RISS 학술연구정보서비스

검색

인기 검색어

    다국어 입력

    http://chineseinput.net/에서 pinyin(병음)방식으로 중국어를 변환할 수 있습니다.

    변환된 중국어를 복사하여 사용하시면 됩니다.

    예시)
    • 中文 을 입력하시려면 zhongwen을 입력하시고 space를누르시면됩니다.
    • 北京 을 입력하시려면 beijing을 입력하시고 space를 누르시면 됩니다.
    닫기

    CO₂超臨界 流體에서 轉化法을 利用한 폴리카보네이트와 폴리프로필렌 非對稱 多孔性 膜의 製造 및 應用 = Preparation and application of asymmetric and porous membranes with polycarbonate and polypropylene by an inversion method in supercritical CO₂fluid

    한글로보기

    https://www.riss.kr/link?id=T9568953

    • 0

      상세조회
    • 0

      다운로드
    서지정보 열기
    • 내보내기
    • 내책장담기
    • 공유하기
    • 오류접수

    부가정보

    다국어 초록 (Multilingual Abstract) kakao i 다국어 번역

    In this study, polycarbonate and polypropylene porous membranes were prepared with supercritical CO_(2). The effects of reaction time, temperature, and pressure of supercritical CO_(2) on the preparation of porous membranes were examined. The electrolyte composite membrane for fuel cell was obtained with the prepared porous membrane.
    The results were as follows.
    1. The prepared polycarbonate and polypropylene porous membranes have sponge structures. The cross sections of the membranes showed asymmetric structures and the surfaces of the membrens showed uniform pore distributions.
    2. The optimum conditions of preparation of polycarbonate porous membrane, considering porosity and tensile strength, were 19 wt% of polycarbonate concentration and 8.1 wt% of polyethylene glycol concentration. The membrane showed porosity of 72∼77 % and tensile strength of 1.8 kgf/㎟.
    3. Considering porosity and tensile strength, the optimum condition of preparation of polypropylene porous membrane was 10 wt% of polypropylene concentration. It showed porosity of 73∼80 % and tensile strength of 0.2 kgf/㎟.
    4. The supercritical CO_(2) was used to extract the polyethylene glycol for the preparation of polycarbonate porous membrane and the optimum extraction conditions were 35 ℃, 150 bar, and 20 min.
    5. The supercritical CO_(2)was employed to extract the camphene for the preparation of polypropylene porous membrane and the optimum conditions of extraction were 45 ℃, 150 bar, and 10 min.
    6. In the preparation of polycarbonate and polypropylene porous membranes, the supercritical CO_(2) in extraction process worked more efficiently by 19 % and 10 % than other liquid solutions such as ultra-pure water and ethanol.
    7. The optimum process for the impregnation of Nafion^(ⓡ) solution into polycarbonate porous membrane was vacuum inhalation method. The prepared polycarbonate composite membrane showed Nafion^(ⓡ) density of 0.83 g/㎤ in the polycarbonate porous membrane and water uptake of 47 %. The polycarbonate composite membrane had about ion conductivity of 0.0024 S/cm, which was 57 % of ion conductivity of Nafion 115 membrane.
    8. The dip coating process was excellent for the impregnation of Nafion^(ⓡ) solution into polypropylene porous membrane. The obtained polypropylene composite membrane showed Nafion^(ⓡ) density of 1.37 g/㎤ in the polypropylene porous membrane and water uptake of 24 %. The polypropylene composite membrane had about ion conductivity of 0.0029 S/cm, which was 57 % of ion conductivity of Nafion 115 membrane.
    번역하기

    In this study, polycarbonate and polypropylene porous membranes were prepared with supercritical CO_(2). The effects of reaction time, temperature, and pressure of supercritical CO_(2) on the preparation of porous membranes were examined. The electrol...

