• 한국자동차공학회논문집
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• 제19권5호
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• pp.143-147
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• 2011

Operating points of a fuel cell system (FCS) can be shifted to its high-efficiency region by hybridization in a fuel cell hybrid vehicle (FCHV), so the hydrogen can be saved. In this paper, the hydrogen consumption of an FCHV is compared to that of a fuel cell vehicle (FCV). A power management strategy is applied to the FCHV and the related simulation is carried out. The concept of equivalent hydrogen consumption is introduced in order to consider the effect of the difference between initial and final battery SOC on the total hydrogen consumption.

• 한국수소및신에너지학회논문집
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• 제33권3호
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• pp.247-254
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• 2022

Slush hydrogen containing liquid and solid hydrogen is expected to achieve zero boil-off by suppressing boil-off gas because heat of fusion for solid absorbe the heat ingress from atmosphere. In this paper, quantitative analysis on storage cost considering specific energy consumption between 1,000 m³ class liquid hydrogen storage system with re-liquefaction and slush hydrogen storage system during equivalent zero boil off period. Even though approximately 50% of total storage capacity should be converted into solid phase during the initial cargo bunkering, total energy consumption to convert into slush hydrogen is relatively 25% less than re-liquefaction energy for boil off hydrogen during zero boil off period. That's because energy consumption of slush phase change take up only 1.8% of liquefaction energy. moreover, annual revenue requirement including CAPEX, OPEX and electric cost for slush hydrogen storage could be more reduced approximately 32.5% than those of liquid hydrogen storage and specific energy storage cost ($/kg-H₂) could also be lowered by about 41.7% compared with liquid hydrogen storage.

• 한국수소및신에너지학회논문집
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• 제35권2호
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• pp.175-184
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• 2024

This study focuses on investigating the importance of managing greenhouse gas emissions from global energy consumption, specifically examining domestic targets for clean hydrogen production. Using life cycle assessment, we evaluated reductions in global warming potential and assessed the carbon neutrality contribution of the domestic hydrogen sector. Transitioning from brown or grey hydrogen to blue or green hydrogen can significantly reduce emissions, potentially lowering CO₂ equivalent levels by 2030 and 2050. These research findings underscore the effectiveness of clean hydrogen as an energy management strategy and offer valuable insights for technology development.

• 한국수소및신에너지학회논문집
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• 제34권4호
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• pp.358-368
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• 2023

The fuel cell market is expected to grow rapidly. Therefore, it is necessary to scale up fuel cells for buildings, power generation, and ships. A multi-stack system can be an effective way to expand the capacity of a fuel cell. Multi-stack fuel cell systems are better than single-stack systems in terms of efficiency, reliability, durability and maintenance. In this research, we developed a residential fuel cell stack and system model that generates electricity using the fuel cell-photovoltaic hybrid system. The efficiency and hydrogen consumption of the fuel cell system were calculated according to the three proposed power distribution methods (equivalent, Daisy-chain, and optimal method). As a result, the optimal power distribution method increases the efficiency of the fuel cell system and reduces hydrogen consumption. The more frequently the multi-stack fuel cell system is exposed to lower power levels, the greater the effectiveness of the optimal power distribution method.

• 대한화학회지
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• 제15권4호
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• pp.183-189
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• 1971

Stoichiometry of hydrazine-bromate reaction has been studied in acid media of varying compositions, elucidating the effects of bromide and chloride ions in sulfuric acid, perchloric acid, hydrochloric acid, and hydrobromic acid at varying concentrations of hydrogen ion and cupric ion. The study shows that the number of red-ox equivalent consumed by one mole of hydrazine becomes practically 4.00 if the concentrations of bromide and hydrogen ions are kept higher than 0.1M and 6M, respectively. The presence of copper tends to reduce the bromate consumption by hydrazine in an irregular manner, but such an effect becomes unimportant if the concentrations of bromide and hydrogen ions are kept sufficiently high.

