• Title/Summary/Keyword: H2 energy

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Supercritical Water Gasification of Low Rank Coal with High Moisture Content (고함수 저등급 석탄의 초임계수 가스화 특성)

  • Yoon, Sang Jun;Lee, Jae Goo;Ra, Ho Won;Seo, Myung Won
    • Transactions of the Korean hydrogen and new energy society
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    • v.24 no.4
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    • pp.340-346
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    • 2013
  • Study on clean and efficient utilization technology for low rank coal with high moisture content is actively ongoing due to limited reserves of petroleum and of high grade coal and serious climate change caused by fossil fuel usage. In the present study, supercritical water gasification of low rank coal was performed. With increasing reaction temperature, content of combustible gases such as $H_2$ and $CH_4$ in the syngas increased while the $CO_2$ content decreased. As the reaction pressure increased from 210 to 300 bar, the $CO_2$ content in the syngas increased while the hydrocarbon gas content decreased. The $H_2$ and $CH_4$ content in the syngas increased slightly with pressure. With the addition of Pd, Pt, and Ru catalysts, it was possible to improve the production of $H_2$. Moreover, the increase of active metal content in the catalyst increased the $H_2$ productivity. The Ru catalyst shows the best performance for increasing the $H_2$ content in the syngas, while decreasing the $CO_2$ content.

The Role of Oxygen in Bunsen Reaction Section of Sulfur-Iodine Hydrogen Production Process (황-요오드 수소 제조 공정의 분젠 반응 부분에서 $O_2$의 역할)

  • Hong, Dong-Woo;Kim, Hyo-Sub;Kim, Young-Ho;Park, Chu-Sik;Bae, Ki-Kwang
    • Transactions of the Korean hydrogen and new energy society
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    • v.21 no.4
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    • pp.278-285
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    • 2010
  • The Sulfur-Iodine (SI) thermochemical hydrogen production process of a closed cycle consists of three sections, which are so called the Bunsen reaction section, the $H_2SO_4$ decomposition section and the HI decomposition section. To identify the role of oxygen that can be supplied to the Bunsen reaction section via the $H_2SO_4$ decomposition section, Bunsen reactions with a $SO_2,\;SO_2-O_2$ mixture and $SO_2-N_2$ mixture as feed gases were carried out using a stirred reactor in the presence of $I_2/H_2O$ mixture. As the results, the amounts of $I_2$ unreacted under the feed of mixture gases were higher than those under the feed of $SO_2$ gas only, and the amount of HI produced was relatively decreased. The results of Bunsen reaction using $SO_2-O_2$ mixture were similar to those using $SO_2-N_2$ mixture. It may be concluded that an oxygen in $SO_2-O_2$ mixture has a role as a carrier gas like a nitrogen in $SO_2-N_2$ mixture. The effects of oxygen were decreased with increasing temperature and decreasing oxygen content in $SO_2-O_2$ mixture.

A Strategy to Increase Microbial Hydrogen Production, Facilitating Intracellular Energy Reserves

  • Lee, Hyo Jung;Park, Jihoon;Lee, Joo-Young;Kim, Pil
    • Journal of Microbiology and Biotechnology
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    • v.26 no.8
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    • pp.1452-1456
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    • 2016
  • Overexpression of the genes encoding phosphoeneolpyruvate carboxykinase (pckA) and NAD-dependent malic enzyme (maeA) facilitates higher intracellular ATP and NAD(P)H concentrations, respectively, under aerobic conditions in Escherichia coli. To verify a hypothesis that higher intracellular energy reserves might contribute to H2 fermentation, wild-type E. coli strains overexpressing pckA and maeA were cultured under anaerobic conditions in a glucose minimal medium. Overexpression of pckA and maeA enabled E. coli to produce 3-times and 4-times greater H2 (193 and 284 nmol, respectively) than the wild type (66 nmol H2). The pckA and maeA genes were further overexpressed in a hydrogenase-3-enhanced E. coli strain. The hydrogenase-3-enhanced strain (W3110+fhlA) produced 322 nmol H2, whereas the ATP-enhanced strain (W3110+fhlA+pckA) produced 50% increased H2 (443 nmol). Total H2 in the NAD(P)H-enhanced strain (W3110+fhlA+maeA) was similar to that in the control strain at 319 nmol H2. Possible explanations for the contribution of the increased cellular energy reserves to the enhanced hydrogen fermentation observed are discussed based on the viewpoint of metabolic engineering strategy.

Solar Cooling Technology (태양열 냉방 시스템)

  • Baek, Nam-Choon
    • Solar Energy
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    • v.18 no.2
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    • pp.31-49
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    • 1998
  • Four main solar cooling technologies have been developed over the past twenty years are considered in this paper. These technologies include absorption, vapor compression, desiccant, adsorption, etc. All of these solar cooling technologies considered here are solar thermal ones. The destails of the thermodynamic cycle of these solar cooling technologies are given. The general concept of these solar cooling and the relative advantages among them are also presented. At last, the status and outlook for each approach are summarized.

