• Journal of the Korean Society for Marine Environment & Energy
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• v.17 no.2
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• pp.116-121
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• 2014

In order to study the improvement of the multi stage regeneration cycles, muti-stage processes were applied to the cycles, respectively or together. The kinds of the cycles are multi stage reheater cycle (MS) and multi stage reheater regeneration cycle (MSR). Working fluid used was R134a and R245fa. Temperature of the heat source was $65^{\circ}C$, $75^{\circ}C$, and $85^{\circ}C$, and temperature of the heat sink was $5^{\circ}C$. Optimization simulation was conducted for improving the gross power and efficiency with multi stage reheater regeneration cycle for ocean thermal energy conversion(OTEC) with changing of a heat source, kind of the working fluid, and type of the cycle. Performance analysis of the various components was simulated by using the Aspen HYSYS for analysis of the thermodynamic cycle. R245fa shows better performance than R134a. This paper showed the most suitable working fluid with changing of a heat source and the kinds of working cycle. Compared to each other, MS showed better performance at gross power and MSR showed higher cycle efficiency.

• Journal of the Korean Institute of Gas
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• v.18 no.2
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• pp.41-47
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• 2014

In this work a thermodynamic performance analysis is carried out for a combined cycle consisted of an organic Rankine cycle (ORC) and a LNG cycle. The combined system uses a low grade waste heat in the form of sensible energy and the LNG cold energy is used for power generation as well as for heat sink. The effects of the key parameters of th system such as turbine inlet pressure, condensation temperature and source temperature on the characteristics of system are throughly investigated. The simulation results show that the thermodynamic performance of the combined system can be significantly improved compared to the normal ORC which is not using the LNG cold energy.

• Proceedings of the Korean Society of Propulsion Engineers Conference
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• 2000.11a
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• pp.18-18
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• 2000

산업용 가스터빈에서 대기로 방출되는 배기열을 효과적으로 이용하기 위한 역 브레이튼 사이클 가스터빈(Reverse Brayton Cycle Gas Turbine) 엔진의 출력과 비연료 소비율 및 열효율을 기본 브레이튼 사이클 엔진, 재열사이클에 역 브레이튼 사이클을 추가한 엔진, 역 브레이튼 사이클에 중간냉각기를 추가한 엔진의 출력, 비연료 소비율 및 열효율을 비교하였다.(중략)

• Journal of Advanced Marine Engineering and Technology
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• v.40 no.6
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• pp.476-483
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• 2016

An organic Rankine cycle for ocean thermal energy conversion system is a generating cycle using the temperature difference between surface water and deep water of the ocean. The working fluid is an important factor in the thermodynamic performance of an organic Rankine cycle. There is pinch point analysis as thermodynamic analysis of an organic Rankine cycle. This study performed a thermodynamic performance analysis according to variation in the pinch point temperature difference in heat exchangers and variation of outlet temperature of heat source and heat sink. It analyzed the thermodynamic performance by applying seven types of simple working fluids in a simple Rankine cycle for ocean thermal energy conversion that was designed according to pinch point analysis. As a result of the performance analysis, cycle irreversibility and total exergy destruction factor more decreased, and second law efficiency more increased in the lower pinch point temperature difference and temperature variation of heat source and heat sink in heat exchangers. In addition, the irreversibility changed greatly at a point that occurred in the thermodynamic variation. Among the selected working fluids, RE245fa2 showed the best thermodynamic performance, and the performance of all working fluids was observed to be similar. It needs a strict theoretical basis about diverse factors with thermodynamic performances in selecting heat exchangers and working fluids.

• Proceedings of the Korea Society for Energy Engineering kosee Conference
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• 1993.05a
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• pp.120-125
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• 1993

석탄가스화 복합사이클 발전시스템에서 스팀터빈 발전시스템은 1차 사이클인 가스터빈사이클에서 나오는 폐열을 이용하여 발생하는 증기로 구동되며, 증기의 일부는 가스화기로 들어가서 가스화 반응에 이용된다. 이와 같은 시스템의 설계나 평가를 위해서는, 주어진 시스템에 대한 열 및 물질수지 정산을 구할 수 있는 능력을 갖추는 것이 필요하다. 본 연구에서는 주어진 시스템의 성능을 평가할 수 있는 프로그램을 개발하여 IGCC(Integrated Gasification Combined Cycle)System의 증기터빈 사이클과 유사한 증기터빈기계의 열 및 물질정사고 성능 해석에 적용하였다. (중략)

• Proceedings of the Korean Information Science Society Conference
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• 2002.10e
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• pp.34-36
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• 2002

단말기 페이징이란 특정한 이동 단말장치의 정확한 위치를 결정하는 과정을 말한다. 페이징 비용은 단말기를 찾기 위한 페이징 사이클의 수와 검색되는 셀의 수에 비례한다.본 논문에서는 이러한 페이징 비용을 감소시키기 위하여, 실생활에서 단말기 사용자의 이동 패턴이 일정하다는 가정 하에 Shortest-Distance-First 방식에 단말기 사용자의 이동경로 이력 리스트를 부가한 이동경로 기반의 페이징 기법을 제안하고 폴링 사이클의 수와 폴링 시그널의 수 관점에서 시뮬레이션을 통해 기존 SDF 단말기 페이징 기법과 성능을 비교 분석한다. 시뮬레이션 결과를 통하여 제안된 방식이 폴링 사이클과 폴링 시그널의 수를 감소시킴을 보여준다

