• 대한전기학회:학술대회논문집
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• 대한전기학회 1996년도 하계학술대회 논문집 C
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• pp.1409-1411
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• 1996

Direct Methanol Fuel Cell(DMFC) using Pt-Ru electrocatlayst and Nafion menbrane can provide high performance if operating conditions are well designed. In this study, operating temperature, pressure, and fuel flow rate were changed to obtain optimum operating conditions of DHFC single cell. Performance of DMFC were increased by the increase of operating temperature. The concentration of fuel methanol was 2.0M $CH_{3}OH$ and pressure difference of cathode and anode was 2 atm were showed maximum performance of DMFC single cell with showing the current density of 160 $mA/cm^2$ at 0.2V cell voltage.

• Journal of Electrochemical Science and Technology
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• 제7권2호
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• pp.146-152
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• 2016

A combined system with PEMFC and reformer is introduced and optimized for the real use of this kind of system in the future. The hydrogen source to operate the PEMFC system is methanol, which needs two parts of methanol reforming reaction and preferential oxidation (PROX) for the hydrogen fuel process in the combined operation PEMFC system. With the optimized methanol steam reforming condition, we tested PROX reactions in various operation temperature from 170 to 270 ℃ to investigate CO concentration data in the reformed gases. Using these different CO concentration, PEMFC performances are achieved at the combined system. Pt/C and Ru promoted Pt/C were catalysts were used for the anode to compare the stability in CO contained gases. The alloy catalyst of PtRu/C shows higher performance and better resistance to CO than the Pt/C at even high CO amount of 200 ppm, indicating a promotion not only to the activity but also to the CO tolerance. Furthermore, in a system point of view, there is a fluctuation in the PEMFC operation due to the unstable fuel supply. Therefore, we also modified the methanol reforming by a scaled up reactor and pressurization to produce steady operation of PEMFC. The optimized system with the methanol reformer and PEMFC shows a stable performance for a long time, which is providing a valuable data for the PEMFC commercialization.

• 멤브레인
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• 제13권3호
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• pp.191-199
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• 2003

본 연구는 직접메탄을 연료전지(Direct Methanol Fuel Cell, DMFC)용 전해질 막으로 이용되는 양이온교환막의 개발에 관한 것이다. 투과증발공정에서 메탄을 Barrier로 잘 알려져 있는 Poly(vinyl alcohol)을 Base polymer로 사용하고 양이온 교환기가 포함되어 있는 Poly(acrylic acid)를 가교제로 사용하여 가교제의 함량변화에 따른 메탄을 투과도(Methanol permeability), 이온전도도(Ion conductivity), 이온교환용량(Ion exchange capacity), 함수율(Water content), 고정이온농도(Fixed ion concentration)를 통해 막 특성을 측정하였다. 메탄올 투과도와 이온전도도는 가교제인 PAA함량이 증가함에 따라 감소하다가 15%이상에서는 증가하는 경향을 보였다. 이것은 가교제의 함량증가로 인한 가교의 영향과 가교제에 포함되어 있는 친수성기의 도입으로 이와 같은 결과가 나타난다고 예상된다. 실험결과를 통해 DMFC에 적용가능성이 있는 막은 $25^{\circ}C,\; 50^{\circ}C$에서의 메탄을 투과도가 $6.49{\times}10^{-8}/cm^2/s,\; 2.85{\times}10^{-7}/cm^2/s$, $25^{\circ}C,\; 50^{\circ}C$에서의 이온전도도가 $2.66{\times}10^{-3}\;S/cm,\; 9.16{\times}10^{-3}\;S/cm,$ 이온교환용량이 1.32 meq/g membrane, 함수율이 0.25 g $H_2O$/g membrane, 고정이온농도가 5.25 meq/g $H_2O$인 PVA/PAA-$160^{\circ}C$ 15% 막으로 예측된다.

• 멤브레인
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• 제15권1호
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• pp.1-7
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• 2005

Sulfunated poly(ether ether ketone) (SPEEK) (60%)와 Poly(ether sulfone) (PES) (40%)의 블렌드에 다양한 종류의 polysilsesquioxane (PSQ)구를 첨가하여 전해질 막을 제조하였다. 이 때 PSQ구의 양은 10 wt%로 고정하였다. 제조된 막을 사용하여 PSQ 구의 종류에 따른 메탄올 투과도, 수소 이온 전도도, 그리고 이온 교환 용량의 변화를 측정한 결과 모든 경우에 있어서 수소 이온 전도도와 메탄올 투과도가 Nafion 117보다 낮았으며 PSQ 구를 함유하지 않은 SPEEK/PES(6:4) 블렌드보다는 높았다. 특히, MS64구와 VTMOS구를 포함한 전해질 막의 경우에는 수소 이온 전도도와 메탄올 투과도의 비로 나타내는 선택도가 25℃에서 Nafion 117보다 2배 이상 높았다.

• 한국고분자학회:학술대회논문집
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• 한국고분자학회 2006년도 IUPAC International Symposium on Advanced Polymers for Emerging Technologies
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• pp.270-270
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• 2006

We have prepared polymer electrolyte membranes (PEMs) for DMFC from polymer mixture of poly(vinyl alcohol) and poly(vinyl alcohol-co-2-acrylamido-2-methylpropane sulfonic acid) (AP-2) changing the AP-2 content. The proton conductivity(${\Box}$) and methanol permeability(P) of the PEMs increase with increasing AP-2 content because the water content of the PEMs increases with increasing AP-2 content. The proton permselectivity of the PEMs, which is defined as ${\Box}={\Box}/P$, indicates higher values than that of $Nafion{(R)}$117.

