• Clean Technology
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• v.18 no.4
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• pp.360-365
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• 2012

With rapid increase in municipal solid waste (MSW) due to the rising economy, solid waste gasification emerges as one of the promising technologies. Separation of the carbon monoxide (CO) and hydrogen ($H_2$) from syngas obtained by gasification of MSW was studied using the polyamide composite membrane. The separation characteristics of the CO and $H_2$ were studied at different gas flow rates and stage cuts. The permeability of CO and $H_2$ along with the selectivity of $H_2$ with respect to CO was obtained. Furthermore, the Arrhenius plots were obtained to estimate the activation energies of CO and $H_2$ permeabilites.

• Resources Recycling
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• v.12 no.5
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• pp.42-49
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• 2003

Characteristics of reduction and carbidization for hematite ore with a wide size range have been investigated at high temperature(590∼64$0^{\circ}C$) under $H_2$ and $H_2$-CO gas mixtures. The apparent activation energy for reduction of hematite ore with H2 gas was found to be 20 kJ/mol. The weight loss by reduction was about 28% md the weight gain by carbidization was about 5%. The measured values of weight change were compared with those calculated from equation (3) & (5) and fairly good agreement was obtained. The rate of carbidization was increased with an decrease in temperature, particle diameter and gas ratio($H_2$/ CO). The free carbon was increased with decrease in gas ratio($H_2$/ CO). The rate of carbidization was increased with mixing of $H_2$ gas but this effect was not proportional to fraction of $H_2$ gas. It was also found that the rate of carbidization was the maximum in the $H_2$ gas fraction of 0.5. It is considered that $H_2$ plays a part as a catalyst for formation of iron carbide($Fe_3$C).

• 한국신재생에너지학회:학술대회논문집
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• 2010.06a
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• pp.218.2-218.2
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• 2010

저분자량의 가스와 물이 물리적 결합으로 이루어진 가스 하이드레이트는 상대적으로 많은 양의 가스가 포집될 수 있다는 특성을 이용하여 다양한 분야에서 활발한 연구가 진행되고 있다. 본 연구에서는 매립지에서 발생되는 매립가스를 하이드레이트의 원리를 이용하여 효율적으로 저장 및 수송하기위한 공정에 적용하기위해 필요한 매립지 가스 하이드레이트의 상평형에 대한 특성을 분석하고자한다. 일반적으로 매립지 가스에는 메탄이 약 50%, 이산화탄소가 약 35%, 질소가 약 6% 포함되어 있으며 그 밖에 산소, 수분, 암모니아 황화수소 메르캅탄 등 할로겐 계통을 포함한 탄화수소계화합물 수십여종이 포함되어 있다. 이러한 매립지가스를 하이드레이트화 하기위해서는 매립지가스에 포함된 다양한 성분들이 하이드레이트 형성에 미치는 영향을 알아볼 필요가 있다. 특히 황화수소의 경우 독성이 있으며, 실제 플랜트에서 장비의 부식등 악영향을 미치므로 이와 관련한 기초 연구가 필요하다. 따라서 본 연구에서는 메탄, 이산화탄소, 황화수소가 각각 49.9%, 50.05%, 500ppm의 조성으로 이루어진 혼합가스를 이용하여 하이드레이트 생성 및 해리 시 거동을 측정하고 그 상평형 영역을 기존데이터와 비교분석 하였다. 25bar, 36bar에서 측정한 상평형 데이터는 한국해양대학교 에서 측정한 결과와 마찬가지로 실제 상평형 영역이 CSMHYD 프로그램으로 예측한 것보다 하이드레이트의 안정영역이 약 2bar 정도 높게 형성되는 것을 확인하였으며, $CH_4+CO_2+H_2S$ 혼합가스 하이드레이트의 생성 시 mol consumption은 $CH_4+CO_2$ 혼합가스 하이드레이트와 유사하게 나타났다. 이 결과로 유추하건대, 황화수소의 첨가는 하이드레이트의 형성 압력을 높이지만, 하이드레이트 형성률에는 크게 영향을 미치지 않는다고 할 수 있다.

