• Title/Summary/Keyword: Hydrogen production efficiency

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Hydrogen Production for PEMFC Application in Plasma Reforming System (PEMFC용 플라즈마 개질 시스템의 수소 생산)

  • Yang, Yoon Cheol;Chun, Young Nam
    • Korean Chemical Engineering Research
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    • v.46 no.5
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    • pp.1002-1007
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    • 2008
  • The purpose of this paper studied the optimal hydrogen production condition of plasma reforming system to operate the PEMFC. Plasma reforming reactor used with Ni catalyst reactor at the same time, So $H_2$ concentration increased. Also the WGS and PrOx reactor were designed to remove CO concentration under 10 ppm, because CO has effect on catalyst poisoning of PEMFC. The maximum $H_2$ production condition in plasma reforming system was S/C ratio 3.2, $CH_4$ flow rate 2.0 L/min, catalytic reactor temperature $700{\pm}5^{\circ}C$ and input power 900 W. At this time, the concentration of produced syngas was $H_2$ 70.2%, CO 7.5%, $CO_2$ 16.2%,$CH_4$ 1.8%. The hydrogen yield, hydrogen selectivity and $CH_4$ conversion rate were 56.8%, 38.1% and 92.2% respectively. The energy efficiency and specific energy requirement were 37.0%, 183.6 kJ/mol. In additional, The experiment of $CO_2/CH_4$ ratio proceeded. Also WGS reactor experiment was proceeding on optimum condition of plasma reactor and the exit concentration were $H_2$ 68%, CO 337 ppm, $CO_2$ 24.0%, $CH_4$ 2.2%, $C_2H_4$ 0.4%, $C_2H_6$ 4.1%. At this time, experiment result of PrOx reactor were $H_2$ 51.9%, CO 0%, $CO_2$ 17.3%.

Statistical Optimization of Medium for Formate-driven Bio-hydrogen Production by the Hyperthermophilic Archaeon, Thermococus onnurineus (초고온성 고세균 Thermococcus onnurineus의 개미산으로부터 바이오수소 생산을 위한 통계적 배지 최적화)

  • Lee, Sung-Mok;Kim, Tae Wan;Lee, Hyun Sook;Lee, Jung-Hyun;Kang, Sung Gyun
    • Ocean and Polar Research
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    • v.39 no.4
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    • pp.269-277
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    • 2017
  • Medium compositions for the hyperthermophilic archaeon, Thermococcus onnurineus NA1 was statistically optimized to enhance formate-driven hydrogen ($H_2$) production by using response surface methodology. From the Plackett-Burman design-based experiment, it was confirmed that among the minor components of medium such as KCl, $MgSO_4$, $NH_4Cl$, Cystein-HCl, trace elements, Fe-EDTA and $CaCl_2$, the trace elements were screened as the only positively effective components with respect to $H_2$ production. Subsequently, the optimal concentrations of the trace elements and the major components of a medium such as NaCl, yeast extract and sodium formate were determined from the five-level central composite design (CCD)-based experiment. The resulting quadratic model predicted the maximum $H_2$ production of 46.6 mmol/L in serum bottle and it was validated experimentally using the optimal medium initially supplemented with 26.70 g/L of NaCl, 9.81 g/L of sodium formate, 3.50 g/L of yeast extract and 4.59 mL/L of trace elements. From the duplicate batch cultivations in the fermentor using the optimized medium, the a maximum $H_2$ production rate up to 71.8 mmol/L/h could be obtained, which was a 65% enhanced value compared with that obtained using the control medium, showing the high efficiency of the optimized medium.

Development of MgFe2O4 as an oxygen carrier material for chemical looping hydrogen production

  • Jong Ha Hwang;Ki-Tae Lee
    • Journal of Ceramic Processing Research
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    • v.21 no.1
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    • pp.57-63
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    • 2020
  • Chemical looping hydrogen production (CLHP) is an attractive technology for H2 production due to its ability to produce H2 and capture CO2 from fossil fuels simultaneously. In this paper, we present MgFe2O4 as an oxygen carrier material with high efficiency, low cost, and stable properties for CLHP. The redox reactions occurred reversibly in the fuel, steam, and air reactor as MgFe2O4→MgO/Fe, MgO/Fe→MgO/Fe3O4, and MgO/Fe3O4→MgFe2O4, respectively. The oxygen transfer capacities of MgFe2O4 for 5% H2/N2 and 5% CO/N2 gases were about 23 wt% at 900 ℃. Both the oxygen transfer capacity and rate were well maintained during 10 redox cycles at 900 ℃. No phase changes or agglomeration occurred as the redox cycle number increased. Similarly, MgFe2O4 did not exhibit significant degradation in its total amount or maximum rate of H2 production during four redox cycles. The average calculated amount of H2 production for MgFe2O4 was 2,806 L/day per unit mass (kg).

