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논문 기본 정보

자료유형
학위논문
저자정보

한단비 (수원대학교, 수원대학교 대학원)

지도교수
백영순
발행연도
2018
저작권
수원대학교 논문은 저작권에 의해 보호받습니다.

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이 논문의 연구 히스토리 (4)

초록· 키워드

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As population activity increases, the amount of biogas generated increases as the amount of organic waste generated increases. In recent years, organic wastes have been treated by landfilling, feed conversion, composting, incineration, etc. Recently, efforts have been made to utilize energy from organic wastes by generating large amounts of methane, and methane generated from organic wastes can be supplied stably, the organic matter is abundant, and the difference in quality is not great. In particular, CH₄ and CO₂ generated from sewage sludge and livestock manure treatment are 60 ~ 70% and 30 ~ 35%, and CH₄ and CO₂ generated from food wastes are 60 ~ 80% and 20 ~ 40% And In case of landfill gas, CH₄ and CO₂ have a composition of 40 ~ 60% and 40 ~ 60%. The biogas are mainly used by directly burning, using heat, applying to electric power or automobile, or connecting natural gas (NG) with piping to supply city gas. Therefore, not only is biogas used in localized utilization areas, but also in the case of electric power, there are problems such as installation of facilities necessary for transportation to the consumer. Therefore, in order to use the regenerated energy from the biogas more widely, it is necessary to convert the biogas to methanol, LNG or DME, which is a liquid fuel which is convenient to store and transport, or a synthesis gas manufacturing technology is desperately needed.
In this study, experiments were conducted to produce hydrogen and carbon monoxide through various biogas reactions on Ni/Ce-ZrO₂/Al₂O3 catalysts. Synthetic gas production experiments were carried out on a wide range of concentrations of methane and carbon dioxide, the major constituents of biogas from various organic wastes. In particular, the effect of (O₂ + CO₂)/CH₄ (= R'') on the yields of hydrogen and carbon monoxide was experimentally investigated. The effect of methane, carbon dioxide and oxygen on the reaction was investigated. In addition, the experiment was carried out continuously for 200 hours under the condition of the best conversion of carbon dioxide and methane. Also simulation for syngas synthesis from the CO₂ reforming of CH₄ were computed by employing total Gibbs free energy minimization method using PRO/II simulator, and compared with the experiment value.

목차

Ⅰ. 서 론 1
1. 연구 목적 1
2. 연구범위 및 방법 3
1) 연구범위 3
2) 연구방법 3
3. 연구동향 4
1) 바이오가스 생성 4
2) 바이오가스 활용 5
(가) 혐기성소화조 가스(ADG, Anaerobic Digester Gas) 7
(나) 매립지 가스(LFG, Landfill Gas) 9
3) 합성가스 제조반응 11
(가) 부분산화 개질반응(POX, Partial Oxidation) 11
(나) 수증기 개질반응(SMR, Steam Methane Reforming) 12
(다) 이산화탄소 개질반응(CDR, Carbon Dioxide Reforming) 13
(라) 삼중 개질반응(TRM, Tri-Reforming of Methane) 16
(마) 자열 개질반응(ATR) 17
(바) SCR 반응 18
Ⅱ. 이론적 고찰 21
1. 개질반응 이론 21
1) Dry reforming(DR) 반응 21
2) Steam reforming(SR) 반응 22
3) Gibbs Free Energy 식 23
2. 반응 시뮬레이션 28
1) PRO/II simulator 28
2) 열역학 상태방정식 28
3) 반응 Simulation 방법 29
Ⅲ. 실험방법 31
1. 실험장치 및 방법 31
1) 실험장치 31
2) 촉매제조 33
(가) XRD 측정 35
(나) BET 측정 35
(다) SEM 측정 36
3) 실험 방법 37
Ⅳ. 결과 및 토론 39
1. Reforming 방법에 따른 CH4과 CO2 전환율에 미치는 영향 39
1) Dry reforming 반응 39
2) Steam reforming 반응 42
2. Reforming 방법에 따른 H2와 CO 수율의 영향 44
1) Dry reforming 반응 44
2) Steam reforming 46
3. Reforming 방법에 따른 H2/CO Ratio 영향 49
4. CH4/CO2의 전환율과 H2/CO수율에 미치는 O2/CO2 영향 51
5. R’(=(O2+CO2)/CH4)값에 따른 영향 53
1) R’값에 따른 CH4와 CO2 전환율의 영향 53
2) 시뮬레이션과의 비교 59
Ⅴ. 결 론 61
ABSTRACT 63
참고 문헌 66

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