• Title/Summary/Keyword: Energy conversion ratio

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The Characteristics of Coal Gasification using Microwave Plasma (마이크로웨이브 플라즈마를 이용한 석탄가스화 특성 연구)

  • Kim, Doo-Il;Lee, Jae-Goo;Kim, Yong-Ku;Yoon, Sang-Jun
    • Journal of Hydrogen and New Energy
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    • v.23 no.1
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    • pp.93-99
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    • 2012
  • The investigation of clean and environment-friendly coal utilization technology is actively progressed due to high oil price and serious climate change caused by greenhouse gas emissions. In this study, the plasma gasification was performed using a 6kW microwave plasma unit under various reaction conditions: the particle sizes of coal ($45{\mu}m-150{\mu}m$), $O_2$/fuel ratio (0 - 1.3), and steam/fuel ratio (0 - 1.5). The $H_2$ composition decreases with decreasing coal particle size. With increasing $O_2$/fuel ratio, the $H_2$ composition in the syngas decreased while the $CO_2$ composition increased. As the steam/fuel ratio increased from 0 to 1.5, the $H_2$ composition in the syngas increased while the $CO_2$ composition decreased. From the results, it was proven that the variation of syngas composition greatly affected by $O_2$/fuel ratio than steam/fuel ratio. The $H_2$ composition in the syngas, carbon conversion, and cold gas efficiency increased with increasing plasma power.

Partial Oxidation of Methane Over Ceria-promoted Catalysts Derived from Ni-substituted Hydrotalcite (세리아가 첨가된 니켈 치환 하이드로탈사이트로부터 유도된 촉매에 의한 메탄의 부분산화)

  • Lee, Seung-Hwan;Kim, Mi-So;Kwak, Jung-Hun;Lim, Tae-Hoon;Nam, Suk-Woo;Hong, Seong-Ahn;Yoon, Ki-June
    • New & Renewable Energy
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    • v.4 no.2
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    • pp.39-44
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    • 2008
  • Partial oxidation of methane was carried out by ceria-promoted Ni-substituted hydrotalcite-derived catalysts ($Ce_xNi_3$-HTlc ; x=$0.3{\sim}1.2$) in a fixed-bed reactor. The Ce/Ni ratio of 0.3/3 in the catalyst showed the best catalytic activity but the Ce/Ni ratio became higher above 0.3/3, the catalyst became less active in short-term tests. No ceria promoted catalyst was started to decrease $CH_4$ conversion after 20 h but the Ce/Ni ratio 0.3/3 catalyst was kept its stability in long-term tests.

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Transesterification for FAME production of Rapeseed Oil

  • Jeong, Gwi-Taek;Yun, Dae-Hyeon;Gang, Chun-Hyeong;Choe, Byeong-Cheol;Lee, Un-Taek;Park, Don-Hui
    • 한국생물공학회:학술대회논문집
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    • 2003.04a
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    • pp.164-168
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    • 2003
  • Fatty acid methyl esters (FAMEs) show large potential applications as diesel substitutes, and they are known as biodiesel fuel. Biodiesel fuel as a renewable energy is an alternative that can reduce energy dependence on petroleum and air pollution. Several processes for the production of biodiesel fuel have been developed. Transesterification process under alkali-catalysis and short-chain alcohol gives high level yield of methyl esters in short reaction times. In this research, transesterification of rapeseed oil was investigated to produce the FAMEs. Experimental reaction conditions included molar ratio of oil to alcohol, concentration of catalyst, types of catalysts, reaction time, and reaction temperature. The conversion ratio of rapeseed oil enhanced with the alcohol-oil mixing ratio and with the reaction temperature.

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Biogas Reforming through Microwave Receptor Heating (마이크로웨이브 수용체 가열을 통한 바이오가스 개질)

  • Young Nam Chun;June An
    • New & Renewable Energy
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    • v.20 no.1
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    • pp.126-134
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    • 2024
  • Biogas, composed mainly of methane (CH4) and carbon dioxide (CO2), is a renewable gas that can serve as an alternative energy source. In this study, we developed a new microwave reformer and analyzed its reforming characteristics. We observed that higher temperatures of the microwave receptor led to increased reforming efficiency. By supplying appropriate amounts of methane and steam, we could prevent carbon generated from the thermal decomposition reaction of carbon dioxide from depositing on the catalytic active layer, thus avoiding the inhibition of catalytic activity. Hydrogen generation was enhanced when maintaining the biogas ratio and steam supply at adequate levels. Increasing the SiC ratio in the receptor improved the uniformity of temperature distribution and growth rate, resulting in higher conversion rates of the reforming process.

