloride, barium chloride, barium sulfide, barium sulfate, barium carbonate, and barium acetate.
  • the alkali metal precursor or alkaline earth metal precursor may be in a concentration of 0.025 to 3 M (mol / L), but is not limited thereto.
  • the concentration of the alkali metal precursor or alkaline earth metal precursor is less than 0.025 M, there may be a problem that the amount of carbon dioxide adsorption is lowered due to insufficient amount of metal in activated carbon, and the concentration of the alkali metal precursor or alkaline earth metal precursor is 3 When M is exceeded, the specific surface area of the activated carbon is drastically reduced, which may cause a problem of deterioration of carbon dioxide adsorption efficiency.
  • the concentration of the alkali metal precursor or alkaline earth metal precursor is preferably 0.025 to 3 M, especially considering the optimization of the amount of metal and specific surface area in the activated carbon, the concentration of the alkali metal precursor or alkaline earth metal precursor is It is more preferable that it is 0.1-1 M.
  • the preparing of the mixed solution may be prepared by dissolving 5 to 20 parts by weight of activated carbon and 0.75 to 30 parts by weight of an alkali metal precursor or an alkaline earth metal precursor with respect to 100 parts by weight of distilled water, but is not limited thereto.
  • the activated carbon when the activated carbon is included in less than 5 parts by weight based on 100 parts by weight of distilled water, there is a problem that the efficiency of the overall process is reduced, and also when the activated carbon is included in excess of 20 parts by weight based on 100 parts by weight of distilled water, And the alkaline earth metal precursor may not bond evenly with the activated carbon may cause a problem that the carbon dioxide adsorption efficiency is reduced.
  • the alkali metal precursor or the alkaline earth metal precursor when included in an amount of less than 0.75 parts by weight based on 100 parts by weight of distilled water, the number of metal oxides of the activated carbon may be low, resulting in a decrease in carbon dioxide adsorption efficiency. Including more than 30 parts by weight of the metal precursor or alkaline earth metal precursor may reduce the specific surface area of the activated carbon to reduce the space for the carbon dioxide is adsorbed may cause a problem that can not adsorb a large amount of carbon dioxide.
  • the preparing of the mixed solution is preferably prepared by dissolving 5 to 20 parts by weight of activated carbon and 0.75 to 30 parts by weight of an alkali metal precursor or an alkaline earth metal precursor with respect to 100 parts by weight of distilled water.
  • preparing the mixed solution is based on 100 parts by weight of distilled water, 10 to 15 parts by weight of activated carbon and 1 to 5 alkali metal precursors or alkaline earth metal precursors. It is more preferable to melt
  • the preparing of the first stirring solution may be performed by stirring the mixed solution at 100 to 400 rpm for 15 to 45 minutes at room temperature, but is not limited thereto.
  • the activated carbon is not properly mixed when stirring below 100 rpm when preparing the first stirring solution, and also when the stirring is exceeding 400 rpm when preparing the first stirring solution, alkali metal As soon as the oxide is combined with the activated carbon, the oxide is separated, which may cause a problem that the binding reaction does not proceed smoothly.
  • the adding of the acid catalyst may add a Lewis acid catalyst or an organic acid catalyst to the first stirring solution, but is not limited thereto.
  • the acid catalyst added to the first stirring solution is a catalyst having weak acidity
  • the Lewis acid catalyst or the organic acid catalyst has strong acidity. It is preferred to be a prominent catalyst.
  • the pH of the first stirring solution may be maintained at 1 to 3.
  • the first stirring solution is preferably maintained at a pH of 1 to 3, especially considering the reaction rate and safety aspects, the pH of the first stirring solution is more preferably maintained at 2 to 2.5.
  • the Lewis acid catalyst is hydrochloric acid (HCl), bromic acid (HBr), sulfuric acid (H 2 SO 4 ), phosphoric acid (H 3 PO 4 ), carbonic acid (H 2 CO 3 ), titanium chloride (TiCl 4 ), iron chloride (III) (FeCl 3 ) and aluminum chloride (AlCl 3 ) may be any one selected from, but is not limited thereto.
  • the organic acid catalyst is selected from the group consisting of sulfonic acid, picric acid, tartaric acid, citric acid, ethylenediaminetetraacetic acid, and pyrophosphoric acid. It may be any one, but is not limited thereto.
  • the preparing of the second stirring solution may be prepared by stirring the first stirring solution to which the acid catalyst is added at 100 to 400 rpm at room temperature for 24 to 72 hours, but is not limited thereto.
  • the activated carbon is not properly mixed when stirring at less than 100 rpm when preparing the second stirring solution, and also when the stirring is exceeding 400 rpm when preparing the second stirring solution alkali metal
  • the oxide may be separated and cause a problem in that the coupling reaction does not proceed smoothly.
  • the step of preparing the alkali metal oxide-activated carbon or alkaline earth metal oxide-activated carbon may be prepared by filtering the second stirring solution at 80 to 200 ° C. for 4 to 8 hours, but is not limited thereto.
  • the step of preparing the alkali metal oxide-activated carbon or alkaline earth metal oxide-activated carbon when dried to less than 80 °C may cause a problem that the performance is reduced due to the moisture remaining, and also exceeds 200 °C Drying may cause a problem that the addition reaction may proceed due to the phenomenon of the metal material bound to the activated carbon.
  • the drying when the drying is less than 4 hours, the problem of moisture remaining may occur, and if the drying for more than 8 hours, The heat applied can cause problems that the addition reaction can proceed.
  • the step of preparing the alkali metal oxide-activated carbon or alkaline earth metal oxide-activated carbon is preferably prepared by drying the second stirring solution at 80 to 200 ° C. for 4 to 8 hours after filtering.
  • the step of preparing the alkali metal oxide-activated carbon or alkaline earth metal oxide-activated carbon may be performed for 5 to 6 hours at 120 to 150 ° C. after filtering the second stirring solution. It is more preferable to prepare by drying.
  • the method may further include vacuum packaging after preparing the alkali metal oxide-activated carbon or alkaline earth metal oxide-activated carbon, but is not limited thereto.
  • the activated carbon material for automobile interior filters treated with alkali metals of the present invention and a method for manufacturing the same according to the present invention will be described in more detail.
  • the present invention is not limited by these examples.
  • Example 1 Activated Carbon Material for Automobile Interior Filter Treated with Alkaline Earth Metal
  • a mixed solution was prepared by dissolving 15 parts by weight of activated carbon and 2 parts by weight of barium hydroxide (60 parts by weight of a barium hydroxide solution when the weight was calculated at a concentration of 0.1 M) based on 100 parts by weight of distilled water.
  • the mixed solution prepared by using a stirrer (MSH-20A, Korean Science) was stirred at 300 rpm for 30 minutes at room temperature to prepare a first stirring solution.
  • Hydrochloric acid was added to the first stirring solution as an acid catalyst to maintain a pH of the first stirring solution at 2.
  • Example 1 Except for using barium acetate instead of barium hydroxide (Barium hydroxide), under the same conditions as in Example 1 was prepared an activated carbon material for automobile interior filter treated with alkaline earth metal.
  • barium hydroxide Barium hydroxide
  • a mixed solution was prepared by dissolving 15 parts by weight of activated carbon and 2 parts by weight of barium hydroxide (60 parts by weight of a barium hydroxide solution when the weight was calculated at a concentration of 0.1 M) based on 100 parts by weight of distilled water.
  • the mixed solution prepared by using a stirrer (MSH-20A, Korean Science) was stirred at 300 rpm for 30 minutes at room temperature to prepare a first stirring solution.
  • the first stirring solution was stirred at 300 rpm for 24 hours at room temperature to prepare a second stirring solution.
  • the filtered alkali metal oxide-activated carbon was dried at 120 ° C. for 6 hours to filter the interior of the alkali metal. Activated carbon material was prepared.
  • a mixed solution was prepared by dissolving 15 parts by weight of activated carbon and 2 parts by weight of barium hydroxide (60 parts by weight of a barium hydroxide solution when the weight was calculated at a concentration of 0.1 M) based on 100 parts by weight of distilled water.
  • the mixed solution prepared using the stirrer (MSH-20A, Korean Science) was stirred at 300 rpm for 30 minutes at 80 ° C to prepare a first stirring solution.
  • the first stirring solution was stirred at 300 rpm for 24 hours at 80 ° C. to prepare a second stirring solution.
  • the filtered alkali metal oxide-activated carbon was dried at 120 ° C. for 6 hours to filter the interior of the alkali metal. Activated carbon material was prepared.
  • the carbon-containing gas is treated with an activated carbon material for automobile interior filters treated with alkali metals prepared according to Examples 1 to 3, conventional activated carbon, and an alkali metal prepared according to Comparative Example 1.
  • the amount of carbon dioxide adsorbed through GC was collected by flowing the activated carbon material for the vehicle interior filter and collecting the gas, and the results are shown in FIG. 3, and the conditions are as follows.
  • Tester hp 6890a gc, agilent
  • Example 3 is a view showing the carbon dioxide adsorption change amount of the activated carbon not treated with alkali metal and the activated carbon material treated with alkali metals prepared according to Example 1 and Comparative Example 2.
  • Example 4 is a view showing the carbon dioxide adsorption change amount of the activated carbon material treated with an alkali-free metal and the alkali-based metal prepared according to Example 1 and Comparative Example 1.
  • Example 1 is relatively mild reaction conditions (room temperature conditions) compared to the conventional method for manufacturing activated carbon material for automobile interior filters (Comparative Example 2) manufactured by reflux at high temperature (80 ° C). Activated carbon material for the filter can be prepared, the activated carbon material was confirmed that the carbon dioxide adsorption performance is excellent.
  • FIG. 5 is a view showing a carbon dioxide adsorption change amount of the activated carbon material treated with an alkali-based metal prepared according to Examples 1 to 3.
  • the Brunauer-Emmett-Teller equation is obtained by adsorbing and desorbing nitrogen gas to activated carbon materials for automobile interior filters treated with alkali metals prepared according to Example 1, and activated carbons not treated with alkali metals.
  • the specific surface area was calculated using the Brunauer-Emmett-Teller equation (hereinafter referred to as the 'BET equation').
  • the specific surface area of the activated carbon material for automobile interior filters treated with alkali metals prepared according to Example 1 was smaller than the specific surface area of activated carbon not treated with alkali metals.
  • the specific surface area is reduced because the activated carbon having a porous structure is located inside and outside the pores as the hydroxide of the alkali metal formed on the surface of the activated carbon is oxidized by the reaction while the alkali-based metal is processed.
  • Electron probe micro analysis (hereinafter referred to as 'EPMA') of an activated carbon material treated with an alkali-based active carbon, an alkali-based metal according to Example 1, Comparative Example 1, and Comparative Example 2 was performed. It was.
  • Example 8 is a view showing the results of EPMA analysis of activated carbon material treated with alkaline earth metal elements according to Example 1.
  • FIG. 9 is a view showing EPMA analysis results of activated carbon materials treated with alkaline earth metal elements according to Comparative Example 1.
  • FIG. 9 is a view showing EPMA analysis results of activated carbon materials treated with alkaline earth metal elements according to Comparative Example 1.
  • FIG. 10 is a view showing the EPMA analysis results of the activated carbon material treated with alkaline earth metal elements according to Comparative Example 2.
  • Example 11 is a view showing the EPMA analysis result after storing the activated carbon synthesized in Example 1 in a sealed container for 30 days.
  • FIG. 12 is a view showing the EPMA analysis result after storing the activated carbon material according to Comparative Example 2 in a closed container for 30 days.
  • the amount of barium is significantly reduced, which is 30 days in an airtight container because it is not possible to chemically bond between activated carbon and barium by adding an acid catalyst even if heat is applied during the reaction. After storage for a while barium does not remain inside the activated carbon it can be seen that the amount of barium significantly reduced.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Geology (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Inorganic Chemistry (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Catalysts (AREA)

Abstract

The present invention relates to an alkali-based metal-treated activated carbon material for an automotive filter, and a preparation method therefor. The present invention relates to a method for preparing an alkali-based metal-treated activated carbon material for an automotive filter, comprising the steps of: preparing a mixture solution by dissolving activated carbon and an alkali metal precursor or an alkaline earth metal precursor in distilled water; preparing a first stirred solution by stirring the mixture solution at room temperature; adding an acid catalyst to the first stirred solution; preparing a second stirred solution by stirring the acid catalyst-added first stirred solution at room temperature; and preparing alkali metal oxide-activated carbon or alkaline earth metal oxide-activated carbon by filtering the second stirred solution, and then drying the same. According to the present invention, the alkali-based metal-treated activated carbon material for an automotive filter, having been prepared at a room temperature condition and through a process of adding an acid catalyst, has an effect of enabling the adsorption amount of carbon dioxide to be increased over that of a conventional activated carbon material.

