• 자원리싸이클링
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• 제25권1호
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• pp.48-59
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• 2016

화석연료를 사용하는 선박이나 자동차는 $CO_2$가스를 과대하게 발생하므로 지구 온난화에 영향을 주기 때문에 화석연료 대신 수소를 사용하는 수소연료전지자동차(FCV)가 크게 각광을 받고 있다. 우리나라는 현대자동차가 FCV자동차를 미국, 일본, 독일 등의 선진국들의 자동차회사와 경쟁적으로 개발하고 있다. 수소는 제철소의 코크스 공장, 서유화학공장의 부산물로 얻으며, 석탄, 메탄가스 등을 고온에서 증기와 반응시켜서 메탄 수증기개질법과 압력스윙흡착법 또는 막분리형멤브레인개질 법을 이용한 수소분리형개질방법으로 고순도 수소를 제조하거나 물을 전기분해하여 제조한다. 수소는 전자공업, 금속 및 화학공업, 로켓 연료 및 공장, 병원, 가정용 등의 연료전지시스템이나 FCV의 연료로 사용하고 있다. 수소의 저장은 수소용기에 수소를 압축하는 방법과 액화수소로 저장하는 방법이 일반적이고, 최근 수소화물이나 유기화학하이드라이드법으로 저장하여 수소스테이션에 운반해서 사용한다. 우리나라는 현재 13개소의 수소스테이션이 가동 중에 있으며, 향후 43개소를 설치할 계획이다.

• 한국터널지하공간학회 논문집
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• 제24권4호
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• pp.305-316
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• 2022

화석연료의 고갈과 환경문제의 대안으로 수소에너지가 부각되고 있으며, 자동차 산업에서도 수소차의 보급이 증가하고 있다. 그러나 수소는 가연농도 범위가 4~75%로 넓은 가연영역을 가지고 있어 수소차 사고 시 안전에 대한 우려가 높은 실정이다. 특히, 터널이나 지하주차장과 같은 반밀폐 공간에서는 수소누출에 따른 화재나 폭발이 대형사고를 유발할 가능성이 높기 때문에 수소누출에 따른 가연영역 분석을 통해 수소 안전성에 대한 검토가 필요한 실정이다. 이에 본 연구에서는 표준단면의 도로터널에서 수소차량의 수소 누출조건과 터널 내 풍속에 따른 수소농도 해석을 수행하여 터널 내 풍속이 가연영역에 미치는 영향을 검토하였다. 수소의 누출조건은 1개의 탱크와 3개의 탱크가 통시에 TPRD를 통해 누출되는 조건과 대형크랙이 발생하여 누출하는 조건으로 하였으며, 터널 내 풍속은 0, 1, 2.5, 4.0 m/s를 고려하였다. 가연영역에 대한 검토결과, 1 m/s 이상의 풍속이 존재하는 경우에는 풍속이 없는 경우와 비교하여 최대 25%수준까지 감소하는 것으로 나타나고 있으며, 풍속증가에 따른 가연영역의 감소효과는 거의 없는 것으로 나타나고 있다. 특히 대형크랙이 발생하여 약 2.5초 만에 완전히 누출되는 경우에는 풍속이 증가하면 가연영역이 약간 증가하는 것으로 나타나고 있다. 또한 하향 분출되는 경우에 풍속이 작은 차량하부 영역에 수소가스가 상당히 긴 시간동안 잔류하는 것으로 분석되었다.

• 드라이브 ㆍ 컨트롤
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• 제20권1호
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• pp.49-54
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• 2023

• 펄프종이기술
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• 제33권3호
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• pp.84-99
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• 2001

