• Title/Summary/Keyword: chemical facility

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FT-IR analysis of flame resistant chemical mixture

  • Kim, Younsu;Seo, Jihyung;Choe, Yoong Kee;Sohn, Youngku;Kim, Jeongkwon
    • Analytical Science and Technology
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    • v.34 no.1
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    • pp.17-22
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    • 2021
  • In this study, flame retardant mixtures of decabromodiphenylethane (DBDPE) and Sb2O3 were analyzed using Fourier transform infrared (FT-IR) spectroscopy. The experimentally obtained wavenumbers of DBDPE and Sb2O3 were 1321 and 949 cm-1, respectively, whereas those obtained by theoretical calculation were 1370 and 818 cm-1, respectively. Strong correlation was observed between the mixing molar ratios and observed peak area ratios, suggesting that FT-IR analysis can be used to obtain relative amounts of the individual components of flame retardant mixture.

Influence of D.I. Water Pressure and Purified $N_2$ Gas on the Inter Level Dielectric-Chemical Mechanical Polishing Process (탈이온수의 압력과 정제된 $N_2$ 가스가 ILD-CMP 공정에 미치는 영향)

  • Kim, Sang-Yong;Seo, Yong-Jin;Kim, Chang-Il;Chung, Hun-Sang;Lee, Woo-Sun;Chang, Eui-Goo
    • Proceedings of the Korean Institute of Electrical and Electronic Material Engineers Conference
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    • 2000.04b
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    • pp.31-34
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    • 2000
  • It is very important to understand the correlation of between inter layer dielectric(ILD) CMP process and various facility factors supplied to equipment system. In this paper, the correlation between the various facility factors supplied to CMP equipment system and ILD CMP process were studied. To prevent the partial over-polishing(edge hot-spot) generated in the wafer edge area during polishing, we analyzed various facilities supplied at supply system. With facility shortage of D.I. water(DIW) pressure, we introduced an adding purified $N_2(PN_2)$ gas in polishing head cleaning station for increasing a cleaning effect. DIW pressure and PN2 gas factors were not related with removal rate, but edge hot-spot of patterned wafer had a serious relation. We estimated two factors (DIW pressure and PN2 gas) for the improvement of CMP process. Especially, we obtained a uniform planarity in patterned wafer and prohibited more than 90% wafer edge over-polishing. In this study, we acknowledged that facility factors supplied to equipment system played an important role in ILD-CMP process.

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Analysis of Ventilation Performance of PCVD Facility for Solar Cell Manufacturing (Explosion Prevention Aspect) (태양전지 제조용 PCVD설비의 환기 성능 분석(폭발 방지 측면))

  • Lee, Seoung-Sam;An, Hyeong-hwan
    • Journal of the Korean Institute of Gas
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    • v.26 no.5
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    • pp.35-40
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    • 2022
  • PCVD (Plasma Chemical Vapor Deposition), a solar cell manufacturing facility, is a facility that deposits plasma generated in a chamber (NH3, SIH4, O2 on a wafer. In the PCVD facility, gas movement and injection is performed in the gas cabinet, and there are many leak points inside because MFC, regulator, valve, pipe, etc. are intricately connected. In order to prevent explosion in case of leakage of NH3 with an upper explosive limit (UEL) of 33.6% and a lower explosive limit (LEL) of 15%, the dilution capacity must be capable of allowing the concentration of NH3 to be out of the explosive range. This study was analyzed using the CFD analysis technique, which can confirm the dilution ability in 3D and numerical values when NH3 gas leaks from the existing PCVD gas cabinet. As a result, it was concluded that it corresponds to medium dilution and that testicular ventilation is possible through facility improvement.

Decomposition of Ethylene by Using Dielectric Barrier Discharge Plasma (유전체 배리어 방전 플라즈마를 이용한 에틸렌의 분해)

  • Jang, Doo Il;Lim, Tae Hun;Lee, Sang Baek;Mok, Young Sun;Park, Hoeman
    • Applied Chemistry for Engineering
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    • v.23 no.6
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    • pp.608-613
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    • 2012
  • Dielectric barrier discharge plasma reactor was applied to the removal of ethylene from a simulated storage facility ($1.0m^3$) of fruits and vegetables. The system operated in a closed-loop mode by feeding the contaminated gas to the plasma reactor and recirculating the treated gas back to the storage facility. The experiments were carried out with parameters such as discharge power, circulation flow rate, initial ethylene concentration and treatment time. The rate of ethylene decomposition was mainly controlled by the discharge power and the treatment time. With the other conditions kept constant, the ethylene decomposition rate in the presence of the manganese oxide ozone control catalyst installed downstream from the plasma reactor was lower than that in the absence of it. The suggests that unreacted ozone from the plasma reactor accumulated in the storage facility where it additionally decomposed ethylene. On the basis of an initial ethylene concentration of 50 ppm, the energy requirement for completing the decomposition was about 60 kJ.

