• 한국분무공학회지
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• 제22권4호
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• pp.210-217
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• 2017

A gasoline direct injection engine has an intake air temperature can be lowered by the fuel vaporization in the combustion chamber increase the volume efficiency is high compression ratio. Therefore, study for injection rate and characteristics which influence mixture formation in combustion chamber is important. Movement of the injector needle has a direct effect on the injection of the fuel, such as formation of cavitation, the fuel injection rate, etc. Therefore, recent studies on the dynamic characteristics of the injector considering the movement of the needle have been reported, but it takes a lot of time and cost to experimentally confirm the movement of the needle inside the injector. In this study, AMESim, a commercial 1-D code, and Star-CCM+, a 3-D CFD code, were used to predict the dynamic performance of the injector with needle motion. In order to predict the movement of the needle under the high pressure, the result of the surface pressure distribution according to the movement of the needle was derived by using the morphing technique of flow analysis. In addition, we predicted the injection rate of the injector considering the movement of the needle in conjunction with the 1-D code. The injection rate of the injector was measured by the BOSCH's method and the results were similar to those of the simulation results. This method can predict the injection rate and injection characteristics and this result is expected to be used to predict the performance of gasoline direct injection engines with low cost and time in the future.

• 한국해양환경ㆍ에너지학회지
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• 제17권4호
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• pp.268-273
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• 2014

어판장에서 발생되는 생선 손질 폐기물의 자원화를 목적으로 탄화실험을 실시하였다. 어류폐기물의 원소조성을 살펴본 결과 탄소함량과 수소함량이 각각 51.1%와 7.6%, 산소함량이 30.5%로 나타났다. 특히 질소와 황의 함량이 각각 9.8%와 1.0%로 높아 악취문제 등이 심각할 수 있다는 것을 알 수 있었다. 어류폐기물의 원소조성을 다른 폐기물과 비교해볼 때 탄소 및 수소의 함량이 상당히 높은 것으로 나타나 생선폐기물의 최종처리는 열적처리가 적합한 것으로 나타났다. 고등어, 갈치, 조기를 대상으로 내장이나 몸통, 개별 생선이나 이들을 혼합한 시료 모두에 대하여 탄화실험을 실시한 결과 탄화되는 패턴은 시료 종류에 관계없이 유사한 경향을 나타내었다. 탄화시간에 따른 수율변화는 탄화시간 5분, 10분일 때 탄화온도 변화에 따른 수율 변화가 크게 나타났고, 탄화시간 15분 이후에는 탄화온도 변화에 따른 수율 변화가 미미한 것으로 나타났다. 또한 탄화시간 30분 이상부터는 각 온도별로 시간변화에 따른 수율 변화가 미미한 것으로 나타나 탄화시간에 따른 수율변화는 30분 이상부터는 큰 영향을 미치지 않는 것으로 나타났다. 탄화온도에 따른 차이는 탄화온도 $400^{\circ}C$에서는 1차 휘발이 미미하여 2차 휘발이 일어난 $500^{\circ}C$와의 수율차가 크게 나타났다. 또한 탄화온도를 $600^{\circ}C$, $700^{\circ}C$로 하여 10분 이상 탄화시킨 결과 수율차는 미미한 것으로 나타났다.

• Journal of Biosystems Engineering
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• 제34권5호
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• pp.351-357
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• 2009

This study was conducted to verify the simulation model through the drying test, and investigate effect of factors, such as temperature of drying air, airflow rate, and velocity of the airflow, on the drying. The low temperature drying simulation model was developed based on the circulation dry simulation model presented by Keum et al. (1987), and by modifying low temperature thin layer drying model, equilibrium moisture content model, latent heat of vaporization model, and crack ratio prediction model. The heat pump and experimental dryer with a capacity of 150kg were used for the test. The RMSE between the predicted and measured value was 0.27% (drying temperature), 0.15% (crack ratio), and 2.08% (relative humidity), so the relevance of the model was verified. In addition, the effect of drying temperature, airflow rate, and velocity of the airflow on the drying was examined. The experimental results showed that the crack ratio at drying temperature of $25{\sim}40^{\circ}C$ was allowable. Moreover, at below $30^{\circ}C$, variation of the crack ratio was slight, but drying time was delayed. Given these results, the drying temperature of over $30^{\circ}C$ was effective. As the airflow rate increased, required energy dramatically increased. Whereas drying rate slowly increased, so loss of drying efficiency was caused. Considering these results, the dryer needed to be designed and adjusted to lower than $30\;m^3/min{\cdot}ton$. As velocity of the airflow increased, required drying energy increased when the velocity of the airflow was over $5\;m^3$/hr, while crack ratio and drying rate showed little variation.

