11.10.2013 Views

2. ENVIRONMENTAL ChEMISTRy & TEChNOLOGy 2.1. Lectures

2. ENVIRONMENTAL ChEMISTRy & TEChNOLOGy 2.1. Lectures

2. ENVIRONMENTAL ChEMISTRy & TEChNOLOGy 2.1. Lectures

SHOW MORE
SHOW LESS

Create successful ePaper yourself

Turn your PDF publications into a flip-book with our unique Google optimized e-Paper software.

Chem. Listy, 102, s265–s1311 (2008) Environmental Chemistry & Technology<br />

( x,<br />

+ N , k)<br />

= 0.<br />

C j<br />

( x,<br />

−N , k)<br />

= 0.<br />

C j<br />

C<br />

( x,<br />

j,<br />

N ) = 0.<br />

+ k<br />

( ∞)<br />

Dz<br />

C(<br />

x,<br />

j,<br />

0)<br />

=<br />

C(<br />

x,<br />

j,<br />

2)<br />

.<br />

2∆z(<br />

v −W<br />

) + D<br />

z<br />

( ∞)<br />

(7b)<br />

(7c)<br />

(7d)<br />

(7e)<br />

For integration of the system of ODEs (7) the 4 th order<br />

Runge-Kutta method was chosen. It has sufficient accuracy<br />

as is shown in the next chapter.<br />

Results<br />

As was mentioned above equation (3) supposes one point<br />

source that has constant strength. It means that the amount of<br />

pollutant is constant during time. The wind flows along x axis<br />

with constant speed and the ground is flat everywhere. In our<br />

experiments, all diffusion coefficients were constant in every<br />

space points during time, for simplicity.<br />

now everything is defined to solve our model of<br />

PDE (3) with boundary conditions (3a–e). The experiment<br />

has been done with following coefficient setting. The diffusion<br />

coefficients has been set like that: D y = 0.23 m 2 s –1 ,<br />

D z = 0.23 m 2 s –1 which is the parameter of ammonia, other<br />

coefficients has been: v = 2 m s –1 , W = 3 m s –1 , u x = 2 m s –1 ,<br />

Q = 0.1 kg s –1 and H = 1.5 m.<br />

The space discretization has been chosen as follows:<br />

N i = 600, N j = 50, N k = 50, Δx = 0.005 m, Δy = 0.05 m and<br />

Δz = 0.05 m. In this case the assumed space 3 m × <strong>2.</strong>5 m × <strong>2.</strong>5 m<br />

has been discretized into 1,500,000 points in which the equations<br />

have been calculated.<br />

V i s u a l i z a t i o n<br />

We made simple program/tool for solving given A-DE<br />

and for the visualization of the results with possibility of<br />

comparison the analytical and the obtained numerical soluti-<br />

Fig. 1. xy plane cut in zero depth, which means that the ground<br />

pollutant dispersion is shown. The wind flows from left to right<br />

s388<br />

ons. The program has possibility to make the cuts through the<br />

perpendicular grid in XY, XZ and YZ planes in any depth and<br />

the appropriate grid points can be plotted.<br />

Fig. 1. and Fig. <strong>2.</strong> show the XY and XZ cuts for our<br />

above-defined experiment. The level of gray (the lighter the<br />

more concentrated) expresses the amount of concentration of<br />

pollutant at each point - the most concentrated means approximately<br />

0.5% of source concentration.<br />

Fig. <strong>2.</strong> xZ plane cut in depth of 25 of overall depth 50 which<br />

means that the cut in depth of point source is shown. The wind<br />

flows from left to right<br />

Scales of axes (x is horizontal, y is vertical) in figures<br />

above are these:<br />

• Fig. 1.: x axis: m, y axis: m<br />

• Fig. <strong>2.</strong>: x axis: m, y axis: m<br />

The three-dimension (3D) visualization is another way<br />

to represent the calculated data in space. It has many advantages<br />

and gives to the user tool for fast investigation of the<br />

result. Many methods of gas or fluid visualization were developed<br />

however not all are suitable for our purpose. We can<br />

mention the stream ribbons, stream surfaces, particle traces,<br />

vector fields etc. 7 .<br />

Fig. 3. 3D visualization of pollutant dispersion in the atmosphere.<br />

The white color points show the highest concentration of<br />

pollutant, the black color points show its low concentration

Hooray! Your file is uploaded and ready to be published.

Saved successfully!

Ooh no, something went wrong!