• 설비공학논문집
• /
• 제28권8호
• /
• pp.325-330
• /
• 2016

This study was conducted to develop a heating system for a fuel cell-driven electric vehicle. The system consists of a compressor, an expansion device and three heat exchangers. A conventional air source heat exchanger is used as primary heat exchanger of the system, and an additional water source heat exchanger is used as a pre-heater to supply heat to the upstream air of the primary heat exchanger. On the other hand, the third heat exchanger consists of a water-to-refrigerant heat exchanger. The heat source of the pre-heater and the water-refrigerant heat exchanger is the waste heat from the fuel cell's stack. In the experiment, the indoor and the outdoor air temperature were fixed, and the compressor speed, EEV opening and waste heat temperature were varied. The results indicate that the $COP_h$ of the proposed system is 3.01 when the system is operating at a 1,200 rpm compressor speed, 50% EEV opening, and $50^{\circ}C$ waste heat source temperature in air pre-heater operation. However, when the system uses a water-refrigerant heat exchanger, the $COP_h$ increases to up to 9.42 at the same compressor speed and waste heat source temperature with 75% EEV openings.

• 한국신재생에너지학회:학술대회논문집
• /
• 한국신재생에너지학회 2010년도 춘계학술대회 초록집
• /
• pp.123.1-123.1
• /
• 2010

The solid oxide fuel cell (SOFC) has attracted great deal of attention due to its high electrical efficiency, high waste-heat utilization, fuel flexibility, and application versatility. However, SOFC technology is still not matured enough to fulfill the practical requirements for commercialization. Therefore, all the research and development activities are mainly focused on a development of practically viable SOFCs with higher performance and better reliability. We were successful in fabricating high-performance anode-supported unit cells by employing hierarchically controlled multi-layered electrodes for both structural reliability and high performance. In addition, a novel composite sealing gasket made it possible to achieve excellent sealing integrity even with considerable surface irregularities in a multi-cell planar arrayed stack.

• 한국환경보건학회지
• /
• 제32권1호
• /
• pp.8-18
• /
• 2006

The aim of this study is to evaluate the emission characteristics of mercury, lead, arsenic, and selenium from medium size municipal solid waste incinerators(MSWIs) in Korea. The concentrations of mercury, lead, arsenic, and selenium emitted from medium size MSWI stack were $2.67\;{\mu}g/Sm^3,\;0.38\;mg/Sm^3,\;1.33\;{\mu}g/Sm^3,\;0.28\;{\mu}g/Sm^3$, respectively. The concentration levels of mercury, lead, arsenic in flue gas from medium size MSW incinerator stacks selected were nearly detected under the Korea criteria level. Removal efficiencies of mercury, lead, arsenic, and selenium in waste heat boiler(WHE) and cooling tower(CT) were $90.36\%,\;69.76\%,\;43.04\%,\;40.64\%$, respectively. In general, the removal efficiencies of mercury and lead in WHE were higher than those of arsenic and selenium in WHE. Emission gas temperature reduction from waste heat boiler(WHB) and cooling tower(CT) can control mercury and lead of medium size MSWIs. To evaluate the relationship between mercury, lead, arsenic, selenium of fly ash and those of flue gas, it was carried out to correlation analysis of each metal concentration in the fly ash and in the flue gas from medium size MSWIs. From the correlation analysis, the coefficients of mercury, lead, arsenic, and selenium were 0.61, -0.38, 0.87, 0.28, respectively. The results of correlation analysis revealed that it should be highly positive to the correlation coefficients of mercury and arsenic in the fly ash and those of the flue gas emitted from medium size MSWIs. As it were, the concentrations of mercury and arsenic of flue gas from medium size MSWIs are high unless mercury and arsenic in fly ash are properly controlled in dust collection step in medium size MSWIs. It was also concluded that mercury, lead, arsenic, and selenium from MSWIs stacks could be controlled by waste heat boiler(WHE) and dust collecting step in medium size MSWIs.

