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Analysis of the Deformed Unit Cell by Clamping Force Through the FEM and CFD Interaction (FEM과 CFD 연동을 통한 스택 체결 시 압력에 의해 변형된 단위 전지 해석)

  • YOO, BIN;LIM, KISUNG;JU, HYUNCHUL
    • Transactions of the Korean hydrogen and new energy society
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    • v.32 no.4
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    • pp.228-235
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    • 2021
  • Polymer electrolyte membrane fuel cells (PEMFC) are currently being used in various transport applications such as drones, unmanned aerial vehicles, and automobiles. The power required is different according to the type of use, purpose, and the conditions adjusted using a cell stack. The fuel cell stack is compressed to reduce the size and prevent fuel leakage. The unit cells that make up the cell stack are subjected to compression by clamping force, which makes geometrical changes in the porous media and it impacts on cell performance. In this study, finite elements method (FEM) and computational fluid dynamics (CFD) analysis for the deformed unit cell considering the effects of clamping force is performed. First, structural analysis using the FEM technique over the deformed gas diffusion layer (GDL) considering compression is carried out, and the resulting porosity changed in the GDL is calculated. The PEMFC model is then verified by a three-dimensional, two-phase fuel cell simulation applying the physical properties and geometry obtained before and after compression. The detailed simulation results showed different concentration distributions of fuel between the original and deformed geometry, resulting in the difference in the distribution of current density is represented at compressed GDL region with low oxygen concentration.

A Study on the Characteristics of Temperature Distribution Related to Geometry of Tube in Hydrogen Storage Vessel (수소 저장용 탱크의 튜브 형상에 따른 온도분포 특성에 대한 수치해석 연구)

  • OH, SEUNG JUN;YOON, JEONG HWAN;JEON, KYUNG SOOK;KIM, JAE KYU;PARK, JOON HONG;CHOI, JEONGJU
    • Transactions of the Korean hydrogen and new energy society
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    • v.32 no.4
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    • pp.205-211
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    • 2021
  • Recently, it is necessary for study on renewable energy due to environmental pollution and fossil fuel depletion. Therefore, in this study, the filling temperature according to the nozzle geometry was evaluated based on the limit temperature specified in SAEJ2601 for charging hydrogen, a new energy. There are three types of nozzles, normal, angle and round, fixed the average pressure ramp rate at 52.5 MPa/min, and the injection temperature was set at 293.4 K. As a result, the lowest temperature distribution was found in the round type, although the final temperature did not differ significantly in the three types of nozzles. In addition, Pearson's coefficient was calculated to correlate the mass flow rate with the heat transfer rate at the inner liner wall, which resulted in a strong linear relationship of 0.98 or higher.

Hydriding Kinetics on Mg2NiHx-5wt% CaO Composites (Mg2NiHx-5wt% CaO 복합재료의 수소화 속도)

  • SHIN, HYO-WON;HWANG, JUNE-HYEON;KIM, EUN-A;HONG, TAE-WHAN
    • Transactions of the Korean hydrogen and new energy society
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    • v.32 no.3
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    • pp.156-162
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    • 2021
  • Mg hydride has a relatively high hydrogen storage amount of 7.6wt%, and inexpensive due to abundant resources, but has high reaction temperature and long reaction time because of treble oxidation reactivity and upper activation energy. Their range of applications could be further extended if their hydrogenation kinetics and degradation behavior could be improved. Therefore, the effect of CaO has improved the hydrogenation kinetics and slowed down the degradation. This study focused on investigating whether to improve the hydrogenation kinetics by synthesizing Mg2NiHx-5wt% CaO composites. The Mg2NiHx-5wt% CaO composites have been synthesized by hydrogen induced mechanical alloying. The synthesized composites were characterized by performing X-ray diffraction, Scanning Electron Microscopy, Brunauer-Emmett-Teller, Thermogravimetric, and Sivert's type automatic pressure-composition-temperature analysis. Hydriding kinetics were performed using an automatic PCT measurement system and evaluated over the temperature range of 423 K, 523 K, and 623 K. As a result of calculating the hydrogen adsorption amount through the hydrogenation kinetics curve, it was calculated as about 0.42wt%, 0.91wt%, and 1.15wt%, the highest at 623 K and the lowest at 423 K.

