• Journal of the Korean Institute of Gas
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• v.15 no.6
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• pp.20-27
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• 2011

The consequence analysis (CA) is widely using in the petrochemical plant through adoption of the process safety management (PSM) system, but it has not practical problem that the CA was not reflected effects for employee count, business interruption loss, utility usage, and etc.. In this study, to establish the practical emergency response plan and to achieve risk based management, the consequence based on the damage area and the financial loss were estimated and compared through application on facilities in the petrochemical plant. If the damage area is used, the consequence category must be determined by safety area considering simultaneously damage area, fatality area and toxic area. Also, the consequences based on the financial loss is more practical method for the case of considering process properties and circumstances.

• Transactions of the Korean Society of Mechanical Engineers A
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• v.35 no.2
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• pp.143-148
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• 2011

Corrosion at the top of a distillation column is a common problem in refineries and chemical plants. In particular, severe damage has been inflicted in refineries by corrosive materials such as hydrogen sulfide and chlorine. Therefore, the mechanism of the corrosion occurring at the top of a distillation column has been analyzed, and a model for forecasting the corrosion rate has been developed. Four major materials were selected for modeling: $H_2S$, $CO_2$, $H^+$ and $Cl^-$. These were selected by taking into consideration their effect on the corrosion rate. Studies on the transport phenomenon and reaction engineering for this model were carried out, and the reliability of the model was verified on the basis of the data measured at a real refinery.

• Korean Chemical Engineering Research
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• v.44 no.5
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• pp.425-434
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• 2006

The operability and productivity of continuous processes, especially in petrochemical industries have made remarkable improvement during the past twenty years through advanced process control (APC) typified by model-based predictive control. On the other hand, APC have not been actively practiced in industrial batch processes typified by batch polymerization reactors. Perhaps the main cause for this has been the lack of reliable batch process APC techniques that can overcome the unique problems in industrial batch processes. Recently, some noteworthy progress is being made in this area. New high-performance batch process control techniques that can accommodate and also overcome the unique problems of industrial batch processes have been proposed on the basis of iterative learning control (ILC). In this review paper, recent advancement in the batch process APC techniques are presented, with a particular focus on the variations of the so called Q-ILC method, with the hope that they are widely practiced in different industrial batch processes and enhance their operations.

• Korean Chemical Engineering Research
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• v.56 no.3
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• pp.421-429
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• 2018

We performed process and CFD simulations of a 100 kW fuel cell system. By process simulation, we derived the input flow rate of each unit process and the recycle diesel flow rate. Through CFD simulation considering the recycle diesel flow, more efficient operational condition was found. Using 6 desulfurize reactors, a TSA process for a 100 kW fuel cell system was successfully constructed. Heat interference between reactors was found to be negligible. These results will contribute to increasing the efficiency of fuel cell system and the developed desulfurizing module design will contribute to the clean petrochemical technology as well as fuel cell systems.

• Proceedings of the Korean Institute of Industrial Safety Conference
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• 1998.11a
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• pp.83-88
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• 1998

방향족 화합물은 합성수지, 합성고무, 합성섬유 등의 석유화학제품의 원료와 2성분 또는 3성분 이상을 혼합한 도료공업에서 광범위하게 사용되고 있다. 그러나 이들 물질들은 공정상의 제조, 저장, 처리과정에서 고온, 고압의 조건에서 많이 노출되어 있을 뿐 아니라 취급과 사용 중에 부주의로 인한 폭발과 화재사고가 증가하고 있다. 그러므로 사고예방을 위해서는 취급하는 물질의 기본적인 위험 특성을 정확하게 파악하여 예방대책을 강구하여야 하므로, 인화성 액체의 경우에는 위험성의 지표인 인화점(Flash point)을 반드시 파악하여야 한다. (중략)

• Proceedings of the Korea Air Pollution Research Association Conference
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• 2000.04a
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• pp.369-370
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• 2000