Description

알칼리계 금속이 처리된 자동차 내부 필터용 활성탄소 소재 및 이의 제조방법Activated carbon material for automobile interior filter treated with alkali metal and method for manufacturing same

본 발명은 자동차 내부 필터로 사용되는 활성탄소에 알칼리계 금속을 처리하여 이산화탄소 흡착성능을 증대시킬 수 있는 알칼리계 금속이 처리된 자동차 내부 필터용 활성탄소 소재 및 이의 제조방법에 관한 것이다.The present invention relates to an activated carbon material for automobile interior filters treated with an alkali-based metal which can increase carbon dioxide adsorption performance by treating an alkali metal to activated carbon used as an automobile interior filter, and a method of manufacturing the same.

삶의 질적 향상으로 주거공간 및 차량실내 공기 질의 중요성이 부가되면서 공기 중의 각종 유해성분 제거기술개발 및 상품화가 본격화되고 있다. 이러한 가운데, 차량 실내에 CO2 또는 배기 가스 센서를 장착하여 차량 실내의 공기가 질적으로 향상됨에 따라 새로운 개념의 차량 실내 에어필터 요구가 증대되고 있다. With the improvement of quality of life, the importance of air quality in residential spaces and vehicle interiors has been added, and the development and commercialization of technologies for removing various harmful components in the air are in earnest. In the meantime, as the air in the vehicle is qualitatively improved by installing the CO 2 or the exhaust gas sensor in the vehicle interior, a new concept of the vehicle interior air filter is increasing.

현재의 차량 실내에서 사용되는 에어필터의 경우, 미세물질 제거 및 세균번식 억제 등의 기능에만 국한되어 있으나, 고급 차량에서 사용되는 에어필터의 경우, 휘발성 유기화합물(Volatile Organic Compounds; VOCs) 가스 및 질소산화물(NOω), 황산화물(SOω) 계열의 가스를 포집할 수 있는 기능을 가지고 있다.In the case of the air filter used in the current vehicle interior, it is limited to the function of removing fine substances and suppressing the propagation of bacteria, but in the case of the air filter used in the luxury vehicle, VOCs gas and nitrogen It has the function to trap oxides (NO ω ) and sulfur oxides (SO ω ).

그러나, 오래 전부터 지속적으로 문제 되어온 이산화탄소(CO2) 가스를 포집할 수 있는 에어필터는 현재 전무한 상태이다.However, there are currently no air filters capable of capturing carbon dioxide (CO 2 ) gas, which has been a problem for a long time.

특히, CO2의 경우 지구온난화 가스로 분류되어 규제가 되고 있는 실정이며, 차량 실내에 CO2 가스가 축적될 경우, 운전자의 졸음을 유발하여 사고로 이어질 수 있는 위험한 가스로써 이를 흡착하고 제어할 수 있는 신개념 필터 소재 개발 연구가 필요한 시점이지만, 아직까지 이러한 연구는 전무한 상황이다.In particular, CO 2 is classified as a global warming gas and is regulated. When CO 2 gas is accumulated inside a vehicle, it can be adsorbed and controlled as a dangerous gas that may cause drowsiness of the driver and lead to an accident. There is a need for a new concept filter material development study, but there is no such research.

따라서, 차량용 실내 필터에 사용되는 활성탄소에 적절한 작용기를 도입하여 이산화탄소 흡착성능을 구현할 수 있는 소재에 대한 연구 개발이 시급한 실정이다.Therefore, there is an urgent need for research and development on materials capable of implementing carbon dioxide adsorption performance by introducing appropriate functional groups into activated carbon used in vehicle interior filters.

본 발명의 목적은 자동차 내부 필터로 사용되는 활성탄소에 알칼리계 금속을 처리하여 이산화탄소 흡착성능을 증대시킬 수 있는 자동차 내부 필터용 활성탄소 소재 및 이의 제조방법을 제공하는 데에 있다.An object of the present invention is to provide an activated carbon material for a vehicle interior filter and a method for manufacturing the same that can increase carbon dioxide adsorption performance by treating an alkali metal to activated carbon used as a vehicle interior filter.

상기 목적을 달성하기 위하여, 본 발명은 활성탄소 표면에 알칼리 금속의 수산화물 또는 알칼리 토금속의 수산화물이 담지된, 알칼리계 금속이 처리된 자동차 내부 필터용 활성탄소 소재를 제공한다.In order to achieve the above object, the present invention provides an activated carbon material for automobile interior filters treated with alkali-based metal, the hydroxide of alkali metal or hydroxide of alkaline earth metal on the surface of the activated carbon.

또한, 본 발명은 증류수에 활성탄소와 알칼리 금속 전구체 또는 알칼리 토금속 전구체를 용해시켜 혼합용액을 준비하는 단계; 상기 혼합용액을 상온에서 교반시켜 제1교반용액을 준비하는 단계; 상기 제1교반용액에 산촉매를 첨가하는 단계; 산촉매가 첨가된 제1교반용액을 상온에서 교반시켜 제2교반용액을 준비하는 단계; 및 상기 제2교반용액을 필터링 후 건조하여 알칼리 금속 산화물-활성탄소 또는 알칼리 토금속 산화물-활성탄소를 제조하는 단계를 포함하는, 알칼리계 금속이 처리된 자동차 내부 필터용 활성탄소 소재 제조방법을 제공한다.In addition, the present invention comprises the steps of dissolving the activated carbon and alkali metal precursor or alkaline earth metal precursor in distilled water to prepare a mixed solution; Preparing a first stirring solution by stirring the mixed solution at room temperature; Adding an acid catalyst to the first stirring solution; Preparing a second stirring solution by stirring the first stirring solution added with the acid catalyst at room temperature; And filtering and drying the second stirring solution to produce an alkali metal oxide-activated carbon or an alkaline earth metal oxide-activated carbon. .

본 발명에 따른 상온 조건 및 산촉매를 첨가하는 공정을 통해 제조된 알칼리계 금속이 처리된 자동차 내부 필터용 활성탄소 소재의 경우, 종래 활성탄소에 비해 이산화탄소 흡착량을 증가시킬 수 있는 효과가 있다.In the case of activated carbon materials for automobile interior filters treated with alkali-based metals prepared through the process of adding room temperature conditions and acid catalysts according to the present invention, there is an effect that can increase the amount of carbon dioxide adsorption compared to conventional activated carbon.

도 1은 알칼리 금속 및 알칼리 토금속의 이산화탄소 흡착 매커니즘을 나타낸 도면;1 illustrates a carbon dioxide adsorption mechanism of alkali metals and alkaline earth metals;

도 2는 본 발명인 알칼리계 금속이 처리된 자동차 내부 필터용 활성탄소 소재 제조방법을 나타낸 순서도;Figure 2 is a flow chart showing a method for producing an activated carbon material for automobile interior filter treated with an alkali metal of the present invention;

도 3은 알칼리 금속이 처리되지 않은 활성탄소와 실시예 1 및 비교예 1에 따라 제조된 알칼리계 금속을 처리한 활성탄소 소재의 이산화탄소 흡착 변화량을 나타낸 도면;3 is a view showing the carbon dioxide adsorption change amount of the activated carbon material treated with alkali metal and alkali-based metals prepared according to Example 1 and Comparative Example 1;

도 4는 알칼리 금속이 처리되지 않은 활성탄소와 실시예 1 및 비교예 2에 따라 제조된 알칼리계 금속을 처리한 활성탄소 소재의 이산화탄소 흡착 변화량을 나타낸 도면;4 is a view showing the carbon dioxide adsorption change amount of the activated carbon material treated with alkali metal and alkali-based metals prepared according to Example 1 and Comparative Example 2;

도 5는 실시예 1 내지 실시예 3에 따라 제조된 알칼리계 금속을 처리한 활성탄소 소재의 이산화탄소 흡착 변화량을 나타낸 도면;5 is a view showing the carbon dioxide adsorption change amount of the activated carbon material treated with an alkali-based metal prepared according to Examples 1 to 3;

도 6은 알칼리 금속이 처리되지 않은 활성탄소의 비표면적 측정결과(a) 및 실시예 1에 따른 알칼리계 금속을 처리한 활성탄소 소재의 비표면적 측정결과(b)를 나타낸 도면;6 is a view showing a specific surface area measurement result (a) of activated carbon not treated with an alkali metal and a specific surface area measurement result (b) with an activated carbon material treated with an alkali metal according to Example 1;

도 7은 알칼리 토금속이 처리되지 않은 활성탄소의 EPMA 분석결과를 나타낸 도면;7 shows EPMA analysis results of activated carbon not treated with alkaline earth metals;

도 8은 실시예 1에 따른 알칼리 토금속계 금속을 처리한 활성탄소 소재의 EPMA 분석결과를 나타낸 도면; 8 is a view showing an EPMA analysis result of an activated carbon material treated with alkaline earth metals according to Example 1;

도 9는 비교예 1에 따른 알칼리 토금속계 금속을 처리한 활성탄소 소재의 EPMA 분석결과를 나타낸 도면;9 is a view showing an EPMA analysis result of an activated carbon material treated with alkaline earth metals according to Comparative Example 1;

도 10은 비교예 2에 따른 알칼리 토금속계 금속을 처리한 활성탄소 소재의 EPMA 분석결과를 나타낸 도면;10 is a view showing an EPMA analysis result of an activated carbon material treated with alkaline earth metals according to Comparative Example 2;

도 11은 실시예 1에 따른 알칼리 토금속계 금속을 처리한 활성탄소 소재를 밀폐용기에 30일 동안 보관한 후 EPMA 분석결과를 나타낸 도면; 및11 is a view showing the EPMA analysis result after storing the activated carbon material treated with alkaline earth metal-based metal according to Example 1 for 30 days in an airtight container; And

도 12는 비교예 2에 따른 알칼리 토금속계 금속을 처리한 활성탄소 소재를 밀폐용기에 30일 동안 보관한 후 EPMA 분석결과를 나타낸 도면이다. 12 is a view showing the results of EPMA analysis after storing the activated carbon material treated with alkaline earth metals according to Comparative Example 2 in a closed container for 30 days.

이하, 본 발명인 알칼리계 금속이 처리된 자동차 내부 필터용 활성탄소 소재 및 이의 제조방법을 보다 상세하게 설명한다.Hereinafter, the activated carbon material for automobile interior filter treated with alkali metal of the present invention and a method of manufacturing the same will be described in more detail.

