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Development and Demonstration of 150W Fuel Cell Propulsion System for Unmanned Aerial Vehicle (UAV) (무인항공기용 150W급 연료전지 동력원 개발 및 실증)

  • Yang, Cheol-Nam;Kim, Yang-Do
    • Transactions of the Korean hydrogen and new energy society
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    • v.23 no.4
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    • pp.300-309
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    • 2012
  • Long endurance is a key issue in the application of unmanned aerial vehicles. This study presents feasibility test results when fuel cell system as an alternative to the conventional engine is applied for the power of the UAV after the 150W fuel cell system is developed and packaged to the 1/4 scale super cub airplane. Fuel cell system is operated by dead-end method in the anode part and periodically purged to remove the water droplet in flow field during the operation. Oxygen in the air is supplied to the stack by the two air blowers. And fuel cell stack is water cooled by cooling circuit to dissipate the heat generated during the fuel cell operation. Weight balance is considered to integrate the stack and balance of plant (BOP) in package layout. In flight performance test, we demonstrated 4 times standalone take-off and landing. In the laboratory test simulating the flight condition to quantify the energy flow, the system is analyzed in detail. Sankey diagram shows that electric efficiency of the fuel cell system is 39.2%, heat loss 50.1%, parasitic loss 8.96%, and unreacted purged gas 1.67%, respectively compared to the total hydrogen input energy. Feasibility test results show that fuel cell system is high efficient and appropriate for the power of UAV.

Operation Results of a 5kW-Class SOFC System Composed of 2 Sub-Module Stacks (2 모듈 스택을 이용한 5kW급 SOFC 시스템 운전결과)

  • Lee, Tae-Hee;Choi, Mi-Hwa;Yoo, Young-Sung
    • Transactions of the Korean hydrogen and new energy society
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    • v.22 no.5
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    • pp.609-615
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    • 2011
  • A 5 kW class SOFC system for cogeneration power units was consisted of a hot box part and cold BOPs. High temperature components such as a stack, a fuel reformer, a catalytic combustor, and heat exchanges are arranged in the bot box considering their operating temperatures for the system efficiency. The hot box was made of ceramic boards for the thermal insulation. A 5 kW class SOFC stack was composed of 2 sub-modules and each module had 64 cells with $15{\times}15cm^2$ area and stainless steel interconnects. The 5 kW class SOFC system was operated with a hydrogen and a city gas. With a hydrogen, the total power of the stacks was about 7.1 kWDC and electrical efficiency was about 49.3% at 80 A. With a city gas, the total power of the stacks was about 5.7 $kW_{DC}$ and electrical efficiency was about 38.8% at 60 A. Under self-sustained operating condition, the system efficiency including a power conditioning loss and a consumed power by BOPs was about 30.2%.

Catalytic Activity Tests in Gas-Liquid Interface over Cu-ZnO/Al2O3 Catalyst for High Pressure Water-Gas-Shift Reaction (고압 WGS 반응을 위한 Cu-ZnO/Al2O3 촉매상에서 기-액 계면 촉매 반응 특성 연구)

  • Kim, Se-Hun;Park, No-Kuk;Lee, Tae-Jin
    • Transactions of the Korean hydrogen and new energy society
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    • v.22 no.6
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    • pp.905-912
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    • 2011
  • In this study, the novel concept catalytic reactor was designed for water-gas shift reaction (WGS) under high pressure. The novel concept catalytic reactor was composed of an autoclave, the catalyst, and liquid water. Cu-ZnO/$Al_2O_3$ as the low temperature shift catalyst was used for WGS reaction. WGS in the novel concept catalytic reactor was carried out at the ranges of 150~$250^{\circ}C$ and 30~50 atm. The liquid water was filled at the bottom of the autoclave catalytic reactor and the catalyst of pellet type was located at the gas-liquid water interface. It was concluded that WGS reaction occurred over the surface of catalysts partially wetted with liquid water. The conversion of CO for WGS was also controlled with changing content of Cu and ZnO used as the catalytic active components. Meanwhile, the catalyst of honey comb type coated with Cu-ZnO/$Al_2O_3$ was used in order to increase the contact area between wet-surface of catalyst and the reactants of gas phase. It was confirmed from these experiments that $H_2$/CO ratio of the simulated coal gas increased from 0.5 to 0.8 by WGS at gas-liquid water interface over the wet surface of honey comb type catalyst at $250^{\circ}C$ and 50 atm.

