• 한국연소학회지
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• 제9권4호
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• pp.28-34
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• 2004

Numerical simulations of freely propagating flames burning $H_2/HCl/Air$ Air mixtures were performed at atmospheric pressure in order to understand the effect of hydrogen chloride on flame structures. The chemical and physical effects of hydrogen chloride on flame structures were observed. A chemical kinetic mechanism was developed, which involved 26 gas-phase species and 198 forward elementary reactions. Under several equivalence ratios the flame speeds were calculated and compared with those obtained from the experiments, the results of which were in good agreement. As hydrogen chloride as additive was added into $H_2/Air$ flame, the flame speed, radical concentration and NO production rate were decreased. The chemical effect of hydrogen chloride caused the reduction of radical concentration, and then the decrease of the net rate of NO production. It was found that the influence in the reduction of $EI_{NO}$ with the addition of hydrogen chloride was attributed more due to the chemical effect than the physical effect.

• 한국태양에너지학회 논문집
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• 제37권2호
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• pp.13-22
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• 2017

Two-step water splitting thermochemical cycle with $CeO_2/ZrO_2$ foam device was investigated by using a solar simulator composed of 2.5 kW Xe-Arc lamp and mirror reflector. The hydrogen production of $CeO_2/ZrO_2$ foam device depending on heat recovery of Thermal-Reduction step and Water-Decomposition step was analyzed, and the hydrogen production of $CeO_2/ZrO_2$ and $NiFe_2O_4/ZrO_2$ foam devices was compared. Resultantly, the quantity of hydrogen generation increased by 52.02% when the carrier gas of Thermal-Reduction step is preheated to $200^{\circ}C$ and, when the $N_2/steam$ is preheated to $200^{\circ}C$ in the Water-Decomposition step, the quantity of hydrogen generation increased by 35.85%. Therefore, it is important to retrieve the heat from the highly heated gases discharged from each of the reaction spaces in order to increase the reaction temperature of each of the stages and thereby increasing the quantity of hydrogen generated through this.

• Nuclear Engineering and Technology
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• 제48권5호
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• pp.1174-1183
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• 2016

Hydrogen release during severe accidents poses a serious threat to containment integrity. Mitigating procedures are necessary to prevent global or local explosions, especially in large steel shell containments. The management of hydrogen safety and prevention of over-pressurization could be implemented through a hydrogen reduction system and spray system. During the course of the hypothetical large break loss-of-coolant accident in a nuclear power plant, hydrogen is generated by a reaction between steam and the fuel-cladding inside the reactor pressure vessel and also core concrete interaction after ejection of melt into the cavity. The MELCOR 1.8.6 was used to assess core degradation and containment behavior during the large break loss-of-coolant accident without the actuation of the safety injection system except for accumulators in Beznau nuclear power plant. Also, hydrogen distribution in containment and performance of hydrogen reduction system were investigated.

• Korean Journal of Chemical Engineering
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• 제35권11호
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• pp.2290-2295
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• 2018

An acceleration stress test (AST) was performed to evaluate the durability of a polymer membrane in a polymer electrolyte membrane fuel cell (PEMFC) for 500 hours. Previous studies have shown that hydrogen crossover measured by linear sweep voltammetry (LSV) increases when the polymer membrane deteriorates in the AST process. On the other hand, hydrogen crossover of the membrane often decreases in the early stages of the AST test. To investigate the cause of this phenomenon, we analyzed the MEA operated for 50 hours using the AST method (OCV, RH 30% and $90^{\circ}C$). Cyclic voltammetry and transmission electron showed that the electrochemical surface area (ECSA) decreased due to the growth of electrode catalyst particles and that the hydrogen crossover current density measured by LSV could be reduced. Fourier transform infrared spectroscopy and thermogravimetric/differential thermal analysis showed that -S-O-S- crosslinking occurred in the polymer after the 50 hour AST. Gas chromatography showed that the hydrogen permeability was decreased by -S-O-S- crosslinking. The reduction of the hydrogen crossover current density measured by LSV in the early stages of AST could be caused by both reduction of the electrochemical surface area of the electrode catalyst and -S-O-S- crosslinking.