본 발명의 발명자들은 종래 필터 소재로서 이용되는 활성탄소에 저온 공정으로 산촉매를 첨가하여 알칼리계 금속을 처리함으로써 이산화탄소 흡착량을 증대시킬 수 있음을 밝혀내어 본 발명을 완성하였다.The inventors of the present invention have found that the adsorption amount of carbon dioxide can be increased by adding an acid catalyst to an activated carbon used as a filter material in a low temperature process to treat an alkali metal, thereby completing the present invention.

본 발명은 활성탄소 표면에 알칼리 금속의 수산화물 또는 알칼리 토금속의 수산화물이 담지된, 알칼리계 금속이 처리된 자동차 내부 필터용 활성탄소 소재를 제공한다.The present invention provides an activated carbon material for automobile interior filters treated with an alkali-based metal, on which an activated metal surface is loaded with an alkali metal hydroxide or an alkaline earth metal hydroxide.

상기 알칼리 금속은 리튬(Li), 나트륨(Na), 칼륨(K), 및 루비듐(Rb)로 이루어진 군에서 선택된 어느 하나일 수 있으며, 이에 제한되는 것은 아니다.The alkali metal may be any one selected from the group consisting of lithium (Li), sodium (Na), potassium (K), and rubidium (Rb), but is not limited thereto.

상기 알칼리 토금속은 칼슘, 스트론튬, 및 바륨으로 이루어진 군에서 선택된 어느 하나일 수 있으며, 이에 제한되는 것은 아니다.The alkaline earth metal may be any one selected from the group consisting of calcium, strontium, and barium, but is not limited thereto.

또한, 본 발명은 증류수에 활성탄소와 알칼리 금속 전구체 또는 알칼리 토금속 전구체를 용해시켜 혼합용액을 준비하는 단계; 상기 혼합용액을 상온에서 교반시켜 제1교반용액을 준비하는 단계; 상기 제1교반용액에 산촉매를 첨가하는 단계; 산촉매가 첨가된 제1교반용액을 상온에서 교반시켜 제2교반용액을 준비하는 단계; 및 상기 제2교반용액을 필터링 후 건조하여 알칼리 금속 산화물-활성탄소 또는 알칼리 토금속 산화물-활성탄소를 제조하는 단계를 포함하는, 알칼리계 금속이 처리된 자동차 내부 필터용 활성탄소 소재 제조방법을 제공한다.In addition, the present invention comprises the steps of dissolving the activated carbon and alkali metal precursor or alkaline earth metal precursor in distilled water to prepare a mixed solution; Preparing a first stirring solution by stirring the mixed solution at room temperature; Adding an acid catalyst to the first stirring solution; Preparing a second stirring solution by stirring the first stirring solution added with the acid catalyst at room temperature; And filtering and drying the second stirring solution to produce an alkali metal oxide-activated carbon or an alkaline earth metal oxide-activated carbon. .

도 1은 알칼리 금속 및 알칼리 토금속의 이산화탄소 흡착 매커니즘을 나타낸 도면이다.1 is a view showing a carbon dioxide adsorption mechanism of alkali metals and alkaline earth metals.

도면을 참조하면, 알칼리 금속 산화물(MO)과 알칼리 토금속 수산화물(M(OH)2)의 경우 이산화탄소와 반응할 경우 알칼리 금속 탄산염 또는 알칼리 토금속 탄산염(MCO3)를 형성하여 이산화탄소를 흡착하게 된다.Referring to the drawings, in the case of the alkali metal oxide (MO) and alkaline earth metal hydroxide (M (OH) 2 ) it reacts with carbon dioxide to form an alkali metal carbonate or alkaline earth metal carbonate (MCO 3 ) to adsorb carbon dioxide.

상기 알칼리 금속 전구체는 수소화칼륨(Potassium hydride), 수산화칼륨(Potassium hydroxide), 칼륨디산화물(Potassium dioxide), 과망간산칼륨(Potassium permanganate), 탄산칼륨(Potassium carbonate), 탄산수소칼륨(Potassium bicarbonate), 염화칼륨(Potassium chloride), 아이오딘화칼륨(Potassium iodide), 브로민화칼륨(Potassium bromide), 플루오르화칼륨(Potassium fluoride), 시안화칼륨(Potassium cyanide), 시안산칼륨(Potassium cyanate), 싸이오시안산칼륨(Potassium thiocyanate), 질산칼륨(Potassium nitrate), 아질산칼륨(Potassium nitrite), 황산칼륨(Potassium sulfate), 황산수소칼륨(Potassium bisulfate), 아황산칼륨(Potassium sulfite), 헥사플루오르인산칼륨(Potassium hexafluorophosphate), 제삼인산칼륨(Potassium phosphate tribasic), 인산수소칼륨(Dibasic potassium phosphate), 인산이수소칼륨(Potassium dihydrogen phosphate), 중크롬산칼륨(Potassium dichromate), 크롬산칼륨(Potassium chromate), 브롬산칼륨(Potassium bromate), 메톡사이드 칼륨(Potassium methoxide), 에톡사이드 칼륨(Potassium ethoxide), 아세트산칼륨(Potassium acetate), 포타슘 싸이오아세테이트(Potassium thioacetate), 폼산칼륨(Potassium formate), 요오드산칼륨(Potassium iodate), 과요오드산칼륨(Potassium periodate), 염소산칼륨(Potassium chlorate), 과염소산칼륨(Potassium perchlorate), 및 수소화붕소칼륨(Potassium borohydride)으로 이루어진 군에서 선택된 어느 하나일 수 있으며, 이에 제한되는 것은 아니다.The alkali metal precursors are potassium hydride, potassium hydroxide, potassium dioxide, potassium permanganate, potassium carbonate, potassium bicarbonate, potassium chloride (Potassium chloride), Potassium iodide, Potassium bromide, Potassium fluoride, Potassium cyanide, Potassium cyanate, Potassium cyanate Potassium thiocyanate, Potassium nitrate, Potassium nitrite, Potassium sulfate, Potassium bisulfate, Potassium sulfite, Potassium hexafluorophosphate Potassium triphosphate tribasic, Dibasic potassium phosphate, Potassium dihydrogen phosphate, Potassium dichromate, Cal chromate Potassium chromate, Potassium bromate, Potassium methoxide, Potassium ethoxide, Potassium acetate, Potassium thioacetate, Potassium formate formate, Potassium iodate, Potassium periodate, Potassium chlorate, Potassium perchlorate, and Potassium borohydride It is possible to, but is not limited to.

상기 알칼리 토금속 전구체는 질산바륨(Barium nitrate), 수산화바륨(Barium hydroxide), 염화바륨(Barium chloride), 황화바륨(Barium sulfide), 황산바륨(Barium sulfate), 탄산바륨(Barium carbonate), 아세트산바륨(Barium acetate), 산화바륨(Barium oxide), 과산화바륨(Barium peroxide), 요오드화바륨(Barium iodide), 플루오르화바륨(Barium fluoride), 브롬화바륨(Barium bromide), 과염소산바륨(Barium perchlorate), 크롬산바륨(barium chromate), 아철산바륨(Barium ferrite), 망간산바륨(Barium manganate), 인산바륨(barium phosphate), 바륨지르코네이트(Barium zirconate), 바륨아이소프로폭사이드(Barium isopropoxide), 바륨 싸이오설페이트(Barium thiosulfate), 바륨(Ⅱ) 아세틸아세토네이트(Barium(II) acetylacetonate hydrate), 요오드산바륨수화물(Barium iodate monohydrate), 바륨 메타포스페이트(Barium metaphosphate), 이염기성인산바륨(dibasic barium phosphate), 싸이오시안산바륨(Barium thiocyanate hydrate), 과요오드산바륨(Barium periodate), 및 2-에틸헥산산바륨(Barium 2-ethylhexanoate)으로 이루어진 군에서 선택된 어느 하나일 수 있으며, 이에 제한되는 것은 아니다.The alkaline earth metal precursors include barium nitrate, barium hydroxide, barium chloride, barium chloride, barium sulfide, barium sulfate, barium carbonate, and barium acetate. Barium acetate, Barium oxide, Barium peroxide, Barium iodide, Barium iodide, Barium fluoride, Barium bromide, Barium perchlorate, Barium chromium (Barium perchlorate) barium chromate, barium ferrite, barium manganate, barium phosphate, barium zirconate, barium isopropoxide, barium thiosulfate (Barium thiosulfate), Barium (II) acetylacetonate hydrate, Barium iodate monohydrate, Barium metaphosphate, Dibasic barium phosphate, Sa Coming may be Ansan barium (Barium thiocyanate hydrate), and periodic acid barium (Barium periodate), and 2-ethylhexanoate, barium any one selected from the group consisting of (Barium 2-ethylhexanoate), but is not limited thereto.

상기 알칼리 금속 전구체 또는 알칼리 토금속 전구체는 0.025 내지 3 M(mol/ℓ)의 농도일 수 있으며, 이에 제한되는 것은 아니다.The alkali metal precursor or alkaline earth metal precursor may be in a concentration of 0.025 to 3 M (mol / L), but is not limited thereto.

구체적으로, 상기 알칼리 금속 전구체 또는 알칼리 토금속 전구체의 농도가 0.025 M 미만일 경우 활성탄 내의 금속양이 부족하여 이산화탄소 흡착양이 저하되는 문제점이 발생할 수 있으며, 또한 상기 알칼리 금속 전구체 또는 알칼리 토금속 전구체의 농도가 3 M을 초과할 경우 활성탄의 비표면적이 급격하게 줄어들어 이산화탄소 흡착 효율이 저하되는 문제점을 야기할 수 있다.Specifically, when the concentration of the alkali metal precursor or alkaline earth metal precursor is less than 0.025 M, there may be a problem that the amount of carbon dioxide adsorption is lowered due to insufficient amount of metal in activated carbon, and the concentration of the alkali metal precursor or alkaline earth metal precursor is 3 When M is exceeded, the specific surface area of the activated carbon is drastically reduced, which may cause a problem of deterioration of carbon dioxide adsorption efficiency.

따라서, 상기 알칼리 금속 전구체 또는 알칼리 토금속 전구체의 농도는 0.025 내지 3 M인 것이 바람직하며, 특히 활성탄 내의 금속양 및 비표면적의 최적화되는 점을 고려하였을 때, 상기 알칼리 금속 전구체 또는 알칼리 토금속 전구체의 농도는 0.1 내지 1 M인 것이 보다 바람직하다.Therefore, the concentration of the alkali metal precursor or alkaline earth metal precursor is preferably 0.025 to 3 M, especially considering the optimization of the amount of metal and specific surface area in the activated carbon, the concentration of the alkali metal precursor or alkaline earth metal precursor is It is more preferable that it is 0.1-1 M.

상기 혼합용액을 준비하는 단계는 증류수 100 중량부에 대하여, 활성탄소 5 내지 20 중량부와 알칼리 금속 전구체 또는 알칼리 토금속 전구체 0.75 내지 30 중량부를 용해시켜 준비할 수 있으며, 이에 제한되는 것은 아니다.The preparing of the mixed solution may be prepared by dissolving 5 to 20 parts by weight of activated carbon and 0.75 to 30 parts by weight of an alkali metal precursor or an alkaline earth metal precursor with respect to 100 parts by weight of distilled water, but is not limited thereto.

구체적으로, 증류수 100 중량부에 대하여 활성탄소가 5 중량부 미만으로 포함될 경우 전반적인 공정의 효율이 떨어지는 문제점이 있으며, 또한 증류수 100 중량부에 대하여 활성탄소가 20 중량부를 초과하여 포함될 경우 알칼리 금속 전구체, 및 알칼리 토금속 전구체가 활성탄소와 고르게 결합하지 못하여 이산화탄소 흡착 효율이 줄어드는 문제점을 야기할 수 있다.Specifically, when the activated carbon is included in less than 5 parts by weight based on 100 parts by weight of distilled water, there is a problem that the efficiency of the overall process is reduced, and also when the activated carbon is included in excess of 20 parts by weight based on 100 parts by weight of distilled water, And the alkaline earth metal precursor may not bond evenly with the activated carbon may cause a problem that the carbon dioxide adsorption efficiency is reduced.