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The Study on the Surface State of Mg2Ni Exposed to Air by a Chemical Treatment (화학처리방법을 이용한 공기중에 노출된 Mg2Ni의 표면상태에 관한 연구)

  • Han, Jeong-Seop
    • Transactions of the Korean hydrogen and new energy society
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    • v.6 no.2
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    • pp.91-100
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    • 1995
  • To investigate the surface state of $Mg_2Ni$ which was exposed to the air, a chemical treatment was undertaken with $H_2SO_4$ solution. During chemical treatment, the change of pH was measured continuously and the chemically treated specimen was hydrided to study the effect of chemical treatment on the hydrogenation. The pH changing behavior with the various $H_2SO_4$ concentration appeared very diffemrently. Especially in the solution including 3CC $H_2SO_4$, the behavior of pH change can be divided 3 steps. It is also shown that the $Mg_2Ni$ chemically treated with $H_2SO_4$ can be hydrided even under room temperature. By the SEM observation the was reasion that after chemical treatment the surface of a particle was covered with Ni layer.

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Development of a Methanol Absorption System for the Removal of $H_2S$, COS, $CO_2$ in Syngas from Biomass Gasifier (바이오매스 가스화 내의 $H_2S$, COS, $CO_2$ 복합 제거를 위한 메탄올 흡수탑 개발)

  • Eom, Won Hyun;Kim, Jae Ho;Lee, See Hoon
    • Applied Chemistry for Engineering
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    • v.23 no.1
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    • pp.23-27
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    • 2012
  • To make synthetic liquid fuel from biomass such as wood pellet, energy crop and so on, a biomass to liquid (BTL) process by using a biomass gasifier with Fisher-Tropsch (FT) reaction was developed. However $H_2S$, COS and $CO_2$ in syngas from biomass gasifiers resulted in a decrease of the conversion efficiency and the deactivation of the catalyst. To remove acid gases in syngas, a lab-scale methanol absorption tower was developed and the removal characteristics of acid gases were investigated. The methanol absorption tower efficiently removed $H_2S$ and COS with a removal of $CO_2$, so it could be useful process for the BTL process.

Heterogeneous Photocatalytic Bleaching of Methyl Orange (광화학반응을 이용한 메틸오렌지의 탈색)

  • Lee, Tai K.;Kim, Dong H.;Kim, Kyung N.;Chungmoo Auh
    • Proceedings of the Korea Society for Energy Engineering kosee Conference
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    • 1995.05a
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    • pp.60-68
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    • 1995
  • This work wes performed to investigate the photocatalytic decolorization of waste water from textile industries. Methyl orange was used as a target dye with suspended Hombikat TiO$_2$ photocatalyst with a recirculating annular photoreactor. 1 wt % Pt-doped Hombikat thin film tubular reactor with parabolic reflector also wes usedin this experiment. The pH effect and flow rate effect on photobleaching of 0.012 g/l methyl orange solution, AtpH=3 Colour of methyl orange was completely bleached in 30 min with a 20 W UV lamp.

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Analysis of Reactivity of Zn-Based Desulfurization Sorbents for Reducing Power, Water Vapor Content and H2S Content of the Coal Gas in a Batch-Type Fluidized-Bed Reactor (회분식 유동층반응기에서 세 종류 아연계 탈황제의 석탄가스 환원도, 수분함량, 황화수소함량에 따른 반응성 평가)

  • Park, Young Cheol;Jo, Sung-Ho;Son, Jae-Ek;Yi, Chang-Keun
    • Korean Chemical Engineering Research
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    • v.47 no.6
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    • pp.710-714
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    • 2009
  • In this study, we analyzed the desulfurization performance of Zn-based dry sorbents according to the reducing power, water vapor content and $H_2S$ inlet concentration of coal gas in a batch-type fluidized-bed reactor. We used three different coal gas composition with different reducing power such as KRW air-blown coal gas, Shell oxygenblown coal gas and IAE coal gas. The experiments were performed by changing the inlet concentration of water vapor and $H_2S$ in a coal gas. Water vapor content was varied from 5% to 30% and $H_2S$ inlet concentration from 0.5% to 2.0%. As both the water vapor content and $H_2S$ inlet concentration increased, desulfurization performance of Zn-based sorbents decreased regardless of the reducing power of the coal gas. The minimum desuflurization performance was, however, above 99.5% for all experimental conditions, which implied that Zn-based dry sorbents could be used to remove $H_2S$ up to 99%.