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2 |
Predicting the drift
and spread
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Many computer models exhibit astounding limitations. It is usual that forecasting models for gas clouds are not able to consider the structure of the ground or water surface (e.g. flat country, forest, calm water, rough sea). Some models cannot even consider mountains as obstacles for the cloud drift.
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Below in Subchapter 2.6 a few examples are given on forecasting systems, just for the purpose of exemplification. The objective has neither been to try to find the “best” system, nor to evaluate or compare such systems. |
2.2 Gas cloudsForecasting the spread in air (Figure 1-13, Method F1) Applicable for Groups G, GD, E, ED, FE, FED, DE (all Groups with G or E) Forecasting
the spread of gas clouds in air can be estimated very roughly for the
Groups G and GD by means of Figure 2 - 2. Such estimates should always be regarded with
reservations and never be alternatives for monitoring. |
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Health Risk |
Fire/Explosion Risk |
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Release |
Ammonia, vinyl chloride, chlorine |
Methane (LNG), propane (LPG), butane (LPG), ethylene, butylene-butadiene |
Ammonia, vinyl chloride, methane (LNG), propane (LPG), butane (LPG), ethylene, butylene-butadiene |
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tonnes |
metres/ /nautical miles downwind |
metres/ /nautical miles downwind |
metres/ /nautical miles downwind |
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0.1 |
1,000 / 0.62 |
200 / 0.12 |
200 / 0.12 |
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1 |
2,000 / 1.24 |
400 / 0.25 |
400 / 0.25 |
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10 |
5,000 / 3.11 |
1,000 / 0.62 |
1,000 / 0.62 |
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100 |
10,000 / 6.21 |
2,000 / 1.24 |
2,000 / 1.24 |
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1,000 |
20,000 / 12.43 |
4,000 / 2.49 |
4,000 / 2.49 |
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Figure 2 - 2 |
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N.B. |
The above Figure 2 - 2 can also be applied to liquid chemicals (which are flammable or especially hazardous for health) in the Groups E, ED, FE, FED and DE. The spread of evaporated gas, from spills of these chemicals, can be calculated very roughly by multiplying the values in the table by VP/100, where VP is the liquid’s vapour pressure in kPa, which is less than 100 at ambient temperature. |
2.3 Floating spillsIt is
complicated to forecast the behaviour of a chemical spill that floats on
the water surface. The spill’s fate is influenced by the following
processes: |
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a) |
The drift on the surface |
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b) |
The spread on the surface |
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c) |
Evaporation |
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d) |
Dissolution |
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e) |
Chemical reactions and other conversion processes |
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Various laboratory models have been developed (e.g. Ref. 7), but very few have been validated against real spills under operational conditions at sea. Simple forecasting models have been developed for spills of chemicals that float on the water surface. For the sake of simplicity the spills are supposed neither to evaporate nor dissolve. This principle can also be used for manual calculations and is briefly described below. Forecasting the spread on water surface (Figure 1-13, Method F2) Applicable
for Groups FE, FED, F and FD (all Groups with F) |
|
Figure 2 - 4 shows how a floating chemical slick’s drift can be calculated by means of a vector diagram in the same way as oil spills. However, most chemical spills belonging to the above mentioned Groups, except for F, will disappear by evaporation and/or dissolution within roughly 10 hours.
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Forecasting the dispersion in
water body
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Concentration 1 g/m3 |
Concentration 1 mg/m3 |
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Release tonnes |
a metres |
nautical miles |
a metres |
nautical miles |
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1 |
500 |
0.3 |
5,000 |
3 |
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10 |
1,000 |
0.5 |
10,000 |
5 |
|
100 |
2,000 |
1 |
20,000 |
11 |
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1,000 |
4,000 |
2 |
40,000 |
22 |
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Figure 2 - 6 |
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It is very difficult to calculate the fate of a spill that sinks to the bottom. The reason for this is the number of parameters that influence the process (cf. Figure 2 - 7). |
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The chemical’s density affects the velocity by which the chemical sinks to the bottom. Its surface tension and solubility (even if very low) influence its behaviour on the water surface as well as its dispersing and spread in the water body during its sinking towards the seabed. The water current together with the water depth and the chemical’s density have a decisive importance for how long distance the chemical will move in the current’s direction before it touches the bottom. |
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Picture source: P. Ashworth, UK |
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Figure 2 -7 |
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The chemical’s duration on the bottom is among other factors dependant on its solubility. If the solubility is e.g. 1% or 0.001% it must obviously have a pronounced effect on its duration on the seabed. Also the existence of water currents close to the bottom influence the duration. The chemical may also penetrate into the bottom sediment. The degree of penetration depends on the sediment’s properties and structure. |
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Forecasting computer model |
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Name
ALOHA (Areal
Locations of Hazardous Atmospheres) |
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Application
Gases |
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Information Emergency responders can use ALOHA to predict the behaviour of a chemical gas in the event of an accidental release. ALOHA is a part of the decision support system CAMEO (Computer Aided Management of Emergency Operations) developed by US National Oceanic and Atmospheric Administration (NOAA) in cooperation with US Environmental Protection Agency (EPA). (Ref. 6)
