The objective of this study was to evaluate effects of feeding methods on in vitro ruminal fermentation, total gas and methane production in Hanwoo steers. Six Hanwoo steers fitted with rumen cannula (430 ± 21 kg of body weight) were randomly assigned to one of three feeding systems: 1) feeding forage 1 hour after concentrate, 2) feeding concentrate 1 hour after forage, 3) feeding mixed ration. Rumen fluid sampled from each animals was incubated 24 hours with maize or timothy substrates in in vitro. Ruminal pH was increased in feeding method 2 or maize substrate than that of other methods or timothy substrate (P < 0.001). The production of total volatile fatty acid, acetate, propionate, butyrate, and valerate were increased when steers fed diets using feeding method 1 or rumen fluid was incubated with maize substrate (P < 0.001). Increased production of total gas and methane was observed in feeding method 1 and maize substrate compared to those of other methods or timothy substrate (P < 0.001). Due to the inconsistent results between ruminal fermentation and gas production in this study, further research is required to estimate effects of feeding method on enteric fermentation and gas production in in vivo.

막 분리 운전방식에 따른 음폐수 소화가스의 도시가스용 바이오메탄 생산연구를 상업용 시설을 대상으로 수행하였다. 연구결과 바이오메탄의 순도는 4SBR과 3SDR 모두 98.9%를 달성할 수 있었다. 소화가스 내 메탄 회수율은 4SBR 88.1%, 3SDR 79.4%이었고, 처리 소화가스량 대비 바이오메탄 생산율도 4SBR이 53.5%로 3SDR의 49.4%보다 높았다. 그러나 막 분리시설에 공급되는 가스 중 반송 가스의 비율은 4SBR이 56.5%로 3SDR 보다 두 배가량 컸으며, 이로 인해 최대 처리량에 있어서는 3SDR이 양호한 결과를 보였다. 따라서 소화가스 200 Nm3/day 이하는 4SBR, 240 Nm3/day 이상에서는 3SDR이 경제성이 좋은 것으로 판단되었다. 공정 운전변수들의 평균값 대비 운전 값들의 상대편차는 전반적으로 4SBR이 컸으며, 또한 주 운전조절 수단인 바이오메탄 인출압력 대비 주요 지표들의 상관관계에 있어서는 3SDR가 보다 직접적인 관계를 보여주었다.

We investigate the reduction of SnO2 and the generation of syngas(H2, CO) using methane(CH4) and hydrogen(H2) or a mixed gas of methane and hydrogen as a reducing gas. When methane is used as a reducing gas, carbon is formed by the decomposition of methane on the reduced Sn surface, and the amount of generated carbon increases as the amount and time of the supply of methane increases. However, when hydrogen is used as a reducing gas, carbon is not generated. High purity Sn of 99.8 % and a high recovery rate of Sn of 93 % are obtained under all conditions. The effects of reducing gas species and the gas mixing ratio on the purity and recovery of Sn are not significantly different, but hydrogen is somewhat more effective in increasing the purity and recovery rate of Sn than methane. When 1 mole of methane and 1 mole of hydrogen are mixed, a product gas with an H2/CO value of 2, which is known to be most useful as syngas, is obtained.

메탄은 중요한 온실가스 중의 하나이며, 바이오가스의 주 성분이다. 이러한 바이오가스로부터 메탄의 몰분율 농도 를 0.95 이상으로 회수하기 위하여 폴리설폰 중공사 분리막 모듈을 3단으로 연결하여 회수율을 99% 이상으로 얻을 수 있도 록 공정을 설계하고 전산 모사하였다. 수치 해석 시 이산화탄소 투과도와 선택도를 이산화탄소의 부분증기압 함수로 나타내어 전산 모사를 수행하여 정확도를 높이고자 하였다. 공급 기체 압력, 공급 기체 내 메탄 농도, 그리고 분리막 모듈 내 분리막 면적이 클수록, 생성물 내 메탄 몰분율 농도가 증가함을 알 수 있었다. 그러나 생성물 내 메탄 몰분율 농도를 0.95 이상, 동시 에 메탄 회수율을 99% 이상 얻기 위해서는 분리막 모듈의 분리막 면적을 적절히 선택하여야 하며, 선정된 분리막 모듈을 다단 공정으로 구성함에도 불구하고 공급 기체 압력, 공급 기체 유속, 그리고 공급 기체 메탄 농도를 제한적 범위 내에서 조절 하여야 함을 알 수 있었다.

