• 한국연소학회:학술대회논문집
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• 2014.11a
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• pp.259-262
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• 2014

• Proceedings of the Korean Society of Precision Engineering Conference
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• 2009.06a
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• pp.199-200
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• 2009

• Bulletin of Food Technology
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• v.15 no.2
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• pp.107-111
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• 2002

초고압 가공처리는 별동의 화학 보존제를 사용하지 않고도 저온에서 식품유래 미생물을 사멸시킬 수 있기 때문에 식품분야에서 주목받는 새로운 가공기술이다. 이러한 초고압 처리의 장점 덕분에 관능적 특성이 우수하고 영양성분이 그대로 보존되는 고품질 식품의 제조도 가능하다. 고압 조건에서의 미생물 사멸정도를 측정하기 위해서는 흔히 실험실 규모의 장비(그림 1)을 사용하여 소량의 미생물 접종액을 처리함으로서 대량 처리시(그림 2)의 양상을 예측할 수 있다. 초기에 개발된 실험실 귬의 초고압 처리장비에는 일반적으로 고압용기 내부에 온도감지 장치가 부착되어 있지 않아, 압력 조건 하에서의 압축발열 및 순간 감압냉각 효과가 제대로 보고되지 않았다. 그러나 가열효과를 고려하지 않으면 초고압 처리기 특유의 가압 특성 대문에 실험 결과의 재현성을 얻기가 힘들고, 특히 대용량 생산설비의 경우 더욱 그러하다. 이론적으로 초고압 처리는 매우 예측 가능한 공정이다. 즉 고압요기 내부에서는 어느 지점이던 간에 압력이 고르게 분포되고, 가열 확산에 근거한 처리공정과는 달리 압력이 모든 지점에 순간적으로 공정상 불균일이 야기될 소지가 있는 부분은 오직 압축에 다른 발열과 열 전달에 의한 온도 편차에 기인한다. 실제로 처리 대상 제품과 압력 전달매체의 압축시 발열정도 차이와 시료, 매체, 고압용기 간의 열 손실 또는 열 흡수 대문에 고압처리 공정에서 온도가 일정하지 않을 수 있다.

• Transactions of the Korean Society of Mechanical Engineers B
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• v.30 no.6 s.249
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• pp.594-601
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• 2006

Optimization study has been carried out to design an energy efficient, high temperature vacuum furnace which satisfies users' design requirements. First of all, the transient temperature distribution and the uniform temperature zone results have been compared with the steady state results to validate the feasibility of using steady state solution when constructing the thermal analysis DB. In order to check the accuracy, the interpolated results using thermal analysis DB have been compared with the computational and the experimental results. In this study, total heat flux is selected as the objective function, and the geometry parameters of vacuum furnace including the thickness of insulator, the heat zone sizes and the interval between heater and insulator are the design variables. The Uniform temperature zone sizes and the wall temperature are imposed as the design constraints. With negligible computational cost a high temperature vacuum furnace which has $40\sim60%$ reduction in total heat flux is designed using thermal analysis DB.

• Proceedings of the Korea Society for Energy Engineering kosee Conference
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• 2010.04a
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• pp.188-188
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• 2010

수소 에너지는 화석연료의 한정된 매장량과 연소시 발생되는 환경문제를 해결하기 위해 가장 이상적인 대체에너지로서 주목을 받고 있다. 그러나 현재까지의 기술로는 경제성 있는 수소 제조가 쉽지 않다. 그 방법 중 바이오매스 및 유기성폐기물의 가스화를 통한 수소제조분야는 자원의 재순환, 페기물 처리, 열원의 이용, 직접적인 $CO_2$ 삭감 등의 부수적인 효과가 높아 경제성 있는 수소제조법으로 평가되고 있다. 이에 본 연구에서는 수소 생산을 목적으로 하는 가스화기와 초고온개질기로 구성된 Twin-Bed 가스화 시스템을 개발하고, 이를 이용한 Wood pellet(미송)의 가스화 특성 및 생성 가스의 초고온개질 특성을 고찰하는 것을 목적으로 한다. 가스화기의 시간변화에 따른 생성 가스 수율에 대한 결과, 생성 가스 수율은 약 20분경과 후 안정화되었으며, 실험 2시간 동안의 $H_2,\;CH_4,\;CO,\;CO_2$의 평균 수율은 각각 17.77, 11.94, 42.13, 28.16 Vol.%의 결과를 보였다. 가스화기로부터 생성된 가스는 down-draft 형태의 고온개질기로 도입시켜, $1100^{\circ}C$의 초고온에서 개질반응을 수행하였다. $CH_4$의 경우 11.95 Vol.%에서 0 Vol.%로 거의 대부분 분해되었으며, $H_2$는 17.77 Vol.%에서 25.46 Vol.%로 약 65.8% 증가하는 결과를 나타냈다. 또한 수소 생성량은 평균 5 L/min kg-Biomass이었다. 냉가스 효율은 72.1%로서 나타나, 일반적으로 폐기물의 냉가스 효율인 약 50% 전후의 결과에 비하여 높은 효율을 보였다.

