4.3 Underpressure in Ullage Space of Ballast Water Tank
Deoxygenation is enhanced by the under-pressure, as can be seen from the following simple argument. Let p be pressure of water at a given depth in the absence of underpressure. Let pu be the absolute value of the negative pressure at the top. Let Y be the weight fraction of oxygen in the water without underpressure and Yu - the same weight fraction with underpressure. Then by Henry's Law:
 
From this equation we conclude that solubility of oxygen is reduced by underpressure. This factor becomes even more significant as a bubble rises to the surface, and the pressure inside decreases.

For example, if p=14.7 psi (the usual value at the surface of the tank) and the absolute value of the underpressure is 2 psi, then the solubility of oxygen is reduced by approximately 14%.
4.4 Carbon Dioxide Transfer
Since we assumed that the pressure inside the bubble depends only on the pressure of the liquid surrounding it, we can write:
(1)
By definition we have nCO2 = xn. Differentiating this equation we obtain:
(2)
However, since the reaction of carbon dioxide with water is the dominant cause of change in the chemical composition, we can write:
 
Combining this with the Equation (2) yields the following equation:
(3)
In addition, we can solve for n = xn+nN to obtain
(4)
From the Law of Mass Action kinetics we have:
(5)
For the partial pressure of carbon dioxide we have, according to Dalton's Law pCO2 = xp.

Combining the equations (1), (3), (4), and (5) yields:
 
This equation can be integrated to obtain:
(6)
where
 
This equation can be used to calculate the parameters of the systems, including residence time of a bubble, required to achieve the desired molar fraction of carbon dioxide in the bubble. The latter quantity is related to the pH and the concentration of carbon dioxide in the water, as we shall see in the next subsection.
4.5 Concentration of Carbon Dioxide in Water and pH Calculation
Concentration of carbon dioxide in water can be determined as the ratio of the number of moles transferred from the bubble to the volume of the tank. The number of moles transferred from each bubble can be determined from the value of x as follows. By definition, we have:
 
Solving for nCO2 we find:
 
which gives the following answer for the concentration of carbon dioxide in water:
(7)
The concentration of the hydrogen ions in the water can be calculated from c by solving the following equation for h:
(8)
The pH can be then found by taking the -log h.
 
We can also solve the Equation (8) for c and substitute the result into the Equation (7). This yields after some tedious, but straightforward algebra the following relationship between the desired molar fraction of carbon dioxide in the bubble and the desired concentration of hydrogen ions in the water:
(9)
The equations (6) and (9) constitute a closed-form mathematical model of carbon dioxide transfer usable for design of the treatment system.
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