Safety Analysis of a Hydrogen Isotopes Process (수소동위원소 공정 안전해석)

  • Chung, Hong-Suk;Kang, Hyun-Goo;Chang, Min-Ho;Cho, Seung-Yon;Kim, Won-Kuk;Nam, Jae-Yeon;Kim, Duk-Jin;Song, Kyu-Min;Paek, Seung-Woo;Koo, Dae-Seo;Chung, Dong-You;Lee, Jeong-Min;Kim, Chang-Shuk;Jung, Ki-Jung;Yun, Sei-Hun
    • Transactions of the Korean hydrogen and new energy society
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    • v.23 no.3
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    • pp.219-226
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    • 2012
  • A nuclear fusion fuel cycle plant is composed of various subsystems such as a hydrogen isotope storage and delivery system, a tokamak exhaust processing system, and a hydrogen isotope separation system. Korea shares in the construction of the International Thermonuclear Experimental Reactor fuel cycle plant with the EU, Japan and US, and is responsible for the development and supply of the storage and delivery system. We thus present details on the hydrogen isotope process safety. The main safety analysis procedure is to use a hazard and operability study. Nine segments were studied how the plant might deviate from its design purpose. We present a detailed description of the process, examine every part of it to determine how deviations from the design intent can occur and decide whether these deviations can give rise to hazards. We determine possible causes and note protective systems, evaluate the consequences of the deviation, and recommend actions to achieve our safety goal.

Chemical Looping Combustion Characteristics of Coal and Char in a Batch Type Fluidized Bed Reactor (회분식 유동층 반응기에서 석탄과 촤의 매체순환연소 특성)

  • Ryu, Ho-Jung;Hyun, Ju-Soo;Kim, Young-Joo;Park, Yeong-Seong;Park, Moon-Hee
    • Transactions of the Korean hydrogen and new energy society
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    • v.22 no.6
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    • pp.884-894
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    • 2011
  • Effects of temperature, volatile content, particle diameter and solid input weight were investigated in the batch fluidized bed reactor using OCN703-1100 particle as oxygen carrier and Roto coal and char as fuels. Two solid fuels represented the best reactivity at different temperature, $900^{\circ}C$ for Roto coal and $950^{\circ}C$ for char, respectively. However, we selected $900^{\circ}C$ as the best operating temperature because the improvement of reactivity of char at $950^{\circ}C$ was negligible. Char represented better reactivity than Roto coal because char contains low volatile than Roto coal. For both solid fuels, reactivities were improved with increasing of the particle diameter. These results were explained by solid mixing tests in a transparent fluidized bed using two char particles having different particle size ranges and OCN703-1100 particle. The bigger particle showed better solid mixing with OCN703-1100 particle, and therefore, represented better reactivity. For both solid fuels, reactivities were improved with increasing of the solid input weight within the experimental conditions of this study because the weight of coarse particles increased with the solid input weight increased, and therefore, these coarse particles can mix well with the oxygen carrier.

Hydrogen Production from Hyperthermophilic Archaebacteria Thermococcus onnurineus NA1 (초고온성 고세균 Thermococcus onnurineus NA1에 의한 수소생산)

  • Kim, Ok-Sun;Na, Jeong-Geol;Kim, Hae-Jin;Rhee, Young-Woo;Kim, Mi-Sun
    • Transactions of the Korean hydrogen and new energy society
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    • v.22 no.5
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    • pp.671-677
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    • 2011
  • A hyperthermophilic archaeon, $Thermococcus$ $onnurineus$ NA1 was studied to investigate its fermentation characteristics using various carbon sources including formate, maltose and carbon monoxide during the anaerobic batch cultivation at $80^{\circ}C$. Formate was the best carbon source for cell growth and hydrogen production among others. In the batch culture on formate, it was found that the cell concentration increased exponentially by 12 hrs of culture, after which the cell growth and formate consumption was retarded. Hydrogen production was continued more than 24 hrs although the cell growth was ceased at 18 hrs. Hydrogen production rate was directly correlated with the cell growth and formate degradation up to 18 hrs, and the average hydrogen production yield was 1.05 mole-$H_2$/mole-formate. Cell growth and hydrogen production were optimized at the initial pH 6-7, while inhibited at the initial pH lower than 5 and higher than 9.

Development of the SiO2/Nano Ionomer Composite Membrane for the Application of High Temperature PEMFC (전기방사를 이용한 SiO2/nano ionomer 복합 막의 제조 및 고온 PEMFC에의 응용)

  • Na, Hee-Soo;Hwang, Hyung-Kwon;Lee, Chan-Min;Shul, Yong-Gun
    • Transactions of the Korean hydrogen and new energy society
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    • v.22 no.5
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    • pp.569-578
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    • 2011
  • The $SiO_2$ membranes for polymer electrolyte membrane fuel cell (PEMFC) are preapared by electrospinning method. It leads to high porosity and surface area of membrane to accommodate the proton conducting materials. The composite membrane was prepared by impregnating of Nafion ionomer into the pores of electrospun $SiO_2$ membranes. The $SiO_2$:heteropolyacid (HPA) nano-particles as a inorganic proton conductor were prepared by microemulsion process and the particles are added to the Nafion ionomer. The characterization of the membranes was confirmed by field emission scanning electron microscope (FE-SEM), thermogravimetry analysis (TGA), and single cell performance test for PEMFC. The Nafion impregnated electrospun $SiO_2$ membrane showed good thermal stability, satisfactory mechanical properties and high proton conductivity. The addition of the $SiO_2$:HPA nano-particle improved proton conductivity of the composite membrane, which allow further extension for operation temperature in low humidity environments. The composite membrane exhibited a promising properties for the application in high temperature PEMFC.