Photoelectrochemical Water Oxidation and $CO_2$ Conversion for Artificial Photosynthesis

  • Park, Hyunwoong
    • Proceedings of the Korean Vacuum Society Conference
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    • 2013.08a
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    • pp.70-70
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    • 2013
  • As the costs of carbon-footprinetd fuels grow continuously and simultaneously atmospheric carbon dioxide concentration increases, solar fuels are receiving growing attention as alternative clean energy carriers. These fuels include molecular hydrogen and hydrogen peroxide produced from water, and hydrocarbons converted from carbon dioxide. For high efficiency solar fuel production, not only light absorbers (oxide semiconductors, Si, inorganic complexes, etc) should absorb most sunlight, but also charge separation and interfacial charge transfers need to occur efficiently. With this in mind, this talk will introduce the fundamentals of solar fuel production and artificial photosynthesis, and then discuss in detail on photoelectrochemical (PEC) water splitting and CO2 conversion. This talk largely divides into two section: PEC water oxidation and PEC CO2 reduction. The former is very important for proton-coupled electron transfer to CO2. For this oxidation, a variety of oxide semiconductors have been tested including TiO2, ZnO, WO3, BiVO4, and Fe2O3. Although they are essentially capable of oxidizing water into molecular oxygen, the efficiency is very low primarily because of high overpotentials and slow kinetics. This challenge has been overcome by coupling with oxygen evolving catalysts (OECs) and/or doping donor elements. In the latter, surface-modified p-Si electrodes are fabricated to absorb visible light and catalyze the CO2 reduction. For modification, metal nanoparticles are electrodeposited on the p-Si and their PEC performance is compared.

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Numerical Study on Geometries and Operating Parameters of a Steam Reformer for Hydrogen Production (수소 생산을 위한 수증기 개질기의 형상 변화와 작동 조건에 대한 수치해석 연구)

  • Byun, Kang-Soo;Lee, Jae-Seong;Kim, Ho-Young
    • Journal of the Korean Society of Combustion
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    • v.16 no.3
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    • pp.1-11
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    • 2011
  • The main objective of this paper is to investigate characteristic of steam reformer at various geometries and operating conditions. In this paper, the steam reforming is studied by a numerical method and three dimensional simulations were used for effective analytical study. User - Defined Function (UDF) was used to simultaneously calculate reforming and combustion reaction. And the numerical model is validated with experimental results at the same operating conditions. In order to understand the relationship between operating conditions such as gas hourly space velocity(GHSV), mass flow rate of combustor inlet, various numerical investigations are carries out for various geometries. Numerical results show that cylindrical geometry is more effective than rectangular geometry for heat transfer to reactors and reforming efficiency. As mass flow rate of combustor inlet increase, reaction occurs more faster and temperature increase with each geometry. On the other hand, reaction and hydrogen conversion decrease as mass flow rate of reactor decreases.

Adsorptive removal of odour substances and NO and catalytic esterification using empty fruit bunch derived biochar

  • Lee, Hyung Won;Kim, Jae-Kon;Park, Young-Kwon
    • Carbon letters
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    • v.28
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    • pp.81-86
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    • 2018
  • Empty fruit bunch (EFB) char was used to remove $NO_x$ and odorous substances. The physicochemical properties of the EFB chars were altered by steam or KOH treatments. The Brunauer-Emmett-Teller surface area and porosity were measured to determine the properties of the modified EFB chars. The $deNO_x$ and adsorption test for hydrogen sulphide and acetaldehyde were performed to determine the feasibility of the modified EFB chars. The KOH-treated EFB (KEFB) char revealed higher $deNO_x$ efficiency than with commercial activated carbon. The Cu-impregnated EFB char also had high $deNO_x$ efficiency at temperatures higher than $150^{\circ}C$. The KEFB char showed the highest hydrogen sulphide and acetaldehyde adsorption ability, followed by the steam-treated EFB char and untreated EFB char. Moreover, the product prepared by sulfonation of EFB char showed excellent performance for esterification of palm fatty acid distillate for biodiesel production.