• 가스산업과 기술
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• 제5권1호
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• pp.39-47
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• 2002

With the expansion of natural gas demands in many countries, the necessity of LNG receiving terminals has been increased. The offshore LNG Floating Storage and Regasification Unit (FSRU) attracts attentions not only for a land based LNG receiving terminal alternative, but also for a feasible and economic solution. Nowadays, as the reliability of offshore oil and gas floating facilities and LNG carriers gains with proven worldwide operations, the FSRU can achieve a safety level that can be comparable to an onshore terminal. The design development related with safety features of the FSRU has been extensively carried out by oil and gas companies, shipyards, engineering companies, and equipment vendors, and has been successful so far in many fields. The construction of the FSRU can be achieved by integrating various technologies and experiences from many disciplines and many participating companies and vendors. In this paper, reviews on some of the important design features and design improvements on FSRU together with the practical construction aspects in cargo containment, vaporization system, ESD system, and operation modes, have been covered in comparison with actual LNG carrier, onshore receiving terminal, and FPSO systems. In order to materialize an FSRU project, the technical and economic justification has to be preceded. It is believed that once the safety and technical soundness is convinced, the FSRU can bring a higher project feasibility by reducing the overall construction time and cost. Through this study, an FSRU design readily applicable to an actual project has been developed by incorporating experiences gained from many marine and offshore projects. The wide use of proven standard technologies adopted in the series construction of LNG carriers and offshore FPSOs will bring the project efficiency and reliability.

• 한국태양에너지학회:학술대회논문집
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• 한국태양에너지학회 2012년도 춘계학술발표대회 논문집
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• pp.364-369
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• 2012

The development of solar thermal energy used adsorption desalination technology have been examined as a viable option for supplying clean energy. In this study, the modelling of the main devices for solar thermal energy used and adsorption desalination system was introduced. Silica gel type adsorption desalination system is considered to be a promising low-temperature heat utilization system. The design is divided into three parts. First, the evaporator for the vaporization of the tap water is designed, and then the reactor for the adsorption and release of the steam is designed, followed by the condenser for the condensation of the fresh water is designed. In addition, new features based on the energy balance are also included to design absorption desalination system. In this basic research, One-bed(reactor) adsorption desalination plant that employ a low-temperature solar thermal energy was proposed and experimentally studied. The specific water yield is measured experimentally with respect to the time controlling parameters such as heat source temperatures, coolant temperatures, system switching and half-cycle operational times. Desalination is processes that permeate our daily lives, but It requires substantial energy input, powered either from electricity or from thermal input. From the environmental and sustainability perspecives, innovative thermodynamic cycles are needed to produce the above-mentioned useful effects at a lower specific energy input. This article describes the development of adsorption cycles for the production of desalting effects. We want that this adsorption system can be driven by low temperature heat sources at 60 to $80^{\circ}C$, such as renewable, solar thermal energy.

• 한국안광학회지
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• 제7권1호
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• pp.1-8
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• 2002

나무로 만든 안구 모형에 콘택트렌즈를 부착시키고 헤어스프레이, 향수, 비눗물, 스킨로션 등 물질을 분무한 후 시간의 경과에 따른 렌즈의 형상 변화를 관찰하였다. 알코올이 함유되어 있는 헤어스프레이와 향수를 소프트 콘택트렌즈에 분무하는 경우 렌즈의 형상변형이 가장 심하였으며 분무종료 후 1분 이내에 렌즈가 뒤집히는 현상이 확인되었다. 헤어스프레이에 함유되어 있는 resin 에어졸의 분사거리가 짧을수록 분사시간이 길수록 렌즈의 변형이 심하였다. 알코올의 증발이 수반되는 기화열 방출에 의해 콘택트렌즈 앞 뒤 면에 온도차가 발생하고 이에 따른 팽창률의 차이가 렌즈 변형의 원동력으로 간주된다. 알코올이 포함되어 있지 않은 물질을 콘택트렌즈에 분무하는 경우에는 함유되어 있는 성분들의 계면활성 작용으로 인하여 기포만 발생할 뿐 렌즈의 변형은 미미하였다.