The role played by reservoirs in the biogeochemical cycles of elements is a subject of ongoing debate. Recent research has revealed that reservoirs emit significant levels of greenhouse gases. To assess the importance of reservoirs in monsoon climate areas as a source of methane gas into the atmosphere, we investigated variations in organic carbon (OC) input into the reservoir, oxic state changes, and finally the amount of methane emitted (focusing on the ebullition pathway) in Lake Soyang, which is the largest reservoir in South Korea. Total organic carbon (TOC) concentrations were higher during summer after two years of heavy rainfall. The sedimentation rates of particulate organic carbon (POC) and particulate organic nitrogen (PON) were higher in the epilimnion and hypolimnion than the metalimnioin, indicating that autochthonous and allochthonous carbon made separate contributions to the TOC. During stratification, oxygen depletion occurred in the hypolimnion due to the decomposition of organic matter. Under these conditions, H2S and CH4 can be released from sediment. The methane emissions from the reservoir were much higher than from other natural lakes. However, the temporal and spatial variations of methane ebullition were huge, and were clearly dependent on many factors. Therefore, more research via a well-organized field campaign is needed to investigate methane emissions.

Global warming is considered one of the great challenges of the twenty-first century. In order to reduce the ever-increasing amount of methane (CH4) released into the atmosphere, and thus its impact on global climate change, CH4 storage technologies are attracting significant research interest. CH4 storage processes are attracting technological interest, and methane is being applied as an alternative fuel for vehicles. CH4 storage involves many technologies, among which, adsorption processes such as processes using porous adsorbents are regarded as an important green and economic technology. It is very important to develop highly efficient adsorbents to realize techno-economic systems for CH4 adsorption and storage. In this review, we summarize the nanomaterials being used for CH4 adsorption, which are divided into non-carbonaceous (e.g., zeolites, metal-organic frameworks, and porous polymers) and carbonaceous materials (e.g., activated carbons, ordered porous carbons, and activated carbon fibers), with a focus on recent research.

We developed a high-performance methane gas sensor based on a SnO2 hollow hemisphere array structure of nano-thickness. The sensor structures were fabricated by sputter deposition of Sn metal over an array of polystyrene spheres distributed on a planar substrate, followed by an oxidation process to oxidize the Sn to SnO2 while removing the polystyrene template cores. The surface morphology and structural properties were examined by scanning electron microscopy. An optimization of the structure for methane sensing was also carried out. The effects of oxidation temperature, film thickness, gold doping, and morphology were examined. An impressive response of ~220% was observed for a 200 ppm concentration of CH4 gas at an operating temperature of 400˚C for a sample fabricated by 30 sec sputtering of Sn, and oxidation at 800˚C for 2 hr in air. This high response was enabled by the open structure of the hemisphere array thin films.

The characteristics of odor generation with the production of resources by utilization of methane gases in landfill sites was investigated, and the effect of making resources with landfill gases on the reduction of odor was analyzed in recent years. The greenhouse gas was estimated to reduce from the range of 1,334,940~209,875 tCO₂e with the period of 2008~2017, and the effective odor was diminished with considerable amount. The more effective methods of odor removal with the utilization of waste gases were estimated by studies of similar cases to acquire standard methods of making energy resources by waste gases.