A Study on the Efficiency Improvement of the Power Generation Process Using New Working Fluids Composed of Methane, Ethylene, Ethane, and Propane and the Cold Heat Contained in the Liquefied Natural Gas (메탄, 에틸렌, 에탄 및 프로판으로 구성된 새로운 작동 유체와 액화 천연가스의 냉열을 활용한 발전 공정의 효율 향상에 대한 연구)

  • JUNGHO CHO
    • Journal of Hydrogen and New Energy
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    • v.35 no.3
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    • pp.318-323
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    • 2024
  • In this paper, computer modeling works have been performed for the power generation Rankine cycle using new working fluids and liquefied natural gas (LNG) cold heat. PRO/II with PROVISION released January 2023 from AVEVA company was used, and Peng-Robinson equation of the state model with Twu's alpha function was selected for the modeling of the power generation cycle. Optimal working fluid composition was determined to maximize LNG cold heat to increase power generation efficiency and net power production.

Characteristics of Hydrogen Production from Methanol and Ethanol Using Plasma Reactor and Ozone Decomposition Catalyst (플라즈마 리액터 및 오존분해 촉매를 이용한 메탄올 및 에탄올로부터 수소발생특성)

  • Koo, Bon-Kook;Kim, Yong-Chun;Jang, Mun-Gug;Kim, Jong-Hyun;Park, Jae-Youn;Han, Sang-Bo
    • Journal of the Korean Institute of Illuminating and Electrical Installation Engineers
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    • v.25 no.10
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    • pp.116-124
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    • 2011
  • In this work, the effect of the initial concentration of methanol and ethanol, and the addition of oxygen molecules were discussed to improve the hydrogen generation using non-thermal plasma reactor effectively. In addition, the effect of ozone decomposition catalyst of manganese dioxide and its quantity was investigated. First, hydrogen concentration increased until an initial concentration of about 40,000[ppm] of methanol and thereafter it was saturated. Henceforth, hydrogen concentration decreased with increasing the oxygen percent on the carrier gas of nitrogen about both substances. Related with the effect of catalyst, it increased upto 60[g], but it was not changed largely after that. Consequently, it is confirmed that the hybrid process using plasma process and catalytic surface chemical reaction is a very promising way to increase the efficiency of hydrogen generation as investigated in this work.

A Numerical Study on the Flame Arrestor for Safety Valve of Hydrogen (수소 안전밸브용 역화방지기의 성능 평가에 대한 수치해석 연구)

  • OH, SEUNG JUN;YOON, JEONG HWAN;KIM, SI POM;CHOI, JEONGJU
    • Journal of Hydrogen and New Energy
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    • v.33 no.4
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    • pp.391-399
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    • 2022
  • Hydrogen is one of the energy carriers and has high energy efficiency relative to mass. It is an eco-friendly fuel that makes only water (H2O) as a by-product after use. In order to use hydrogen conveniently and safely, development of production, storage and transfer technologies is required and attempts are being made to apply hydrogen as an energy source in various fields through the development of the technology. For transporting and storing hydrogen include high-pressure hydrogen gas storage, a type of storage technologies consist of cryogenic hydrogen liquid storage, hydrogen storage alloy, chemical storage by adsorbents and high-pressure hydrogen storage containers have been developed in a total of four stages. The biggest issue in charging high-pressure hydrogen gas which is a combustible gas is safety and the backfire prevention device is that prevents external flames from entering the tank and prevents explosion and is essential to use hydrogen safely. This study conducted a numerical analysis to analyze the performance of suppressing flame propagation of 2, 3 inch flame arrestor. As a result, it is determined that, where the flame arrestor is attached, the temperature would be lowered below the temperature of spontaneous combustion of hydrogen to suppress flame propagation.

Hydrogen Production by the High Temperature Steam Electrolysis of NiO/YSZ/Pt Cell (NiO/YSZ/Pt 전해셀의 고온 수증기 전해에 의한 수소제조 특성)

  • Yu, Ji-Haeng;Kim, Young-Woon;Lee, Shi-Woo;Seo, Doo-Won;Hong, Ki-Suk;Han, In-Sub;Woo, Sang-Kuk
    • Journal of Hydrogen and New Energy
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    • v.17 no.1
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    • pp.62-68
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    • 2006
  • High temperature electrolysis is a promising technology to produce massively hydrogen using renewable and nuclear energy. Solid oxide fuel cell materials are candidates as the components of steam electrolysers. However, the polarization characteristics of the typical electrode materials during the electrolysis have not been intensively investigated. In this study, NiO electrode was deposited on YSZ electrolyte by spin coat process and firing at $1300^{\circ}C$. Pt electrode was applied on the other side of the electrolyte to compare the polarization characteristics with those by NiO during electrolysis. The $H_2$ evolution rate was also monitored by measuring the electromotive force of Lambda probe and calculated by thermodynamic consideration. At low current density, Pt showed lower cathodic polarization and thus higher current efficiency than Ni, but the oxidation of Ni into NiO caused the increase of anodic resistance with increasing current density. High overpotential induced high power consumption to produce hydrogen by electrolysis.