• The Magazine of the Society of Air-Conditioning and Refrigerating Engineers of Korea
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• v.33 no.10
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• pp.30-33
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• 2004

화학 반응에 필요한 고온의 열에너지를 태양열 고집광 기술을 이용하여 화학 에너지로 변화하는 기술을 소개한다.

• Journal of Institute of Convergence Technology
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• v.2 no.1
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• pp.13-17
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• 2012

Concentrated Solar Power (CSP) is a renewable energy to generate electricity by using solar thermal energy as a heat source to drive turbines or engines for thermodynamic cycles. This paper introduces ongoing projects in SolarPACES(Solar Power and Chemical Energy systems) under the REWP(Renewable Energy Working Party) in the IEA(International Energy Agency). Then, the current status of international CSP markets and domestic activities is summarized. Finally, the CSP outlook by IEA and the key technological challenges to be overcome for its realization are presented.

• 한국신재생에너지학회:학술대회논문집
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• 2008.05a
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• pp.174-177
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• 2008

The proceeding of the $14^{th}$ biennial concentrating solar power SolarPACES symposium was closely reviewed and summarized to have an overview on up-to-date concentrated solar thermal technologies. A number of studies covering parabolic trough concentrating system, central receiver technology, solar fuels, dish and others were presented in the symposium which was held in Las Vegas, USA, from 4 to 7, 2008. Based on this overview a brief summary of technology trend and prospects were added in the paper.

• 한국신재생에너지학회:학술대회논문집
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• 2007.06a
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• pp.688-692
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• 2007

Solar thermal power generation allows additional benefits of cheap thermal storage and easy hybridization with other fossil fuel-driven power generation. KIER has been performing the project for solar thermal chemical reaction hybrid power generation. The project is to build and operate the first solar thermal chemical reaction hybrid power generation system in Korea. For concentrating solar thermal energy $m^2$ dish type concentrator was adapted and a heliostat is installed for reflecting horizontal insolation to the dish concentrator. At the moment building the dish concentrator including mirror and heliostat with sun tracking system was completed and it's performance are being closely evaluated. This paper will introduce some detailed designs and construction procedures which we have experienced so far.

• 한국태양에너지학회:학술대회논문집
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• 2009.04a
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• pp.55-60
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• 2009

The purpose of the research is to develop the high performance solar chemical reactor for producing hydrogen using steam reforming reaction of methane. A specific shape chemical reactor is suggested: spiral type reactor. The reactor is installed on the dish-type solar thermal system of Inha University. The temperatures, $CH_4$ conversion rates are measured. At specific condition, $CH_4$ conversion rates of the spiral type reactor are about 92%. The spiral type reactor gives reasonably good performance without any problems caused by highly concentrated solar radiation.

• Proceedings of the SAREK Conference
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• 2009.06a
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• pp.774-779
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• 2009

The purpose of this research is to develop the high performance of solar chemical reactor for producing hydrogen by methane reforming reaction with steam. Two shape of chemical reactor is suggested: first type is filled with porous material and second type is spiral type. These reactors is installed on the dish-type thermal system of Inha University, Inha Dish-1. Performance analysis of these two reactors is conducted from getting methane conversion.

• Journal of the Korean Solar Energy Society
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• v.24 no.2
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• pp.73-81
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• 2004

태양열의 이용에 있어 직접접촉식 열교환기(DCHX)는 여러 가지 잇점을 제공한다. 그중에서도 제일 부각되는 것은 폐쇄형 열교환기의 대체에 다른 경비 절약과 작은 온도차에서도 열교환이 가능한 뛰어난 열성능일 것이다. 본 연구는 액-액 타입의 직접접촉식 열교환기에 대한 열성능 실측을 통하여 직접 접촉 열교환에 대한 이해를 증진하고 아울러 태양열에의 적용성을 평가하고자 하였다. 실측 시스템은 집열기와 펌프 그리고 직접접촉식 열교환기로 구성되어 있는데 작동유체의 종류에 따라 서로 다른 두 가지 방법에 의해 열교환기 내로 유입되도록 하였다. 작동유체로는 Texatherm 46과 물이 사용되었는데 이는 이들 유체가 서로 전이지 않고 높은 온도$(<150^{\circ})$에서도 화학적으로도 안전하며 열적으로도 비교적 양호한 성능을 가지고 있기 때문이다 본 연구는 실측을 통해 열교환기 내에서의 미미한 열성층화 현상에 대한 메카니즘을 확인하였으며 아울러 열교환기의 작동유체에 따라 작동의 안정성과 열적 성능(11% 차이)이 다르게 나타날 수 있음을 보여주고 있다.

• Journal of the Korean Solar Energy Society
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• v.21 no.3
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• pp.1-8
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• 2001

The chemical heat storage as the one way of utilization for high temperature solar energy was considered. The stram reforming reaction of methane was chosen for endothermic reaction. The reactor was made of stainless steel and the dimension was 6.25 mm I.D. and 30 cm long coiled tube because of the geometry requirement of solar receiver. The methane conversion was increased linearly with reaction temperature and nickel content of catalyst. The methane conversion was 60% at $600^{\circ}C$ and 90% at $900^{\circ}C$. The feasibility of steam reforming of methane as the conversion of solar energy to chemical heat storage was confirmed.

• Journal of the Korean Solar Energy Society
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• v.21 no.4
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• pp.29-35
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• 2001

The chemical heat storage as the one way of utilization for high temperature solar energy was considered. The stram reforming reaction of methane was chosen for endothermic reaction. The reactor was made of stainless steel tube and it's dimension was 0.635 cm I.D. and 30 cm long, coiled tube because of the geometry requirement of solar receiver The effects of space velocity and reactants mole ratio on the methane conversion and CO selectivity were examined. From the experimental results, the optimum steam/methane mole ratio was determined.

• Journal of the Korean Solar Energy Society
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• v.29 no.1
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• pp.44-49
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• 2009

Steam reforming of methane in the high temperature solar chemical reactor bas advantage in its heating method. Using concentrated solar energy as a heating source of the reforming reaction can reduce the $CO_2$ emission by 20% compared to hydrocarbon fuel. In this paper, the simulation result of methane-steam reforming on a high temperature solar chemical reactor(SCR) using Fluent 6.3.26 is presented. The high temperature SCR is designed for the Inha Dish-1, a Dish type solar concentrator installed in Songdo city. Basic SCR performance factors are referred to the former researches of the same laboratory. Inside the SCR porous metal is used for a receiver/reactor. The porous metal is carved like a dome shape on the incident side to increase the heat transfer. Also, ring-disc set of baffle is inserted in the porous metal region to increase the path length. Numerical and physical models are also used from the former researches. Methane and steam is mixed with the same mole fraction and injected into the SCR. The simulation is performed for a various inlet mass flow rate of the methane-steam mixture gas. The result shows that the average reactor temperature and the conversion rate change appreciably by the inlet mass flow rate of 0.0005 kg/s.