• Journal of the Korea Academia-Industrial cooperation Society
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• v.14 no.4
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• pp.1548-1554
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• 2013

This paper presents the analysis on performance characteristics of R744-R410A cascade refrigeration system to offer the basic design data for the operating parameters of this system. The performance of cascade refrigeration system is analyzed by using EES program. The operating parameters include compressor efficiency, and condensing and evaporating temperature in R410A high- and R744 low-temperature cycle, respectively. The COP of this system increases with the decrease of condensing temperature, and increases with the increasing evaporating temperature. And the COP of this system increases with the compression efficiency. Therefore, it can be seen that the compression efficiency, and evaporating and condensing temperature of R744-R410A cascade refrigeration system have an effect on the COP of this system. Also, it can be known that the cascade evaporation temperature with the highest efficiency in each parameter is present. Thus, it is an important to design R744-R410A cascade refrigeration system by considering these parameters.

• Proceedings of the Korean Institute of Surface Engineering Conference
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• 2018.06a
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• pp.137-137
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• 2018

이 연구에서는 리튬이온전지용 음극 활물질의 리튬이온 저장 용량을 최적화시키기 위한 새로운 방법이 제안되었다. 그 방법은 솔루션 플라즈마 프로세스를 사용하여 원자 단위의 리튬을 탄소 기반 물질의 내부에 도핑 시키고, 열처리를 통해 그 내부를 재설계하는 것이다. 리튬이온전지용 음극 활물질로 리튬금속 자체를 사용하려는 시도는 있었으나, 이는 충전 및 방전 사이클이 반복됨에 따라 리튬이 수지상으로 석출되어 내부를 단락시키거나, 리튬금속 자체의 폭발성에 의한 취급상의 제약이 있었다. 한편, 원자 단위로 탄소 내부에 도핑 된 리튬은 열처리 과정 동안 탄소 내부에서 확산함으로써 더 많은 리튬이 저장될 수 있는 공간을 만들었고, 사이클이 반복됨에 따라 서서히 충전 및 방전 반응에 참여함으로써 전지의 성능을 개선시켰다. 리튬이 도핑 된 탄소의 전기화학적 테스트 결과를 Fig. 1에 나타내었다. 실험 결과에서 보여진 초기 고용량 및 장기 사이클 특성은 탄소 내부에 도핑 된 리튬이 전지 성능의 향상에 중요한 역할을 한다는 것을 시사한다. 또한, 사이클이 반복됨에 따라 점차 증가하는 용량은 첫 사이클에서 형성된 solid electrolyte interphase의 비가역 용량을 보상할 수 있을 것으로 생각된다. 이상의 결과를 통해, 탄소 내부에 원자단위의 리튬을 도핑시키는 새로운 접근은 리튬이온전지의 성능 개선을 위한 효과적인 방법이 될 수 있을 것으로 보이며, 향후 리튬 이외의 다른 원소들, 즉 소듐과 같은 물질에 대하여 도핑을 시도한다면 새로운 분야에서 이와 같은 접근법이 유용하게 적용될 수 있을 것으로 사료된다.

• Journal of Advanced Marine Engineering and Technology
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• v.35 no.1
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• pp.46-52
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• 2011

A study on the improvement for cycle efficiency of closed-type ocean thermal energy conversion (OTEC) was studied to obtain the basic data for the optimal design of cycle. For that, OTEC cycle with a generator, a reheater and a multi-turbine was simulated and analyzed. The basic thermodynamic model for OTEC is Rankine cycle and the surface seawater of $26^{\circ}C$ and deep seawater of $5^{\circ}C$ were used for the heat source of evaporator and condenser, respectively. Ammonia is used as the working fluid. The cycle efficiency increased when generator is added with 0.9 generator effectiveness. When the reheater and multi-turbine are applied in the basic cycle, the cycle efficiency showed 3.14% and the capacity of heat exchanger decreased for same total cycle power. For the OTEC cycle with the generator, the reheater and the multi-turbine showed the highest cycle efficiency and increased the efficiency by more than 6.5% comparing with the basic OTEC cycle.

• Journal of Advanced Marine Engineering and Technology
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• v.35 no.2
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• pp.182-188
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• 2011

In this paper, analysis on the performance characteristics of R744-R404A cascade refrigeration system is presented to offer the basic design data for the operating parameters of the system. The operating parameters considered in this study include subcooling and superheating degree, compressor efficiency, and condensing and evaporating temperature in R404A high- and R744 low-temperature cycle, respectively. The main results were summarized as follows : It was observed that the highest COP of the system is achieved by higher superheating degree in R744 cycle than that in R404A cycle. The COP of the system increased by giving the subcooling degree in both cycles. The COP of the cascade system is the highest value when the system is operated at an optimum evaporation temperature.