• Resources Recycling
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• v.15 no.1 s.69
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• pp.12-19
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• 2006

Rice straw is one or the main renewable energy sources in Korea. Bio-oil is produced from rice straw with a lab-scale equipment mainly with a fluidized bed and a char removal system. It was investigated how the reaction temperature affected the production of bio-oil and the efficiency of a char removal system. To elucidate how the temperature depended on the production of bio-oil, experiments were conducted at $466^{\circ}C,\;504^{\circ}C\;and\;579^{\circ}C$, respectively. The mass balance was established in each experiment, and the produced gas and oil were analyzed with the aid of GCs and a GC-MS system. The char removal system is composed of a cyclone and a hot filter. Tn the experiments, we observed that the production of bio-oil was decreased with temperature, and the bio-oil contained very useful chemicals.

• Proceedings of the Korean Institute of Resources Recycling Conference
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• 2005.10a
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• pp.47-58
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• 2005

Rice straw is one of the main renewable energy sources in Korea, and bio-oil is produced from rice straw with a lab. scale plant equipped mainly with a fluidized bed and a char removal system. We investigated how the reaction temperature affected the production of bio-oil and the efficiency of a char removal system. To elucidate how the temperature depended on the production of bio-oil, experiment were conducted between $450^{\circ}C\;and\;600^{\circ}C$ with a feed rate of about 300g/h. The mass balance was established in each experiment, and the produced gas and oil were analyzed with the aid of GCs and a GC-MS system. The char removal system is composed of a cyclone and a hot filter. In the experiments, we observed that the optimum reaction temperature range for the production of bio-oil is between $450^{\circ}C\;and\;500^{\circ}C$.

• 한국신재생에너지학회:학술대회논문집
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• 2005.06a
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• pp.487-490
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• 2005

재생 가능한 자원인 동식물성 기름으로부터 만들어지는 수송용 연료 바이오디젤은 낮은 대기오염물질 배출과 $CO_2$ Neutral 특성으로 환경친화적인 연료로 인정올 받으며 전세계적으로 그 생산량이 급격히 증가하고 있다 한국에서는 년간 20만톤의 폐식용유가 배출되며 이중 약 10만톤이 회수 가능한 것으로 추산된다. 폐식용유의 무단 폐기로 인한 수질오염과 폐기물의 자원 재활용 및 에너지 생산 관점에서 폐식용유를 바이오디젤 원료로 사용하는 연구가 많이 진행되었다. 높은 함량의 유리지방산을 함유한 폐식용유를 효율적으로 전이에스테르화(methanolysis) 하기 위해서는 먼저 산 촉매를 이용한 유리지방산의 전환 제거가 필요하다 본 연구에서는 다양한 종류의 강산성 이온교환 수지를 폐식용유의 전처리(pre-esterification)용 고체 산 촉매로 회분식 반응기에서 테스트하였으며 그 결과 Amberlyst-15가 유리지방산의 에스테르화 반응에 가장 적합한 것으로 나타났다. 회분식 반응기에서 도출된 최적 전처리 반응조건을 적용한 200시간 이상의 연속 전처리 운전결과 폐식용유에 함유된 $5\%$의 유리지방산이 $90\%$이상 전환제거 되었다 전처리 반응 후의 폐식용유를 균질계 염기촉매(KOH) 존재하에 메탄올과 전이에스테르화 반응을 시킨 결과 바이오디젤로 불리는 지방산메틸에스테르(Fatty Acid Methyl Ester, FAME)의 생산 수율은 $85\%$로 얻어졌으며 국내 바이오디젤 표준 규격에 따른 연료특성 분석 결과 FAME의 농도 규격을 제외한 모든 항목이 국내 규격을 만족하였다 폐식용유 바이오디젤의 FAME 농도가 $94.3\%$로 국내 규격$96.5\%$에 미달하는 문제는 식물성 원료유로 제조한 고순도 바이오디젤과 혼합 사용하거나 감압 증류 공정을 통해 고농도의 폐식용유 바이오디젤을 제조하여 해결 가능하다. 대전시 신성동 소재의 음식점에서 수거한 폐식용유를 원료로 하여 생산한 바이오디젤의 차량 배출가스 실증 테스트 결과 경유 차량의 주 오염물질인 PM과 Soot 및 기타 오염물질의 배출량은 감소하였으나 NOx의 배출량은 약간 증가하는 것으로 나타났다