This study was carried out to acquire basic data necessary for the use of rice-straw chemical pulp. It investigated the proper bleaching conditions when rice-straw chemical pulp(alkaline sulfite-${Na_2}{S_2}{O_4}$) was bleached using the various kinds of bleaching agents by the two-stages bleaching methods. And, physical properties of pulps bleached with eight kinds of two-stages bleaching methods were tested. The results of this study were as follow; 1. The first-stage bleaching was conducted under the proper conditions with chlorine(C). And then, the proper conditions related to the calcium chlorite(H), hydrogen peroxide(P) and sodium hydrosulfite(Y) bleaching as the second-stage bleaching were investigated. The proper conditions of CH stage were determined to be 0.3% concentration of calcium chlorite, $30^{\circ}C$ of reaction temperature and 20min. of reaction time. For CP stage, the proper conditions of concentration of hydrogen peroxide, reaction temperature and reaction time were 1.5%, $60^{\circ}C$ and 90min., respectively. And for CY stage, the proper conditions were 0.5% concentration of sodium hydrosulfite, $40^{\circ}C$ of reaction temperature and 90min. of reaction time. 2. The first-stage bleaching was conducted under the proper conditions with chlorine dioxide(D). And then, the proper conditions related to the calcium chlorite(H), hydrogen peroxide(P) and sodium hydrosulfite(Y) bleaching as the second-stage bleaching were investigated. The proper conditions of DH stage were determined to be 0.5% concentration of calcium chlorite, $25^{\circ}C$ of reaction temperature and 5min. of reaction time. For DP stage, the proper conditions of concentration of hydrogen peroxide, reaction temperature and reaction time were 1.0%, $70^{\circ}C$ and 90min., respectively. And for DY stage, the proper conditions were 0.3% concentration of sodium hydrosulfite, $50^{\circ}C$ of reaction temperature and 20min. of reaction time. 3. The first-stage bleaching was conducted under the proper conditions with calcium chlorite(H). kAnd then, the proper conditions related to the hydrogen peroxide(P) and sodium hydrosulfite(Y) bleaching as the second-stage bleaching were investigated. The proper conditions of HP stage were determined to be 0.3% concentration of hydrogen peroxide, $30^{\circ}C$ of reaction temperature and 60min. of reaction time. For HY stage, the proper conditions of concentration of sodium hydrosulfite, reaction temperature and reaction time were 2.5%, $60^{\circ}C$ and 30min., respectively. 4. When the rice-straw chemical pulps were bleached with eight kinds of two-stages bleaching methods in the proper conditions mentioned above, respectively, the final brightnesses after CH, CP, CY, DH, DP, DY, HP, and HY bleachings were 62.0, 74.3, 61.4, 58.9, 66.9, 62.9, 50.4 and 60.1, respectively. And strengthes of pulps bleached with DP and DH methods were comparatively higher than those of pulps bleached with other bleaching methods.

• 펄프종이기술
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• 제31권5호
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• pp.86-94
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• 1999

Alkaline peroxide bleaching of chemi-mechanical pulp is a very complicated system where various process factors affect the bleacing performance and pulp properties. Traditional onefactor-at a time method is ineffective and costly infinding the optimal bleaching conditions. In this study, statistical experimental design and multiple regression method wre used to investigated the interactions among various bleaching factors and to find out the possbile maximal brightness development during one stage alkaline peroxide bleacing of TMP. The TMP was made from 10% Korean red pine and 90% Korean spruce and had an initial brightness of 54.5% ISO. the TMP was pretreated with EDTA(0.5% on O.D. pulp, 3% pulp consistency, 30$^{\circ}C$ for 60 minutes) and bleached in a 2 L Mark V Quantum Reactor at 750 rmp, 7.5% of bleaching consistency and with 0.05% magnesium sulfate addition. The ranges of chemical factors studied , based on oven-ried pulp, were 1-5% for hydrogen peroxide, 1-4% for sodium hydroxide and 1-4% for sodium silicate. The rages of reaction temperature and time were 50-90$^{\circ}C$ and 40-180minutes respectively. Interactions of hydrogen peroxide with alkali , time with temperature ature, alkali with time and silicate with temperature were found to be significant which means that hydrogen peroxide bleaching will be favored at stable concentration of perhydroxyl ion, relatively short time and low temperature, and high level of silicate. Mathematical model which has good predictability for target brightness in one stage peroxide bleaching can also be established easily. Base ion the model, maximal brightness of 70% ISO was found to at 50$^{\circ}C$ and 50 minutes by chemical additions of 5% for hydrogen peroxide, 3.2-3.4% for sodium hydroxide and 4% for silicate based on O.D. pulp. However, this result might not be suitable for situation where furnishes are different from ours, or different pretreatment is used, or bleaching carried out at different pulp consistency. In these cases it will be good to re-investigate the process by a similar methodology as was used in this study.

• 한국펄프종이공학회:학술대회논문집
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• 한국펄프종이공학회 2000년도 추계학술발표논문집
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• pp.15-21
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• 2000

In chlorine dioxide delignification and bleaching the formation of chlorate is undesirable because it does not react with lignin and is harmful to the environment. Chlorate is mainly formed from the in-situ generated hypochlorus acid which is also the main reason for AOX formation. In previous literature scavengers of hypochlorous acid such as sulfamic aicd, DMSO, and hydrogen peroxide have been added to bleaching stages to reduce AOX formation but less attention has been paid to chlorate reduction. This paper thus focuses on the reduction of chlorate content caused by the following additives, sulfamic acid, DMSO, hydrogen peroxide, and oxalic acid. The results show that only sulfamic acid and DMSO reduce chlorate formation under our chlorine dioxide prebleaching conditions. Results by UV spectroscopy and pH adjustment show that scavengers react with hypochlorous acid much faster than with chlorine. Hydrogen peroxide and oxalic acid react with HClO/$Cl_2$much slower than DMSO and sulfamic acid do. The reason for the ineffectiveness of hydrogen peroxide and oxalic acid is ascribed to their slow reaction rates with HClO compared to that of chlorate formation. The fact that only 30-35% of the chlorate can be reduced by sulfamic acid and DMSO when charged in same mole ratio to chlorine dioxide, suggested that the reaction rate of DMSO and sulfamic acid with hypochlorous aicd are of the same magnitude as that of chlorate formation.