또한, 증류수 100 중량부에 대하여 알칼리 금속 전구체 또는 알칼리 토금속 전구체를 0.75 중량부 미만으로 포함할 경우 활성탄소의 산화금속의 수가 적어 이산화탄소 흡착효율이 떨어지는 문제점이 발생할 수 있으며, 또한 증류수 100 중량부에 대하여 알칼리 금속 전구체 또는 알칼리 토금속 전구체를 30 중량부를 초과하여 포함할 경우 활성탄의 비표면적을 감소시켜 이산화탄소가 흡착되는 공간이 줄어들어 많은 양의 이산화탄소 흡착을 하지 못하는 문제점을 야기할 수 있다.In addition, when the alkali metal precursor or the alkaline earth metal precursor is included in an amount of less than 0.75 parts by weight based on 100 parts by weight of distilled water, the number of metal oxides of the activated carbon may be low, resulting in a decrease in carbon dioxide adsorption efficiency. Including more than 30 parts by weight of the metal precursor or alkaline earth metal precursor may reduce the specific surface area of the activated carbon to reduce the space for the carbon dioxide is adsorbed may cause a problem that can not adsorb a large amount of carbon dioxide.

따라서, 상기 혼합용액을 준비하는 단계는 증류수 100 중량부에 대하여, 활성탄소 5 내지 20 중량부와 알칼리 금속 전구체 또는 알칼리 토금속 전구체 0.75 내지 30 중량부를 용해시켜 준비하는 것이 바람직하다.Therefore, the preparing of the mixed solution is preferably prepared by dissolving 5 to 20 parts by weight of activated carbon and 0.75 to 30 parts by weight of an alkali metal precursor or an alkaline earth metal precursor with respect to 100 parts by weight of distilled water.

특히, 활성탄소 내의 금속 양과 비표면적의 상관관계를 고려하였을 때, 상기 혼합용액을 준비하는 단계는 증류수 100 중량부에 대하여, 활성탄소 10 내지 15 중량부와 알칼리 금속 전구체 또는 알칼리 토금속 전구체 1 내지 5 중량부를 용해시켜 준비하는 것이 보다 바람직하다.In particular, considering the correlation between the amount of metal in the activated carbon and the specific surface area, preparing the mixed solution is based on 100 parts by weight of distilled water, 10 to 15 parts by weight of activated carbon and 1 to 5 alkali metal precursors or alkaline earth metal precursors. It is more preferable to melt | dissolve and prepare a weight part.

상기 제1교반용액을 준비하는 단계는 혼합용액을 상온에서 100 내지 400 rpm으로 15 내지 45분 동안 교반시켜 준비할 수 있으며, 이에 제한되는 것은 아니다.The preparing of the first stirring solution may be performed by stirring the mixed solution at 100 to 400 rpm for 15 to 45 minutes at room temperature, but is not limited thereto.

구체적으로, 상기 제1교반용액을 준비할 때 100 rpm 미만으로 교반시킬 경우 활성탄소가 제대로 섞이지 않게 되는 문제점이 있으며, 또한 상기 제1교반용액을 준비할 때 400 rpm을 초과하여 교반시킬 경우 알칼리 금속 산화물이 활성탄소와 결합하자 마자 분리되어 결합반응이 순조롭게 진행되지 않는 문제점을 야기할 수 있다. Specifically, there is a problem in that the activated carbon is not properly mixed when stirring below 100 rpm when preparing the first stirring solution, and also when the stirring is exceeding 400 rpm when preparing the first stirring solution, alkali metal As soon as the oxide is combined with the activated carbon, the oxide is separated, which may cause a problem that the binding reaction does not proceed smoothly.

따라서, 상기 제1교반용액을 준비할 때 100 내지 400 rpm으로 교반시키는 것이 바람직하며, 특히 활성탄소가 기벽에 튀지 않고 고르게 교반되는 점을 고려하였을 때, 상기 제1교반용액을 준비할 때 300 rpm으로 교반시키는 것이 보다 바람직하다.Therefore, it is preferable to stir at 100 to 400 rpm when preparing the first stirring solution, especially when considering that the activated carbon is stirred evenly without splashing on the substrate wall, 300 rpm when preparing the first stirring solution It is more preferable to stir with.

상기 산촉매를 첨가하는 단계는 제1교반용액에 루이스 산촉매 또는 유기산촉매를 첨가할 수 있으며, 이에 제한되는 것은 아니다.The adding of the acid catalyst may add a Lewis acid catalyst or an organic acid catalyst to the first stirring solution, but is not limited thereto.

구체적으로, 상기 제1교반용액에 첨가되는 산촉매가 약산성을 띄는 촉매일 경우 pH 조절을 위해 많은 양이 들어가게 되면 의도치 않은 부가반응이 진행될 수 있는 문제점이 있기 때문에, 루이스 산촉매 또는 유기산촉매는 강산성을 띄는 촉매인 것이 바람직하다.Specifically, in the case where the acid catalyst added to the first stirring solution is a catalyst having weak acidity, if a large amount is added for pH control, an unintended addition reaction may proceed, so that the Lewis acid catalyst or the organic acid catalyst has strong acidity. It is preferred to be a prominent catalyst.

또한, 상기 제1교반용액에 산촉매를 첨가함으로써, 제1교반용액의 pH는 1 내지 3으로 유지될 수 있다.In addition, by adding an acid catalyst to the first stirring solution, the pH of the first stirring solution may be maintained at 1 to 3.

구체적으로, 상기 제1교반용액의 pH가 1 미만일 경우 교반용액의 추후처리에 안전 상의 문제점이 발생할 수 있으며, 또한 상기 제1교반용액의 pH가 3을 초과할 경우 반응속도가 느려져 부가적인 반응을 유도할 수 있는 문제점을 야기할 수 있다.Specifically, when the pH of the first stirring solution is less than 1, a safety problem may occur in the subsequent treatment of the stirred solution, and when the pH of the first stirring solution exceeds 3, the reaction rate is slowed, thereby causing an additional reaction. It may cause inducible problems.

따라서, 상기 제1교반용액은 pH가 1 내지 3으로 유지되는 것이 바람직하며, 특히 반응속도 및 안전성 측면을 고려하였을 때, 상기 제1교반용액의 pH는 2 내지 2.5로 유지되는 것이 보다 바람직하다.Therefore, the first stirring solution is preferably maintained at a pH of 1 to 3, especially considering the reaction rate and safety aspects, the pH of the first stirring solution is more preferably maintained at 2 to 2.5.

상기 루이스 산촉매는 염산(HCl), 브롬산(HBr), 황산(H2SO4), 인산(H3PO4), 탄산(H2CO3), 염화티타늄(TiCl4), 염화철(Ⅲ)(FeCl3) 및 염화알루미늄(AlCl3)으로 이루어진 군에서 선택된 어느 하나일 수 있으며, 이에 제한되는 것은 아니다.The Lewis acid catalyst is hydrochloric acid (HCl), bromic acid (HBr), sulfuric acid (H 2 SO 4 ), phosphoric acid (H 3 PO 4 ), carbonic acid (H 2 CO 3 ), titanium chloride (TiCl 4 ), iron chloride (III) (FeCl 3 ) and aluminum chloride (AlCl 3 ) may be any one selected from, but is not limited thereto.

상기 유기산촉매는 설폰산(sulfonic acid), 피크르산(picric acid), 타르타르산(tartaric acid), 시트르산(citric acid), 에틸렌디아민테트라아세트산(ethylenediaminetetraacetic acid), 및 피로인산(pyrophosphoric acid)으로 이루어진 군에서 선택된 어느 하나일 수 있으며, 이에 제한되는 것은 아니다.The organic acid catalyst is selected from the group consisting of sulfonic acid, picric acid, tartaric acid, citric acid, ethylenediaminetetraacetic acid, and pyrophosphoric acid. It may be any one, but is not limited thereto.

상기 제2교반용액을 준비하는 단계는 산촉매가 첨가된 제1교반용액을 상온에서 100 내지 400 rpm으로 24 내지 72시간 동안 교반시켜 준비할 수 있으며, 이에 제한되는 것은 아니다.The preparing of the second stirring solution may be prepared by stirring the first stirring solution to which the acid catalyst is added at 100 to 400 rpm at room temperature for 24 to 72 hours, but is not limited thereto.

구체적으로, 상기 제2교반용액을 준비할 때 100 rpm 미만으로 교반시킬 경우 활성탄소가 제대로 섞이지 않게 되는 문제점이 있으며, 또한 상기 제2교반용액을 준비할 때 400 rpm을 초과하여 교반시킬 경우 알칼리 금속 산화물이 활성탄소에 결합하자 마자 분리되어 결합반응이 순조롭게 진행되지 않는 문제점을 야기할 수 있다.Specifically, there is a problem that the activated carbon is not properly mixed when stirring at less than 100 rpm when preparing the second stirring solution, and also when the stirring is exceeding 400 rpm when preparing the second stirring solution alkali metal As soon as the oxide binds to the activated carbon, the oxide may be separated and cause a problem in that the coupling reaction does not proceed smoothly.

따라서, 상기 제2교반용액을 준비할 때 100 내지 400 rpm으로 교반시키는 것이 바람직하며, 특히 활성탄소가 기벽에 튀지 않고 고르게 교반되는 점을 고려하였을 때, 상기 제2교반용액을 준비할 때 300 rpm으로 교반시키는 것이 보다 바람직하다.Therefore, it is preferable to stir at 100 to 400 rpm when preparing the second stirring solution, especially considering that the activated carbon is stirred evenly without splashing on the substrate wall, 300 rpm when preparing the second stirring solution It is more preferable to stir with.

상기 알칼리 금속 산화물-활성탄소 또는 알칼리 토금속 산화물-활성탄소를 제조하는 단계는 제2교반용액을 필터링 후 80 내지 200℃에서 4 내지 8시간 동안 건조하여 제조할 수 있으며, 이에 제한되는 것은 아니다.The step of preparing the alkali metal oxide-activated carbon or alkaline earth metal oxide-activated carbon may be prepared by filtering the second stirring solution at 80 to 200 ° C. for 4 to 8 hours, but is not limited thereto.

구체적으로, 상기 알칼리 금속 산화물-활성탄소 또는 알칼리 토금속 산화물-활성탄소를 제조하는 단계에서, 80℃ 미만으로 건조할 경우 수분이 잔존하여 성능이 저하되는 문제점이 발생할 수 있으며, 또한 200℃를 초과하여 건조할 경우 활성탄소에 결합된 금속물질이 들뜨는 현상으로 인해 부가반응이 진행할 수 있는 문제점을 야기할 수 있다.Specifically, in the step of preparing the alkali metal oxide-activated carbon or alkaline earth metal oxide-activated carbon, when dried to less than 80 ℃ may cause a problem that the performance is reduced due to the moisture remaining, and also exceeds 200 ℃ Drying may cause a problem that the addition reaction may proceed due to the phenomenon of the metal material bound to the activated carbon.

또한, 상기 알칼리 금속 산화물-활성탄소 또는 알칼리 토금속 산화물-활성탄소를 제조하는 단계에서, 4시간 미만으로 건조할 경우 수분이 잔존하는 문제점이 발생할 수 있으며, 또한 8시간을 초과하여 건조할 경우 계속해서 가해지는 열로 인해 부가반응이 진행될 수 있는 문제점을 야기할 수 있다.In addition, in the step of preparing the alkali metal oxide-activated carbon or alkaline earth metal oxide-activated carbon, when the drying is less than 4 hours, the problem of moisture remaining may occur, and if the drying for more than 8 hours, The heat applied can cause problems that the addition reaction can proceed.