• Journal of the Korea Academia-Industrial cooperation Society
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• v.10 no.12
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• pp.3971-3976
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• 2009

In this study, we secured wasted oyster shells as raw materials in order to applicate it to corrosion preventive ceramic coating reagent in the drinking water pipeline. Then, we investigated physicochemical properties in terms of basic calcination processing. Oyster shell was composed with 92.08% of $CaCO_3$ and the shapes of the pulverized particles were mostly oval. The calcined oyster shell showed increasing tendency of weight loss and of calcium content with the lapse of time and increase of temperature. The result indicates that the higher calcination processing temperature and the uniformly smaller particle size give more efficiency during calcination process. Therefore it is anticipated to be a good ceramic material to protect a surface of cleaning bed and inside of a tap water pipes from corrosion.

• Applied Chemistry for Engineering
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• v.18 no.5
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• pp.401-406
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• 2007

The status of biodiesel (BD) production and consumption, specifications and market status in Korea are discussed in this review. The main feedstock to produce BD is soybean oil and waste cooking oil in domestic, and some companies have tried to diversify BD feedstocks. Ministry of Agriculture and Forestry (MAF) has begun a pilot project to produce BD feedstock from rapeseed for 3 years since 2007. In July 2006, Ministry of Commerce, Industry & Energy (MOCIE) and the domestic oil industry reached an agreement under which BD0.5 is supplied in market, and 158400 MT of BD would be supplied between 2007 and 2008. MOCIE reported that it will increase BD 0.5% every year to reach BD3 by 2012. It is expected that BD supply would continuously increase domestically in the future.

• Journal of the Korean Ceramic Society
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• v.34 no.2
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• pp.131-138
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• 1997

Silicon carbide films were chemically vapor deposited onto graphite substrates using MTS(Ch3SiCl3) as a source and Ar or H2 as a diluent gas. The experiments were performed at a fixed condition such as a de-position temperature of 130$0^{\circ}C$, a total pressure of 10 torr, and a flow rate of 100 sccm for each MTS and carrier gas. The purpose of this study is to consider the variation of the growth behavior with the addition of each diluent gas. It is shown that the deposition rate leads to maximum value at 200 sccm addition ir-respective of diluent gases and the deposition rate of Ar addition is faster than that of H2 one. It seems that these characteristics of deposition rate are due to varying interrelationship between boundary layer thick-ness and the concentration of a source with each diluent gas addition, when overall deposition rate is con-trolled by mass transport kinetics. The preferred orientation of (220) plane was maintained for the whole range of Ar addition. However, above 200 sccm addition, especially that of (111) plane was more increased in proportion to H2 addition. Surface morphologies of SiC films were the facet structures under Ar addition, but those were gradually changed from facet to smooth structures with H2 addition. Surface roughness be-came higher in Ar, but it became lower in H2 with increasing the amount of diluent gas.

• Journal of Nuclear Fuel Cycle and Waste Technology(JNFCWT)
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• v.7 no.4
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• pp.229-236
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• 2009

There are two types of spent fuels generated from nuclear power plants, CANDU type and PWR type. PWR spent fuels which include a lot of reusable material can be considered to be recycled. CANDU spent fuels are considered to directly disposed in deep geological formation, since they have little reusable material. In this study, based on the Korean Reference spent fuel disposal System(KRS) which is to dispose both PWR and CANDU spent fuels, the more effective CANDU spent fuel disposal systems have been developed. To do this, the disposal canister has been modified to hold the storage basket which can load 60 spent fuel bundles. From these modified disposal canisters, the disposal systems to meet the thermal requirement for which the temperature of the buffer materials should not be over $100^{\circ}C$ have been proposed. These new disposals have made it possible to introduce the concept of long tenn storage and retrievabililty and that of the two-layered disposal canister emplacement in one disposal hole. These disposal concepts have been compared and analyzed with the KRS CANDU spent fuel disposal system in terms of disposal effectiveness. New CANDU spent fuel disposal concepts obtained in this study seem to improve thermal effectiveness, U-density, disposal area, excavation volume, and closure material volume up to 30 - 40 %.

