• Journal of the Korean Society of Manufacturing Technology Engineers
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• v.8 no.2
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• pp.94-94
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• 1999

Natural gas is considered to be on e of the most promising candidates for a clean substitute fuel and a great amount of research on the compressed natural gas(CNG) fueled vehicle has been performed. In this s tudy, we try to understand the property of CNG fuel with using CNG engine experiment. In order to present the direction and application of CNG, we experiment with various operating conditions that is, spark timing, A/F ratio, air quantity and fuel quantity, etc. 11,967 cc engine was used in the experiment and the engine fuel ratio was determined in the way that the performance of dedicated CNG engine is corresponded to that of existing diesel engine. The performance and dedicated CNG engine were measured by changing the fuel injection timing. The dedicated CNG engine was proved to be good in describing the experimental results and according to the actual road test, acceleration and constant speed driving for dedicated CNG engine was better than existing diesel engine.

• Transactions of the Korean hydrogen and new energy society
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• v.25 no.2
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• pp.114-121
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• 2014

The synthesis of Fischer-Tropsch oil is the catalytic hydrogenation of CO to give a range of products, which can be used for the production of high-quality diesel fuel, gasoline and linear chemicals. Our cobalt catalyst was prepared Co/alumina, Co/silica and Co/titania by the incipient wetness impregnation of the nitrates of cobalt with supports. Co-based catalysts was calcined at $400^{\circ}C$ before being loaded into the FT reactors. After the reduction of catalyst has carried out under $450^{\circ}C$, FT reaction of the catalyst has carried out at GHSV of 4,000 under $200^{\circ}C$ and 20atm. From test results, the order of increasing activity for the catalyst was Co/alumina > Co/silica > Co/titania. When the content of Co metal such as 5, 12, 20 and 30wt% was changed, an CO conversion increased as the content of Co metal increased. The activity of catalyst has obtained the best value at 12wt% Co content.

• 한국신재생에너지학회:학술대회논문집
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• 2008.05a
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• pp.345-348
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• 2008

본 연구에서는 가스화 반응, 수성가스 전환 반응, 메탄화 반응 등으로 구성된 SNG제조 공정에 대한 해석을 통해, 석탄 촤의 가스화 반응에 의해 생성된 합성가스를 이용한SNG제조 공정 특성을 파악하고자 하였고, SNG제조 공정 중 가스화 공정에 대한 실험을 통해 가스화 공정의 조건에 따른 합성가스 발생 특성 및 메탄화 반응의 특성을 살펴보았다. 석탄 촤를 대상으로 하여 가스화 공정의 $O_2$/feed ratio와 steam/feed ratio 조건 변화에 따른 합성가스 발생 특성을 살펴본 결과 steam을 투입하지 않은 경우 발생되는 합성가스 중 CO의 농도는 55$\sim$65%, $H_2$ 9$\sim$11%, $CO_2$ 24$\sim$29% 범위였고, $O_2$/feed ratio가 증가할수록 CO의 농도는 증가하고, $H_2$와 $CO_2$의 농도는 감소하는 경향을 나타내었다. 또한,steam을 투입하는 경우 합성가스 중 CO의 농도는 20$\sim$37%, $H_2$ 16$\sim$18%, $CO_2$ 42$\sim$55% 범위였다. 메탄화 공정 해석 결과 메탄의 농도를 최대로 얻을 수 있는 조건은 $H_2$/CO 비가 3인 조건이었고 온도가 낮을 수록 생성농도가 높아짐을 알 수 있었다. 가스화 특성 실험 결과 및 공정해석 결과, 메탄화 반응에 대한 실험 및 공정해석 결과는 고체시료의 가스화 반응을 통해 발생한 합성가스를 이용한 SNG 제조 공정 특성 파악 및 SNG를 제조하기 위해 필요한 단위 공정에 대한 설계 자료 및 운전조건을 결정할 수 있는 주요 인자로 활용될 수 있을 것으로 판단된다.

• 한국신재생에너지학회:학술대회논문집
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• 2007.06a
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• pp.481-484
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• 2007

마이크로 이미징은 물 분자가 하이드레이트 구조로 전환되는 것을 미시적으로 관찰할 수 있다. 본 고에서는 메탄과 $CO_2$ 하이드레이트 생성 실험을 실리카 젤과 bulk water를 이용해 실시하면서 이를 마이크로 이미징으로 관찰한 결과를 제시하고자 한다. Bulk water에서 하이드레이트 shell에 의해 하이드레이트 생성 속도가 제한을 받는 반면, 실리카 젤에서는 미세 pore에서의 생성 특성이 매우 빠르게 진행되는 것으로 관찰되었다.

