• Journal of ILASS-Korea
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• v.17 no.3
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• pp.152-157
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• 2012

This investigation decribes the effect of the combustion and emission characteristics of HCNG engine according to the high purity hydrogen contents. The HCNG fuel was made by the mixture with a high purity hydrogen ($H_2$) and a natural gas. The test vehicle was applied to the bi-fuel (Gasoline and CNG) system and this system was modified from the fuel supply and fuel tank. In addition, the three premixed HCNG fuels with mixed rate of 10, 20 and 30% of hydrogen were used to maintain the safety. In order to analyze the combustion characteristics of HCNG and CNG, the fuel was injected in the combustor with constant volume. The exhaust emission from light duty vehicle with bi-fuel system was analyzed by a chassis dynamometer and emission analyzer. From these results, the reduction rate of NOx emission increased in the HCNG fuel and emission amount of THC and CO shows a similar level with CNG fuel. This study can be utilized the basic data for the development of a new business plans related with HCNG engines.

• Proceedings of the Korea Society for Energy Engineering kosee Conference
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• 1994.05a
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• pp.91-97
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• 1994

본 연구의 목표는 제올라이트 분자체를 흡착제로 사용하여 99.99% 이상의 고순도 질소를 저렴하게 제조하는 PSA(Pressure Swing Adsorption)공정을 개발하고 상업화 설계 자료를 도출하는 것이다. PSA방법에 의한 질소제조는 기존의 심냉법보다 전력원단위가 낮을 뿐만 아니라 on-site방식으로 설치되어 운영되므로 수송경비를 절감할 수 있다. 이러한 장점 때문에 외국의 경우를 보면 PSA의 사용이 날로 증대되고 있다. 현재 국내에 설치중인 질소 PSA는 전량 수입에 의한 것이다. 따라서 본 연구에서 개발한 질소 PSA는 중소규모의 질소가스 사용처에 공급함으로써 에너지절감효과 뿐만아니라, 수입대체효과도 얻을 수 있다.

• The Transactions of The Korean Institute of Electrical Engineers
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• v.62 no.6
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• pp.782-785
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• 2013

Multi-walled carbon nanotubes were synthesized on Ni catalyst using thermal chemical vapor deposition. By introducing ammonia gas during the CNT synthesis process, clean and vertically aligned CNTs without impurities could be prepared. As the ammonia gas increased a partial pressure of hydrogen in the mixed gas during the CNT synthesis process, we could control the CNT synthesis rate appropriately. As the ammonia gas has an etching ability, amorphous carbon species covering the catalyst particles were effectively removed. Therefore catalyst particles could maintain their catalytic state actively during the synthesis process. Finally, we could obtain clean and vertically aligned CNTs by introducing $NH_3$ gas during the CNT synthesis process.

• Proceedings of the Korean Society Of Semiconductor Equipment Technology
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• 2003.12a
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• pp.59-63
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• 2003

체적 음향파 공진기(Film bulk acoustic resonator, FBAR)는 2~10 Ghz 대역의 차세대 이동 통신용 구현에 필수적인 부품이기 때문에 국내외에서 활발한 연구가 진행되고 있다. 본 논문에서는 FBAR 소자 제조를 위한 연구에서 원자층 증착(Atomic layer deposition, ALD) 방법에 의한 ZnO buffer layer 위에 스퍼터링 방법을 이용한 2-step 방법을 사용하여 제조하였다. ALD를 이용한 ZnO buffer layer는 diethylzinc(DEZn)/$H_2O$를 순차적으로 주입하여 증착하였다. 이 때 두 원료물질 사이에 고순도 Ar 가스를 purge gas로 사용하였다. 원료의 주입시간은 1초, 원료간 purge 시간은 23 초로 하고 증착하였다. 2-step 방법을 이용할 경우, 스퍼터링 방법만을 이용하였을 때 보다 우수한 c-축 배향성 및 박막의 표면형상이 관찰되었다. 2-step 방법을 FBAR 소자 제작에 적용할 경우 보다 우수한 특성의 공진기를 제작할 수 있을 것으로 기대된다.

• Korean Journal of Optics and Photonics
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• v.1 no.1
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• pp.28-32
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• 1990

We have constructed and operated a discharge heated copper vapor laser which generated green (510.6 nm) and yellow (578.2 nm) light. The plasma tube was made of high purity (99.8%) alumina tube which has an inner diameter 25 mm and a length 106 cm. The electrodes, made of molybdenum sheet, were separated 108 cm apart. The laser gave an average power of 10 W at repetition rate of 5 kHz, charging voltage of 10 kV, Ne buffer gas pressure of 40 mbar, and the laser tube temperature of $1500^{\circ}C$..

