TOXIC RELEASE AND DISPERSION Flashcards

TOXIC RELEASE AND DISPERSION

1
Q

During an accident, _____can release _____ quickly and in significant enough quantities to spread in dangerous clouds throughout a plant site and the local community

A

Process equipment, toxic materials

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2
Q

Rupture of pressure vessel as a result of ?

A

excessive pressure caused by a runaway reaction

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3
Q

rupture of pipeline containing

A

toxic materials at a high pressure

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4
Q

rupture of a tank containing

A

toxic materials above its atmospheric boiling point

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5
Q

What serious accident emphasize the importance of planning emergencies and designing plants to minimize the occurrence and consequences of toxic release

A

Bhopal Tragedy

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6
Q

Are routinely used to estimate the effects of a release on the plant and community environments

A

Toxic release models

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7
Q

Why must chemical engineers understand all aspects of toxic release?

A
  1. To prevent the existence of release situations
  2. To reduce the impact of a release if one occurs
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8
Q

Understanding all aspects of toxic release of a ChE requires what?

A

Toxic release model

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9
Q

Describes the airborne transport of toxic materials away from the accident site and into the plant and community

A

Dispersion models

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10
Q

After a release of the airborne, toxic material is carried away by the wind in what characteristics?

A

Plume or Puff

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11
Q

Where does the maximum concentration of toxic material is located?

A

At the release point (may not be at ground level)

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12
Q

Concentrations downwind are ____ because of ______ and dispersion of the toxic substance with ____

A

less, turbulent mixing and air

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13
Q

What is the purpose of the toxic release model?

A

Provide a tool for performing release mitigation

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14
Q

Parameters affecting atmospheric dispersion of toxic materials: (5)

A
  1. Wind speed
  2. Atmospheric stability
  3. Ground conditions (buildings, water, trees )
  4. height of the release above ground level
  5. momentum and buoyancy of the initial material released
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15
Q

Are used to estimate the concentrations downwind of a release in which the gas is mixed with fresh air.

A

Neutrally Buoyant Dispersion Models

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16
Q

These models apply to gases at low concentrations, typically in ppm range

A

Neutrally Buoyant Dispersion Models

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17
Q

2 types of neutrally buoyant vapor cloud dispersion models

A
  1. Plume models
  2. Puff models
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18
Q

Describes the steady-state concentration of material released from a continuous source

A

Plume models

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19
Q

The release of a continuous puffs

A

Plume

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20
Q

Were originally developed for dispersion from a smoke stack

A

Plume models

21
Q

Plume can develop when ?

A

There is a leak in a large tank

22
Q

If there is a leak in a large tank what could develop?

23
Q

Describes the temporal concentration of material from a single release of fixed amount of material

A

Puff model

24
Q

Used when you have essentially an instantaneous release and the cloud is swept downwind

A

Puff model

25
Describe a plume
Puff model
26
Pasquill-Gifford or
Gaussian Dispersion Models
27
Guassian Dispersion Model or?
Pasquill-Gifford
28
Because of fluctuations and turbulence, _____ is constantly changing (PG Model)
Diffusivity
29
These equations don't do a good job in predicting dispersion
Traditional transport phenomena equations
30
This assumes that the materials spread out in a normal Gaussian -type distribution
Pasquill-Gifford or Gaussian Dispersion Model
31
According to Pasquill-Gifford Model, as the plume is swept downwind, the concentration profile?
spreads out and decreases
32
This applies only to neutrally buoyant dispersion of gases in which turbulent mixing is the dominant featureof the dispersion
Pasquill-Gifford or Gaussian Dispersion Model
33
Pasquill-Gifford or Gaussian Dispersion Model is valid only for a distance of ? from the release point
0.1 to 1 km
34
Best suited for instantaneous or continuous ground-level releases of dense gases
Dense Gas Dispersion: Britter and McQuaid Model
35
In this model, the release is assumed to occur at ambient temperature and without aerosol or liquid droplet formation
Dense Gas Dispersion: Britter and McQuaid Model
36
Dense Gas Dispersion: Britter and McQuaid Model reuires specification of? (7)
Initial Cloud Volume Initial Plume Volume Flux Duration of release Initial gas density windspeed at a height of 10 m distance downwind ambient gas density
37
Any gas whose density is greater than the density of the ambient air though which it is being dispersed
dense gas
38
A gas with a molecular weight greater than that of air
dense gas
39
A gas with low temperature resulting from autorefrigeration during release
Dense gas
40
Lessening the risk of a release incident by acting on the source in a preventive and protective way
Release Mitigation
41
Reducing the likelihood of an event that could generate a hazardous vapor cloud
preventive way
42
reducing the magnitude of the release and/or exposure of local persons or property
Protective way
43
6 Release Mitigation
1. Inherent Safety 2. Engineering Design 3. Management 4. Early Vapor Detection 5. Countermeasures 6. Emergency response
44
Inventory reduction chemical substitution process attenuation
Inherent safety
45
Physical integrity of seals and construction Process Integrity Emergency Control Spill containment
Engineering design
46
Policies and procedures Training for vapor release Audits and Inspections Equipment testing routine maintenance management of change Security
Management
47
Sensors Personnel
Early vapor detection
48
Water sprays and curtains steam or air curtains deliberate ignition foams
countermeasures
49