• Transactions of the Korean Society of Mechanical Engineers A
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• v.36 no.10
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• pp.1283-1288
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• 2012

A process heat exchanger (PHE) in a nuclear hydrogen system is a key component for transferring the considerable heat generated in a very high temperature reactor (VHTR) to a chemical reaction that yields a large quantity of hydrogen. A performance test on a medium-scale PHE prototype made of $Hastelloy^{(R)}$-X is scheduled in a small-scale gas loop at the Korea Atomic Energy Research Institute. In this study, as a preliminary study before carrying out the performance test in the gas loop, high-temperature structural analysis modeling and macroscopic thermal and structural analysis of the medium-scale PHE prototype by imposing the established displacement boundary constraints were carried out under the gas loop test condition. The results obtained in this study will be compared with the performance test results of the medium-scale PHE prototype in the gas loop.

• Transactions of the Korean Society of Mechanical Engineers A
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• v.35 no.10
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• pp.1249-1255
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• 2011

A PHE (Process Heat Exchanger) is a key component required to transfer heat energy of $950^{\circ}C$ generated in a VHTR (Very High Temperature Reactor) to a chemical reaction that yields a large quantity of hydrogen. A small-scale PHE prototype made of Hastelloy-X was scheduled for testing in a small-scale gas loop at the Korea Atomic Energy Research Institute. In this study, as a part of the evaluation of the high-temperature structural integrity of the PHE prototype, high-temperature structural analysis modeling, and macroscopic thermal and elastic-plastic structural analysis of the PHE prototype were carried out under the gas-loop test conditions as a preliminary qwer123$study before carrying out the performance test in the gas loop. The results obtained in this study will be used to design the performance test setup for the modified PHE prototype.

• Resources Recycling
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• v.16 no.6
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• pp.28-33
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• 2007

Coal is the most abundant energy source and deposited in every area of world. Combustion process with lower efficiency has been mainly used. Therefore, implementation of more efficient technologies, involving gasification, combined cycles and fuel cells, would be a key issue in the plans for more efficient power generation. In these technologies, gasification has been studied for decades. However, coal gasification to high value combustible gas such as hydrogen and carbon monoxide is focused again due to high oil price. The gaseous product, called syngas, can be effectively utilized in a variety of ways ranging from electricity production to chemical industry (as feedstock). In this study, coal gasification with ultra high temperature steam has been performed. The effect of steam/carbon ratio on the produced gas concentrations, gasification rate and additional products like tar, ammonia and cyan compounds has been determined.

• Resources Recycling
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• v.18 no.2
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• pp.51-55
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• 2009

Sawdust and sewage sludge and PE gasification by high temperature steam of Brown gas have been performed in this study. Steam/carbon ratio has been changed from 1 to 5 and the effect of steam/carbon ratio on the produced gas concentrations, gasification rate and tar generation has been determined. Also, the temperature distribution in the gasification reactor has been studied. Highest combustible content in the produced gas is around 70vol% and $H_2$ shows highest content among the combustible compounds. However, the heating value of the produced gas and tar content have been reduced with increasing steam/carbon ratio.

• Transactions of the Korean Society of Mechanical Engineers A
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• v.35 no.9
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• pp.1137-1143
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• 2011

The IHX (intermediate heat exchanger) of a VHTR (very high-temperature reactor) is a core component that transfers the high heat generated by the VHTR at $950^{\circ}C$ to a hydrogen production plant. Korea Atomic Energy Research Institute manufactured a small-scale prototype of a PCHE (printed circuit heat exchanger) that was being considered as a candidate for the IHX. In this study, as a part of high-temperature structural integrity evaluation of the small-scale PCHE prototype, we carried out high-temperature structural analysis modeling and macroscopic thermal and elastic structural analysis for the small-scale PCHE prototype under small-scale gas-loop test conditions. The modeling and analysis were performed as a precedent study prior to the performance test in the small-scale gas loop. The results obtained in this study will be compared with the test results for the small-scale PCHE. Moreover, these results will be used in the design of a medium-scale PCHE prototype.