• Applied Chemistry for Engineering
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• v.19 no.2
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• pp.157-160
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• 2008

The generation of high-purity hydrogen from hydrocarbon fuels is essential for efficient operation of fuel cell. In general, most feasible strategies to generate hydrogen from hydrocarbon fuels consist of a reforming step to generate a mixture of $H_2$, CO, $CO_2$ and $H_2O$ (steam) followed by water gas shift (WGS) and CO clean-up steps. The WGS reaction that shifts CO to $CO_2$ and simultaneously produces another mole of $H_2$ was carried out in a two-stage catalytic conversion process involving a high temperature shift (HTS) and a low temperature shift (LTS). In a typical operation, gas emerges from the reformer is taken through a high temperature shift catalyst to reduce the CO concentration to about 3~5%. The HTS reactor was designed and tested in this study to produce hydrogen-rich gas with CO to a range of 2~4%. The iron based catalysts (G-3C) was used for the HTS to convert the most of CO in the effluent from the partial oxidation (POX) to $H_2$ and $CO_2$ at a relatively high rate. Parametric screening studies were carried out for variations of the following variables: reaction temperature, steam flow rate, components ratio ($H_2/CO$), and reforming gas flow rate.

• Transactions of the Korean hydrogen and new energy society
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• v.12 no.4
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• pp.277-285
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• 2001

We developed a compact, 10 kWe, purifier-integrated reformer which supplies hydrogen for fuel cell vehicles. Our proprietary technologies regarding hydrogen purification by palladium alloy membrane and catalytic combustion by noble metal coated wire-mesh catalyst were combined with the conventional methanol steam reforming technology, resulting in higher conversion, excellent quality of product hydrogen, and better thermal efficiency than any other systems. In this system, steam reforming, hydrogen purification, and catalytic combustion take place all in a single reactor so that the whole system is compact and easy to operate. The module produces $8.2Nm^3/hr$ of 99.999% or higher purity hydrogen with CO impurity less than 10 ppm, which is equivalent to 10 kWe when PEMFC has 45 % efficiency. Thermal efficiency of the module is 81 % and the power density of the module is 1.6 L/kWe. As the results of experiments, cold-start time has been measured about 20 minutes. Response time of hydrogen production to the change of the feed rate has been within 1 minutes.

• Journal of the Korean Institute of Gas
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• v.25 no.4
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• pp.19-26
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• 2021

In this paper, we carried out the process modelling and economical analysis of the 500 kg-H₂/d-class green hydrogen production system process based on biomethane from the Food Bio Energy Center in Chungju. As a result of economic analysis, the NPV(Net present value) after 15 years of operation is 3.831 billion won, the PI(Profitability index method) is 1.42. It was found that the project of 500 kg-H₂/d-class green hydrogen production system has a 20.25% of IRR, which is higher than social discount rate of 4.5% and feasibility is ensured.

• Proceedings of the Korean Vacuum Society Conference
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• 2011.02a
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• pp.286-286
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• 2011

현재의 NEDO (New Energy and industrial technology Development Organization) style Si 정련은 두 단계로 구분되어 있다. 고출력 집속 전자빔을 이용한 금속 실리콘의 1차 용융과 대기압 근처의 플라즈마 아크 용해를 이용해서 B, P를 약간의 반응성 가스를 첨가 하여 제거하는 방법이다. 그러나 저가형 실리콘을 생산하려는 취지와 달리 두 가지의 고가 장비가 필요하다. E-beam melting 장치에서도 반응성이 높은 라디칼을 생성할 수 있다면 하나의 장비에서 두 가지의 정련 작업을 진행시킬 수 있다. 본 연구에서는 고진공에서(< 10-4 Torr) 동작하는 E-beam의 성능에 전혀 영향을 주지 않으면서 플라즈마를 용이하게 생성 시킬 수 있는 방법을 개발하고 이를 적용하여 실제 금속 순도 실리콘 내에 존재하는 B, P가 제거되는지 확인하는 것을 연구 내용으로 한다. 본 연구는 MG (Metal Grade) - Si 을 플라즈마 보조 전자빔 정련을 이용하여 정련한 Si 의 불순물 함량의 개선 효과를 조사하는 것이다. MG-Si 의 정련 방법 중에서 고출력 집속 전자빔을 이용하여 휘발성 오염물질을 제거 후, 플라즈마 아크 용해를 이용해서 B 를 제거하는 방법을 접목시켰다. MG-Si 에 DC power 와 전자빔을 집속시켜서 정련을 하면 챔버 내의 잔류 수증기가 플라즈마에 의해 분해되어 O를 생성하고, B와 반응을 하여 BO 형태로 제거가 된다. 방전 전압 700 V 와 전자빔 가속 전압이 4.5 kV, 방출 전류는 11 A, 진공 챔버 내의 압력은 $7.2{\times}10^{-4}$ Torr에서 정련을 진행하여 B를 제거했다.

• Transactions of the Korean hydrogen and new energy society
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• v.35 no.1
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• pp.90-96
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• 2024

In this paper, a new technology to obtain electronic grade, highly pure carbon dioxide by using membrane and liquefied natural gas (LNG) cold heat assisted cryogenic distillation has been proposed. PRO/II with PROVISION release 2023.1 from AVEVA company was used, and Peng-Robinson equation of the state model with Twu's alpha function to predict pure component vapor pressure versus temperature more accurately was selected for the modeling of the membrane and cryogenic distillation process. Advantage of using membrane separation instead of selecting absorber-stripper configuration for the concentration of carbon dioxide was the reduction of carbon dioxide capture cost.