Title: Senior Design
1- Senior Design
- Guest Lecture 3
- Process Safety Applications
- For Design Engineers
- CHEN 4470
- Spring 2007
2Importance 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.
3Importance 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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13Process 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????
14Process 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.
15Mitigating Process Risk
The operating risk is mitigated through the
application of safeguards that reduce the risk to
an acceptable level.
16Layer 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.
17LOPA 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
18Inherently 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.
19Inherently 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
20Inherently Safe Process Design Example 1
Azeotropic Distillation vs. Pervaporation
Standard Process
Inherently Safer Process
21Conclusions