• Journal of Welding and Joining
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• v.1 no.1
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• pp.30-36
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• 1983

현재의 세계적 경제발전의 침체는 가까운 장래에 급속한 경기회복으로 전환될 전망을 보여주지는 않는다. 한편으로는 기계·전자공학을 중심으로한 기술의 발전, 정보화 사회로의 변화가 눈에 뛸 정도로 급격히 일어나고 있다. 이와 같은 정세속에서 앞으로의 용접기술에는 무엇을 목표로 어떠한 노력이 이루어져야 하는가에 대해, 일본 용접학회, 일본용접협회의 각종 활동을 중심으로 소개하고자 한다. 또한 에너지의 문제는 현재도, 장래도 세계적으로 가장 중요한 문제의 하나다. 에너지 산업의 제분야-유전의 개발, 석유의 채굴과 파이프라인 수송, 액화석유가스(LPG), 액화 천연가스(LNG)의 수송과 저장, 석탄액화, 나아가서는 원자력, 수력 발전 플랜트의 건조 등등-에 있어서 용접기술의 역할은 매우 크다. 1982년 5월 미국에서 '에너지 이용과 용접기술'을 테마로 한 국제회의가 열렸는데 이 회의에서 보고한 일본의 용접기술에 관한 주제를 여기서도 소개하 고자 한다.

• Journal of the Korean Institute of Gas
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• v.19 no.5
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• pp.7-12
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• 2015

Hydrogen is usually produced by using syngas generated by the fuel reforming for natural gas so far. The further process is needed for increasing the hydrogen yield of syngas. However, the process for upgrading the hydrogen yield is accompanied by additional energy sources and economic costs. Thus related studies on the method for using as a mixture in itself have been conducted in order to utilize more efficiently syngas. The effect on the engine performance for methane/syngas mixture of 30kW spark ignition gas engine for power generation has been investigated in this study. As a result, it was found that the combustion phenomena such as the maximum in-cylinder pressure and crank angle at that time have been improved by methane/syngas mixture. Through these, fuel conversion efficiency could be enhanced by about 98% of methane/hydrogen mixture and $NO_x$ emissions could be reduced by about 12% of methane-hydrogen mixture.

• Journal of Energy Engineering
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• v.25 no.4
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• pp.214-225
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• 2016

Gasification is one of the important contribution to resource recycling by conversion of biomass to a variety of energy sources such as alcohol, SNG etc., and to global warming prevention by reduction of green house gases such as $CO_2$. The aim of this study is to draw the optimal operation condition of dual fluidized-bed gasifier with biomass fuel, to verify SNG production efficiency and to establish the basis for the domestic commercialization of dual fluidized bed gasification. As a result, dual fluidized-bed gasifier has the optimal conditions at $826^{\circ}C$ with steam input 1,334 g/hr, air input 5.56 L/min. The carbon conversion is 81% and SNG production efficiency was $CH_4$ 92%.

• Journal of the Korean Institute of Gas
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• v.25 no.6
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• pp.45-52
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• 2021

The government is converting the fuel for trucks, one of the causes of PM in Korea, form diesel to LNG. Mobile LNG station are being developed to solve the problems of insufficient charging infrastructure and facilitate the spread of LNG fuel. In this study, QRA was used th calculate the CA of the facility for a secure design prior to the development of the mobile LNG station and to predict the individual/societal risk the scenario. As a result, the danger of mobile LNG station was in ALARP.

• Korean Chemical Engineering Research
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• v.57 no.3
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• pp.420-424
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• 2019

In SNG (synthetic natural gas) process by proposed RIST(Research Institute of Industrial Science & Technology)-IAE(Institute for Advanced Engineering) (including three adiabatic reactors and one isothermal reactor), the methanation reaction and water gas shift (WGS) reaction take place simultaneously, and the supply of steam with syngas might control the temperature in catalyst bed and deactivate the catalyst. In this study for development of SNG process, the characteristics of the methanation reaction with a Ni-based catalyst by prepared RIST and using a low $H_2/CO$ mole ratio (including $CO_2$ 22%) are evaluated. The operating conditions ($H_2O/CO$ ratio of the $1^{st}$ adiabatic reactor, operating temperature range of $4^{th}$ isothermal reactor, etc.) were reflected the results from previous studies and in the same condition a pilot scale SNG process is carried out. As a results, the pilot scale SNG process is stable and the CO conversion and $CH_4$ selectivity are 100% and 96.9%, respectively, while the maximum $CH_4$ productivity is $660ml/g_{cat}{\cdot}h$.

• Transactions of the Korean hydrogen and new energy society
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• v.25 no.3
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• pp.247-254
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• 2014

The synthesis of Fischer-Tropsch oil is the catalytic hydrogenation of CO to give a range of products, which can be used for the production of high-quality diesel fuel, gasoline and linear chemicals. Our cobalt based catalyst was prepared Co/alumina, silica and titania by the incipient wet impregnation of the nitrates of cobalt and promoter with supports. Cobalt catalysts was calcined at $350^{\circ}C$ before being loaded into the FT reactors. After the reduction of catalyst has been carried out under $450^{\circ}C$ for 24hrs, FT reaction of the catalyst has been carried out at GHSV of 4,000/hr under $200^{\circ}C$ and 20atm. From these test results, we have obtained the results as following ; in case of 12wt% Co-supported $Al_2O_3$, $SiO_2$ and $TiO_2$ catalysts, maximum activities of the catalysts were appeared at the promoters of Mn, Mo and Ce respectively. The activity of 12wt% $Co/Al_2O_3$ added a Mn promoter was about 3 times as high as that of 12wt% $Co/Al_2O_3$ catalyst without promoters. When it has been the experiment at the range of reaction temperature of $200{\sim}220^{\circ}C$ and GHSV of 1,546~5,000/hr, the results have shown generally increasing the activities with the increase of reaction temperature and GHSV.