• 한국신재생에너지학회:학술대회논문집
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• 2010.06a
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• pp.216.2-216.2
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• 2010

본 연구에서는 $H_2+CO_2$(40%) 혼합기체로부터 이산화탄소를 효과적으로 분리/회수 하기 위하여 가스 하이드레이트 형성법을 제안하였다. 하이드레이트의 형성 조건을 보다 완화시켜 주기 위하여 열역학적 촉진제로서 TBAB (Tetra-n-butyl Ammonium Bromide, $(C_4H_9)_4NBr$))와 THF(Tetrahydrofuran)를 각각 첨가하여 열역학적 촉진 현상을 살펴보았다. 다양한 농도의 TBAB(10, 40, 60 wt%)와 THF(1, 5.56, 10 mol%)에 대하여 3상(H - Lw - V) 평형을 측정하였다. 그 결과 40 wt%의 TBAB와 5.56 mol%의 THF의 농도에서 가장 큰 촉진효과를 보였으며 그 이상의 농도에서는 오히려 촉진효과가 줄어드는 것을 확인할 수 있었다. 이러한 결과는 혼합가스 하이드레이트 형성시 양론비 이상의 TBAB와 THF가 첨가될 경우 반응에 참여하지 못한 TBAB와 THF가 가스 하이드레이트 형성을 방해하기 때문이다. 열역학적 촉진제로서 실제공정에 적용할 경우 40 wt%의 TBAB와 5.56 mol%의 THF를 사용하는 것이 가장 효과적일 것으로 사료된다. 본 실험에서 얻어진 결과는 가스 하이드레이트 형성법을 이용한 합성가스 분리 공정 개발에 중요한 기초 자료가 될 것이다.

• Membrane Journal
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• v.21 no.3
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• pp.290-298
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• 2011

The influence of co-existing gases on the hydrogen permeation was studied through a Pd-coated $V_{53}Ti_{26}Ni_{21}$ alloy membrane. The hydrogen permeation characteristics of Pd-coated $V_{53}Ti_{26}Ni_{21}$ alloy membrane have been investigated in the pressure range 1-3 bar under pure hydrogen and hydrogen mixture gas with carbon dioxide and carbon monoxide at $450^{\circ}C$. Preliminary hydrogen permeation experiments have been confirmed that hydrogen flux was $5.36mL/min/cm^2$ for a Pd-coated $V_{53}Ti_{26}Ni_{21}$ alloy membrane (thick: 0.5 mm) using pure hydrogen as the feed gas. In addition, hydrogen fluxes were 4.46, 5.20, $3.91mL /min/cm^2$ for$V_{53}Ti_{26}Ni_{21}$ alloy membrane using $H_2/CO_2$, $H_2/CO$ and $H_2/CO_2/CO$ as the feed gas respectively. Therefore, the hydrogen permeation flux decreased with decrease of hydrogen partial pressure irrespective of temperature and pressure when $H_2/CO_2$, $H_2/CO$ and $H_2/CO_2/CO$ mixture applied as feed gas respectively and permeation fluxes were satisfied with Sievert's law in different feed conditions. It was found from XRD results after permeation test that the Pd-coated $V_{53}Ti_{26}Ni_{21}$ alloy membrane had good stability and durability for various mixtures feeding condition.

• Proceedings of the Korea Society for Energy Engineering kosee Conference
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• 1996.04a
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• pp.107-110
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• 1996

연료전지 발전방식중 용융탄산염형 연료전지 발전방식은 동작온도가 $650^{\circ}C$의 고온에서 동작되기 때문에 발전효율이 높고 석탄가스를 연료로 사용할 수 있으며 또한 배기가스를 이용하여 복합발전시스템으로 구성할 수 있는 등 전력사업에 적용가능성이 가장 큰 새로운 발전방식이다. 이와 같은 이유로 전력연구원에서 개발하고 있는 2kW급 용융탄산염형 스택은 전극유효면적이 1,000$ extrm{cm}^2$인 단위전지를 20단 적층한 Co Flow형 MCFC스택으로, 연료로, 연료극에 H2, CO2, H2O 혼합가스를 그리고 산소극에는 공기, CO2 혼합가스를 이용하여 150A 정부하 상태에서 초기성능이 전압 14.28V, 출력 2.142W의 발전 운전시험에 성공하였고 이때 스택의 단위전지 평균전압은 0.714V를 나타내었다.

