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석유화학공장의 염화수소 누출사고를 통한 대기벤트 시스템의 안전성 향상 방안
마병철(Byung-Chol Ma),이근원(Keun-Won Lee),임지표(Ji-Pyo Im),김영철(Young-Chul Kim) 한국가스학회 2012 한국가스학회지 Vol.16 No.4
이 논문은 2008년 5월 H석유화학에서 발생한 염화수소 누출사고에 대한 염화수소 누출량 및 피해범위를 정량적으로 산정하고 예방대책을 제시하는데 그 목적이 있다. 염화수소 Column의 안전밸브를 통해 누출된 양은 안전밸브 배출용량, 이상상태방정식 및 기계적 에너지 수지 식을 사용하여 계산한 결과, 최소한 76.8 kg의 염화수소가 누출된 것을 알 수 있었다. 또한, PHAST 등의 프로그램을 활용하여 안전밸브 설치 지점(높이 24 m)으로 부터 약 350 m 떨어진 곳에서의 염화수소 농도를 예측한 결과, 지표면 누출로 가정하여 계산하는 ALOHA 및 K-CARM 프로그램에서는 각각 304 ppm과 1,700 ppm로 예측되었고 누출 높이에서의 지표면 값을 계산하는 PHAST 프로그램에서는 1 ppm 이하로 예측되었다. 위 결과는, 사고당시 염화수소가 안전밸브를 통해 최소 76.8 kg이 누출되었고 누출지점으로부터 약 350 m 떨어진 곳에 있던 근로자들이 1 ppm 이하의 농도의 HCl 가스에 폭로되었음을 말해준다. 또한, 이러한 사고를 예방하기 위해서는 염화수소와 같은 독성물질은 스크러버 등을 거쳐 세정 후 안전하게 대기로 배출(방출) 시켜야 한다는 사실을 제시한다. The purpose of this study is to carry out the consequence analysis of an accident related to the release of Hydrogen chloride occurred in a petrochemical company in Korea and suggest the measures to prevent similar accidents from happening again. The total amount released through the safety valve of HCl Column was calculated based on the rated capacity of the safety valve, the ideal gas equation and mechanical energy balance, respectively. As a result of the calculation, we found that the amount of HCl released through the safety valve was at least 76.8 kg. Also, we predicted the dispersion concentration at the position of the injured workers(more than 350 m away from the accident location) using simulation programs such as PHAST. The results of ALOHA and K-CARM are 304 ppm and 1,700 ppm. respectively. However, PHAST calculation indicated that the concentration is less than l ppm. From these results, we can understand that workers were injured by HCl gas released from the safe valve and the concentration of gas might be less than 1 ppm. Also, it is important for toxic gases such as HCl to be vented safely to the atmosphere after scrubbing.
마병철 ( Byung Chol Ma ),권혁면 ( Hyuck Myun Kwon ),김영철 ( Young Chul Kim ) 한국안전학회(구 한국산업안전학회) 2012 한국안전학회지 Vol.27 No.6
The purpose of this study is to suggest new safety technical standards to improve the safety in the incine-ration process. Firstly, we analyzed the major accidents occurred in the incineration process since 1996 and proposed 4 articles which is required to be added newly to the existing KOSHA GUIDE. Secondly, we also performed the HAZOP study for each study node and also suggested 3 articles. Finally, we analyzed recommendations commented for PSM reports which have been submitted from the enterprise located in Honam province since 2005 and proposed 2articles as well. We understand that all 9 articles proposed above, should be added to the KOSHA GUIDE in order to improve the safety in the incineration process and to prevent the major fire and explosion accidents in the design stage.
아크릴산 제조공정 사고사례를 통한 소각 시스템의 안전성 향상 방안
마병철(Byung-Chol Ma),이근원(Keun-Won Lee),임지표(Ji-Pyo Im),김영철(Young-Chul Kim) 한국가스학회 2012 한국가스학회지 Vol.16 No.4
최근 대기환경규제의 강화로 화학공장에서 발생하는 폐가스를 소각 처리하는 경우가 증대되고 있다. 이러한 소각설비는 저장탱크 상부와 배관을 통해 연결되어 화염을 통하여 폐가스를 연소 소각시키기 때문에, 배관을 따라 화염이 역화될 경우에는 치명적인 사고로 연결될 수 있다. 본 연구는 아크릴산 제조공정의 소각시스템에서 발생한 중대산업사고에 대해 폭발의 3요소와 화염의 전파 원인을 분석하여 사고 예방대책 및 안전성 향상 방안을 다음과 같이 제시하였다. 첫째, 소각시스템의 송풍기를 재 가동하기 전에는 공기 또는 불활성 가스로 충분히 희석하여 폭발을 예방하여야 한다. 둘째, 폭굉으로 전이된 화염이 저장탱크로 전파되지 않도록 소각설비의 전단 및 저장탱크 상부에 폭굉용 화염방지기를 설치하는 것이 필요하다. 섯째, 폭연용 화염방지기를 그대로 사용할 경우에는 그 전단에 파열판을 설치하거나 저장탱크 상부와 소각설비의 배관을 후드식으로 연결하여 폭굉으로 전이된 화염을 저장탱크 밖으로 분출시켜야 한다. 마지막으로, 소각설비에 연결된 송풍기의 제어반(MCC)에 순간정전 보상장치인 시간지연계전기(TDR: time delay relay)등을 설치하여 순간정전 후에도 자동으로 재가동될 수 있도록 조치해야 한다. Recently, waste gas incineration is increasing due to strong environmental regulatory system in Korea. These incinerating facilities are usually connected with the top of the storage tank through pipeline and incinerate off gas with the flame. Therefore, the flame originated from these facilities is likely to move back into pipeline and might cause an explosion of the storage tank. Accordingly, the purpose of this study is to suggest the preventive measures and the way to improve the safety of these incineration systems through the cause analysis of a major industrial accident occurred in a acrylic acid manufacturing process in Korea. As a result of the study, the preventive measures are suggested as follows. (1) Air or inert gas inflow facilities should be well designed to dilute flammable gases into air or inert gas sufficiently before the blower is restarted in order to prevent the explosion (2) It is needed for the detonation-type flame arresters to be installed on the top of the storage tanks. (3) In case of using the deflagration-type flame arresters, it is necessary to install a rupture disk before the arresters, or blow off the flame outside tanks by connecting the tank top and the incinerator with hood-type pipe. (4) TDR should be installed to be restarted automatically after the momentary power failure.
임지표 ( Ji Pyo Yim ),마병철 ( Byung Chol Ma ),정창복 ( Chang Bock Chung ) 한국안전학회(구 한국산업안전학회) 2015 한국안전학회지 Vol.30 No.4
The purpose of this study is to study the safety of a small LPG storage tank with a capacity less than 3 ton when it is exposed to an external fire. First, simulation studies were carried out using ASPEN Plus and PHAST to demonstrate that overpressurization in the tank can be relieved by discharging the LPG through an adequately sized safety valve, but the release may lead to the secondary risk of fire and explosion around the tank. Next, the temporal variations of the temperatures of the lading and tank wall were obtained using AFFTAC, which showed that the tank wall adjacent to the vapor space could be overheated in about 11 min to such a point that the weakened strength might cause a rupture of the tank and subsequent BLEVE. The consequences of the BLEVE were estimated using PHAST. Finally, several practical measures for preventing the hazards of overheating were suggested, including an anti-explosion device, sprinkling system, insulation, heat-proof coating, and enhanced safety factor for tank fabrication. The effectiveness of these measures were examined by simulations using AFFTAC and ASPEN Plus.