Engineering Excellence: Real-World Solutions

Explore our case studies to see how iFluids Engineering tackles real-world challenges across industries. These examples showcase our expertise in:

  • Fluid dynamics analysis
  • Process optimization
  • Safety management
  • Regulatory compliance

Each study demonstrates how we apply innovative techniques to deliver measurable improvements. Whether you’re facing similar challenges or exploring potential enhancements, discover how our solutions drive efficiency and safety.

Use the search bar to find specific cases or browse our diverse project portfolio below.

Indian process safety engineers reviewing HAZOP, LOPA, bow-tie, risk matrix and QRA techniques for oil and gas risk assessment.
Process safety engineers evaluating risk assessment techniques such as HAZOP, LOPA, bow-tie analysis and QRA in line with IEC 31010 guidance.

IEC 31010 Risk Assessment Techniques: A Selection Guide for Oil & Gas Process Safety Studies

IEC 31010:2019, published jointly with ISO as a supporting standard to ISO 31000:2018, provides internationally recognized guidance for selecting and applying risk assessment techniques across engineering, financial, and operational domains.…

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Engineer reviewing a LOPA risk reduction factor and SIL allocation at a SIS cabinet
IEC 61511 requires this RRF-to-SIL allocation step to be traceable through Clause 9 before SIS design begins

LOPA to SIL Allocation Under IEC 61511: From Risk Reduction Factor to SIL Target

IEC 61511, Functional Safety: Safety Instrumented Systems for the Process Industry Sector (consolidated edition IEC 61511-1:2016+AMD1:2017), published by the International Electrotechnical Commission, governs how process facilities identify, allocate, and verify…

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API 580 vs API 581 RBI Vessel Inspection
Ultrasonic thickness data like this feeds the PoF inputs behind both API 580 and API 581.

What a Good Risk-Based Inspection (RBI) Data Package Should Include

Risk-Based Inspection (RBI) under API RP 580 and API RP 581 ranks fixed equipment by probability of failure and consequence of failure, and both halves of that ranking depend entirely…

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API 580, API 581 inspection: engineer measuring pressure vessel thickness
Ultrasonic thickness data like this feeds the PoF inputs behind both API 580 and API 581

API 580 vs API 581: Part-by-Part Technical Comparison for RBI Compliance

API RP 580, Risk-Based Inspection, and API RP 581, Risk-Based Inspection Methodology, are both published by the American Petroleum Institute, and both govern how fixed equipment and piping in hydrocarbon…

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Engineer inspecting centrifugal pump, reciprocating pump, and compressor skids in a process plant

API 610 vs API 674 vs API 618: Selecting the Right Equipment Standard

API 610, API 674, and API 618 govern three distinct classes of rotating equipment used across oil and gas, petrochemical, and gas processing facilities, and confusing their scope is a…

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Engineer in PPE inspecting flame detector mounted on pipe rack at an oil and gas process unit
Detector siting decisions combine hazardous area classification, dispersion behavior, and detection objective.

Fire and Gas Detector Placement Rules: Standards and Engineering Criteria

No single standard governs fire and gas detector placement rules end to end. API RP 505 classifies hazardous areas at petroleum facilities for electrical equipment selection, and its zone maps…

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Indian engineer reviewing a fire and gas detector layout at a refinery, comparing OISD-STD-116 requirements with ISA-TR84.00.07 performance-based mapping.
Integrating OISD-STD-116 fire-protection requirements with ISA-TR84.00.07 performance-based fire and gas system evaluation.

OISD vs ISA TR84.00.07: Reconciling Fire and Gas Mapping Requirements in India

OISD-116, published by India's Oil Industry Safety Directorate, sets prescriptive design rules for fire and gas detection and alarm systems at refineries and gas processing plants. ISA TR84.00.07, issued by…

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API 570 vs API 580 comparison showing piping inspection and risk-based inspection in an industrial plant
Understanding the difference between API 570 piping inspection and API 580 RBI methodology

API 570 vs API 580: Understanding the Key Differences Between Piping Inspection and Risk-Based Inspection 

API 570 vs API 580 Maintaining the integrity of piping systems and pressure equipment is essential for ensuring safe, reliable, and efficient operations across industries such as oil and gas,…

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Steel building frame under construction with drawings, hard hat and steel section representing ANSIAISC 360 16 structural steel design.
ANSI/AISC 360-16 provides the design basis for safe, stable and durable structural steel buildings

ANSI/AISC 360-16 – Specification for Structural Steel Buildings

Overview ANSI/AISC 360-16, commonly known as the Specification for Structural Steel Buildings, is a key reference used in structural steel design. It gives engineers a clear basis for designing steel…

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Aboveground storage tank during lightning storm representing API RP 545 lightning protection and grounding requirements.
API RP 545 provides guidance to reduce lightning-related fire risks in aboveground storage tanks

API RP 545 – Lightning Protection for Aboveground Storage Tanks

Introduction Lightning strikes represent one of the most significant external hazards affecting aboveground storage tanks handling flammable and combustible liquids. A lightning event can introduce extremely high transient currents into…

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