The International Atomic Energy Agency recommends the deep geological disposal system as one of the disposal methods for high-level radioactive waste (HLW), such as spent nuclear fuel. The deep geological disposal system disposes of HLW in a deep and stable geological formation to isolate the HLW from the human biosphere and restrict the inflow of radionuclides into the ecosystem. It mainly consists of an engineered barrier and a natural barrier. Safety evaluation using a numerical model has been performed primarily to evaluate the buffer’s long-term stability. However, although the gas generation rate input for long-term stability evaluation is the critical factor that has the most significant influence on the long-term hydraulic-mechanical behavior of the buffer, in-depth research and experimental data are lacking. In this study, the gas generation rate on the interface between the disposal canister and the buffer material, a component of the engineered barrier, was mainly studied. Gas can be generated between the disposal canister and the buffer material due to various causes such as anaerobic corrosion of the disposal canister metal, organic matter decomposition, radiation decomposition, and steam generation due to high temperature. The generation of gas in such a disposal environment increases the pore gas pressure in the buffer and causes internal cracks. The occurred cracks increase the intrinsic permeability of the buffer, which leads to a decrease in the primary performance of the buffer. For this reason, it is essential to apply the appropriate gas generation rate according to the disposal condition and buffer material for accurate long-term stability analysis. Therefore, the theoretical models regarding the estimation of gas generation were summarized through a literature study. The amount of gas generated was estimated according to the disposal environment and material of the disposal canister. It is expected that estimated values might be used to estimate the long-term stability analysis of buffer performance according to the disposal condition.

In this study, for the treatment efficiency of the IGF process for the treatment of produced water (PW) discharged from the oil sands plant, the bench-scale oil sands plant PWT package was designed, manufactured and evaluated to verify the efficiency of the process. The microbubble generation efficiency and microbubble size change according to the circulation pump pressure were observed, and the correlation between influent concentration and temperature, residence time and oil-water separation performance was analyzed.

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.

수소를 연료로 사용하는 PEMFC는 고효율⋅출력밀도를 나타내며, 짧은 시동시간, 우수한 응답특성에 따라 현지설치형 발전기술로 사용되며, 이를 위한 고효율 연료처리장치가 필수적이다. SMR반응은 연료당 고회수율을 때문에 경제성이 우수하며, 전환율 확보를 위해 700°C, 20 bar 이상의 운전조건에서 수행되며, WGS, PSA의 후단공정을 통해 수소를 생산한다. 분리막 개질기를 이용한 SMR반응은 분리막이 수소를 제거함에 따라 반응효율 증진, 공정온도 저감, 후단공정 배제를 할 수 있어 공정구성 및 경제성이 우수하다. 본 연구에서는 팔라듐분리막 개질기를 사용하여 550°C, 5 bar에서 SMR반응을 통해 수소를 생산하였으며, 개질된 가스의 CO 농도를 최소화하여 고온 PEMFC용 연료처리장치를 개발하였다.

The potential application of palladium-ruthenium composite membranes to the separation of hydrogen from chlorosilane gases in silicon-based industries was investigated. Ru/Pd/Al2O3/PSS membranes were prepared by electroless plating. Hydrogen permeation tests and temperature programmed desorption analysis revealed that the addition of a Ru over layer on Pd changed the hydrogen adsorption characteristics, resulting in improved stability of the membrane at low temperatures. The Ru/Pd/Al2 O3/PSS composite membrane had a stable hydrogen permeation flux of 1.8 m3m-2h-1 over a period of 1,200 h at 180°C without suffering hydrogen embrittlement. After exposure to impurities such as HCl and SiHCl3 , the hydrogen permeation flux of the Ru/Pd/Al2 O3/PSS composite membrane was stable over a period of 9h with feed pressure of 2.0 bar at 225°C.

본 연구에서는 배가스 내 존재하는 오염물질인 NO의 처리효율을 증대시키기 위하여 NO 산화 공정을 연구하였으며, 강력한 산화력의 건식산화제를 제조하는 방법으로 H2O2 촉매분해가 도입되었다. H2O2 분해공정 상에서 적용 가능한 K-Mn/Fe2O3 불균일계 촉매가 제조되었으며, 이들이 가지는 물리화학 적 특성이 H2O2 분해반응에 미치는 영향이 조사되었다. 제조된 건식산화제는 NO가 포함된 모사 배가스를 처리하기 위한 NO 산화공정에 적용되었으며, 다양한 모사 배가스의 유량(5, 10, 20 L/min)에서 약 100% 가까운 NO 전환율을 확인 하였다.