• Journal of Nuclear Fuel Cycle and Waste Technology(JNFCWT)
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• v.15 no.1
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• pp.35-44
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• 2017

A gamma-ray peak of $^{226}Ra$ (186.2 keV) overlaps with one of $^{235}U$ (185.7 keV) in a gamma-ray spectrometry system. Though reference peaks of $^{235}U$ can be used to correct the peak interference of $^{235}U$ in the analysis of $^{226}Ra$, this requires a complicated calculation process and a high limit of quantitation. On the other hand, evaluating $^{226}Ra$ using the correction constant in the overlapped peak can make a rapid measurement of $^{226}Ra$ without the complicated calculation process as well as overcome the disadvantage in the indirect measurement of $^{214}Bi$, which means the confinement of $^{222}Rn$ gas in a sample container and a time period to recover the secular equilibrium. About 93 samples with 6 species for raw-materials and by-products were prepared to evaluate the activity of $^{226}Ra$ using the correction constant. The results were compared with the activity of $^{214}Bi$, which means the indirect measurement of $^{226}Ra$, to validate the method of the direct measurement of $^{226}Ra$ using the correction constant. The difference between the direct and indirect measurement of $^{226}Ra$ was generally below about ${\pm}20%$. However, in the case of the phospho gypsum, a large error of about 50% was found in the comparison results, which indicates the disequilibrium between $^{238}U$ and $^{226}Ra$ in the materials. Application results of the contribution ratio of $^{226}Ra$ were below about ${\pm}10%$. The direct measurement of $^{226}Ra$ using the correction constant can be an effective method for its rapid measurement of raw materials and by-products because the activity of $^{226}Ra$ can be produced with a simple calculation without the consideration of the integrity of a sample container and the time period to recover the secular equilibrium.

• Proceedings of the Materials Research Society of Korea Conference
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• 2003.03a
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• pp.210-210
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• 2003

휘스커상의 뮬라이트의 생성온도와 속도는 출발물질로 사용되는 알루미나와 실리카의 화학적 순도, 입자크기 그리고 결정형태에 의존하며, 알루미나와 실리카의 조성비에 따라 생성되는 뮬라이트의 형태가 변한다. 각 원료에 대한 반응성을 관찰하기 위하여 출발원료인 Al(OH)$_3$, 비정질 SiO$_2$, AlF$_3$를 혼합 각각 단일조성과 2상 및 3상의 원료를 혼합 분쇄하여 분무건조한 조립분말을 5$0^{\circ}C$ 구간으로 나누어 상온에서 130$0^{\circ}C$까지 튜브 로에서 열처리하였다. Al(OH)$_3$와 AlF$_3$를 단독으로 열처리하였을 경우에는 안정한 상태로 열처리가 진행되었으나, 혼합하였을 경우에는 40$0^{\circ}C$ 이상의 온도에서 서서히 반응하였다. 각 온도구간에서 열처리한 시편은 미세구조 관찰과 상분석을 통하여 플루오르 토파즈와 휘스커상의 뮬라이트의 생성을 관찰하였으며, 생성된 휘스커 뮬라이트는 조립의 형상을 원형대로 보존하였으며, 조립의 강도를 측정하기 위하여, 초음파 분산기와, 초음파 Homgeniger를 이용하여 처리한 결과 대부분 원래의 형상을 유지하였다.

• 한국가스학회:학술대회논문집
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• 2007.04a
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• pp.33-36
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• 2007

합성가스는 C1화학을 시작하는 반응원료 물질로 최근 DME(dimethyl-ether), 메탄올, GTL(gas to liquid), CTL(coal to liquid), 암모니아 생성 공정 등 많은 화학공정에 사용되고 있다. 합성가스를 생산하는 방법은 천연가스 개질반응과 석탄의 가스화반응, 그리고 원유의 정제 등을 통해 얻을 수 있다. 삼중개질반응은 천연가스와 산소, 수증기, 이산화탄소를 원료로 $1000^{\circ}C$ 이상의 고온에서 반응시켜 합성가스를 생산하며, 균일반응계와 불균일반응계로 이루어져 있다. 균일반응계에서는 천연가스와 산소가 주로 반응하며, 원료로 투입된 대부분의 산소는 균일반응계에서 소모되어 일산화탄소와 이산화탄소를 생성한다. 삼중개질반응의 균일반응계에서는 산소와 천연가스와의 반응으로 많은 발열이 발생하여 전체 반응계의 온도를 유지할 수 있도록 해준다. 본 연구에서는 산소로 인한 삼중개질반응의 온도 조절과 균일반응계의 온도 분포를 위치에 따라 관찰해 보았으며, 실험과 모사를 통해 비교해 보았다.