석유화학공업단지, 도장공업, 유기용제 제조공정에서 휘발성유기화합물인 가스상 물질이 다양하게 배출되어진다. VOCs 제거하기 위해서 흡착, 연소, 광촉매, 코로나방전에 의한 플라즈마기술 등이 제어기술로 응용되고 있다. 또한 Bio필터를 이용한 휘발성 유기화합물의 제어기술은 비용절감을 위해서 이용되어왔지만, 생물학적 제어기술을 효과적으로 적용하기 위해서는 가스의 농도, 물리적 특성, 온도변화, 함수율 등의 영향인자에 따라서 재거효율이 민감하게 반응하는 특성 때문에 여러 가지 단점을 내포하고 있다. (중략)

• Proceedings of the Korea Air Pollution Research Association Conference
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• 2002.11a
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• pp.356-357
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• 2002

Paint Booth 등의 공정에서 배출되는 휘발성유기화합물(volatile organic compounds, VOCs)등 유해물질로 인한 대기오염의 증가와 이의 이동 확산에 따른 수질 및 토양오염으로 지역 주민의 호흡기 또는 음식물을 통한 노출 위해성이 증가하고 있다. 석유화학단지 및 주변에서 발생되는 VOCs등 유해물질은 발암성 등 만성적으로 환경성 질환을 유발할 가능성이 매우 높다. (중략)

• Proceedings of the Korea Society for Energy Engineering kosee Conference
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• 1999.11a
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• pp.197-204
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• 1999

VOC(volatile organic compound)는 도료제조, 자동차, 선박의 도색, 인쇄, 염색 공정에서 주로 발생하는 휘발성 유기화합물로서 호흡기로 들어가면 중추신경 등 주요 기관의 장애를 일으킬 수 있으며, 질소화합물과 광화학반응을 일으켜 오존을 유발하는 위험물질이다. 정부에서는 1991년 대기환경보존법을 제정하여 유기용제의 배출을 규제하고 있고, 이 법에 따라 금년부터 석유화학정제업, 저유소에 VOC 방지시설을 의무적으로 설치해야 한다.(중략)

• Proceedings of the Korean Vacuum Society Conference
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• 2013.02a
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• pp.290-290
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• 2013

플라즈마 전해산화(Plasma Electrolytic Oxidation)란 저 농도의 알칼리 전해액을 매개로, 고전압을 가해 미세 플라즈마 방전을 유도하여 Al, Mg, Ti 등의 금속표면을 산화시켜 고내식성, 초경합금 수준의 내마모성, 탁월한 절연성과 고경도성을 가지는 산화막을 형성시키는 기술로 전자, 자동차, 의료, 섬유, 해양, 석유화학 산업에 이르기까지 광범위한 분야에 적용되어 우수한 물성을 확보할 수 있는 차세대의 표면처리 기술이다. 본 연구에서는 6061 알루미늄 합금을 이용하여 다양한 전해액 조건에서 플라즈마 전해산화 공정으로 Al2O3 산화막을 형성시켰다. 산화막의 조성 및 미세구조는 XRD와 FE-SEM, EDS를 이용하여 분석하였다. 형성된 산화막은 회색에서 밝은 회색으로 시편 전면에 고르게 나타났다. 전해액 조성을 바꾸어줌에 따라 각기 다른 표면 특성을 가지는 산화막을 얻을 수 있었고, 그에 따른 물성 변화를 분석하였다. 특히 Si 이온 농도를 조절함으로써 피막 성장인자와 표면 미세구조를 제어할 수 있었다.

• Korean Chemical Engineering Research
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• v.46 no.3
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• pp.561-566
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• 2008

Gasification plant using petroleum coke for refinery and power generation process is increased from considering petroleum coke as a valuable fuel. In this study, gasification of petroleum coke was performed to utilize petroleum coke and to develop essential technology using 1T/D coal gasification system. In case of petroleum coke gasification, because of lower reactivity, consumption of oxygen is higher than coal gasification. The calorific value of syngas from petroleum coke mixed with coal at a mass ratio of 1:1 shows about $6.7{\sim}7.2MJ/Nm^3$. Although carbon conversion could reach more than 92% according to oxygen amount, cold gas efficiency shows lower value than the case of coal. Therefore, it was shown that complemental study in burner design to atomize slurry droplet is required to elevate gasification performance of petroleum coke which has lower reactivity than coal.