An Analysis on Stainless Steel for Hydrogen Generator' Pipeline Interacting with Alkaline Solution (알칼리 용액이 수소배관으로 사용되는 Stainless steel에 미치는 영향 분석)

  • Byun, Chang-Sub;Choi, Jin-Young;Lim, Soo-Gon;Hwang, Gab-Jin;Choi, Ho-Sang;Shin, Hoon-Kyu
    • Transactions of the Korean hydrogen and new energy society
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    • v.23 no.3
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    • pp.207-212
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    • 2012
  • This study was performed to observe the change of stainless steel pipe interacting with alkaline solution. We used STS316L and STS304 as samples which were soaked in alkaline solution. We measured the samples by use of FE-SEM, EDX, SIMS to observe the surface and depth profile of both samples. The result showed that the precipitate appeared on the surface of both samples from 5 days. but the precipitate was confirmed to be decreased as time passes. but the quantitative change of precipitates at both samples was different as time passed. The EDX showed that the precipitate is Potassium from solution of Electrolysis. The result also showed that the primary elements of stainless steel pipeline and of Alkaline Solution were changed. The change of primary elements was severe between 5 days to 16 days and was stable around 40 days at both samples. The reaction of STS316L with alkaline solution was lower than STS304. We hoped that this study would be the foundation of developing the electrode of the alkaline hydrogen generator.

A Study of Methane Oxidation over Transition Metal (TM)/CeO2 (TM=Ni, Co, Cu, Fe) (전이금속이 담지된 세리아의 메탄 산화 반응에 대한 연구)

  • Ahn, Ki-Yong;Chung, Yong-Chae;Lee, Jong-Ho
    • Transactions of the Korean hydrogen and new energy society
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    • v.23 no.4
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    • pp.346-352
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    • 2012
  • The properties of methane oxidation were studied in this research over transition metal containing $CeO_2$ (TM/$CeO_2$, TM=Ni, Co, Cu, Fe) with TM content of 5 wt. % at atmospheric pressure. The characteristics of catalysts were investigated by various characterization techniques, including XRD, GC, SEM and EPMA analyses. The catalytic tests were carried out in a fixed Rmix ratio of 1.5 ($CH_4/O_2$) in a fixed-bed reactor operating isothermally at atmospheric pressure. Only the Ni/$CeO_2$ catalysts showed syngas production above $400^{\circ}C$ via typical partial oxidation reaction whereas other catalysts induced complete oxidation resulting in the production of $CO_2$ and $H_2O$ in whole reaction temperature range. From the quantitative analysis on carbon deposition after catalytic tests, Cu/$CeO_2$ was found to show the highest resistance on carbon deposition. Therefore Cu can be proposed as an efficient catalyst element which can be combined with a conventional Ni-based SOFC anode to enhance the carbon tolerance.

Effect of SOx on HC-SCR Kinetics over Ag/Al2O3 Catalyst (SOx 함유 HC-SCR에서 산처리 Ag/Al2O3 촉매의 반응 특성)

  • Lee, Ju-Heon;Park, Jeong-Whan;Kim, Seong-Soo;Yoo, Seung-Joon;Kim, Jin-Gul
    • Transactions of the Korean hydrogen and new energy society
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    • v.22 no.5
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    • pp.714-720
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    • 2011
  • Ethanol was used as reducing agent to remove $NO_x$ exhaust from the stationary source. Pre-treatment with sulfuric acid over $Ag/Al_2O_3$ catalyst was dedicated to overcome the $SO_2$ poisoning effect. The $NO_x$ reduction experiment was performed under the simulated condition of power plant The increased surface area with higher CPSI devoted to increase de-$NO_x$ yield. De-$NO_x$ yield of the $NO_x$ exhaust containing 20 ppm of $SO_2$ increased after acid treatment with 0.7% $H_2SO_4$ over 4.0% $Ag/Al_2O_3$, where the increased dispersion of Ag found from the results of XRD and XPS was the dominant factor for the increased de-$NO_x$ yield. However, the reason for the decreased de-$NO_x$ yield with the acid treatment of higher concentration (1.0% and 2.0%) of $H_2SO_4$ was found to be due to the formation of $Ag_2SO_4$ crystallites found from XRD result. Acid-treated $Ag/Al_2O_3$ catalyst showed maximum de-$NO_x$ yield at higher temperature than non-treated $Ag/Al_2O_3$ catalyst did.