Source Models Flashcards

1
Q

Most incidents in chemical plants result in spills of?

A

Toxic, Flammable, and explosive materials

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
2
Q

Typical incidents might include?

A
  1. Rupture or breakage of a pipeline
  2. A hole in a tank or pipe
  3. Runaway reaction
  4. Fire external to the vessel
How well did you know this?
1
Not at all
2
3
4
5
Perfectly
3
Q

Once the incident is known, _______ are selected to describe how the hazardous materials were discharged from the process

A

Source models

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
4
Q

Is usually done as part of Quantitative Risk
Analysis (QRA) in the design phase to define the limits of the
design envelope and to ensure that the resulting engineering
design to mitigate or remove the hazard is overdesigned.

A

Source Modelling

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
5
Q

Source Modelling is usually done as part of __ in the ____-

A

Quantitative Risk Analysis, Design phase

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
6
Q

The resulting engineering design to mitigate or remove the hazard is _____

A

overdesigned

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
7
Q

Describes the physical and chemical processes occurring during the release of a material

A

Hazardous material event model

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
8
Q

A release could be?

A
  1. Outflow from a vessel
  2. evaporation from a liquid pool
How well did you know this?
1
Not at all
2
3
4
5
Perfectly
9
Q

Source models provide?

A

description of the rate of discharge,
total quantity discharged,
total time of discharge and
state of discharge

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
10
Q

Characterized by the amount of material released

A

Strength of a source

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
11
Q

What governs source strength?

A

Physical state of material
Containment pressure
Temperature

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
12
Q

A release may be:

A

Continuous
Instantaneous

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
13
Q

Source strength is total mass released (kg)

A

instantaneous

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
14
Q

Source strength is rate of mass released (kg/s)

A

Continuous

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
15
Q

Constructed from fundamental/empirical equation representing the physiochemical process occurring during release of materials

A

Source models

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
16
Q

Only can be applied once the incident has been identified

A

Source models

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
17
Q

Technical information needed:

A

Rate of discharge
total quantity discharged
State of discharge

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
18
Q

Other Types of Hazardous Material Event Models

A
  1. Dispersion Model
  2. Fire & Explosion Model
  3. Effect Model
How well did you know this?
1
Not at all
2
3
4
5
Perfectly
19
Q

To describe how the material is transported downwind and dispersed to some concentration levels

A

Dispersion Model

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
20
Q

To convert the source model information into energy hazard potentials

A

Fire & Explosion model

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
21
Q

Example of Energy hazard potential

A

Thermal radiation
Explosion overpressure

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
22
Q

Evaluate potential loss/damage on people, properties and environment

A

Effect model

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
23
Q

Mode of Release (2)

A

Wide aperture release
Limited aperture release

24
Q

Releasing a substantial amount of material in a short time

A

Wide aperture release

25
Large hole developing in process unit
Wide aperture Release
26
Examples of WAR
Overpressure explosion, explosion of a storage tank
27
Slow release of material that causing non-immediate effect to upstream
Limited Aperture Release
28
Examples of LAR
Leaks in flanges, valves and pumps Ruptured Pipes, cracks, relief systems
29
Number of possible release points from a chemical vessel
Relief valve Hole Crack Valve Severed or Rupture Pipe Pump Seal Flange Pipe Connection
30
Types of Release
Gas/Vapor Leak Vapor or Two-Phase Vapor/Liquid Leak Liquid or Liquid Flashing into Vapor
31
Influences type of release
Physical State of a material
32
Source models describing a material release:
1. Flow of Liquid through a hole 2. Flow of liquid through a hole in a tank 3. Flow of Liquid through Pipes 4. Liquids Flashing 5. Liquid pool evaporation or boiling 6. Flow of gases/vapor through holes from vessels or pipes
33
A tank that develops a hole. Pressure of the liquid contained in the tank is converted into kinetic energy as it drains from the hole.
Liquid flow through a hole (Ambient Conditions)
34
Frictional forces of the liquid draining through the hole convert some of the kinetic energy to thermal energy
Liquid flow through a hole (Ambient Conditions)
35
Uses mechanical energy balance for the flow of incompressible liquids through pipes (density is constant)
Flow of liquid through pipes
36
Driving force for the movement of liquid across pipes
Pressure gradient
37
Friction forces between he liquid and the wall of the pipe convert?
Kinetic energy into thermal energy
38
Frictional forces results in a decrease in the liquid ______ and a decrease in the liquid ______
velocity and pressure
39
Normally occurs when a liquid stored under pressure above their normal boiling point experiences sudden ambient environment causing the liquid to flash into vapor sometimes explosively
Flashing
40
If the tank develops a leak, the liquid will?
Partially flash into vapor
41
The process is rapid and is assumed to be adiabatic
Partial flashing
42
Rate of evaporation from a pool depends on:
1. liquid's properties 2. subsoil's properties
43
A key note is if liquid is released into a?
contained pool or not
44
The pool height = volume spilled/cross sectional area of the containment structure
Contained pool
45
Release is not contained then it is called?
Freely spreading pool
46
US EPA Offsite Consequence Analysis Guide recommends a pool depth of ? for not contained pools
1 cm
47
The vapor above the pool is blown away by prevailing winds as a result of vapor diffusion
Evaporation from a pool for Non-boiling liquids
48
The amount of vapor removed through the process of evaporation from a pool (Non-boiling liquids) depends on:
Partial vapor pressure of the liquid Prevailing wind velocity area of the pool
49
Energy contained within the gas or vapor as a result of its pressure is converted into kinetic energy as the gas escapes and expands through the hole
Flow of Vapor though Holes
50
What do change as the gas or vapor exits through the leak?
Density, pressure and temperature
51
Is modeled using two special cases
Vapor flow through pipes
52
Vapor flow through pipes is modeled using two special cases:
Adiabatic and isothermal
53
Corresponds to rapid vapor flow through an insulated pipe
adiabatic case
54
Corresponds to flow through an uninsulated pipe maintained at a constant temperature
Isothermal case
55
Example of isothermal case
Underwater pipeline
56