In this study the production of methane gas and the removal efficiency of nutrients in the anaerobic co-digestion facilitieswith food waste/food waste leachate (FWL), animal manure and food waste leachate (A-MIX), and sewage sludge andfood waste leachate (S-MIX) were investigated. The average amount of the theoretical methane production was 578.4CH4·L/kg·VSin from the anaerobic digestion facilities with FWL, 606.0CH4·L/kg·VSin from those with A-MIX and 570.0CH4·L/kg·VSin from those with S-MIX, respectively. The amount of the practical methane production was 350.7CH4·L/kg·VSin from the anaerobic digestion facilities with FWL, 379.5CH4·L/kg·VSin from those with A-MIX and 348.8CH4·L/kg·VSin from those with S-MIX, respectively. The nutrient compositions of FWL were 3.2g/100g for carbohydrates, 1.8g/100g for proteins and 1.9g/100g for lipids. The nutrient compositions of A-MIX were 0.4g/100g for carbohydrates,2.55g/100g for proteins 0.4g/100g and 0.7g/100g for lipids, respectively. The nutrient compositions of S-MIX were0.4g/100g for carbohydrates, 2.4g/100g for proteins 1.6g/100g and 0.4g/100g for lipids, respectively. The removalratio of carbohydrate was very high over 75% in all facilities and that of lipid was very low below 25%.

Needs for more accurate greenhouse gas (GHG) emission estimation are increasing to prepare for post-Kyoto protocol and emission trading starting from 2015 in Korea. Although GHG emission from landfill is relatively low, uncertainty of methane emissions from landfill is very high compared to the other sectors. Moreover, accurate estimation is needed to design landfill gas collection system and energy generation plant. In this paper, we investigated development methodologies of parameters comprising methane generation potential (L0) which is one of key parameters in methane emission estimation models. DOC included four steps including analysis of waste component, water content, organic carbon content, fossil carbon content. Instead of analysis of organic carbon content and fossil carbon content, biochemical analysis, measuring content of cellulose, hemicellulose, and lignin, is used in MELMod, landfill gas generation model in UK. Methodologies to develop DOCF has several methods including batch test, lysimeter test and test cell. They had difference in scale and similarity to landfill, but it is hard to consider the best method at the present stage. Preceding research on MCF is little. Lysimeter test and test cell can be the candidate to develop MCF, because of flexibility on test condition to characterize the structure of landfill sites. F is defined as fraction of methane in landfill gas. But by carbon flow and mass balance, F should represent fraction of methane in biogas generated by anaerobic decomposition. In this definition, F can be derived by same methods to that of DOCF.

This study was designed to synthesize mesoporous carbon, porous carbonic material and to characterize its surface in an attempt to adsorption methane gas(CH4). Synthesis of mesoporous carbon was carried out under two steps ; 1. forming a RF-silica complex with a mold using CTMABr, a surfactant, and TEOS, raw material of silica, and 2. eliminating silica through carbonization and HF treatment. The mesoporous carbon was synthesized under various conditions of synthesis time and calcination. Eight different types of mesoporous carbon, which were designated as MC1, MC2, MC3, MC4, MCT1, MCT2, MCT3, and MCT4, were prepared depending upon preparation conditions. The analysis of mesoporous carbon characteristics showed that the calcination of silica stabilized the mixed structure of silica and carbonic complex, and made the particle uniform. The results also showed that hydrothermal synthesis time did not have a strong influence on the size of pore. The bigger specific surface area was obtained as the hydrothermal synthesis time was extended. However, the specific surface area was getting smaller again after a certain period of time. In adsorption experiments, CH4 was used as adsorbate. For the case of CH4, MCT3 showed the highest adsorption efficiency.

Most of methane gas result from waste matter in landfill, therefore the persons concerned take an increasing interest in management of gases in landfill. Infrared Gas Analyzer was used to measure components of gases, CH4, CO2, O2, through gas exhausted pipe. To measure amount of the gas flow meter(Portable Hot-Line Current Meter) was used and it was set at right angles with direction of the flow. In this research the total amount of methane gas produced in Beck-Suk Landfill was calculated through FOD method suggested by IPCC. This research found that in Chon-An Beck-Suk Landfill anaerobic resolution was made actively and the amount of methane gas produced there was 54.14%, which is higher than common figure, 50%, in other researches. The components of reclaimed waste matter, especially, organic waste matter can have a great effect of the amount of the greenhouse gases produced in landfill. We can expect that the amount of greenhouse gas will decrease from 2005, when it will be prohibited from carrying kitchen refuse and sludge into landfill.