따라서, 상기 알칼리 금속 산화물-활성탄소 또는 알칼리 토금속 산화물-활성탄소를 제조하는 단계는 제2교반용액을 필터링 후 80 내지 200℃에서 4 내지 8시간 동안 건조하여 제조하는 것이 바람직하다.Therefore, the step of preparing the alkali metal oxide-activated carbon or alkaline earth metal oxide-activated carbon is preferably prepared by drying the second stirring solution at 80 to 200 ° C. for 4 to 8 hours after filtering.

특히, 수분건조 및 부가반응의 차단 등을 고려하였을 때, 상기 알칼리 금속 산화물-활성탄소 또는 알칼리 토금속 산화물-활성탄소를 제조하는 단계는 제2교반용액을 필터링 후 120 내지 150℃에서 5 내지 6시간 동안 건조하여 제조하는 것이 보다 바람직하다.In particular, considering the drying of moisture and the blocking of addition reaction, the step of preparing the alkali metal oxide-activated carbon or alkaline earth metal oxide-activated carbon may be performed for 5 to 6 hours at 120 to 150 ° C. after filtering the second stirring solution. It is more preferable to prepare by drying.

상기 알칼리 금속 산화물-활성탄소 또는 알칼리 토금속 산화물-활성탄소를 제조하는 단계 이후 진공 포장하는 단계를 더 포함할 수 있으며, 이에 제한되는 것은 아니다.The method may further include vacuum packaging after preparing the alkali metal oxide-activated carbon or alkaline earth metal oxide-activated carbon, but is not limited thereto.

구체적으로, 상기 알칼리 금속 산화물-활성탄소 또는 알칼리 토금속 산화물-활성탄소가 공기 중에 노출될 경우 대기 중의 이산화탄소가 지속적으로 알칼리 금속 산화물-활성탄소 또는 알칼리 토금속 산화물-활성탄소에 흡착되기 때문에 이를 자동차 내부 필터에 적용할 경우 필터 성능을 저하시킬 수 있는 바, 진공 포장하는 단계를 더 포함하는 것이 바람직하다.Specifically, when the alkali metal oxide-activated carbon or alkaline earth metal oxide-activated carbon is exposed to air, carbon dioxide in the air is continuously adsorbed to the alkali metal oxide-activated carbon or alkaline earth metal oxide-activated carbon. When applied to the bar can reduce the filter performance, it is preferable to further include a vacuum packaging step.

이하, 하기 실시예에 의해 본 발명인 알칼리계 금속이 처리된 자동차 내부 필터용 활성탄소 소재 및 이의 제조방법을 보다 상세하게 설명한다. 다만, 이러한 실시예에 의해 본 발명이 한정되는 것은 아니다.Hereinafter, the activated carbon material for automobile interior filters treated with alkali metals of the present invention and a method for manufacturing the same according to the present invention will be described in more detail. However, the present invention is not limited by these examples.

<실시예 1> 알칼리 토금속이 처리된 자동차 내부 필터용 활성탄소 소재Example 1 Activated Carbon Material for Automobile Interior Filter Treated with Alkaline Earth Metal

증류수 100 중량부에 대해 활성탄소 15 중량부와 수산화바륨(Barium hydroxide) 2 중량부(0.1 M 농도에서 중량을 계산하였을 때 수산화바륨 용액 60 중량부)를 용해하여 혼합용액을 준비하였다. A mixed solution was prepared by dissolving 15 parts by weight of activated carbon and 2 parts by weight of barium hydroxide (60 parts by weight of a barium hydroxide solution when the weight was calculated at a concentration of 0.1 M) based on 100 parts by weight of distilled water.

교반기(MSH-20A, 대한과학)를 이용하여 준비한 혼합용액을 상온에서 30분 동안 300 rpm으로 교반시켜 제1교반용액을 준비하였다.The mixed solution prepared by using a stirrer (MSH-20A, Korean Science) was stirred at 300 rpm for 30 minutes at room temperature to prepare a first stirring solution.

제1교반용액에 산촉매로 염산을 첨가하여 제1교반용액의 pH를 2로 유지하였다.Hydrochloric acid was added to the first stirring solution as an acid catalyst to maintain a pH of the first stirring solution at 2.

교반기(MSH-20A, 대한과학)를 이용하여, 염산이 첨가된 제1교반용액을 상온에서 24시간 동안 300 rpm으로 교반시켜 제2교반용액을 준비하였다.Using a stirrer (MSH-20A, Korean Science), the first stirring solution added with hydrochloric acid was stirred at 300 rpm for 24 hours at room temperature to prepare a second stirring solution.

제2교반용액에 침전된 알칼리 금속 산화물-활성탄소를 거름종이(filter paper)로 필터링한 후 여과된 알칼리 금속 산화물-활성탄소를 120℃에서 6시간 동안 건조하여 알칼리 토금속이 처리된 자동차 내부 필터용 활성탄소 소재를 제조하였다.Filter the alkali metal oxide-activated carbon precipitated in the second stirring solution with filter paper, and then dry the filtered alkali metal oxide-activated carbon at 120 ° C. for 6 hours to filter the alkaline earth metal. Activated carbon material was prepared.

<실시예 2> 알칼리 토금속이 처리된 자동차 내부 필터용 활성탄소 소재 제조Example 2 Preparation of Activated Carbon Material for Automobile Interior Filter Treated with Alkaline Earth Metal

수산화바륨(Barium hydroxide) 대신에 아세트산바륨(Barium acetate)을 이용한 것을 제외하고는, 상기 실시예 1과 동일한 조건으로 알칼리 토금속이 처리된 자동차 내부 필터용 활성탄소 소재를 제조하였다.Except for using barium acetate instead of barium hydroxide (Barium hydroxide), under the same conditions as in Example 1 was prepared an activated carbon material for automobile interior filter treated with alkaline earth metal.

<실시예 3> 알칼리 금속이 처리된 자동차 내부 필터용 활성탄소 소재 제조Example 3 Preparation of Activated Carbon Material for Automobile Interior Filter Treated with Alkali Metal

수산화바륨(Barium hydroxide) 대신에 수산화칼륨(Potassium hydroxide)을 이용한 것을 제외하고는, 상기 실시예 1과 동일한 조건으로 알칼리 금속이 처리된 자동차 내부 필터용 활성탄소 소재를 제조하였다. Except for using potassium hydroxide instead of barium hydroxide (Potassium hydroxide), an activated carbon material for automobile interior filters treated with alkali metals was prepared under the same conditions as in Example 1.

<비교예 1> 산촉매가 첨가되지 않은 알칼리 토금속이 처리된 자동차 내부 필터용 활성탄소 소재<Comparative Example 1> Activated Carbon Material for Automobile Interior Filter Treated with Alkaline Earth Metal without Acid Catalyst

증류수 100 중량부에 대해 활성탄소 15 중량부와 수산화바륨(Barium hydroxide) 2 중량부(0.1 M 농도에서 중량을 계산하였을 때 수산화바륨 용액 60 중량부)를 용해하여 혼합용액을 준비하였다. A mixed solution was prepared by dissolving 15 parts by weight of activated carbon and 2 parts by weight of barium hydroxide (60 parts by weight of a barium hydroxide solution when the weight was calculated at a concentration of 0.1 M) based on 100 parts by weight of distilled water.

교반기(MSH-20A, 대한과학)를 이용하여 준비한 혼합용액을 상온에서 30분 동안 300 rpm으로 교반시켜 제1교반용액을 준비하였다.The mixed solution prepared by using a stirrer (MSH-20A, Korean Science) was stirred at 300 rpm for 30 minutes at room temperature to prepare a first stirring solution.

교반기(MSH-20A, 대한과학)를 이용하여, 제1교반용액을 상온에서 24시간 동안 300 rpm으로 교반시켜 제2교반용액을 준비하였다.Using a stirrer (MSH-20A, Korean Science), the first stirring solution was stirred at 300 rpm for 24 hours at room temperature to prepare a second stirring solution.

제2교반용액에 침전된 알칼리 금속 산화물-활성탄소를 거름종이(filter paper)로 필터링한 후 여과된 알칼리 금속 산화물-활성탄소를 120℃에서 6시간 동안 건조하여 알칼리 금속이 처리된 자동차 내부 필터용 활성탄소 소재를 제조하였다.After filtering the alkali metal oxide-activated carbon precipitated in the second stirring solution with a filter paper, the filtered alkali metal oxide-activated carbon was dried at 120 ° C. for 6 hours to filter the interior of the alkali metal. Activated carbon material was prepared.

<비교예 2> 산촉매가 첨가되지 않으며, 고온에서 교반시킨 알칼리 토금속이 처리된 자동차 내부 필터용 활성탄소 소재<Comparative Example 2> Activated carbon material for automobile interior filter which is free of acid catalyst and treated with alkaline earth metal stirred at high temperature

증류수 100 중량부에 대해 활성탄소 15 중량부와 수산화바륨(Barium hydroxide) 2 중량부(0.1 M 농도에서 중량을 계산하였을 때 수산화바륨 용액 60 중량부)를 용해하여 혼합용액을 준비하였다. A mixed solution was prepared by dissolving 15 parts by weight of activated carbon and 2 parts by weight of barium hydroxide (60 parts by weight of a barium hydroxide solution when the weight was calculated at a concentration of 0.1 M) based on 100 parts by weight of distilled water.

교반기(MSH-20A, 대한과학)를 이용하여 준비한 혼합용액을 80℃에서 30분 동안 300 rpm으로 교반시켜 제1교반용액을 준비하였다.The mixed solution prepared using the stirrer (MSH-20A, Korean Science) was stirred at 300 rpm for 30 minutes at 80 ° C to prepare a first stirring solution.

교반기(MSH-20A, 대한과학)를 이용하여, 제1교반용액을 80℃에서 24시간 동안 300 rpm으로 교반시켜 제2교반용액을 준비하였다.Using a stirrer (MSH-20A, Korean Science), the first stirring solution was stirred at 300 rpm for 24 hours at 80 ° C. to prepare a second stirring solution.

제2교반용액에 침전된 알칼리 금속 산화물-활성탄소를 거름종이(filter paper)로 필터링한 후 여과된 알칼리 금속 산화물-활성탄소를 120℃에서 6시간 동안 건조하여 알칼리 금속이 처리된 자동차 내부 필터용 활성탄소 소재를 제조하였다.After filtering the alkali metal oxide-activated carbon precipitated in the second stirring solution with a filter paper, the filtered alkali metal oxide-activated carbon was dried at 120 ° C. for 6 hours to filter the interior of the alkali metal. Activated carbon material was prepared.

<실험예 1> 이산화탄소 흡착성능 평가Experimental Example 1 Evaluation of Carbon Dioxide Adsorption Performance

가스크로마토그래피(gas chromatography; 'GC')를 이용하여 이산화탄소 흡착성능을 평가하였다.The adsorption performance of carbon dioxide was evaluated using gas chromatography ('GC').

구체적으로, 이산화탄소가 함유된 가스를 실시예 1 내지 실시예 3에 따라 제조된 알칼리계 금속이 처리된 자동차 내부 필터용 활성탄소 소재, 종래 활성탄소, 및 비교예 1에 따라 제조된 알칼리 금속이 처리된 자동차 내부 필터용 활성탄소 소재에 흘려주어 가스를 포집한 후 GC를 통해 흡착된 이산화탄소 양을 계산하였고, 그 결과를 도 3에 나타내었으며, 조건은 하기와 같다.Specifically, the carbon-containing gas is treated with an activated carbon material for automobile interior filters treated with alkali metals prepared according to Examples 1 to 3, conventional activated carbon, and an alkali metal prepared according to Comparative Example 1. The amount of carbon dioxide adsorbed through GC was collected by flowing the activated carbon material for the vehicle interior filter and collecting the gas, and the results are shown in FIG. 3, and the conditions are as follows.