• 한국산업융합학회 논문집
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• 제26권6_3호
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• pp.1289-1295
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• 2023

Polyurethane foam insulation required for storing and transporting cryogenic liquefied gas is already widely used as a thermal insulation material for commercial LNG carriers and onshore due to its stable price and high insulation performance. These polyurethane foams are reported to have different mechanical performance depending on the density, and the density parameter is determined depending on the amount of the blowing agent. In this study, density-dependent polyurethane foam was fabricated by adjusting the amount of blowing agent. The mechanical properties of polyurethane foam were analyzed in the room temperature and cryogenic temperature range of -163℃ at 1.5 mm/min, which is a quasi-static load range, and the cells were observed through microstructure analysis. The characteristics of linear elasticity, plateau, and densification, which are quasi-static mechanical behaviors of polyurethane foam, were shown, and the correlation between density and mechanical properties in a cryogenic environment was confirmed. The correlation between mechanical behavior and cell size was also analyzed through SEM morphology analysis. Polyurethane foam with a density of 180 kg/m³ had a density about twice as high as that of a polyurethane foam with a density of 96 kg/m³, but yield strength was about 51% higher and cell size was about 9.5% smaller.

• 한국습지학회지
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• 제25권4호
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• pp.291-296
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• 2023

철강산업의 산 회수설비에서 발생하는 염화수소 가스를 처리하기 위하여 마이크로버블을 발생할 수 있는 습식스크러빙 장치(DIWS)가 도입되었다. 산 회수 설비에서 발생하는 염소가스는 수소 가스와 결합하여 염화수소 가스의 농도를 50% 정도 증가시켰다. DIWS장치에 염소 제거를 위한 Na₂S₂O₃를 투입한 이후의 유입수 염화수소 가스 농도는 13.1 ~13.4 ppm, 유출수는 1.5~1.7 ppm이었고, 제거율은 87.5~88.8%로 안정되게 유지하였다. DIWS는 대기배출기준을 안정적으로 만족함에 따라 현장 적용에 적용할 수 있는 공정으로 판단된다.

• Journal of Microbiology and Biotechnology
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• 제18권3호
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• pp.532-538
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• 2008

For the newly isolated $H_2$-producing chemoheterotrophic bacterium Citrobacter amalonaticus Y19, anaerobic glucose metabolism was studied in batch cultivation at varying initial glucose concentrations (3.5-9.5 g/l). The carbon-mass and energy balances were determined and utilized to analyze the carbon metabolic-pathways network. The analyses revealed (a) variable production of major metabolites ($H_2$, ethanol, acetate, lactate, $CO_2$, and cell mass) depending on initial glucose levels; (b) influence of NADH regeneration on the production of acetate, lactate, and ethanol; and (c) influence of the molar production of ATP on the production of biomass. The results reported in this paper suggest how the carbon metabolic pathway(s) should be designed for optimal Hz production, especially at high glucose concentrations, such as by blocking the carbon flux via lactate dehydrogenase from the pyruvate node.

• 한국전기전자재료학회:학술대회논문집
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• 한국전기전자재료학회 2009년도 춘계학술대회 논문집
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• pp.91-91
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• 2009

In the past decade, Pd based thin films have been studied far hydrogen gas sensors due to their high possibility for energy industry and environmental applications. In this work, we report a navel method to fabricate highly sensitive hydrogen gas sensors based on PdO thin films. The films were deposited on Si substrates in Ar and $O_2$ ambient using reactive sputtering system. A semiconductor process has been utilized to fabricate PdO films with t=40nm. We observed the resistance changes of the PdO films with various $H_2$ concentrations. It was found that the electrical properties of the thin films depend on the composition of oxygen. The sensitivity is defined as $S\;=\;(R_0-R)/R{\times}100%$, where R and $R_0$ are the resistances in the presence of exposing the hydrogen gas and air, respectively. The sensitivity of the thin films was found to be as high as about 95%. After exposing to hydrogen gas, we discovered that the nano-sized cracks formed on the surface of the PdO thin films. The nano-cracks formed in deoxidized PdO thin films were known by playing a key role to reduce more than 4 times the response time of absorption. Our results illustrate that the deoxidized PdO thin films can be used as hydrogen sensors.