• 한국신재생에너지학회:학술대회논문집
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• 2009.06a
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• pp.817-820
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• 2009

Research on usage of syngas produced by waste gasification is on going all around the world. Syngas which consists of $H_2$, CO, $CO_2$, $N_2$, has different combustion characteristics from current city gas; due to distinct flame propagation speed of the fuel, syngas has different spark timing and air fuel ratio at maximum generating efficiency. This is why finding both the optimum point of spark timing and air fuel ratio is so important in order to improve thermo efficiency and secure stable running of gas generated by relatively low heating value syngas. Moreover, since emission of $NO_x$ is strictly regulated, it is important to operate lean burn condition that reduces NOx emission.

• Membrane Journal
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• v.23 no.1
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• pp.1-11
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• 2013

Poly(ether imide) (PEI)-poly(dimethylsioxane) (PDMS) composite membranes and their modules were prepared, which are capable of selective $CO_2$ separation from the mixture gas. The gas flow rate, concentration, recovery ratio of $H_2$ and removal ratio of $CO_2$ outflowing by stage-cut were characterized at $25^{\circ}C$ and the constant pressure. In addition, to increase the recovery ratio of $H_2$, one stage, two stage series connection, and three stages series + parallel connection tests were carried out. When the stage-cut was 0.32 for the three stages connection operation, the concentration $H_2$ of the produced gas and the recovery ratio of $H_2$ was 97% and 85%, respectively. And also the removal ratio of $CO_2$ was 90% was obtained and the recycled gas concentration was similar with that of the feed gases.

• Transactions of the Korean Society of Mechanical Engineers B
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• v.27 no.2
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• pp.227-235
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• 2003

The WSGG-based narrow band model was employed to solve the radiative transfer equations along isothermal and non-isothermal paths through $CO_2-H_2O-N_2$ gas mixtures at 1 atm. When the WSGGM is applied for arbitrary gas mixtures by considering the multiplication property of transmissivity in overlapping bands, the number of gray gases is significantly increased. To reduce the computation time, three different regrouping methods for the gray gases are tested in obtaining the mean absorption coefficient for each gray gas group. Among them, the regrouping method by minimizing the regrouping error shows the best results. For the isothermal media, 10 gray gases show fairly good agreement with the results by statistical narrow band(SNB) model which are regarded as reference solutions. For non-isothermal media, 20 gray gases show good agreement with reference solutions.

• Membrane Journal
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• v.22 no.1
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• pp.16-22
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• 2012

The influence of co-existing gases on the hydrogen permeation without sweep gas was studied through a Pd-coated $V_{99.8}B_{0.2}$ alloy membrane. Membranes have been investigated in the pressure range 1.5-8.0 bar under pure hydrogen, hydrogen-carbon dioxide and hydrogen-carbon monoxide gas mixture without sweep gas at $400^{\circ}C$. Preliminary hydrogen permeation experiments without sweep gas have been confirmed that hydrogen flux was $40.7mL/min/cm^2$ for a Pd-coated $V_{99.8}B_{0.2}$ alloy membrane (thick : 0.5 mm) using pure hydrogen as the feed gas. In addition, hydrogen flux was $21.4mL/min/cm^2$ for $V_{99.8}B_{0.2}$ alloy membrane using $H_2/CO_2$ as the feed gas. The hydrogen permeation flux decreased with decrease of hydrogen partial pressure irrespective of pressure when $H_2/CO_2$and $H_2/CO$mixture applied as feed gas respectively and permeation fluxes were satisfied with Sievert's law in different feed conditions. It was found from XRD, SEM/EDX results after permeation test that the Pd-coated $V_{99.8}B_{0.2}$ alloy membrane had good stability and durability for various mixtures feeding condition.