• Journal of Advanced Marine Engineering and Technology
• /
• 제35권5호
• /
• pp.590-599
• /
• 2011

연료전지시스템의 고효율화를 목적으로 수소가 가진 화학적 에너지를 최대한 전력화하기 위하여 연료전지에서 발생하는 폐열을 적극 활용할 필요가 있다. 이런 목적에 폐열을 이용하는 증기터빈과 연료 전지를 결합시킨 SOFC/ST 하이브리드시스템이 적합하다. 본 논문은 SOFC/ST 하이브리드시스템에 대한 셀의 작동온도와 전류밀도, 연소기 출구 온도, 보일러 출구 가스온도가 시스템의 성능에 미치는 영향 등을 시뮬레이션을 통하여 검토한 것으로 증기터빈의 일정 조건에서는 연료전지 스택에서 다량의 폐열이 발생하는 경우가, 연료전지의 일정 조건에서는 연소기에 추가적 연료 공급을 억제하는 경우에서 하이브리드시스템의 효율이 증가됨을 확인하였다.

• Journal of Advanced Marine Engineering and Technology
• /
• 제40권7호
• /
• pp.563-568
• /
• 2016

본 연구는 연료전지 자동차용 공기조화기의 난방성능평가를 위하여 기존의 전반적인 히트펌프 시스템 중 공기열원 히트펌프 시스템의 증발기를 판형열교환기로 교체하여 시스템에 흐르는 냉매와 연료전지 스택 폐열을 직접 열교환이 가능한 수열원 이용이 가능한 난방시스템의 성능실험을 수행하였다. 실험결과에서 압축기의 회전수가 높을수록 소비동력이 증가하였다. 공기열원 이용방식의 경우 압축기 회전수가 1,200rpm이고 EEV개도가 25%인 경우 $COP_h$가 2.03으로 가장 높게 나타났고, 같은 압축기의 회전수에서 수열원 시스템은 EEV개도가 75% 및 스택 폐열의 온도가 $50^{\circ}C$인 경우 $COP_h$가 9.42로 가장 높게 나타났다.

• 터널과지하공간
• /
• 제21권6호
• /
• pp.518-525
• /
• 2011

본 연구에서는 고준위 방사성 폐기물 처분장의 특징인 높은 고도 차이와 폐기물에서 발생하는 발열량에 따른 자연 환기력을 계산하고 이를 바탕으로 자연 환기량을 계산하였다. 고준위 방사성 폐기물 처분장은 열엔진과 유사한 폐쇄 싸이클의 열역학적인 과정을 따른다고 볼 수 있다. 지하처분장내 고준위 폐기물의 발열에 의한 열이 공기에 추가되고 이로 인해 공기가 upcast 수직갱을 통해 위로 올라가는 동안 팽창됨에 따라 주위에 일을 하고, 이때 한 일에 의해 첨가된 열의 일부분은 임시로 기계적 에너지로 변함으로서 공기의 흐름을 촉진할 수 있다. 이는 처분장 내에서 지속적이고 강력한 열원이 존재한다면 자연 지속적인 공기의 싸이클적 흐름을 가능하게 할 것이다. 이를 바탕으로 고준위 방사성 폐기물의 심지층 처분시 발생되는 자연 환기량을 수학적 방법으로 계산한 결과 굴뚝효과에 의하여 폐기물 발열량에 따라 $74{\sim}183$Pa의 자연 환기력이 계산되고 이에 따른 자연 환기량은 $92.5{\sim}147.7m^3/s$이 계산되었다. 또한 CFD의 자연환기량 해석결과는 $82{\sim}143m^3/s$로서 수학적인 방 법과 비교하여 매우 비슷한 결과를 나타내었다.

• 한국수소및신에너지학회논문집
• /
• 제30권1호
• /
• pp.21-28
• /
• 2019

Reversible solid oxide fuel cell (ReSOC) system was integrated with waste steam for electrical energy storage in distributed energy storage application. Waste steam was utilized as external heat in SOEC mode for higher hydrogen production efficiency. Three system configurations were analyzed to evaluate techno-economic performance. The first system is a simple configuration to minimize the cost of balance of plant. The second system is the more complicated configuration with heat recovery steam generator (HRSG). The third system is featured with HRSG and fuel recirculation by blower. Lumped models were used for system performance analyses. The ReSOC stack was characterized by applying area specific resistance value at fixed operating pressure and temperature. In economical assessment, the levelized costs of energy storage (LCOS) were calculated for three system configurations based on capital investment. The system lifetime was assumed 20 years with ReSOC stack replaced every 5 years, inflation rate of 2%, and capacity factor of 80%. The results showed that the exergy round-trip efficiency of system 1, 2, 3 were 47.9%, 48.8%, and 52.8% respectively. The high round-trip efficiency of third system compared to others is attributed to the remarkable reduction in steam requirement and hydrogen compression power owning to fuel recirculation. The result from economic calculation showed that the LCOS values of system 1, 2, 3 were 3.46 ¢/kWh, 3.43 ¢/kWh, and 3.14 ¢/kWh, respectively. Even though the systems 2 and 3 have expensive HRSG, they showed higher round-trip efficiencies and significant reduction in boiler and hydrogen compressor cost.