Hydrothermal Pressure Effect over Preparation of MoS2: Catalyst Characterization and Direct Methanation (수열 압력 제조 조건이 MoS2 촉매 특성과 직접 메탄화 반응에 미치는 영향)

  • PARK, JEONGHWAN;KIM, SEONGSOO;KIM, JINGUL
    • Journal of Hydrogen and New Energy
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    • v.29 no.2
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    • pp.170-180
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    • 2018
  • After $MoS_2$ catalyst was prepared at 1, 30, and 70 atm, the hydrothermal pressure effect over preparation of $MoS_2$ was investigated in terms of catalyst characterization and direct methanation. Multifaceted characterization techniques such as XRD, BET, SEM, TPR, EDS, and XPS were used to analyze and investigate the effect of high pressure over the preparation of surface and bulk $MoS_2$ catalyst. Result from XRD, SEM, and BET demonstrated that $MoS_2$ was more dispersed as preparation pressure was increased, which resulted finer $MoS_2$ crystal size and higher surface area. EDS result confirmed that bulk composition was $MoS_2$ and XPS result showed that S/Mo mole ratio of surface was about 1.3. TPR showed that $MoS_2$ prepared at 30 atm possessed higher active surface sites than $MoS_2$ prepared at 1 atm and these sites could contribute to higher CO yield during methanation. Direct methanation was used to evaluate the CO conversion of the both catalysts prepared at 1 atm and 30 atm and reaction condition was at feed mole ratio of $H_2/CO=1$, GHSV=4800, 30 atm, temperature($^{\circ}C$) of 300, 350, 400, and 450. $MoS_2$ prepared at 30 atm showed more stable and higher CO conversion than $MoS_2$ prepared at 1 atm. Faster deactivation was occurred over $MoS_2$ prepared at 1 atm, which indicated that preparation pressure of $MoS_2$ catalyst was the dominant factor to improve the yield of direct methanation.

A Numerical Study of Unsteady Flow around a Vertical Axis Turbine for Tidal Current Energy Conversion (조류발전용 수직축 터빈 주위의 비정상 유동 수치해석)

  • Jung, Hyun-Ju;Rhee, Shin-Hyung;Song, Mu-Seok;Hyun, Beom-Soo
    • Journal of the Korean Society for Marine Environment & Energy
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    • v.12 no.1
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    • pp.9-14
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    • 2009
  • A numerical investigation was performed based on the Reynolds-Averaged Navier-Stokes(RANS) equations for the two-dimensional unsteady flow around a vertical axis turbine(VAT) with three or four blades. VAT is one of the promising devices for tidal current energy conversion. The geometry of the turbine blade was $NACA65_3$-018 airfoil, for which CFD analysis using Fluent was carried out at several angles of attack and the results were compared with the corresponding experimental data for validation and calibration. Then CFD simulations were carried out for the whole vertical axis turbine with a two-dimensional setup. The CFD simulation demonstrated the usefulness of the method to study the typical unsteady flows around VATs and the results showed that the optimum turbine efficiency could be achieved for carefully selected combinations of the number of blade and Tip-Speed Ratio(TSR).

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Partial oxidation of n-butane over ceria-promoted nickel/calcium hydroxyapatite (세리아가 첨가된 니켈/칼슘 하이드록시 아파타이트 촉매 상의 부탄 부분산화 연구)

  • Kwak, Jung-Hun;Lee, Sang-Yup;Kim, Mi-So;Nam, Suk-Woo;Lim, Tae-Hoon;Hong, Seong-Ahn;Yoon, Ki-June
    • 한국신재생에너지학회:학술대회논문집
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    • 2007.11a
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    • pp.89-92
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    • 2007
  • Partail oxidation(POX) of n-butane was investigated in this research by employing ceria-promoted Ni/calcium hydroxyapatite catalysts ($Ce_xNi_{2.5}Ca_{10}(OH)_2(PO_4)_6$ ; x = $0.1{\sim}0.3$) which had recently been reported to exhibit good catalytic performance in POX of methane and propane. The experiments were carried out with changing ceria content, $O_2/n-C_4H_{10}$ ratio and temperature. As the $O_2/n-C_4H_{10}$ feed ratio increased up to 2.75, n-$C_4H_{10}$ conversion and $H_2$ yield increased and the selectivity of methane and other hydrocarbons decreased. But with $O_2/n-C_4H_{10}$ = 3.0, $n-C_4H_{10}$ conversion and $H_2$ yield decreased. This is considered due to that too much oxygen may inhibit the reduction of Ni or induce the oxidation of Ni, which results in poor catalytic activity. The optimum $O_2/n-C_4H_{10}$ ratio lay between 2.50 and 2.75. $Ce_{0.1}Ni_{2.5}Ca_{10}(OH)_2(PO_4)_6$ showed the highest $n-C_4H_{10}$ conversion and $H-2$ yield on the whole. In durability tests, higher hydrogen yield and better catalyst stability were obtained with the $O_2/n-C_4H_{10}$ ratio of 2.75 than with the ratio of 2.5.