• 한국가스학회지
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• 제21권2호
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• pp.20-25
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• 2017

압축 천연가스에 수소를 혼합한 HCNG 연료를 사용하는 HCNG 버스에 대해 WHVC 차량시험 결과를 토대로 연료 경제성 및 $CO_2$ 배출특성을 분석하였다. 동급 CNG 버스 및 디젤버스 시험결과와 비교하여 HCNG 버스의 연비 개선효과와 $CO_2$ 저감효과를 고찰하였다. $CO_2$ 배출특성은 탄소배출계수에 따른 연료효과와 연비에 의한 효과로 분석하였다. 분석결과 HCNG 버스는 CNG 버스 보다 연비는 11.5% 개선되었고 디젤버스와는 동등수준을 보이는 것으로 나타났다. 또한 $CO_2$ 배출 특성으로 HCNG 버스는 CNG 버스에 비해 20.4% 개선효과가 있고 디젤버스에 비해 34.5% 향상되는 것으로 분석되었다. 이산화탄소 배출특성은 연료성분에 따른 탄소배출계수와 엔진성능에 따른 연비에 영향을 받는 것으로 귀결되었다.

• 한국수소및신에너지학회논문집
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• 제30권2호
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• pp.136-146
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• 2019

A solid oxide fuel cell (SOFC) based hybrid desiccant cooling system model is developed to study the effect of fuel utilization rate of the SOFC on the reduction of energy consumption and $CO_2$ emission. The SOFC-based hybrid desiccant cooling system consists of an SOFC system and a Hybrid desiccant cooling system (HDCS). The SOFC system includes a stack and balance of plant (BOP), and HDCS. The HDCS consists of desiccant rotor, indirect evaporative cooler, electric heat pump (EHP), and heat exchangers. In this study, using energy load data of a commercial office building and SOFC-based HDCS model, the amount of ton of oil equivalent (TOE) and ton of $CO_2$ ($tCO_2$) are calculated and compared with the TOE and $tCO_2$ generation of the EHP using grid electricity.

• 한국수산과학회지
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• 제26권5호
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• pp.493-501
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• 1993

유처리제의 생분해도와 유처리제가 해수중의 용존산소에 미치는 영향을 구명하기 위해서 세 제품의 유처리제(SG, GL, WC)와 비이온 계면활성제(OA-5)에 대한 TOD분석, 원소분석 및 해수중에서의 생분해 실험을 행한 결과를 요약하면 다음과 같다. 1. 1mg의 유처리제는 $2.37{\sim}2.80mg$의 TOD, 1mg의 비이온 계면활성제는 2.45mg의 TOD를 나타내었다. 2. 유처리제는 탄소가 $67.6{\sim}76.5\%$, 수소가 $10.2{\sim}12.3\%$였고, 비이온 계면활성제는 탄소가 $65.3\%$, 수소가 $10.3\%$였으며 어느 것에서도 질소는 검출되지 않았다. 3. 유처리제는 생분해시 제품에 따라 다소 차이가 있었으나 1mg의 유처리제가 $0.403{\sim}0.595mg$의 $BOD_5$ 및 $0.703{\sim}0.855mg$의 $BOD_{20}$를 유발하였다. 또한 1mg의 비이온 계면활성제는 0.50mg의 $BOD_5$ 및 0.97mg의 $BOD_{20}$를 나타내었다. 4. 해수중에서 탈산소계수($K_1$)는 유처리제(4.0mg/l)의 경우 $0.121{\sim}0.171/day$, 비이온 계면활성제(2.0mg/l)의 경우 0.181/day로 나타났다. 또한 유처리제 1mg의 최종산소요구량($L_o$)은 $0.789{\sim}0.953mg$로서 계면활성제 1mg의 최종산소요구량 0.956mg과 비슷하였으며, Glucose 1mg의 TOD값 1.07mg에 접근하는 값이었다. 5. 해수 중의 생분해도($BOD_5/TOD$)에 있어서, 유처리제는 $17{\sim}21\%$, 비이온 계면활성제는 약 $20\%$로서 모두 중간 분해군에 속하였다.