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Senior Design

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Title: Senior Design


1
  • Senior Design
  • Guest Lecture 3
  • Process Safety Applications
  • For Design Engineers
  • CHEN 4470
  • Spring 2007

2
Importance of Process Safety
  • The safety record of the chemical process
    industry is the responsibility of all of us in
    the profession.
  • Process safety is important for employees, the
    environment, the general public, and its the
    law.
  • As process design engineers we are tasked with
    reducing the risk of operating a chemical
    manufacturing process to a level acceptable to
    employees, regulatory authorities, insurance
    underwriters and the community at large.
  • Recent chemical plant disasters underscore the
    importance of this point in terms of both human
    and financial losses.

3
Importance of Process Safety
  • Sonatrach LNG Plant - Skikda, Algeria, January
    2004
  • Incident
  • A defective, high pressure, steam boiler
    ruptured.
  • The resultant explosion on rupture damaged nearby
    vessels containing flammables.
  • Flammable loss of containment resulted in further
    fires and explosions.
  • Result
  • 23 workers were killed.
  • Nine bodies never recovered.
  • 74 were injured.
  • 800,000,000 (U.S.) estimated property damage.

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Process Safety Terminology
Hazard vs. Risk
  • HAZARD is a measure of the severity of the
    consequences of a catastrophic failure of a given
    process or system, regardless of the likelihood
    and without considering safeguards.
  • RISK is the combination of both the severity of
    the worst case consequence and the likelihood of
    the initiating cause occurring.
  • In short, for an EXISTING PROCESS, we have little
    influence on the HAZARD, but through the
    application of safeguards, we can reduce the RISK
    of operating the process.

How do we quantify the Hazards of a process????
14
Process Hazard Analysis
  • Process Hazard Analysis (PHA) is a technique for
    determining the RISK of operating a process or
    unit operation.
  • PHAs are required by law for process handling
    threshhold quantities for certain listed Highly
    Hazardous Chemicals (HHC) or flammables.
  • Various techniques have been approved for
    conducting PHAs
  • HAZOP
  • What If?
  • FMEA
  • In general, a PHA is conducted as a series of
    facilitated, team brainstorming sessions to
    systematically analyze the process.

15
Mitigating Process Risk
The operating risk is mitigated through the
application of safeguards that reduce the risk to
an acceptable level.
16
Layer of Protection Analysis
  • LOPA is a quantitative technique for reducing the
    RISK of a process.
  • The theory of LOPA is based on not putting all
    your eggs in one basket.
  • The layers mitigate the process RISK as
    determined by the PHA.
  • Each layer reduces the RISK of operating the
    process.

17
LOPA Example
  • Failure of Transfer Pump leading to overfill of
    Process Vessel.
  • Potential release of material to the environment
    requiring reporting or remediation.
  • Potential personnel injury due to exposure to
    material.
  • Severity would be based on properties of the
    material released.

http//powerlink.powerstream.net/002/00174/051222b
p/BPAnimations.asx
18
Inherently Safe Process Design
  • Inherent safety is a concept based on eliminating
    the causes and/or reducing the consequences of
    potential process upsets.
  • Inherently Safe Process Design is a technique
    applied during the conceptual phase of process
    design.
  • Inherently Safe Process Design targets the
    HAZARD, rather than reducing the RISK after the
    fact.
  • This technique is based on making inherently
    safer design choices at a point in the process
    development where the engineer has the most
    influence on the final design.

19
Inherently Safe Process Design
Inherently safe process design can be grouped
into 5 categories

Category
Example
1
Intensification
Continuous reactor vs. batch reactor
2
Substitution
Change of feedstock
3
Attenuation
Alternate technology
4
Limitation of effects
Minimization of storage volume
5
Simplification
Gravity flow vs. pumping
20
Inherently Safe Process Design Example 1
Azeotropic Distillation vs. Pervaporation

Standard Process
Inherently Safer Process
21
Conclusions
  • Questions Comments
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