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Solar Detoxification of Trichloroethylene in Waste Water with Slurry Batchtype Photoreactor (Slurry batch형 광화학 반응기를 이용한 폐수 내의 Trichlroethylene의 분해)

  • Lee, Tai-K.;Kim, Dong-H.;Cho, Sug-H.;Auh, Chung-Moo
    • Solar Energy
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    • v.12 no.3
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    • pp.10-20
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    • 1992
  • In this experiment, photochemical reaction has been applied to destroy TCE in water phase. The main target of this work is to investigate the technical feasibility of large scale of solar detoxification reactor for water treatment. The results have revealed that solar detoxification utilizing photon energy from the sun is the most attractive process to decompose organic toxins in water phase at room temperature. The detailed results from this work are as follows; (1) The highest conversion ratio of TCE was obtained by using $TiO_2$, annatase as a photocatalyst among $TiO_2$ anatase, $TiO_2$ rutile and $V_2O_5$ under the same experimental condition. The anatase crystal structure was confirmed with XRD analysis, and its surface area was 7.748 $m^2/g$ from the BET-$N_2$ measurement (2) 0.1 wt% of $TiO_2$ anatase has been adopted as optimal quantity for batch slurry reactor at this experimental conditions. (3) The effect of hydrogen peroxide on the conversion of TCE was investigated. Its optimal quantity was 0.06 vol. % under this experimental conditions. (4) The effect of oxygen on the conversion of TCE also was studied by controlling the head space in photoreactor. Results indicated that sufficient amount of oxygen should be supplied to accomplish the highest conversion rate of TCE in water phase.

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Thermodynamic Analysis of Thermochemical Process for Water Splitting (고온열 이용 공정의 열역학적 해석)

  • Kim, Jong-Won;Son, Hyun-Myung;Lee, Sana-Ho;Sim, Kyu-Sung;Jung, Kwang-Deog
    • Journal of Hydrogen and New Energy
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    • v.13 no.3
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    • pp.204-213
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    • 2002
  • In this work, hydrogen production by a 2-step water-spritting thermochemical cycle based on metal oxides redox pairs was investigated on the bases of the thermodynamics and technical feasibility. Also, a 2nd-law analysis performed on the closed cyclic process indicates a maximum exergy conversion efficiency of 7.1% when using a solar cavity-receiver operated at 2300K and air/Fe3O4 molar ratio = 10.

Comparison of Properties of Two Kinds of Anion Exchange Membranes with Different Functional Group for Alkaline Fuel Cells (알칼라인 연료전지용 다른 작용기들을 갖는 두 종류의 음이온 교환 막들의 특성 비교)

  • LEE, SEUNGYEON;YOO, DONG JIN
    • Journal of Hydrogen and New Energy
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    • v.29 no.5
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    • pp.458-465
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    • 2018
  • This study reports the fabrication of anion exchange membranes (AEMs) containing two kinds of functional groups: i) trimethylphosphite (TMP) and ii) trimethylamine (TMA). We carried out the synthesis of polymers to enhance thermal stability and ion conductivity. The alternative polymer was prepared using 2,2-bis(4-hydroxy-3-methylphenyl)propane and decafluorobiphenyl. The membrane was fabricated by solution casting method. The thermal stability of membranes was examined by TGA. The physiochemical properties of membranes were also investigated in terms of water uptake, swelling ratio, ion exchange capacity, and ion conductivity. The hydroxide ion conductivity of the membranes reached about 20.2 mS/cm for quaternary ammonium poly(arylene ether) (QA-PAE) containing TMA moiety and 5.1 mS/cm for quaternary phosphonium PAE (QP-PAE) containing TMP moiety at $90^{\circ}C$.