- 시험기기: hp 6890a gc, agilentTester: hp 6890a gc, agilent

- 이산화탄소 함량: 30%CO2 content: 30%

- 유량속도: 0.1 ㎖/min-Flow rate: 0.1 ml / min

- 측정시간: 90분Measurement time: 90 minutes

도 3은 알칼리 금속이 처리되지 않은 활성탄소와 실시예 1 및 비교예 2에 따라 제조된 알칼리계 금속을 처리한 활성탄소 소재의 이산화탄소 흡착 변화량을 나타낸 도면이다.3 is a view showing the carbon dioxide adsorption change amount of the activated carbon not treated with alkali metal and the activated carbon material treated with alkali metals prepared according to Example 1 and Comparative Example 2.

도면을 참조하면, 기존 활성탄소(2.00669 mmol/g), 및 비교예 1에 따라 제조된 알칼리 금속이 처리된 자동차 내부 필터용 활성탄소 소재(3.85334 mmol/g)에 비해 실시예 1에 따라 제조된 알칼리계 금속이 처리된 자동차 내부 필터용 활성탄소 소재(4.07508 mmol/g)의 이산화탄소 흡착성능이 우수함을 알 수 있다.Referring to the drawings, compared to the activated carbon (2.00669 mmol / g), and the activated carbon material (3.85334 mmol / g) for car interior filters treated according to Comparative Example 1 prepared according to Example 1 It can be seen that the carbon dioxide adsorption performance of the activated carbon material (4.07508 mmol / g) for automobile interior filters treated with alkali metals is excellent.

산촉매를 첨가할 경우 전체 용액이 산성화되면서 알칼리계 금속의 분산도가 올라가기 때문에 알칼리계 금속이 비교적 고르게 분포함으로 인하여 이산화탄소 흡착량이 증가하였음을 알 수 있다.When the acid catalyst is added, since the total solution is acidified, the alkali metal dispersibility increases, and thus the amount of carbon dioxide adsorption increased due to the relatively even distribution of the alkali metal.

또한, 상기 실시예 1에 따라 제조된 알칼리계 금속이 처리된 자동차 내부 필터용 활성탄소 소재를 30일 동안 밀폐보관 하였을 때 이산화탄소 흡착량의 감소는 미미하게 나타났다. 이는, 산촉매 첨가로 인하여 알칼리계 금속들이 화학적 결합을 통해 계속해서 활성탄소 내에 그대로 잔존하기 때문에 이산화탄소 흡착량이 미미하게 나타났음을 알 수 있다.In addition, when the activated carbon material for automobile interior filters treated with alkali metals prepared according to Example 1 was kept for 30 days, the reduction in carbon dioxide adsorption amount was minimal. This indicates that the amount of carbon dioxide adsorption was minimal because the alkali metals remained in the activated carbon through chemical bonds due to the addition of the acid catalyst.

반면에, 비교예 1에 따라 제조된 알칼리 금속이 처리된 자동차 내부 필터용 활성탄소 소재를 30일 동안 밀폐보관 하였을 때 이산화탄소 흡착량이 급격히 감소함을 확인하였다.On the other hand, when the activated carbon material for automobile interior filters treated with alkali metals prepared according to Comparative Example 1 was kept for 30 days, it was confirmed that the amount of carbon dioxide adsorption rapidly decreased.

구체적으로, 비교적 극성을 띄는 알칼리계 금속들이 비극성인 활성탄소와의 친화도가 약해져서 한쪽으로 이동하거나, 또는 물리적 흡착력이 떨어지기 때문에 이산화탄소 흡착량이 급격히 감소하였음을 알 수 있다.Specifically, it can be seen that the amount of carbon dioxide adsorption drastically decreased because relatively polar alkali metals have less affinity with nonpolar activated carbon and move to one side, or because the physical adsorption power is reduced.

도 4는 알칼리 금속이 처리되지 않은 활성탄소와 실시예 1 및 비교예 1에 따라 제조된 알칼리계 금속을 처리한 활성탄소 소재의 이산화탄소 흡착 변화량을 나타낸 도면이다.4 is a view showing the carbon dioxide adsorption change amount of the activated carbon material treated with an alkali-free metal and the alkali-based metal prepared according to Example 1 and Comparative Example 1.

도면을 참조하면, 기존 활성탄소(2.00669 mmol/g), 및 비교예 2에 따라 제조된 알칼리 금속이 처리된 자동차 내부 필터용 활성탄소 소재(3.87457 mmol/g)에 비해 실시예 1에 따라 제조된 알칼리계 금속이 처리된 자동차 내부 필터용 활성탄소 소재(4.07508 mmol/g)의 이산화탄소 흡착성능이 우수함을 알 수 있다.Referring to the drawings, compared to the activated carbon (2.00669 mmol / g), and the activated carbon material for automobile interior filters (3.87457 mmol / g) prepared according to Comparative Example 2 prepared according to Example 1 It can be seen that the carbon dioxide adsorption performance of the activated carbon material (4.07508 mmol / g) for automobile interior filters treated with alkali metals is excellent.

즉, 실시예 1의 제조방법은 고온(80℃)에서 환류반응을 통해 제조되는 종래 자동차 내부 필터용 활성탄소 소재 제조방법(비교예 2)에 비해 상대적으로 온화한 반응조건(상온조건)으로 자동차 내부 필터용 활성탄소 소재를 제조할 수 있으며, 이에 제조된 활성탄소 소재는 이산화탄소 흡착 성능이 우수함을 확인하였다.That is, the manufacturing method of Example 1 is relatively mild reaction conditions (room temperature conditions) compared to the conventional method for manufacturing activated carbon material for automobile interior filters (Comparative Example 2) manufactured by reflux at high temperature (80 ° C). Activated carbon material for the filter can be prepared, the activated carbon material was confirmed that the carbon dioxide adsorption performance is excellent.

도 5는 실시예 1 내지 실시예 3에 따라 제조된 알칼리계 금속을 처리한 활성탄소 소재의 이산화탄소 흡착 변화량을 나타낸 도면이다.5 is a view showing a carbon dioxide adsorption change amount of the activated carbon material treated with an alkali-based metal prepared according to Examples 1 to 3.

도면을 참조하면, 다양한 알칼리계 금속 전구체 중에서도 특히 수산화바륨(Barium hydroxide)을 이용하여 제조된 활성탄소 소재가 이산화탄소 흡착 성능이 가장 우수함을 확인하였다.Referring to the drawings, it was confirmed that among the various alkali-based metal precursors, the carbon dioxide adsorption performance of the activated carbon material prepared using barium hydroxide (Barium hydroxide) is the most excellent.

<실험예 2> 비표면적 측정Experimental Example 2 Measurement of Specific Surface Area

비표면적 측정기(QUDRASORB SI)를 이용하여 실시예 1에 따라 제조된 알칼리계 금속이 처리된 자동차 내부 필터용 활성탄소 소재, 및 알칼리계 금속이 처리되지 않은 활성탄소의 비표면적을 측정하였다.The specific surface area of the activated carbon material for automobile interior filters treated with alkali metals prepared according to Example 1, and activated carbons not treated with alkali metals, was measured using a specific surface area meter (QUDRASORB SI).

구체적으로, 실시예 1에 따라 제조된 알칼리계 금속이 처리된 자동차 내부 필터용 활성탄소 소재, 및 알칼리계 금속이 처리되지 않은 활성탄소에 질소 가스를 흡탈착하여 브루나우어-에메트-텔러 방정식(Brunauer-Emmett-Teller equation; 이하 'BET 방정식')을 통해 비표면적을 계산하였다.Specifically, the Brunauer-Emmett-Teller equation is obtained by adsorbing and desorbing nitrogen gas to activated carbon materials for automobile interior filters treated with alkali metals prepared according to Example 1, and activated carbons not treated with alkali metals. The specific surface area was calculated using the Brunauer-Emmett-Teller equation (hereinafter referred to as the 'BET equation').

도 6을 참조하면, 실시예 1에 따라 제조된 알칼리계 금속이 처리된 자동차 내부 필터용 활성탄소 소재의 비표면적이 알칼리계 금속이 처리되지 않은 활성탄소의 비표면적보다 작게 나타났다. Referring to FIG. 6, the specific surface area of the activated carbon material for automobile interior filters treated with alkali metals prepared according to Example 1 was smaller than the specific surface area of activated carbon not treated with alkali metals.

이는 다공성 구조를 갖는 활성탄소가 알칼리계 금속이 처리되는 동안 활성탄소 표면에 형성된 알칼리 금속의 수산화물이 반응에 의해 산화되면서 기공 내외부에 위치함으로 인해 비표면적이 줄어든 것으로 판단된다.This is because the specific surface area is reduced because the activated carbon having a porous structure is located inside and outside the pores as the hydroxide of the alkali metal formed on the surface of the activated carbon is oxidized by the reaction while the alkali-based metal is processed.

<실험예 3> EMPA 정성 및 정량 분석Experimental Example 3 Qualitative and Quantitative Analysis of EMPA

알칼리 금속이 처리되지 않은 활성탄소, 실시예 1, 비교예 1, 및 비교예 2에 따른 알칼리계 금속을 처리한 활성탄소 소재의 전자 프로브 마이크로 분석(electron probe micro analysis; 이하 'EPMA')을 수행하였다.Electron probe micro analysis (hereinafter referred to as 'EPMA') of an activated carbon material treated with an alkali-based active carbon, an alkali-based metal according to Example 1, Comparative Example 1, and Comparative Example 2 was performed. It was.

구체적으로, 전계 방사 프로브 마이크로 분석기(Field Emission Probe Micro Analyzer, JXA8530F(5CH))를 이용하여 알칼리 금속이 처리되지 않은 활성탄소, 실시예 1, 비교예 1, 및 비교예 2에 따른 알칼리계 금속을 처리한 활성탄소 소재에 가속된 전자빔을 충돌시켜 각 원자마다 방출하는 X-ray의 에너지가 다름을 이용하여 상기 시료들이 구성된 원소를 분석하였고, 그 결과를 하기 나타내었다.Specifically, using an field emission probe micro analyzer (JXA8530F (5CH)), the alkali-based activated carbon, alkali metals according to Example 1, Comparative Example 1, and Comparative Example 2 were not used By analyzing the energy of the X-rays emitted from each atom by colliding the accelerated electron beam with the treated activated carbon material, the elements composed of the samples were analyzed and the results are shown below.

도 7은 알칼리 금속이 처리되지 않은 활성탄소의 EPMA 분석결과를 나타낸 도면이다.7 is a view showing the results of EPMA analysis of activated carbon not treated with alkali metal.

도면을 참조하면, 일반적인 상용화 활성탄소에는 대부분 C 원소와, O 원소가 주로 검출되는 것을 알 수 있다. Referring to the drawings, it can be seen that the C and O elements are mainly detected in general commercially available activated carbon.

도 8은 실시예 1에 따른 알칼리 토금속계 원소를 처리한 활성탄소 소재의 EPMA 분석결과를 나타낸 도면이다.8 is a view showing the results of EPMA analysis of activated carbon material treated with alkaline earth metal elements according to Example 1.

도면을 참조하면, 도 7과 비교하여 바륨의 양이 눈에 띄게 증가한 것을 확인할 수 있다.Referring to the drawings, it can be seen that the amount of barium is significantly increased compared to FIG.