• 분석과학
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• 제11권3호
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• pp.222-228
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• 1998

15종의 분자량이 낮은 휘발성 유기용매 물질류를 사용하여 에탄올에 대한 분리분석 등을 검토하기 위하여 5가지 충진 칼럼과 2가지 모세관 칼럼을 이용한 기체 크로마토그래피 실험에서 Gaskuropack 54 와 DB-1 column이 좋은 분리능을 보여 주었다. GC 기화평형법에 의한 생체물 시료의 알코올 농도 측정에서 0.6N 과염소산, 1M 메타인산 및 염화나트륨 포화용액을 이용한 salt-effect 첨가실험은 그 중 염화나트륨 포화 용액이 알코올 농도값을 얻는데는 가장 안정된 값을 보였다. 혈액 및 각 조직의 시료들에서 시간에 따른 농도변화 실험에서 에틸알코올 농도 변화, 무게 변화, 함수분 변화, 헤마토크리트 변화치 영향을 함께 실험한 결과, 용기의 직경에 따르는 알코올 농도의 감소 변화를 1차 함수로 제안 할 수 있었으며, NISI에 조사 의뢰된 25 부검 사례에서 각 장기별 에틸알코올 분배농도에 대한 실험에서 뇌, 혈액, 신장, 비장, 간장, 폐장의 순으로 분포율이 낮아지는 결과를 얻을 수 있었다.

• 한국항공우주학회지
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• 제39권3호
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• pp.232-241
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• 2011

하이브리드 로켓은 난류 산화제 유동과 고체 추진제의 기화로 인한 분사 유동 사이의 상호 작용에 의해 복잡한 형태의 혼합 전단층이 존재한다는 특별한 성질을 가지고 있다. 본 논문에서는 유동 간섭에 의해 표면에서 발생하는 진동 유동의 물리적 특성을 연구하기 위하여 압축성 효과를 고려한 질량분사가 있는 덕트 유동의 LES(Large Eddy Simulation) 해석을 수행하였다. 계산 결과에 따르면, 기화 질량이 분출됨에 따라 주유동방향 와류의 특성이 강해지고 국부적으로 발생하는 역류 현상을 근거로 벽면 근방에서 원주방향 와류가 생성됨을 확인하였다. 그리고 시간 특성을 갖고 나타나는 와류 흘림 현상은 혼합 전단층에 기인한 유동 불안정성에 의해 촉진되었으며, 분출유동에 의해 발달한 고유 진동 유동을 의미하는 압력 섭동의 특정 진동수가 $\omega$=8.8에서 검출됨을 확인하였다.

• 한국태양에너지학회:학술대회논문집
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• 한국태양에너지학회 2011년도 춘계학술발표대회 논문집
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• pp.204-209
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• 2011

According to the environment report of UN, korea was classified as potable water shortage countries. Approximately 71% of the Earth's surface is covered by ocean. However, it is difficult to use for industry of residential purpose without a certain processing. The development of solar and waste-heat used absorption desalination technology have been examined as a viable option for supplying clean energy. In this study, the modelling of the main devices for solar and waste-heat used and adsorption desalination system was introduced. The design is divided into three parts. First, the evaporator for the vaporization of the top water is designed, and then the reactor for the adsorption and release of the steam is designed, followed by the condenser for the condensation of the fresh water is designed. In addition, new features based on the energy balance are also included to design absorption desalination system. In this basicresearch, One-bed(reactor) adsorption desalination plant that employ a low-temperature solar and waste energy was proposed and experimentally studied. The specific water yield is measured experimentally with respect to the time controlling parameters such as heat source temperatures, coolant temperatures, system switching and half-cycle operational times.

• Restorative Dentistry and Endodontics
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• 제10권1호
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• pp.85-92
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• 1984

The aim of this study was to examine the influence of the speed of grinding and coolants on mercury vaporization during amalgam removal. Forty amalgam filled stone dies were stored at $37^{\circ}C$ and 100% relative humidity for 7 days prior to the beginning of the mercury vapor experiment and were divided into 4 different groups; In Group I; Used by high speed without coolant & evacuator during amalgam removal. In Group II; Used by high speed with coolant & evacuator during amalgam removal. In Group III; Used by low speed without coolant & evacuator during amalgam removal. In Group IV; Used by low speed with coolant & evacuator during amalgam removal. The amalgam specimens were removed in a 30-second time period and mercury vapor was collected with membrane filter at 27mm from the site of removal and 45 degree above there. Samples in Group II, IV were removed with coolant spray at a flow rate of 30 ml/min with high-velocity evacuator. Mercury vapor collected membrane filter was analysed by Atomic Absorption Spectrophotometer using cold vapor method. The results were as follows; 1. The mercury vapor levels were obtained all of the Groups. 2. The mercury vapor levels of the Group II, IV (with coolant & evacuator) were less than that of the Group I, III (without coolant & evacuator). 3. The highest mercury vapor level recorded during amalgam removal procedure was Group I (used by high speed without coolant & evacuator) and its record was $0.78{\pm}0.09\;mg/m^3$, which exceed the T.L.V. by 15 times. 4. The mercury vapor level of the Group IV (used by low speed with coolant & evacuator) was more than that of the Group II (used by high speed with coolant & evacuator), but its difference was not significant, statistically. (p > 0.05)