Study of Cooling Characteristics of 18650 Li-ion Cell Module with Different Types of Phase Change Materials (PCMs) (PCM 종류에 따른 18650 리튬-이온 셀 모듈의 냉각 특성 연구)

  • YU, SIWON;KIM, HAN-SANG
    • Transactions of the Korean hydrogen and new energy society
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    • v.31 no.6
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    • pp.622-629
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    • 2020
  • The performance and cost of electric vehicles (EVs) are much influenced by the performance and service life of the Li-ion battery system. In particular, the cell performance and reliability of Li-ion battery packs are highly dependent on their operating temperature. Therefore, a novel battery thermal management is crucial for Li-ion batteries owing to heat dissipation effects on their performance. Among various types of battery thermal management systems (BTMS'), the phase change material (PCM) based BTMS is considered to be a promising cooling system in terms of guaranteeing the performance and reliability of Li-ion batteries. This work is mainly concerned with the basic research on PCM based BTMS. In this paper, a basic experimental study on PCM based battery cooling system was performed. The main purpose of the present study is to present a comparison of two PCM-based cooling systems (n-Eicosane and n-Docosane) of the unit 18650 battery module. To this end, the simplified PCM-based Li-ion battery module with two 18650 batteries was designed and fabricated. The thermal behavior (such as temperature rise of the battery pack) with various discharge rates (c-rate) was mainly investigated and compared for two types of battery systems employing PCM-based cooling. It is considered that the results obtained from this study provide good fundamental data on screening the appropriate PCMs for future research on PCM based BTMS for EV applications.

Characterization of NiO and Co3O4-Doped La(CoNi)O3 Perovskite Catalysts Synthesized from Excess Ni for Oxygen Reduction and Evolution Reaction in Alkaline Solution (과량의 니켈 첨가로 합성된 NiO와 Co3O4가 도핑된 La(CoNi)O3 페로브스 카이트의 알칼리용액에서 산소환원 및 발생반응 특성)

  • BO, LING;RIM, HYUNG-RYUL;LEE, HONG-KI;PARK, GYUNGSE;SHIM, JOONGPYO
    • Transactions of the Korean hydrogen and new energy society
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    • v.32 no.1
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    • pp.41-52
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    • 2021
  • NiO and Co3O4-doped porous La(CoNi)O3 perovskite oxides were prepared from excess Ni addition by a hydrothermal method using porous silica template, and characterized as bifunctional catalysts for oxygen reduction reaction (ORR) and oxygen evolution reaction (OER) for Zn-air rechargeable batteries in alkaline solution. Excess Ni induced to form NiO and Co3O4 in La(CoNi)O3 particles. The NiO and Co3O4-doped porous La(CoNi)O3 showed high specific surface area, up to nine times of conventionally synthesized perovskite oxide, and abundant pore volume with similar structure. Extra added Ni was partially substituted for Co as B site of ABO3 perovskite structure and formed to NiO and Co3O4 which was highly dispersed in particles. Excess Ni in La(CoNi)O3 catalysts increased OER performance (259 mA/㎠ at 2.4 V) in alkaline solution, although the activities (211 mA/㎠ at 0.5 V) for ORR were not changed with the content of excess Ni. La(CoNi)O3 with excess Ni showed very stable cyclability and low capacity fading rate (0.38 & 0.07 ㎶/hour for ORR & OER) until 300 hours (~70 cycles) but more excess content of Ni in La(CoNi)O3 gave negative effect to cyclability.

Reaction Characteristics of WGS Catalyst for SEWGS Process in a Pressurized Fluidized Bed Reactor (가압 유동층 반응기에서 SEWGS 공정을 위한 WGS 촉매의 반응특성)

  • Kim, Ha-Na;Lee, Dong-Ho;Lee, Seung-Yong;Hwang, Taek-Sung;Ryu, Ho-Jung
    • Transactions of the Korean hydrogen and new energy society
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    • v.23 no.4
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    • pp.337-345
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    • 2012
  • To check effects of operating variables on reaction characteristics of WGS catalyst for SEWGS process, water gas shift reaction tests were carried out in a pressurized fluidized bed reactor using commercial WGS catalyst and sand(as a substitute for $CO_2$ absorbent) as bed materials. Simulated syngas(mixed with $N_2$) was used as a reactant gas. Operating temperature was $210^{\circ}C$ and operating pressure was 20 bar. WGS catalyst content, steam/CO ratio, gas velocity, and syngas concentration were considered as experimental variables. CO conversion increased as the catalyst content and steam/CO ratio increased. CO conversion at fluidized bed condition was higher than that of fixed bed condition. However, CO conversion were maintained almost same value within the fluidized bed condition. CO conversion decreased as the syngas concentration increased. The optimum operation condition was confirmed and long time water gas shift reaction test up to 24 hours at the optimum operating conditions was carried out.

