Proceedings of the International Conference on Sustainable Engineering, Infrastructure and Development, ICO-SEID 2022, 23-24 November 2022, Jakarta, Indonesia

Research Article

Failure Risk Analysis in Amine Contactor Unit Using Failure Mode and Effect Analysis (FMEA) Method at PT X

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  • @INPROCEEDINGS{10.4108/eai.23-11-2022.2341590,
        author={Hafiz Arie Rachmantyo and Betanti  Ridhosari and Ari  Rahman},
        title={Failure Risk Analysis in Amine Contactor Unit Using Failure Mode and Effect Analysis (FMEA) Method at PT X},
        proceedings={Proceedings of the International Conference on Sustainable Engineering, Infrastructure and Development, ICO-SEID 2022, 23-24 November 2022, Jakarta, Indonesia},
        publisher={EAI},
        proceedings_a={ICO-SEID},
        year={2023},
        month={12},
        keywords={gas failures h2s fmea rpn},
        doi={10.4108/eai.23-11-2022.2341590}
    }
    
  • Hafiz Arie Rachmantyo
    Betanti Ridhosari
    Ari Rahman
    Year: 2023
    Failure Risk Analysis in Amine Contactor Unit Using Failure Mode and Effect Analysis (FMEA) Method at PT X
    ICO-SEID
    EAI
    DOI: 10.4108/eai.23-11-2022.2341590
Hafiz Arie Rachmantyo1, Betanti Ridhosari1,*, Ari Rahman1
  • 1: Department of Environmental Engineering, Faculty of Infrastructure Planning, Pertamina University
*Contact email: betanti.ridhosari@universitaspertamina.ac.id

Abstract

PT X is an oil and natural gas company. One necessary production process is contaminant separation. The separation is done through a sweetening process using an amine contactor unit. The process involves hydrocarbon gases, H2S, and CO2. This process could potentially fail. Thus, it should be managed because chemical materials can harm occupational health, safety, and the environment. FMEA is a method to assess the risk of failures. Risk assessment begins by identifying potential hazards, then analyzing them based on hazard probability levels, risk severity levels, and the effectiveness of control measures, called detection. The assessment of the three main components in the amine contactor unit (pipes, valves, instruments) found potential failures: leaks, corrosion, and faulty pressure differential instruments. The highest risk priority number (RPN) from each component was in the gas inlet pipe, gas inlet valve, and instrument level control valve.