Integration of the Urea Fertilizer Industry Process Safety Index
DOI:
https://doi.org/10.55927/fjss.v2i4.7853Keywords:
IPSV, Urea, Index Value, Process Safety AssessmentAbstract
The chemical industry has different stages of the production process, depending on the materials used and the products produced. Typically, previous approaches only use one or two parameters. The focus of this study is on a safety assessment metric called the Index Process Safety Value (IPSV). The evaluation process using IPSV involves initially identifying parameters, evaluating each parameter using IPSV, and then integrating the assessments. Integration assessments can be used to ascertain the level of risk involved in the standardization process. Standardization is carried out to ensure the specific attributes of each industrial process flow. Where in this standardization there are variations in index values and levels of potential danger. This main and initial process is the core of the Urea production process stages. Of the several stages of the urea production process, the one with the highest level of danger is during the production of Urea in the synthesis process, namely in the Reactor (DC101) with an index value of 0.4, while the lowest is in the urea synthesis process, namely in the Condenser (EA101) with the average index value is 0.28. This IPSV method can be used to analyze process safety, especially for the urea synthesis unit at Factory 5 of PT Pupuk Kaltim
Downloads
References
Cave, S.R. and Edward, D.W. (1997), “Chemical Process Route Selection Based On Assessment of Inherent Environmental Hazard”, Computers Chemical Engineering, Vol.21, S965-S970.
Chauvel, A., Lefebvre, G. (1998), Petrochemical Processes: Technical and Economic Characteristics Second Edition, Gulf Publishing Company, Paris. Dow Chemical Company, (1987).
Dow’s Fire & Explosion Index Hazard Classification Guide, sixth ed. American Institute of Chemical Engineers, New York.
Edwards, D.W., Lawrence, D., (1993). Assessing the inherent safety of chemical process routes: is there a relation between plant costs and inherent safety? Trans. IChemE 71 (B), 252–258
Gupta, J.P., Edwards, D.W. (2003), “A Simple Graphical Method for Measuring Inherent Safety”, J. Hazard. Material 104, 15-30.
Heikkila, A.M. (1999), Inherent Safety Process Plant Design – an Index Based Approach, Helsinki University of Technology
Khan, Faisal I., Amyotte, Paul R. (2005), “I2SI: A Comprehensive Quantitative Tool for Inherent Safety and Cost Evaluation”, J. Loss Prevention in the Process Industrial 18, 310-326.
Kletz, T. (2009), Inherently Safer Chemical Processes, second edition, John Wiley & Sons, Inc., New York.
Pupuk Kalimantan Timur, PT. (2013), Piping & Instrument Flow Diagram Synthesis Section (No. DWG K5-02-E1-PD-5A-T). Toyo Engineering Corporation
Pupuk Kalimantan Timur, PT. (2022), Material Safety Data Sheet Urea & Ammonia. Bontang Kalimantan Timur.
Sukardi, Rikho Dhyatmiko., Sri Hartono, Nurmuafix, Dkk. (2014), “Panduan Pengoperasian Pabrik Urea Kaltim 5”, PT Pupuk Kalimantan Timur, Bontang.
Downloads
Published
How to Cite
Issue
Section
License
Copyright (c) 2023 Mahfud, Chaidir Rahman

This work is licensed under a Creative Commons Attribution 4.0 International License.

