Effects of Bed Insert Geometry and Shape of WGS Catalysts on CO Conversion in a Fluidized Bed Reactor for SEWGS Process (SEWGS 공정을 위한 유동층 반응기에서 내부 삽입물의 모양 및 WGS 촉매의 형상이 CO 전환율에 미치는 영향)

  • Ryu, Hojung;Kim, Hana;Lee, Dongho;Bae, Dalhee;Hwang, Taeksung
    • Transactions of the Korean hydrogen and new energy society
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    • v.24 no.2
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    • pp.150-159
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    • 2013
  • To enhance the performance of SEWGS system by holding the WGS catalyst in a SEWGS reactor using bed inserts, effects of insert geometry and shape of WGS catalysts on CO conversion were measured and investigated. Small scale fluidized bed reactor was used as experimental apparatus and WGS catalyst (particle and tablet) and sand were used as bed materials. The parallel wall type and cross type bed inserts were used to hold the WGS catalysts. The CO conversion with steam/CO ratio was determined based on the exit gas analysis. The measured CO conversion using the bed inserts showed high value comparable to physical mixing cases. Moreover, gas flow direction was confirmed by bed pressure drop measurement for each case. Most of input gas flowed through the catalyst side when we charged tablet type catalyst into the bed insert and this can cause low $CO_2$ capture efficiency because the possibility of contact between input gas and $CO_2$ absorbent is low in this case. New bed insert geometry was proposed based on the results from this study to enhance contact between input gas and WGS catalyst and $CO_2$ absorbent.

A Study on Fostering Plan for the Hydrogen Industry in Changwon City (창원시 수소 산업 2040 중장기 육성계획 수립 연구)

  • PARK, MIN-JU;KIM, HAK-MIN;GU, YUN-JEONG;JEONG, CHANG-HOON;KANG, BOO MIN;HA, SEUNG WOO;JEONG, DAE-WOON
    • Transactions of the Korean hydrogen and new energy society
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    • v.31 no.6
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    • pp.509-521
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    • 2020
  • This study aims to propose a mid- to long-term fostering plan for the hydrogen industry customized to Changwon City by reviewing the government's policy and the status of the domestic and foreign hydrogen industry. The adopted methodologies were policy analysis, literature review, field investigation, and committee operation that could consider institutions, knowledge (technology), and networking between activity subjects. The short-term projects and long-term projects for the fostering plan are established using these methodologies. The short-term projects were structured so that the ongoing hydrogen industry fostering plan leads to a successful result, and the hydrogen mobility field is expanded to not only land vehicles but also marine and air vehicles. The long-term projects consist of a high proportion of the hydrogen utilization field to take advantage of the industrial strength of Changwon City, and a support system for new and turning companies for localization of parts was added to provide industrial competitiveness.

Operation Characteristics According to Steam Temperature and Effectivenss of External Steam-Related SOEC System (외부 수증기 연계 SOEC 시스템의 공급 스팀 온도 및 열교환기 유용도에 따른 시스템 BOP 및 운전 특성 분석)

  • KIM, YOUNG SANG;LEE, YOUNG DUK;AHN, KOOK YOUNG;LEE, DONG KEUN;LEE, SANG MIN;CHOI, EUN JUNG
    • Transactions of the Korean hydrogen and new energy society
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    • v.31 no.6
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    • pp.596-604
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    • 2020
  • Solid oxide electrolysis cell (SOEC) attracts much attention because of its high energy efficiency among many water-electrolysis technologies. SOEC operates at temperatures above 700℃, so that the water required for water-electrolysis must be supplied in the form of steam. When the steam to be supplied to the SOEC is generated by the SOEC system itself, an enormous amount of latent heat is required to vaporize the water, so additional energy must be supplied to the SOEC system. On the other hand, if the steam can be supplied from the outside, a small amount of energy is required to raise the temperature of the low temperature steam, so that the SOEC system can be operated without additional energy supply from outside, which enables efficient water-electrolysis. In this study, we figure out the size of heat exchanger for various steam temperature and effectiveness of heat exchanger, and propose the energy efficiency of the system.

Recent Activities of Solid Oxide Fuel Cell Research in the 3D Printing Processes (3D 프린팅 공정을 이용한 고체 산화물 연료전지 연구 동향)

  • MASAUD, ZUBAIR;KHAN, MUHAMMAD ZUBAIR;HUSSAIN, AMJAD;ISHFAQ, HAFIZ AHMAD;SONG, RAK-HYUN;LEE, SEUNG-BOK;JOH, DONG WOO;LIM, TAK-HYOUNG
    • Transactions of the Korean hydrogen and new energy society
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    • v.32 no.1
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    • pp.11-40
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    • 2021
  • Solid oxide fuel cell (SOFC) has received significant attention recently because of its potential for the clean and efficient power generation. The current manufacturing processes for the SOFC components are somehow complex and expensive, therefore, new and innovative techniques are necessary to provide a great deal of cell performance and fabricability. Three-dimensional (3D) printing processes have the potential to provide a solution to all these problems. This study reviews the literature for manufacturing the SOFC components using 3D printing processes. The technical aspects for fabrication of SOFC components, 3D printing processes optimization and material characterizations are discussed. Comparison of the SOFC components fabricated by 3D printing to those manufactured by conventional ceramic processes is highlighted. Further advancements in the 3D printing of the SOFC components can be a step closer to the cost reduction and commercialization of this technology.