Risk Ppt Petro

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    PETROCHEMICAL REFINERY

    By:-

    Shikha Jaglan

    Abhishek MalikAmit Sinha

    Abhinav Sharan

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    RISK MANAGEMENT OF

    PETROCHEMICAL REFINERY

    INTRODUCTION In the competitive world of today, companies need safe and reliable

    operations for the wellbeing of employees, people in the community and

    the environment.

    We need to verify or make certain that our activities are safe enough.To go further with this statement we need to ask ourselves:-

    What do we mean by safe enough? How do we verify that anacceptable level of safety has been achieved

    What is the metric that we use for measuring risk ?

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    Why Petrochemical ?

    The petrochemical process industries represent a significant contribution tothe world economy.

    Equipment failures or operator errors can lead to sudden and unexpectedchanges in the plant operation.

    If these disruptions to normal process operation exceed the capabilities ofthe operators or the capacity of the safety systems, a severe accident can

    occur, potentially producing a devastating fire, explosion, or toxic release.

    The industry is potentially more hazardous than others.

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    Process Overflow

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    Crude oil processing1. High Temperature

    2. High Pressure

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    Risk Identification

    At Furnace1. BLEVE, is an acronym for "boiling liquid expanding vapourexplosion". This is a type of explosion that can occur when a vesselcontaining a pressurized liquid is ruptured. Such explosions can beextremely hazardous. "Blast Levelling Everything Very Effectively.

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    2. Vapor Cloud Explosion:-(1) Sudden release of a large quantity of flammable vapor. Typically

    this occurs when a vessel, containing a superheated and pressurizedliquid, ruptures.(2) Dispersion of the vapor throughout the plant site while mixingwith air.(3) Ignition of the resulting vapor cloud.

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    3. Rupturing of PIPE

    4. Short Circuit E.g. IOCL The fire broke out when petrolwas being transferred from depot to pipeline. There was aleak in valve of pipeline, which connected fuel tank to

    distribution point. The fire caused due to short circuit.5. Contamination of storage tanks. This can happen due tocorrosion inside the tank , reaction with the underground

    water (soil).This also includes spill or leak from the tank .

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    Risk Assessment

    ALARP-as low as reasonably

    practicable

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    Fault tree AnalysisExplosion in a furnace

    OVER PRSSURE Source of

    ignition

    Electricalspark

    Flamesnear

    furnace

    Burning

    cigarette

    Failure ofearthing

    Inside therefinery Outside

    sources

    Extra

    heatingof gases

    Failure

    of safetyvalve

    Corrosion

    of criticalparts ofboiler

    Negligenceby

    employees

    Poor

    maintenance

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    Risk Control

    The process of risk control embodies two methods:-1. Risk avoidance:-

    a. Effecting changes in the nature of theorganizations activities

    b. Changing the location of premises2. Risk reduction(loss prevention)Fire prevention measures:-a. safety education, increase the intensity of training

    b. Most Petrochemical fire Accident that the main

    factors causing fire accidents is human, material andenvironment, people are the most fundamental factor.Stringent fire safety management, standard workpractices are needed.

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    Fire preventive measures contd.

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    Analysis of losses

    (overall)

    100

    16.2

    15.2

    7.0

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    Conclusions and Recommendations

    Most of the risks are very hazardous so proper

    checklists should be maintained . Minimize human error by providing propertraining.

    Promote ownership of machinery/furnaces

    among the workers. Balance competing goals of security of supply,

    affordability, meeting demand growth andclimate change considerations.

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    Thank You

    Any Questions?