도 9는 비교예 1에 따른 알칼리 토금속계 원소를 처리한 활성탄소 소재의 EPMA 분석결과를 나타낸 도면이다.FIG. 9 is a view showing EPMA analysis results of activated carbon materials treated with alkaline earth metal elements according to Comparative Example 1. FIG.

도면을 참조하면, 도 8과 같이 도 7과 비교하여 바륨의 양이 증가한 것을 확인할 수 있다.Referring to the drawings, it can be seen that the amount of barium increased compared to FIG.

도 10은 비교예 2에 따른 알칼리 토금속계 원소를 처리한 활성탄소 소재의 EPMA 분석결과를 나타낸 도면이다.10 is a view showing the EPMA analysis results of the activated carbon material treated with alkaline earth metal elements according to Comparative Example 2.

도면을 참조하면, 도 8에서처럼 도 7에 비해 바륨의 양이 증가한 것을 확인할 수 있다.Referring to the drawings, it can be seen that the amount of barium is increased compared to FIG.

도 11은 실시예 1에 의해 합성된 활성탄소를 밀폐용기에 30일 보관한 뒤 EPMA 분석결과를 나타낸 도면이다. 11 is a view showing the EPMA analysis result after storing the activated carbon synthesized in Example 1 in a sealed container for 30 days.

도면을 참조하면, 도 7과 비교하여 바륨의 양이 거의 줄어들지 않은 것을 확인할 수 있다. 이는, 산촉매 처리를 함으로써, 활성탄소와 바륨 간의 화학적 결합을 유도할 수 있고, 이를 통해 30일 뒤에도 활성탄소 내부에 바륨이 잔존함을 알 수 있다.Referring to the drawings, it can be seen that the amount of barium hardly decreased in comparison with FIG. 7. This, by the acid catalyst treatment, can induce a chemical bond between the activated carbon and barium, through which it can be seen that the barium remains in the activated carbon after 30 days.

도 12는 비교예 2에 따른 활성탄소 소재를 밀폐용기에 30일 보관한 뒤 EPMA 분석결과를 나타낸 도면이다. 12 is a view showing the EPMA analysis result after storing the activated carbon material according to Comparative Example 2 in a closed container for 30 days.

도면을 참조하면, 바륨의 양이 현저하게 줄어든 것을 확인할 수 있는데, 이는 반응 시에 열을 가해주더라도 산촉매를 첨가하지 않음으로써, 활성탄소와 바륨 간에 화학적 결합을 할 수 없기 때문에 밀폐용기에 30일 동안 보관한 후 바륨이 활성탄소 내부에 잔존하지 않게 되어 바륨의 양이 현저히 줄었음을 알 수 있다.Referring to the drawings, it can be seen that the amount of barium is significantly reduced, which is 30 days in an airtight container because it is not possible to chemically bond between activated carbon and barium by adding an acid catalyst even if heat is applied during the reaction. After storage for a while barium does not remain inside the activated carbon it can be seen that the amount of barium significantly reduced.

이상과 같이, 본 발명은 비록 한정된 실시예와 도면에 의해 설명되었으나, 본 발명은 이것에 의해 한정되지 않으며 본 발명이 속하는 기술 분야에서 통상의 지식을 가진 자에 의해 본 발명의 기술 사상과 아래에 기재될 청구범위의 균등 범위 내에서 다양한 수정 및 변형이 가능함은 물론이다.As mentioned above, although this invention was demonstrated by the limited embodiment and drawing, this invention is not limited by this, The person of ordinary skill in the art to which this invention belongs, Of course, various modifications and variations are possible within the scope of equivalents of the claims to be described.

Claims (14)

활성탄소 표면에 알칼리 금속의 수산화물 또는 알칼리 토금속의 수산화물이 담지된, 알칼리계 금속이 처리된 자동차 내부 필터용 활성탄소 소재.Activated carbon material for automobile interior filters treated with alkali-based metals, wherein an alkali metal hydroxide or alkaline earth metal hydroxide is supported on the surface of the activated carbon. 청구항 1에 있어서,The method according to claim 1, 상기 알칼리 금속은,The alkali metal, 리튬(Li), 나트륨(Na), 칼륨(K), 및 루비듐(Rb)로 이루어진 군에서 선택된 어느 하나인 것을 특징으로 하는, 알칼리계 금속이 처리된 자동차 내부 필터용 활성탄소 소재.Activated carbon material for automotive interior filters treated with alkali metal, characterized in that any one selected from the group consisting of lithium (Li), sodium (Na), potassium (K), and rubidium (Rb). 청구항 1에 있어서,The method according to claim 1, 상기 알칼리 토금속은,The alkaline earth metal is, 칼슘, 스트론튬, 및 바륨으로 이루어진 군에서 선택된 어느 하나인 것을 특징으로 하는, 알칼리계 금속이 처리된 자동차 내부 필터용 활성탄소 소재.Activated carbon material for automobile interior filter treated with alkali metal, characterized in that any one selected from the group consisting of calcium, strontium, and barium. 증류수에 활성탄소와 알칼리 금속 전구체 또는 알칼리 토금속 전구체를 용해시켜 혼합용액을 준비하는 단계;Preparing a mixed solution by dissolving activated carbon and an alkali metal precursor or an alkaline earth metal precursor in distilled water; 상기 혼합용액을 상온에서 교반시켜 제1교반용액을 준비하는 단계;Preparing a first stirring solution by stirring the mixed solution at room temperature; 상기 제1교반용액에 산촉매를 첨가하는 단계;Adding an acid catalyst to the first stirring solution; 산촉매가 첨가된 제1교반용액을 상온에서 교반시켜 제2교반용액을 준비하는 단계; 및Preparing a second stirring solution by stirring the first stirring solution added with the acid catalyst at room temperature; And 상기 제2교반용액을 필터링 후 건조하여 알칼리 금속 산화물-활성탄소 또는 알칼리 토금속 산화물-활성탄소를 제조하는 단계를 포함하는, 알칼리계 금속이 처리된 자동차 내부 필터용 활성탄소 소재 제조방법.Filtering and drying the second stirring solution to prepare an alkali metal oxide-activated carbon or an alkaline earth metal oxide-activated carbon. 청구항 1에 있어서,The method according to claim 1, 상기 알칼리 금속 전구체는,The alkali metal precursor, 수소화칼륨(Potassium hydride), 수산화칼륨(Potassium hydroxide), 칼륨디산화물(Potassium dioxide), 과망간산칼륨(Potassium permanganate), 탄산칼륨(Potassium carbonate), 탄산수소칼륨(Potassium bicarbonate), 염화칼륨(Potassium chloride), 아이오딘화칼륨(Potassium iodide), 브로민화칼륨(Potassium bromide), 플루오르화칼륨(Potassium fluoride), 시안화칼륨(Potassium cyanide), 시안산칼륨(Potassium cyanate), 싸이오시안산칼륨(Potassium thiocyanate), 질산칼륨(Potassium nitrate), 아질산칼륨(Potassium nitrite), 황산칼륨(Potassium sulfate), 황산수소칼륨(Potassium bisulfate), 아황산칼륨(Potassium sulfite), 헥사플루오르인산칼륨(Potassium hexafluorophosphate), 제삼인산칼륨(Potassium phosphate tribasic), 인산수소칼륨(Dibasic potassium phosphate), 인산이수소칼륨(Potassium dihydrogen phosphate), 중크롬산칼륨(Potassium dichromate), 크롬산칼륨(Potassium chromate), 브롬산칼륨(Potassium bromate), 메톡사이드 칼륨(Potassium methoxide), 에톡사이드 칼륨(Potassium ethoxide), 아세트산칼륨(Potassium acetate), 포타슘 싸이오아세테이트(Potassium thioacetate), 폼산칼륨(Potassium formate), 요오드산칼륨(Potassium iodate), 과요오드산칼륨(Potassium periodate), 염소산칼륨(Potassium chlorate), 과염소산칼륨(Potassium perchlorate), 및 수소화붕소칼륨(Potassium borohydride)으로 이루어진 군에서 선택된 어느 하나인 것을 특징으로 하는, 알칼리계 금속이 처리된 자동차 내부 필터용 활성탄소 소재 제조방법.Potassium hydride, Potassium hydroxide, Potassium dioxide, Potassium permanganate, Potassium carbonate, Potassium bicarbonate, Potassium chloride, Potassium iodide, Potassium bromide, Potassium fluoride, Potassium cyanide, Potassium cyanate, Potassium cyanate, Potassium thiocyanate, Nitrate Potassium nitrate, Potassium nitrite, Potassium sulfate, Potassium bisulfate, Potassium sulfite, Potassium hexafluorophosphate, Potassium phosphate tribasic, Dibasic potassium phosphate, Potassium dihydrogen phosphate, Potassium dichromate, Potassium chromate, Calcium bromide Potassium bromate, Potassium methoxide, Potassium ethoxide, Potassium acetate, Potassium thioacetate, Potassium formate, Potassium formate iodate, Potassium periodate, Potassium chlorate, Potassium perchlorate, Potassium borohydride, Alkali-based metal, characterized in that any one selected from the group consisting of This method of manufacturing activated carbon material for automotive interior filters. 청구항 1에 있어서,The method according to claim 1, 상기 알칼리 토금속 전구체는,The alkaline earth metal precursor is 질산바륨(Barium nitrate), 수산화바륨(Barium hydroxide), 염화바륨(Barium chloride), 황화바륨(Barium sulfide), 황산바륨(Barium sulfate), 탄산바륨(Barium carbonate), 아세트산바륨(Barium acetate), 산화바륨(Barium oxide), 과산화바륨(Barium peroxide), 요오드화바륨(Barium iodide), 플루오르화바륨(Barium fluoride), 브롬화바륨(Barium bromide), 과염소산바륨(Barium perchlorate), 크롬산바륨(barium chromate), 아철산바륨(Barium ferrite), 망간산바륨(Barium manganate), 인산바륨(barium phosphate), 바륨지르코네이트(Barium zirconate), 바륨아이소프로폭사이드(Barium isopropoxide), 바륨 싸이오설페이트(Barium thiosulfate), 바륨(Ⅱ) 아세틸아세토네이트(Barium(II) acetylacetonate hydrate), 요오드산바륨수화물(Barium iodate monohydrate), 바륨 메타포스페이트(Barium metaphosphate), 이염기성인산바륨(dibasic barium phosphate), 싸이오시안산바륨(Barium thiocyanate hydrate), 과요오드산바륨(Barium periodate), 및 2-에틸헥산산바륨(Barium 2-ethylhexanoate)으로 이루어진 군에서 선택된 어느 하나인 것을 특징으로 하는, 알칼리계 금속이 처리된 자동차 내부 필터용 활성탄소 소재 제조방법.Barium nitrate, Barium hydroxide, Barium chloride, Barium chloride, Barium sulfide, Barium sulfate, Barium carbonate, Barium carbonate, Barium acetate, Oxidation Barium oxide, Barium peroxide, Barium iodide, Barium iodide, Barium fluoride, Barium bromide, Barium perchlorate, Barium chromate, Barium chromate Barium ferrite, barium manganate, barium phosphate, barium zirconate, barium isopropoxide, barium isopropoxide, barium thiosulfate, Barium (II) acetylacetonate hydrate, barium iodate monohydrate, barium metaphosphate, dibasic barium phosphate, barium thiocyanate thiocyanate activated carbon for automobile interior filters treated with alkali metals, characterized in that it is any one selected from the group consisting of hydrate, barium periodate, and barium 2-ethylhexanoate. Material manufacturing method. 청구항 1에 있어서,The method according to claim 1, 상기 알칼리 금속 전구체 또는 알칼리 토금속 전구체는,The alkali metal precursor or alkaline earth metal precursor, 0.025 내지 3 M(mol/ℓ)의 농도인 것을 특징으로 하는, 알칼리계 금속이 처리된 자동차 내부 필터용 활성탄소 소재 제조방법.Method of producing an activated carbon material for automobile interior filter treated with alkali metal, characterized in that the concentration of 0.025 to 3 M (mol / L). 청구항 1에 있어서,The method according to claim 1, 상기 혼합용액을 준비하는 단계는,Preparing the mixed solution, 증류수 100 중량부에 대하여, 활성탄소 5 내지 20 중량부와 알칼리 금속 전구체 또는 알칼리 토금속 전구체 0.75 내지 30 중량부를 용해시켜 준비하는 것을 특징으로 하는, 알칼리계 금속이 처리된 자동차 내부 필터용 활성탄소 소재 제조방법.Manufacture of activated carbon material for automobile interior filters treated with alkali-based metals, characterized by dissolving 5 to 20 parts by weight of activated carbon and 0.75 to 30 parts by weight of an alkali metal precursor or an alkaline earth metal precursor with respect to 100 parts by weight of distilled water. Way. 청구항 1에 있어서,The method according to claim 1, 상기 제1교반용액을 준비하는 단계는,Preparing the first stirring solution, 혼합용액을 상온에서 100 내지 400 rpm으로 15 내지 45분 동안 교반시켜 준비하는 것을 특징으로 하는, 알칼리계 금속이 처리된 자동차 내부 필터용 활성탄소 소재 제조방법.Method for producing an activated carbon material for automobile interior filter treated with alkali metal, characterized in that the mixture is prepared by stirring for 15 to 45 minutes at 100 to 400 rpm at room temperature. 청구항 1에 있어서,The method according to claim 1, 상기 산촉매를 첨가하는 단계는,Adding the acid catalyst, 제1교반용액에 루이스 산촉매 또는 유기산촉매를 첨가하는 것을 특징으로 하는, 알칼리계 금속이 처리된 자동차 내부 필터용 활성탄소 소재 제조방법.A method of producing an activated carbon material for automobile interior filters in which an alkali metal is treated, comprising adding a Lewis acid catalyst or an organic acid catalyst to the first stirring solution. 청구항 10에 있어서,The method according to claim 10, 상기 루이스 산촉매는,The Lewis acid catalyst, 염산(HCl), 황산(H2SO4), 인산(H3PO4), 탄산(H2CO3), 염화티타늄(TiCl4), 염화철(Ⅲ)(FeCl3) 및 염화알루미늄(AlCl3)으로 이루어진 군에서 선택된 어느 하나인 것을 특징으로 하는, 알칼리계 금속이 처리된 자동차 내부 필터용 활성탄소 소재 제조방법.Hydrochloric acid (HCl), sulfuric acid (H 2 SO 4 ), phosphoric acid (H 3 PO 4 ), carbonic acid (H 2 CO 3 ), titanium chloride (TiCl 4 ), iron chloride (III) (FeCl 3 ) and aluminum chloride (AlCl 3) Method of manufacturing an activated carbon material for automobile interior filter treated with alkali metal, characterized in that any one selected from the group consisting of. 청구항 10에 있어서,The method according to claim 10, 상기 유기산촉매는,The organic acid catalyst, 설폰산(sulfonic acid), 피크르산(picric acid), 타르타르산(tartaric acid), 시트르산(citric acid), 에틸렌디아민테트라아세트산(ethylenediaminetetraacetic acid), 및 피로인산(pyrophosphoric acid)으로 이루어진 군에서 선택된 어느 하나인 것을 특징으로 하는, 알칼리계 금속이 처리된 자동차 내부 필터용 활성탄소 소재 제조방법.One selected from the group consisting of sulfonic acid, picric acid, tartaric acid, citric acid, ethylenediaminetetraacetic acid, and pyrophosphoric acid. Characterized in that the method for producing an activated carbon material for automobile interior filter treated with alkali metal. 청구항 4에 있어서,The method according to claim 4, 상기 제2교반용액을 준비하는 단계는,Preparing the second stirring solution, 산촉매가 첨가된 제1교반용액을 상온에서 100 내지 400 rpm으로 24 내지 72시간 동안 교반시켜 준비하는 것을 특징으로 하는, 알칼리계 금속이 처리된 자동차 내부 필터용 활성탄소 소재 제조방법.The first stirring solution to which the acid catalyst is added is prepared by stirring for 24 to 72 hours at 100 to 400 rpm at room temperature, alkali-based metal treated car activated carbon material manufacturing method. 청구항 4에 있어서,The method according to claim 4, 상기 알칼리 금속 산화물-활성탄소 또는 알칼리 토금속 산화물-활성탄소를 제조하는 단계는,Producing the alkali metal oxide-activated carbon or alkaline earth metal oxide-activated carbon, 제2교반용액을 필터링 후 80 내지 200℃에서 4 내지 8시간 동안 건조하여 제조하는 것을 특징으로 하는, 알칼리계 금속이 처리된 자동차 내부 필터용 활성탄소 소재 제조방법.After the second stirring solution is filtered and dried for 4 to 8 hours at 80 to 200 ℃, characterized in that the manufacturing method of the activated carbon material for automobile interior filter treated with alkali metal.
PCT/KR2017/013400 2016-12-16 2017-11-23 Alkali-based metal-treated activated carbon material for automotive filter, and preparation method therefor Ceased WO2018110852A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
KR10-2016-0172243 2016-12-16
KR1020160172243A KR101845175B1 (en) 2016-12-16 2016-12-16 Activated carbon materials for filter of vehicle interior treated with alkaline metal and preparing method thereof

