• Title/Summary/Keyword: chemical process safety

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A Study of Risk Reduction by SIL(Safety Integrity Level) Determination (SIL(Safety Integrity Level) 선택에 의한 리스크 감소에 관한 연구)

  • Kim, Jung-Hwan;Kim, Bum-Su;Yang, Jae-Mo;Jang, Chang-Bong;Kim, Min-Seop;Jung, Sang-Yong;Ko, Jae-Wook
    • Journal of the Korean Institute of Gas
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    • v.15 no.5
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    • pp.57-62
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    • 2011
  • Modern chemical plants including petroleum refinery and gas industries have evolved into more complex and specialized. In these industrial complexes, it is important to maintain acceptable safety level protecting from various potential disasters caused by fire, explosion and the leakage of toxic materials. Recently possibility and consequence of accidents are increasing in the industrial process. So there is a trade-off between the plant operation efficiency and safety level. In this study SIF(Safety instrument Functions) was incorporated into SIL(Safety Integrity Levels). As a result, the safety level was upgraded by designing resonable allocation of safety instruments.

Quantitative Risk Analysis of a Pervaporation Process for Concentrating Hydrogen Peroxide (과산화수소 농축을 위한 투과증발공정의 정량적 위험성 분석)

  • Jung, Ho Jin;Yoon, Ik Keun;Choi, Soo Hyoung
    • Korean Chemical Engineering Research
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    • v.52 no.6
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    • pp.750-754
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    • 2014
  • Quantitative risk analysis has been performed for a pervaporation process for production of high test peroxide. Potential main accidents are explosion and fire caused by a decomposition reaction. As the target process has a laboratory scale, the consequence is considered to belong to Category 3. An event tree has been developed as a model for occurrence of a decomposition reaction in the target process. The probability functions of the accident causes have been established based on the frequency data of similar events. Using the constructed model, the failure rate has been calculated. The result indicates that additional safety devices are required in order to achieve an acceptable risk level, i.e. an accident frequency less than $10^{-4}/yr$. Therefore, a layer of protection analysis has been applied. As a result, it is suggested to introduce inherently safer design to avoid catalytic reaction, a safety instrumented function to prevent overheating, and a relief system that prevents explosion even if a decomposition reaction occurs. The proposed method is expected to contribute to developing safety management systems for various chemical processes including concentration of hydrogen peroxide.

Quantitative Analysis of Thermal Radiation in Flare Stack (플레어스택의 정량적인 복사열 분석)

  • Jung, Sang-Yong;Lee, Heon-Seok;Kim, Bum-Su;Yoo, Jin-Hwan;Park, Chul-Hwan;Ko, Jae-Wook
    • Journal of the Korean Institute of Gas
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    • v.14 no.1
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    • pp.37-41
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    • 2010
  • The most important element for improving the process safety that occurs from the flare system installed to convert into safe materials by burning the inflammable or toxic gases within the process and this is specified in the API 521 Code so that the radiation does not cause a risk factor. The flames that occur from the flare stack holds the shape of jet fire due to the pressure and flow velocity of discharge gas. This study has identified the shape of flames by using the Chamberlain Model rather than the API 521 Code method, analyzing the radiation due to this.

Case Study of Safety Management at Small Industry Handling Hazardous Chemicals (유해화학물 취급 중소기업 시설 관리실태 현황 및 개선방안)

  • Song, Eunhee;Lee, Donghoon;Cho, Youngho;Kwak, Dongho;Park, Kyoshik
    • Journal of the Korean Institute of Gas
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    • v.21 no.4
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    • pp.21-29
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    • 2017
  • Small and medium industry facility handling hazardous chemicals was inspected and summarized. The inspection results were summarized in four categories such as hazards to process, storage, workers, and the others. The result was applied to further improvement of the facility. In conclusion, the industry intented to satisfy minimum requirement of regulation and they do not pay attention to keep maintaining the facility in integrity condition.