This article examines two questions: (1) whether the Production Sharing Contract in oil and gas sectors between different countries should be considered as an international agreement or a private agreement; and (2) how to formulate uplift in the PSC which contains the value of equity for investors and the State. In the Production Sharing Contract, there is problem of setting the tax on oil and gas sector particularly uplift policy relating to the taxation of income in the state revenue sources. This issue is related to the return of controversy of operational costs recognized by the contractor (cost recovery claim). This tax controversy gave rise to uplift that is only levied on oil and gas State owned Enterprises contracting partners in the scheme of the Joint Operating Body, especially in the old fields with advanced technology (Enhanced Oil Recovery). The controversy is related to the declining production and increased production costs that are recognized by the contractor.

온실가스로 인한 지구 온난화 현상이 기후 변화를 초래하고 있기 때문에 메탄과 이산화탄소 감축에 대한 저감 기술이 절실하다. 바이오가스는 음식물쓰레기 처리장, 축산분뇨처리장, 등에서 발생하는데, 본 연구는 음식물쓰레기처리장에서 바이오가스를 분리정제 하기 위해 제습, 탈황, 탈실록산 처리된 바이오가스를 막분리 공정으로 운전하였고, 유량, 압력, 막 면적에 변화에 따른 공정개선으로 98% 이상의 고순도 메탄가스와 90% 이상의 회수율을 만족하는 결과를 얻었다.

The effect of increased carbon dioxide concentration in atmosphere was examined on the pheromone system of Helicoverpa armigera reared from egg stage to adult in three room. Two of three room (2×2×2 m) were treated with carbon dioxide gas as 600 ppm and 1,000 ppm, respectively. Mean of carbon dioxide concentration was 429.1 ppm in the control, 603.3 ppm for 600 ppm, and 1011.5 ppm for 1,000 ppm during experiment. Electroantenograph (EAG) test was conducted on 3-d-old male adults with air, hexane, and a series of their sex pheromone component, Z11-16Al, from 0.01 to 100 ng. The result was that male EAG responses of 600 and 1,000 ppm were 30.3% lower than that of control room. Production of Z11-16:Al was examined on about twenty 2-d-old virgin females. Carbon dioxide increases did not show a statistically significant difference. However, higher amount of sex pheromone was produced in females of 600 and 1,000 ppm. So, This experiment was replicated with different population reared again. The amount of the sex pheromone per female was 108.9 and 118.1 ng in control room, 139.8 and 141.8 ng in 600 ppm room, and 124.6 and 125.8 ng in 1,000 ppm room.

