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HAZOP Case Study – IFS (Proprietary Chemical) 

February 3, 2026

yashpal.iism@gmail.com

Project Number: 24-715.01.615-sil-akv-hazop

HAZOP Study Serial Number: 615

Project Overview

    A Hazard and Operability (HAZOP) Study was conducted for the manufacturing of a proprietary chemical, IFS, at Sajjan India Limited (SIL) now recognised as Cohizon Lifesciences Limited, Ankleshwar, Gujarat, in accordance with IEC 61882:2001 – Hazard and Operability Studies (HAZOP Studies) – Application Guide. The objective was to systematically identify potential hazards and operability issues arising from deviations from design and operating intent.

    The study involved critical project documents like Piping and Instrumentation diagrams (P&IDs), Standard Operating Procedures (SOPs), Cause and Effect (C&E) diagrams etc. A multidisciplinary team reviewed causes, consequences, safeguards, and risk levels, and gave recommendations to enhance process safety, reliability, and emergency preparedness.

    Objective

    The objective of the HAZOP study was to systematically identify potential hazards and operability issues associated with the IFS manufacturing plant and its associated systems, and to reduce the likelihood and consequences of incidents that could impact personnel safety, plant integrity, environmental performance, and operational reliability.

    Methodology

    HAZOP Preparation

    As the process of IFS manufacturing is the trade secret of the Sajjan India Limited, hence critical document required for HAZOP preparations were not shared for back-office preparations. Therefore, in such projects we adopted a different strategy. The project engineer initially visited the Sajjan India Limited facility prior to the start of the HAZOP, and all the HAZOP preparations were done at the Sajjan India limited, Ankleshwar Facility by analysing essential data, including Piping and Instrumentation diagrams (P&IDs) and Process Description. This allowed us to identify the Nodes and the nodes identified were discussed and finalised with SIL team before the start of the HAZOP Study.

     

    Opening Meeting

    We initiated the on-site HAZOP process with an opening meeting. The agenda of the opening meeting was as:

    • Introduction of HAZOP team members.
    • Define the HAZOP methodology to HAZOP team.
    • Clarify roles of the members in HAZOP Team.
    • Process understanding by process/operations so that entire team gets familiar with the manufacturing process.
    • Review of Material Safety Data Sheets so that team has prior information on all the hazards of the chemicals used/handled during the process.
    • Review of thermal hazard / reaction calorimetry tests reports such as RC, DSC etc.

    HAZOP Brainstorming Session

    The HAZOP process was based on the principle that a team approach to hazard analysis will identify more problems than when individuals working separately combine results. The HAZOP team involved was combined of individuals with varying backgrounds and expertise. The expertise was brought together during HAZOP sessions and through a collective brainstorming effort that stimulates creativity and new ideas, and a thorough review of the process under consideration was made.

    The HAZOP team focused on specific Nodes, which were identified before the start of the study. A process parameter was identified, say flow, and an intention is created for the node under consideration. Then a series of guidewords was combined with the parameter “flow” to create deviations. For example, the guideword “no” was combined with the parameter flow to give the deviation “no flow”. The team then focused on listing all the credible causes of a “No flow” deviation beginning with the cause that can result in the worst possible consequence the team can think of. Once the causes are recorded the team listed the consequences, safeguards and any recommendations deemed appropriate. The process was repeated for the next deviation and so on until completion of the node and was repeated for all the Nodes under consideration.

    Key distinctive characteristics of HAZOP:

    • HAZOP was carried using Sphera PHA Pro software and following format was used:

    • Risk Ranking was carried out in 2 stages, that is mitigated risk after existing safeguards and residual risk after HAZOP recommendations if any.
    • Fundamentals of Independent Protection Layer (IPL) was used while identifying existing safeguards and also while providing any recommendation.
    • Various national and internationally accepted guidelines, standards and documents were used in the Study such as:
      • IEC 61882:2001
      • Centre for Chemical Process Safety
      • Gujarat Factory Rules
      • Relevant Material Safety Data Sheets (MSDS)
      • Indian and International Standards
      • ECHA for chemical information
    • Rules followed for identifying safeguards:
      • Rule 1: Safeguards should act before the event happens
      • Rule 2: Approach for deciding type and number of Safeguards. For example: if 4 safeguards are required to meet the risk in ALARP (As Low as Reasonably Practicable) region, then minimum of 2 must be preventive, and 2 can be mitigative. Also, not more than 1 admin control should be there, SIS/SIFs and mechanical safeguards should also be there in adequate number.
      • Rule 3: Safeguards should be Measurable and Auditable (demonstrate the performance)
      • Rule 4: Safeguards should be independent.  
      • Rule 5: Safeguards have the different Probability of Failure on Demand (PFD) and Risk Reduction Factor (RRF).
      • Rule 6: In HAZOP, consider failures of process control, not protection layers or safeguards.
      • Rule 7: In Case of Redundancy of Safeguard, consider Single layer of Protection
      • Rule 8: If Two Layer of Protection/Safeguards in Series, consider one. For example, RD and PSV in series are considered as one single safeguard.
      • Rule 9: If Two Transmitters on same nozzle, consider Single protection layer
    • Where existing safeguards were partial or incomplete, credit for risk reduction was not taken until the recommended actions were implemented. Such safeguards were marked as CNT (Credit Not Taken)
    • Detailed description of Nodes, Deviation, Cause, Consequences, Safeguards and Recommendations
      • HAZOP team did a detailed analysis and all the recordings are made in such a descriptive manner that it is easy to understand. The following image highlights the same.

    About Yashpal singh

    Mr. Yashpal Singh is the Managing Director and Process Safety Expert at HSE RMSPL. With 19 years of experience, he specializes in HAZOP, QRA, and functional safety engineering. He helps clients achieve safe, compliant operations while minimizing industrial risks and incidents.

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