• 한국지하수토양환경학회지:지하수토양환경
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• 제13권1호
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• pp.24-31
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• 2008

혼합균에서 분리 배양한 황환원균에 의해 발생되는 황화수소가 염소계유기오염물질인 트리클로로에틸렌의 환원에 어떠한 영향을 미치는지, 또한 염소계유기오염물질에 대한 환원력이 있다고 알려진 2가철은 황화수소가 존재할 경우 트리클로로에틸렌의 환원과 어떠한 관계에 있는지를 알아보기 위하여 본 실험을 수행하였다. 황환원균에 독성을 나타내지 않는 수준의 트리클로로에틸렌의 농도에서 황화수소 발생 및 트리클로로에틸렌의 분해 실험을 수행한 결과 황산염의 환원으로 발생한 황화수소의 농도는 4.38 mM, 트리클로로에틸렌의 농도는 큰 변화가 없는 것으로 관찰되었으며 이를 통하여 황환원균에 의해 발생되는 황화수소의 농도가 트리클로로에틸렌을 환원시키기에는 부족하다는 것을 알 수 있었다. 그러나 황화수소의 농도가 위 실험에서 발생된 농도보다 100배 정도 높을 경우(438 mM)에는 트리클로로에틸렌에 대한 환원력이 있음을 확인하였다. 대표적인 산화철인 $Fe_2O_3$(3가철)를 첨가하였을 경우, 황환원균의 생장에 따라 황화수소, 2가철 및 트리클로로에틸렌의 농도변화를 관찰하였으며 이를 통하여 황환원균에 의해서 발생된 황화수소가 산화되면서 3가의 산화철을 2가철로 환원시키고 황화수소에 의하여 환원된 2가철이 트리클로로에틸렌을 분해하여 농도를 감소시키는 것을 확인하였다. 위의 실험결과를 바탕으로 낮은 농도의 황화수소는 트리클로로에틸렌의 환원에 영향을 미치지 못하며 다만, 황화수소에 의해 환원된 2가철이 트리클로로에틸렌을 분해시키는 주요한 요인임을 알 수 있었다. 또한 실제 해수중에서 황환원균과 $Fe_2O_3$가 공존할 경우의 트리클로로에틸렌의 제거 효과를 살펴보기 위한 실험을 한 결과 황환원균이 황화수소를 생성하여 트리클로로에틸렌의 제거에 영향을 줄 수 있는 반응들은 황환원균 생장에 필수적인 탄소원의 농도가 확보될 때 가능하다는 결론을 얻을 수 있었다.

• 한국수소및신에너지학회논문집
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• 제17권4호
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• pp.440-447
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• 2006

Solid polymer electrolyte(SPE) membrane with electrodes embedded on both faces offer unique possibilities for the electrochemical cells like water electrolyzer with fuel cell. The Nafion 117 membrane was used as the SPE, and $Pt(NH_3)_4Cl_2$ and $NaBH_4$ as the electrocatalysts and reducing agent, respectively. The 'impregnation-reduction(I-R) method' has been investigated as a tool for the preparation of electrocatalysts for water electrolyzer by varying the concentration of reducing agent and reduction time at fixed concentration of platinum salt, 5 mmol/L. Pt-SPE electrocatalysts prepared by non-equilibrium I-R method showed the lowest cell voltage of 2.17 V at reduction time, 90 min and with concentration of reducing agent 0.8 mol/L and the cell voltage with those by equilibrium I-R method was 2.42 V at reduction time, 60 min and with concentration of reducing agent 0.8 mol/L. The cell voltage were obtained at a current density $1\;A/cm^2$ and $80^{\circ}C$. In water electrolysis, hydrogen production efficiency by Pt-SPE electrocatalyst is 68.2% in case of non-equilibrium I-R method and 61.2% at equilibrium I-R method.