본 시험에서 건초(티머시, 알팔파 및 클라인)와 짚류(톨페스큐 및 볏짚)의 buffer 용해도와 단백질 분획이 실시되었으며, 조사료 자원의 buffer 추출이 in vitro 발효 성상, 분해율 및가스(CO2 및 CH4) 생성량에 미치는 효과를 조사하였다. 다른 조사료에 비해 총 단백질 중buffer 가용성 조단백질과 A fraction은 알팔파건초에서 각각 61% 및 41.77%로 가장 높았으며 볏짚에서 가장 낮았다(각각 42.8% 및19.78%). 총단백질 중 B1 fraction은 조사된 조사료간 비교적 큰 차이를 보이지 않았으나 B2fraction에서는 다른 조사료(6.34~8.85%)에 비하여 톨페스큐짚(10.05%) 및 클라인 건초(12.34)%에서 다소 높은 수준을 보였다. 총 단백질 중B3 fraction이 차지하는 비율은 톨페스큐짚에서38.49%로 가장 높았으나 다른 조사료 자원 간에는 큰 차이가 없었으며, C fraction의 경우 볏짚에서 가장 높은 비율(15.05%)을 보였다. 모든 사료에서 배양 개시 후 3시간(P<0.01) 및 6시간(P<0.05)에서 buffer 추출 전에 비해 추출후 배양액의 pH가 증가되었으며, 배양 6시간(P<0.05) 및 12시간(P<0.001)에서 다른 사료에비해 티모시 건초 및 알팔파 건초로부터의 pH가 낮았다. 배양액의 암모니아 농도는 모든 배양시간에서 가용성 물질의 추출 전 후에 다른조사료에 비해 알팔파 건초에서 가장 높았으나모든 사료의 추출효과는 배양 3시간(P<0.01)에서만 나타났다. 배양액의 총 VFA 농도는 배양24시간까지 알팔파 건초에서 가장 높았던 반면톨페스큐짚과 볏짚에서 가장 낮았다. 또한 모든 조사료에서 buffer 추출 전에 비하여 추출후에 총 VFA 농도가 감소되었다(P<0.01~P<0.001). Acetic acid (C2)의 조성 비율에서는 배양 6시간까지 추출 전에 더 높았으나(P<0.001)사료 간 차이는 없었다. Propionic acid (C3) 조성 비율 역시 배양 개시 후 3, 24 및 48시간(P<0.001)에 추출 전에 더 높았으며, 6 및 12시간의 배양액에서 대부분 건초(티모시, 알팔파 및 클라인)와 짚류(톨페스큐짚 및 볏짚) 간차이가 있는 것으로 조사되었다(P<0.05). 그러나 butyric acid (C4) 조성비율의 경우 대부분의배양시간에서 사료 간 차이는 없었다. 건물에서의 분해율 관련 parameter 중 a 값은 조사된전체 조사료에서 buffer 추출 전이 추출 후에비해서 높았으며(P<0.001), 다른 조사료에 비해톨페스큐짚과 볏짚에서 크게 낮았다(P<0.05).또한 b 값의 경우 역시 추출 전에 비해 추출후에서 현저히 낮았으나(P<0.001) 사료 간 차이는 없었다. 볏짚을 제외한 조사료에서 추출후에 비해 추출 전의 건물 유효분해율(EDDM)이 더 높았다(P<0.001). 조단백질에서의 a, b및 c 값은 추출 전에 비해 추출 후에서 현저히낮았으나(P<0.05) 사료 간 차이는 없었다. 조단백질 유효분해율(EDCP)에서는 다른 조사료 종류에 비해 톨페스큐짚과 볏짚에서 낮았다(P<0.05). 한편, NDF의 경우 a 값과 b 값(P<0.01)및 NDF 유효분해율(EDNDF, P<0.001)은 추출후에 비해 추출 전에 더 높았으나(P<0.01) 사료 간 차이는 보이지 않았다. 반추위미생물에의해 사료분해과정 중 생성되는 CO2 량도 24시간 배양까지는 추출 전에 더 많았으며(P<0.05~P<0.001), 톨페스큐짚과 볏짚에 비해 건초형태의 조사료로부터의 CO2 생성량이 더 많았다(P<0.05~P<0.01). 메탄가스(CH4) 생성량 역시 모든 배양시간에서 추출 전에 비해 추출 후에 크게 감소되었으며(P<0.01~P<0.001), 12~24시간을 제외하고는 짚류에 비해 건초에서 현저히 높은(P<0.05) 것으로 나타났다. 본 시험의 결과를 종합하면, 조사료 자원에 대한 buffer용해도와 단백질의 분획이 in vitro VFA 농도와 분해율 및 gas (CO2 및 CH4) 발생량 간 상호 밀접한 관계를 보이는 것으로 여겨진다. 이에 따라 조사료 이용 효율 개선을 위해 조사료자원에 대한 buffer 용해도와 단백질 분획을 반추동물 TMR 조제에 활용할 필요가 있는 것으로 여겨진다.

Fe based (FeCSiBPCrMoAl) amorphous powder, which is a composition of iron blast cast slag, were produced by a gas atomization process, and sequently mixed with ductile Cu powder by a mechanical ball milling process. The Fe-based amorphous powders and the Fe-Cu composite powders were compacted by a spark plasma sintering (SPS) process. Densification of the Fe amorphous-Cu composited powders by spark plasma sintering of was occurred through a plastic deformation of the each amorphous powder and Cu phase. The SPS samples milled by AGO-2 under 500 rpm had the best homogeneity of Cu phase and showed the smallest Cu pool size. Micro-Vickers hardness of the as-SPSed specimens was changed with the milling processes.

Fe based (FeCSiBPCrMoAl) amorphous powder, which is a composition of iron blast cast slag, were produced by a gas atomization process, and sequently mixed with ductile Cu powder by a mechanical ball milling process. The experiment results show that the as-prepared Fe amorphous powders less than 90 m in size has a fully amorphous phase and its weight fraction was about 73.7%. The as-atomized amorphous Fe powders had a complete spherical shape with very clean surface. Differential scanning calorimetric results of the as-atomized Fe powders less than 90 m showed that the glass transition, T, onset crystallization, T, and super-cooled liquid range T=T-T were 512, 548 and 36, respectively. Fe amorphous powders were mixed and deformed well with 10 wt.% Cu by using AGO-2 high energy ball mill under 500 rpm.

In this study, a new laval type nozzle was designed and manufactured. Using this nozzle tin powder was produced in close coupled system by using nitrogen gas at different operating conditions. The results showed that the increasing the gas pressure up to 1.47 MPa reduced the mean powder size down to 11.39 microns with a gas/melt mass flow rate ratio of 2.0. Powders are spherical in shape and have smooth surfaces.

The spherical and high quality Titanium fine powder "Tilop" has been produced with gas atomization furnace, Sumitomo Titanium Corporation originally designed. Recently, a new process which can produce Ti-alloy(Ti-6Al-4V) powders by utilizing our gas atomization process, of which raw material is sponge titanium pre-mixed with alloy chips or granules has been also developed. The particle size of gas atomized Ti-alloy powder and the mechanical properties of sintered Ti-alloy compacts prepared by metal injection molding were discussed in this study.