Evaluation of Damage Range Variation Based on Operation System of Chlorine Facility in Water Purification Plant using KORA (KORA를 활용한 정수장 염소 취급시설의 운영조건에 따른 피해범위 변화 평가)

  • Kwak, Sollim;Lim, Hyeongjun;Ryu, Taekwon;Choi, Woosoo;Jung, Jinhee;Lee, Jieun;Kim, Jungkon;Lee, Yeonhee;Ryu, Jisung;Yoon, Junheon;Yoon, Yi;Lee, Jinseon
    • Journal of the Korean Institute of Gas
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    • v.22 no.3
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    • pp.84-90
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    • 2018
  • We researched the way to minimize the damage when the chlorine-leak accident take place in a purification plant. Since the level of risk based on the Off-site Risk Assessment(ORA) is a combination of proportional to the number of residents in the damaged area and frequency of accidents, we suggested the adequate conditions to reduce the number of residents in the damaged area by means of the operating temperature of a handling facility, installation of a emergency shut-off valve, and the analysis of the variation of the damaging range in accordance with the type of enclosure. The coverage of damage was calculated by the 'KORA(Korea Off-site Risk Assessment Supporting Tool) program. The research shows that the lower operating temperature gets, the more emergency shut-off valve being installed and the higher enclosure level of facility becomes, the extent of damage gets decreased. The decreasing rate of worst case was 17.6%, 71%, 34.5% respectively, the decreasing rate of alternative case was 31.6%, 69.0%, 34.8% respectively.

A Study on the Improvement of Methodologies for Establishing a Vulnerability Classification of Chemical Terrorism in Public Facilities (다중이용시설 화학테러 취약등급설정 방법론 개선에 대한 연구)

  • Joo, Sun Ho;Kim, Si-Kuk;Hong, Sungchul
    • Fire Science and Engineering
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    • v.34 no.1
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    • pp.89-102
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    • 2020
  • Chemical terrorism using toxic and flammable gases, which could be fatal to the health of the human body, poses a serious threat to the security of most advanced countries, as well as those that are suffering from local disputes, due to the asymmetric information that exists between terrorist actors and victims. The countermeasures against chemical terrorism can be roughly divided into three stages: prevention, response, and probation. The critical factors for each professional response agency, and the personnel that determine the degree and range of chemical terrorism damage, are performing missions successfully in the process of the prevention and the response stage against chemical terrorism. To do this, conducting objective and systematical assessments on facilities that could potentially be the subject of chemical terrorism is more important than anything. In this study, we compared the existing domestic and foreign vulnerable classification systems for chemical terrorism, reviewed the current direction of improvement in domestic classification systems, and suggested more scientific and systematic methodologies through the vulnerability assessment on an actual public facility sample.

Risk Priority Number of Chemical Facilities by the Risk Assessment of Injury Analysis in the Chemical Plant (재해분석을 통한 화학공장의 위험성 평가에 따른 화학설비의 위험도 우선순위)

  • Shin, Woonchul
    • Journal of the Korean Institute of Gas
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    • v.17 no.4
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    • pp.39-44
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    • 2013
  • There have been large explosions at some chemical plants recently. Accidents in chemical plants have been caused mainly by servicing for maintenance. There is a need to find a key target for effective injury prevention in maintenance. In this paper, facilities were selected as a key target and the risk priority numbers of the facilities were calculated in order to prioritize preventative measures. The research method was based on the followings; the list of the facilities is found through injury analysis. Then, the risk of each facility was calculated by the frequency of accidents and the working day loss through injuries. In addition, the risk of the facilities was calculated again by the frequency and the severity based on knowledge and experience of experts. As a result, the facilities in chemical plant maintenance are ranked in order of high to low risk priority number; reactor, dryer, tank lorry, etc. In the future, special measures and attention should be directed according to the risk priority number during the maintenance of chemical plants.

Study on Coal Combustion Characteristics with 1MWth Test Facility (1MWth 실험연소로를 이용한 석탄의 연소특성 연구)

  • Jang, Gil Hong;Chang, In Gab;Jeong, Seok Yong
    • Transactions of the Korean Society of Mechanical Engineers B
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    • v.23 no.11
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    • pp.1464-1472
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    • 1999
  • Design and operation of $1MW_{th}$ pulverized coal combustion testing facility are described. Also the influence of air staging on NOx emission and burnout of coal flames was investigated in this facility. The test facility consisted of coal feeding system, firing system and flue gas treatment system. A top-fired externally air staging burner was adopted in order to avoid influence of gravity on the coal particles and for easy maintenance. Distribution of temperature and chemical species concentration of coal flames could be measured in vertical pass of furnace. Main fuel was pulverized (83.4% less than $80{\mu}m$) Australian high bituminous coal. From variety of test conditions, overall excess air ratio was selected at 1.2(20% excess air). Tho study showed that increasing the staged air resulted in lower NOx omission, and it was suggested to be more than 40% of the total combustion air for the substantial NOx reduction. Sufficient burnout was not achievable when NOx emission was less than 500ppm. Also, the amount of core air did not influence tho NOx reduction.