• 한국수소및신에너지학회논문집
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• 제18권4호
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• pp.452-457
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• 2007

Titanium foil and mesh(anodized tubular $TiO_2$ electrode, ATTE) were anodized in a bath at $5^{\circ}C$ with 20V external bias applied, then annealed at different temperatures($450^{\circ}C{\sim}850^{\circ}C$) to obtain tubular $TiO_2$ on the Ti substrate. The prepared sample was used to investigate rate of hydrogen production as well as Cr(VI) reduction. The ATTEs annealed at relatively lower temperatures showed higher activity than those at relatively higher temperatures. In particular, the Cr(VI) reduction was pH-dependent. To improve photocatalytic Cr(VI) reduction with the ATTEs, two configurations, fixing foil type and rotating mesh type, were also compared. As a result, the rotating mesh type was much more effective for Cr(VI) reaction than the former due to the more efficient use of the light. In the rotating type reactor, as the rotating speed increased, the rate of the Cr(VI) reduction was getting faster.

• 공업화학
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• 제3권2호
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• pp.305-311
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• 1992

수소에 의한 $In_2O_3$의 환원반응을 열중량분석기를 이용하여 실험적으로 연구하였다. $In_2O_3$의 환원반응은 $300^{\circ}C$ 이상에서 일어났다. 환원반응속도는 반응온도에 따라 급격히 증가하였으나, 수소의 유량에 대해선 거의 영향을 받지 않았다. 비반응핵모델을 $In_2O_3$의 환원반응에 적용한 결과 $In_2O_3$의 표면에서 수소와 $In_2O_3$의 화학반응이 율속단계임을 알 수 있었다. $In_2O_3$의 환원반응 겉보기 활성화에너지는 20kcal/g-mol $H_2$였으며 환원반응속도식은 다음과 같이 얻어졌다. ${\frac{dX}{dt}}=1.6{\times}10^5e^{-20000/RT}(1-X)^{2/3}$

• 대한환경공학회지
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• 제28권10호
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• pp.1074-1081
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• 2006

질산성질소와 트리클로로에틸렌(TCE)을 동시에 제거하고자 이들을 화학적 생물학적으로 환원 및 수착시키는 반응매질로서 영가철과 피트(peat)를 이용하였다. 영가철의 수중산화로 발생된 수소가 질산성질소와 TCE를 환원시켜 두 물질이 제거하는데 TCE의 수착제거가 가능한 피트를 이용하고 그에 따른 혼합미생물의 생분해 및 전자전달의 효과를 이용하였다. 질산성질소의 경우 영가철과 피트혼합매질에서 제거효율이 우수하나 제거기작이 환원에 의존하므로 TCE가 공존시 전자에 대한 경쟁으로 그 제거효율이 감소하였으며 멸균처리한 피트를 사용한 실험군과의 결과비교로 탈질균의 작용을 알 수 있었다. TCE의 경우 영가철이 함유된 매질에서 제거효율이 높으며 질산염 공존이 영향을 미치지 못하였다. 생분해하는 혐기성 미생물군의 존재는 시스템에서 발생한 수소와 메탄가스 분석으로 확인하였다.

• 한국분말재료학회지
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• 제16권4호
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• pp.262-267
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• 2009

Disk type porous nickel membrane was fabricated by in-situ reduction/sintering process using compacted NiO/PMMA (PMMA; Polymethyl methacrylate) mixture at $800^{\circ}C$ in hydrogen atmosphere. The porosity (49$\sim$58%) of these membrane was investigated as an amount of PMMA additive. The thermal decomposition and reduction behavior of NiO/PMMA were analyzed by TG/DTA in hydrogen atmosphere and the activation energy for the hydrogen reduction of NiO and thermal degradation of PMMA was calculated as 61.1 kJ/mol, evaluated by Kissinger method. Finally, the filtering performance and pressure drop were measured by particle counting system.