    In this study, polycarbonate and polypropylene porous membranes were prepared with supercritical CO_(2). The effects of reaction time, temperature, and pressure of supercritical CO_(2) on the preparation of porous membranes were examined. The electrolyte composite membrane for fuel cell was obtained with the prepared porous membrane.
    The results were as follows.
    1. The prepared polycarbonate and polypropylene porous membranes have sponge structures. The cross sections of the membranes showed asymmetric structures and the surfaces of the membrens showed uniform pore distributions.
    2. The optimum conditions of preparation of polycarbonate porous membrane, considering porosity and tensile strength, were 19 wt% of polycarbonate concentration and 8.1 wt% of polyethylene glycol concentration. The membrane showed porosity of 72∼77 % and tensile strength of 1.8 kgf/㎟.
    3. Considering porosity and tensile strength, the optimum condition of preparation of polypropylene porous membrane was 10 wt% of polypropylene concentration. It showed porosity of 73∼80 % and tensile strength of 0.2 kgf/㎟.
    4. The supercritical CO_(2) was used to extract the polyethylene glycol for the preparation of polycarbonate porous membrane and the optimum extraction conditions were 35 ℃, 150 bar, and 20 min.
    5. The supercritical CO_(2)was employed to extract the camphene for the preparation of polypropylene porous membrane and the optimum conditions of extraction were 45 ℃, 150 bar, and 10 min.
    6. In the preparation of polycarbonate and polypropylene porous membranes, the supercritical CO_(2) in extraction process worked more efficiently by 19 % and 10 % than other liquid solutions such as ultra-pure water and ethanol.
    7. The optimum process for the impregnation of Nafion^(ⓡ) solution into polycarbonate porous membrane was vacuum inhalation method. The prepared polycarbonate composite membrane showed Nafion^(ⓡ) density of 0.83 g/㎤ in the polycarbonate porous membrane and water uptake of 47 %. The polycarbonate composite membrane had about ion conductivity of 0.0024 S/cm, which was 57 % of ion conductivity of Nafion 115 membrane.
    8. The dip coating process was excellent for the impregnation of Nafion^(ⓡ) solution into polypropylene porous membrane. The obtained polypropylene composite membrane showed Nafion^(ⓡ) density of 1.37 g/㎤ in the polypropylene porous membrane and water uptake of 24 %. The polypropylene composite membrane had about ion conductivity of 0.0029 S/cm, which was 57 % of ion conductivity of Nafion 115 membrane.

    더보기

    목차 (Table of Contents)

    • 목차 = i
    • List of tables = iii
    • List of figures = v
    • 1. 서론 = 1
    • 2. 이론 = 8
    • 목차 = i
    • List of tables = iii
    • List of figures = v
    • 1. 서론 = 1
    • 2. 이론 = 8
    • 2-1. 상전화법에 의한 막제조 = 8
    • 2-1-1. 건습식법 및 습식법 = 8
    • 2-1-2. 열식법 = 10
    • 2-2. 다공성 고분자 분리막에서의 이온전도 = 12
    • 2-3. 초임계 유체의 용해도 = 15
    • 3. 실험 = 19
    • 3-1. 시료 = 19
    • 3-2. 실험장치 = 19
    • 3-3. 실험 방법 = 25
    • 4. 결과 및 고찰 = 33
    • 4-1. 다공성 막의 제조 및 형상 = 33
    • 4-2. 공극률 = 39
    • 4-3. 인장강도 = 44
    • 4-4. 초임계 유체의 추출효율 = 47
    • 4-4-1. 반응시간의 영향 = 47
    • 4-4-2. 온도의 영향 = 54
    • 4-4-3. 압력의 영향 = 60
    • 4-5. 이온 전도도 = 63
    • 4-5-1. 전해질 복합막의 제조 = 63
    • 4-5-2. 전해질 복합막의 이온 전도도 = 65
    • 5. 결론 = 67
    • 참고문헌 = 69
    • Appendices = 77
    • Abstract = 97
    더보기

    분석정보

    View

    상세정보조회

    0

    Usage

    원문다운로드

    0

    대출신청

    0

    복사신청

    0

    EDDS신청

    0

    동일 주제 내 활용도 TOP

    더보기

    주제

    연도별 연구동향

    연도별 활용동향

    연관논문

    연구자 네트워크맵

    공동연구자 (7)

    유사연구자 (20) 활용도상위20명

    이 자료와 함께 이용한 RISS 자료

    나만을 위한 추천자료

    해외이동버튼