Publications (1)

Publication Number Publication Date
WO2018110852A1 true WO2018110852A1 (en) 2018-06-21

Family

ID=61973361

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/KR2017/013400 Ceased WO2018110852A1 (en) 2016-12-16 2017-11-23 Alkali-based metal-treated activated carbon material for automotive filter, and preparation method therefor

Country Status (2)

Country Link
KR (1) KR101845175B1 (en)
WO (1) WO2018110852A1 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113786806A (en) * 2021-09-30 2021-12-14 南通大学 Ternary modified sewage peat defluorinating agent and preparation method thereof
CN113880065A (en) * 2021-11-18 2022-01-04 贵州红星发展股份有限公司 High-purity barium metaphosphate and preparation method thereof

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR102471622B1 (en) * 2020-09-01 2022-11-28 경기대학교 산학협력단 Hydrogen storage mixture and hydrogen generation method using the same
CN114112593B (en) * 2021-12-02 2023-08-25 中国科学院生态环境研究中心 Test method for indicating COD value in water
KR102812804B1 (en) * 2024-12-30 2025-05-27 주식회사 세이버 Oxygen-generating air purifier with improved carbon dioxide removal function
CN119841316B (en) * 2025-01-17 2025-07-29 徐州华睿炭材料科技有限公司 Rosin-based activated carbon and preparation method thereof

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100186680B1 (en) * 1995-06-07 1999-04-15 윌리엄 에프. 마쉬 Absorbent for removal of trace oxygen from inert gases
KR20050028624A (en) * 2003-09-19 2005-03-23 한국전력공사 Adsorbent for carbon dioxide fixation and method for preparing the same
JP2006312164A (en) * 2005-04-04 2006-11-16 Toyota Boshoku Corp GAS ADSORBENT, ITS MANUFACTURING METHOD, AND GAS ADSORPTION FILTER
US20070000385A1 (en) * 2005-07-01 2007-01-04 Stouffer Mark R Adsorbents for removing H2S, other odor causing compounds, and acid gases from gas streams and methods for producing and using these adsorbents
KR20120054958A (en) * 2010-11-22 2012-05-31 한국철도기술연구원 Method for preparing an adsorbent for carbon dioxide and a multi-stage absorption filter using the adsorbent

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100186680B1 (en) * 1995-06-07 1999-04-15 윌리엄 에프. 마쉬 Absorbent for removal of trace oxygen from inert gases
KR20050028624A (en) * 2003-09-19 2005-03-23 한국전력공사 Adsorbent for carbon dioxide fixation and method for preparing the same
JP2006312164A (en) * 2005-04-04 2006-11-16 Toyota Boshoku Corp GAS ADSORBENT, ITS MANUFACTURING METHOD, AND GAS ADSORPTION FILTER
US20070000385A1 (en) * 2005-07-01 2007-01-04 Stouffer Mark R Adsorbents for removing H2S, other odor causing compounds, and acid gases from gas streams and methods for producing and using these adsorbents
KR20120054958A (en) * 2010-11-22 2012-05-31 한국철도기술연구원 Method for preparing an adsorbent for carbon dioxide and a multi-stage absorption filter using the adsorbent

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113786806A (en) * 2021-09-30 2021-12-14 南通大学 Ternary modified sewage peat defluorinating agent and preparation method thereof
CN113880065A (en) * 2021-11-18 2022-01-04 贵州红星发展股份有限公司 High-purity barium metaphosphate and preparation method thereof

Also Published As

Publication number Publication date
KR101845175B1 (en) 2018-04-03

Similar Documents

Publication Publication Date Title
WO2018110852A1 (en) Alkali-based metal-treated activated carbon material for automotive filter, and preparation method therefor
WO2012148040A1 (en) Porous manganese oxide-based lithium adsorbent having a spinel structure, and method for preparing same
JP3531868B2 (en) 12CaO · 7Al2O3 compound that includes active oxygen species and method for producing the same
Valdés et al. Natural zeolite reactivity towards ozone: The role of compensating cations
JP2003128415A (en) 12CaO · 7Al2O3 compound and method for producing the same
Xie et al. Magnetic-field-assisted catalytic oxidation of arsine over Fe/HZSM-5 catalyst: Synergistic effect of Fe species and activated surface oxygen
WO2014098366A1 (en) Production method for a carbon-based composite metal oxide nanocatalyst carrier, and composite metal oxide nanocatalyst carrier therefrom
WO2024101633A1 (en) Magnesium-based cement composition and magnesium-based cement using same
WO2020246746A2 (en) Carbon dioxide adsorbent based on hydrophobic silane-coated amine-functionalized mof/alumina composite
Hernández-Fontes et al. Insight into CO selective chemisorption from syngas mixtures through Li 2 MnO 3; a new H 2 enrichment material
JP2009228106A (en) Method for collecting metal arsenic
WO2013015531A2 (en) Porous manganese oxide-based lithium absorbent having a spinel type structure, and method of fabricating same
WO2014069699A1 (en) Absorbent ball particle for recovering porous lithium by carbonization, and method for preparing same
WO2024214936A1 (en) Method for producing lithium sulfide
KR102601557B1 (en) Copper ferrite, manufacturing method of copper ferrite, method for removing hydrogen sulfide
EP4023591A1 (en) Metal oxide, oxygen adsorption and desorption device, oxygen concentrating device, and method for producing metal oxide
TWI809255B (en) Acid exhaust treatment agent, acid exhaust treatment method and acid exhaust treatment equipment
WO2018155753A1 (en) Renewable water treatment separation membrane and manufacturing method therefor
US20170305754A1 (en) Manufacturing method of mesoporous inorganic oxide and mesoporous inorganic oxide made by the same
WO2023243772A1 (en) Dual metal-organic framework for carbon dioxide adsorption and manufacturing method therefor
CN114669267A (en) Copper-based adsorbent and preparation method and application thereof
JP4818258B2 (en) Method for synthesizing ultramarine pigments
CN108380172B (en) Selective adsorption conversion material for benzene series in gas and preparation method thereof
JP3260826B2 (en) Purification method of nitrous oxide
KR20210153622A (en) Acid exhaust gas treatment agent, acid exhaust gas treatment method and acid exhaust gas treatment facility

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 17881575

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 17881575

Country of ref document: EP

Kind code of ref document: A1