A Study on Knowledge Representation for Recognizing Hazardous States in Chemical Processes (화학공정의 위험상태 인식을 위한 지식 표현에 관한 연구)

  • 안대명;황규석
    • Journal of the Korean Society of Safety
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    • v.11 no.3
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    • pp.104-111
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    • 1996
  • A system was developed that could predict hazardous states for safe operation of chemical plants. This system aimed to prevent hazards of chemical processes from misoperation before real operation. In this study, a data base was organized which consisted of all hazards in the chemical processes. The structure of process was represented by signed direct graph(SDG) of NODEs and ARCs. Each NODE and ARC have property variables ; connected structure and state of processes etc. The hazards that could be occurred in processes were divided into two classes ; one is by operation of unit and the other is by hazardous materials. Using Hazardous States Transition Network, we could recognize transition progress of process states.

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Hazardous Material Process Risk Evaluation Using HAZOP and Bow-tie (HAZOP 및 BOW-TIE를 이용한 위험물질 취급공정의 위험성평가)

  • Min-Seo Nam;Byung-Tae Yoo
    • Journal of the Korean Institute of Gas
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    • v.28 no.1
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    • pp.35-43
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    • 2024
  • With continuous advancements in industry, science, and technology, there is a steady increase in the number and utilization of new chemicals. The growing societal emphasis on chemical safety management is paralleled by an increasing public demand for robust safety measures. While various ministries at the government level oversee the safety management of chemical substances, the occurrence of accidents related to chemical substances remains frequent each year due to problems such as aging facilities and careless handling. Upon analyzing domestic chemical accident cases, incidents occurred predominantly in the sequence of leakage, explosion, fire, and others. The main causes of these accidents were examined, revealing facility defects and non-compliance with safety management as the primary contributing factors. In this study, Hazard and Operability Analysis (HAZOP) was employed to identify hazardous risk factors associated with the handling of hydrofluoric acid in workplaces, and a risk assessment was performed using Bow-Tie method. Based on the results of this study, it is expected to enhance safety management plans aimed at preventing chemical accidents in workplaces dealing with similar facilities. Ultimately, these insights contribute to the development of an advanced chemical safety management system, capable of proactively preventing potential chemical accidents.

An Selection of Occupational Safety Curriculum using Analytic Hierarchy Process (AHP를 이용한 산업안전 교과목 선정에 대한 연구)

  • 김유창
    • Journal of Korean Society of Industrial and Systems Engineering
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    • v.24 no.69
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    • pp.87-92
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    • 2001
  • A significant number of all reported accidents in Korea involved education and training Based on the Labor Ministry data, statistics, show the education cause was directly involved in 38% of major accidents, Since safety managers have in charge of safety education at the factory, occupational safety curriculum must be studied to train safety manager effectively. In this study an analysis on relative importance of industrial safety curriculum for a good safety manager was performed by Analytic Hierarchy Process(AHP) The results showed that relative importance of industrial safety curriculum by AHP was safety management(w=0.240) ergonomics and system safety(w=0.201) construction safety(w=0.182) mechanic safety(w=0.139) electronic safety(w=0.134) and chemical safety(w=0.104) in order. The results could be used for industrial safety curriculum planning in university and safety organization such as Korea Occupational safety and Health Agency.

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Development of Changing Management Software(K-MOC) for Chemical Plant (화학공장의 변경관리전산시스템(K-MOC) 개발)

  • Kwon, Hyuck-Myun;Baek, Jong-Bae
    • Journal of the Korean Society of Safety
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    • v.21 no.1 s.73
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    • pp.72-78
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    • 2006
  • In many chemical plants the change or modification is carried out without proper technical review and hazard analysis, and also without adequate technical staff and procedures for comprehensive monitoring of potential hazards resulting from the change. Such changes sometimes affect to the process safety badly if it is not managed properly. Therefore, in order to prevent major industrial accidents caused by change or modification, and also in order to apply Management of Change procedure easily in the field and minimize economic burden of company caused by plant changes, K-MOC(KOSHA-Management of Change) software has been developed and provided to the chemical industry.