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![]() Figure 2 - 8 Graphical ALOHA description of a gas cloud dispersion in air. |
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Properties |
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Advantages |
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Limitations |
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Name
MET (Modells
für
Effekte
mit
Toxischen
Gasen) |
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Application
Gases |
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Information MET makes a dose-effect-coupling for effects of toxic gases and estimates risks of human injuries in the area in the wind direction of the accidental release. The dose as integral of concentration versus time is a good criterion in a model, since it diminishes one important but uncertain source term, the emission time. But doses also are not significant enough, since there is a further toxicological step to the main aim, to estimate the effect of toxic substances on the people in the surrounding area. MET consists of the following four main modules:
The input values that MET needs are: 1) escaped substance weight, 2) wind speed and 3) a threshold value for the substance. Other parameters are automatically provided by the system in order to calculate hazardous distances. MET has modules for simulations of 1) the washout effect of the cloud by rain, 2) the influence of a simultaneous fire and 3) the dispersion characteristics of heavy gases. The model is stable to the large variations of the toxic values, since it can integrate several different values. In addition the lower explosion limit is used to calculate the size of an explosive mixture of a substance and air. The effects on mixtures of substances e.g. from fires can also be calculated.
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Properties
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Advantages |
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Limitations |
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Name
CHEMMAP |
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Application
Floaters, dissolvers, and sinkers |
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Properties
Predicts the dispersion and
fate of marine chemical spills.
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Information CHEMMAP predicts the likely trajectory and fate chemical spills in the marine environment. The system is particularly suited to contingency planning and emergency response for spills of chemical cargoes from ships but may be applied to any chemical discharge. The system contains GIS and a 3D spill model that predicts the movement of chemicals in the water. The model relies on environmental data such as wind and currents, physical data such as the proximity of shorelines, and chemical data that define the chemical's properties. CHEMMAP includes a biological effects model which evaluates the effects of chemical spills on fish, shellfish and wildlife. CHEMMAP incorporates a number of model components including:
- simulation of the
initial release and plume dynamics of a product The model uses physical-chemical properties to predict the fate of a chemical spill. These include density, vapour pressure, water solubility, environmental degradation rates, adsorbed/dissolved partitioning coefficient (KOC), viscosity, and surface tension. CHEMMAP has its own database of 900 chemicals with physical and chemical data properties. A software link is optionally available to a database of more than 40,000 pure substances and 75,000 common mixtures. The latter database also provide guidelines for how to determine the severity of the risk to health, how to handle a spill, how to store and transport chemicals, how to dispose of chemicals, what to do if a chemical catches fire and how to plan for an emergency response. Figure 2 - 11 shows the modelling of an instantaneous release of benzene (10,000 metric tons) at the water surface. The plume display is the Vertical Maximum Dissolved Concentration of Benzene in the water column (mg/m3) 40 hrs after the initial release. The colour-coded legend is located to the right of the plume with a cross section showing the plume in 3-dimensions below the legend. Above the plume is a graph of the mass balance that displays the percent of chemical that has surfaced, evaporated, in the water column, in or on the sediment and what has gone ashore over time.
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Advantages |
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Limitations |
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Name
ChemSIS
(Chemical Spill Information
System) |
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Application
Floaters, dissolvers, and
sinkers |
Properties Predicts the dispersion and fate of marine chemical spills.
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Information
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Advantages |
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Name
3D Transport and
Water Quality Model |
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Application
Dissolvers and
sinkers |
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Properties
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Information
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Figure 2 - 14 shows the modelled distribution four weeks after an experimental release of 100 tons of a low-toxic emulsifier nonyl phenol ethoxylate (water solubility appr. 10 g/l) in the sea off the Finnish coast in the Gulf of Finland. The spill size is 20 km across and the predicted and verified concentrations range from 26 µg/l down to 2 µg/l at the lower edges of the spill. The release site is marked with X. |
![]() Figure 2 - 14 |
The ”3D Transport Model” has been developed in Finland by the National Board of Waters and the Environment and the Finnish Environment Institute (Ref. 9 and Ref . 10).
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The ”3D Transport Model” is available at:
Finnish Environment Institute |
Operational contact point:
Maritime Rescue Coordination Centre (MRCC) Turku, Finland |
Advantages
This model is primarily aimed for the evaluation of ecological changes in
costal waters. In this context it is used for simple three-dimensional
drift calculations of water-soluble chemical spills.
Limitations
When used by itself this model cannot predict the transport and spreading
of substances due to the wind, waves, turbulence and sea currents. These
parameters must be estimated or calculated by a three-dimensional
hydrodynamic model.
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End of Chapter
2 |
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