• 대한전기학회:학술대회논문집
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• 대한전기학회 1999년도 하계학술대회 논문집 D
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• pp.1876-1878
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• 1999

Developed was a 5kW-class polymer electrolyte membrane fuel cell(PEMFC) system comprised of fuel cell stack, fuel processing, thermal and water management subsystems and ancillary equipments. Several large single cells have been fabricated with different gas flow field patterns and paths, and the gas flow field pattern for the stack has been determined based on the single cell performance of thin film membrane electrode assembly (MEA). The PEMFC stack was consisted of 100 cells with an electrode area of $300cm^2$, having serpentine flow pattern. Fuel processing was developed including an autothermal methanol reformer and two preferential CO oxidation reactors. The fuel processing was combined to PEMFC operation system consisted of air compressor and thermal and water management subsystems. The PEMFC stack showed performance of 5kW under the supply of $H_2$ and air, but its performance was lowered to 3.5kW under the supply of reformed gas.

• 한국막학회:학술대회논문집
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• 한국막학회 2004년도 첨단 분리막 연구동향
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• pp.123-134
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• 2004

연로로부터 화학에너지를 직접 전기에너지로 바꾸는 연료전지(Fuel Cells)중 고체형 고분자 전해질 연료전지(Polymer Electrolyte Membrane Fuel Cell: PEMFC)와 직접 메탄올 연료전지(Direct Methanol Fuel Cell: DMFC)는 효율이 높고, zero emission 가능성으로 차세대 수송용 전원으로 각광받고 있는 미래 환경친화적 에너지원이다. 수소와 산소(또는 공기)와의 반응을 이용한 것이 PEMFC이고, 수소를 연료로 쓰지 않고 액체상 메탄올을 직접 연료로 사용하는 것이 DMFC이다. (중략)

• 한국수소및신에너지학회논문집
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• 제22권1호
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• pp.42-50
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• 2011

The Montmorillonite (MMT) in the polymer matrix is expected to reduce methanol permeability due to the tortous path formed by dispersed silicate layers. However, the polymer composite membranes containing non-proton conducting inorganic particle tend to show low proton conductivity. To solve this problem, we used an ion exchange method to prepare functionalized MMT with various silane coupling agents. The modified MMT was randomly dispersed in sulfonated poly (arylene ether sulfone) (SPAES) matrix to prepare SPAES/modified MMT composite membranes. The performances of hybrid membranes for DMFCs application were investigated. The SPAES/modified composite membrane showed increased proton conductivity compared with the non-modified MMT composite membrane. However, the methanol permeability of the SPAES/modified membrane was higher than that of the non-modified MMT.

• Korean Membrane Journal
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• 제5권1호
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• pp.18-24
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• 2003

In order to improve the mechanical properties of the sulfonated polysulfone (SPSf) membranes previously synthesized in our laboratory, poly(vinyl alcohol) (PVA) was blended which is well known as the excellent physical and chemical properties. The resulting membranes blended with several molecular weight of PVA varying from 13,000 to 124,000 have been characterized to investigate the effect of PVA molecular weight in terms of ion conductivities, methanol permeabilities, water contents and ion exchange capacities for both heat treated and untreated membranes at 150$^{\circ}C$. The proton conductivity is decreased as the molecular weight of PVA increases. The plain SPSf-6.0 showed the proton conductivity of 0.078 S/cm whereas the blended membrane with M.W. 31,000 PVA indicated 0.04 S/cm. For methanol permeabilities, when PVA is added to SPAf-6.0, methanol crossover is increased because of the gain of the hydrophilicity from 3.4 to 6.5${\times}$10$\^$-6/ $\textrm{cm}^2$/s. For the annealed blended membranes (with M.W. 31,000 PVA), both the methanol corssover and proton conductivity showed very consistent values, about 2.3${\times}$10$\^$-6/ $\textrm{cm}^2$/s and 0.036 S/cm, respectively.

• 대한전기학회논문지:전기물성ㆍ응용부문C
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• 제53권4호
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• pp.218-224
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• 2004

We present a miniature Direct Methanol Fuel Cell (micro-DMFC) using platinum sputtered microcolumn electrodes with a limited amount of fuel. We use the microcolumn electrode in order to improve the power density of the micro-DMFC that consists of two electrodes and polymer electrolyte. We also design the built-in fuel chamber in the anode for the portable electronics applications. We design and fabricate both microcolumn and planar electrodes, having an identical projective area of 5mm${\times}$5mm. The diffusion current density of the microcolumn electrode is 1.73 times higher than that of the planar electrode at electrode potential of 1.1V in the half-cell test. The micro-DMFC based on the microcolumn electrodes shows the maximum power of 10.8$\pm$7.54㎼(43.23$\pm$0.16㎼/$\textrm{cm}^2$) at the projective area of 5mm${\times}$5mm, while the planar electrode micro-DMFC shows the maximum power of 0.81$\pm$0.42㎼(3.24$\pm$1.68㎼/$\textrm{cm}^2$) at the same projective area. The micro-DMFC based on the microcolumn electrodes shows 13 times higher power density that the micro-DMFC based on the planar electrodes does.