• Environmental Engineering Research
• /
• 제22권3호
• /
• pp.266-276
• /
• 2017

A life cycle impact assessment was applied in an industrial waste incineration plant to evaluate the direct and indirect environmental impacts based on toxicity and non-toxicity categories. The detailed life cycle inventory of material and energy inputs and emission outputs was compiled based on the realistic data collected from a local industrial waste incineration plant, and the Korean life cycle inventory and ecoinvent database. The functional unit was the treatment of 1 tonne of industrial waste by incineration and the system boundary included the incineration plant and landfilling of ash. The result on the variation of the impact by the unit processes showed that the direct impact was decreased by 79.3, 71.6, and 90.1% for the processes in a semi dry reactor, bag filter, and wet scrubber, respectively. Considering the final impact produced from stack, the toxicity categories comprised 91.7% of the total impact. Among the toxicity impact categories, the impact in the eco-toxicity category was most significant. A separate estimation of the impact due to direct and indirect emissions showed that the direct impact was 97.7% of the total impact. The steam recovered from the waste heat of the incineration plant resulted in a negative environmental burden.

• 한국수소및신에너지학회논문집
• /
• 제23권1호
• /
• pp.8-18
• /
• 2012

This paper presents a three-dimensional, transient cold-start polymer electrolyte fuel cell (PEFC) model to numerically evaluate the effects of membrane electrode assembly (MEA) design and cell location in a PEFC stack on PEFC cold start behaviors. The cold-start simulations show that the end cell experiences significant heat loss to the sub-freezing ambient and thus finally cold-start failure due to considerable ice filling in the cathode catalyst layer. On the other hand, the middle cells in the stack successfully start from $-30^{\circ}C$ sub-freezing temperature due to rapid cell temperature rise owing to the efficient use of waste heat generated during the cold-start. In addition, the simulation results clearly indicate that the cathode catalyst layer (CL) composition and thickness have an substantial influence on PEFC cold-start behaviors while membrane thickness has limited effect mainly due to inefficient water absorption and transport capability at subzero temperatures.

• 공업화학
• /
• 제30권1호
• /
• pp.62-67
• /
• 2019

본 연구에서는 2 kW급 SOFC (solid oxide fuel cell)에서 배출되는 고온 배기가스의 폐열회수를 위한 일체형 Hot BoP의 설계와 성능 분석에 대한 연구를 수행하였다. Hot BoP 시스템은 스택 배기가스의 연소를 위한 촉매 연소기와 연소 후 배기가스의 폐열회수를 위한 원통다관형 공기예열기 및 스팀발생기로 구성되었다. 시스템 설계에서 폐열회수 시스템의 배치에 따른 최대 허용열용량을 산출하여 열분배 공정을 분석하였으며, 열전달 방정식을 통하여 공기예열기 및 스팀발생기의 상세설계를 수행하였다. Hot BoP는 방열손실의 저감을 위해 일체형으로 제작되었으며, SOFC와 연계운전을 가정한 스택배기가스를 모사하여 성능실험에 사용하였다. Hot BoP 성능실험에서 부하별 열전달량 및 시스템 효율이 측정 및 분석되었으며, 당량비에 따른 배기가스의 CO 발생량을 측정하여 연소성을 분석하였다. 실험결과로써, 2 kW급 SOFC 정격운전시 배기가스 연소열부하 기준으로 hot BoP의 열적 효율은 약 60%이며, 연소 후 배기가스의 CO 발생량은 당량비 0.25 이상에서 급격히 감소되는 것으로 나타났다.