- Fractions of a gas component in the mixture and liquid phase, at equilibrium -
Equilibrium diagrams are useful to get insight on how the solubility of certain gas component behaves at certain total dilution pressure condition, say p_t, or at certain gas dilution temperature, say T.
Also, the equilibrium diagrams are just the fraction of the gas component in the liquid phase, say x, versus the fraction of the gas component in the gas mixture, say y, for either constant pressure or constant temperature.
So, how do we do that? First, you will need to choose the fixed parameter of the dilution: the total pressure p_t or the temperature T. Let us consider each case in turn but first some explanation of the variables in the solubility data is needed.
How the solubility data is obtained
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You need to know how soluble a gas component is in a given liquid. Two parameters will modify the solubility of this gas component: pressure and temperature.
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Fig. 01 Idealization of solubility meausurements. |
In an experimental setup for this purpose, both pressure and temperature need to be mesarured. A fix coposition of the gas mixture will produce certain pressure and temperature changes and these changes will keep constant once the equilibrium in the system is achieved. This equilibrium is reached when molecules of soluble gas components in the gas mixture and in the liquid do not travel back and forth.
Next, if the composition of the gas mixture is changed, another set of pressure and temperature will be reached at equilibrium, providing in this way data on the solubility of a given gas component. Of course, the composition of the gas mixture is presented as the concentration of the soluble gas component.
One detail is worth to mentioned here. The pressure recorded at the manometer (as shown in the sketch above) corresponds to the total pressure of the gas. However, another pressure contribution needs to be introduced: the partial pressure. Every gas component in the gas mixture (say A, B, C, etc.) will exert a pressure contribution to the total pressure so that,
p_t=p_A+p_B+p_C+\ldots Eq. (01)
where p_A, p_B, p_C, etc. are the partial pressures exerted by each component. If, the gas behaves as an ideal gas, partial pressures can be easily related to the corresponding gas components mole fractions x_A, x_B, x_C, etc. as follows,
x_A=\dfrac{p_A}{p_t},\,\, x_B=\dfrac{p_B}{p_t},\,\, x_C=\dfrac{p_C}{p_t},\,\, etc. Eq. (02)
If, a gas mixture, from which a gas component A is soluble in a liquid, is set in contact with a given amount of liquid then the partial pressure of the gas component A, p_A, will start decreasing but its mole fraction in the liquid will start increasing. After all this mass transfer, the total pressure p_t will be changed since the liquid is incompressible. Therefore, if you know the initial concentration of gas component A in the mixture, you can later estimate the final concentration by just looking to the total pressure p_t in the manometer.
What about equilibrium? Well, concentration gradients and rate of diffusion are indicative that the system is out of equilibrium. So, for equilibrium to be reached, all gradients must fall to zero. The equilibrium reached is one called dynamic equilibrium because there is time dependency or in other words: the soluble gas component molecules do not cease to move back and forth between the gas mixture and the liquid. In this dynamic equilibrium, the rate at which soluble gas component molecules enter the liquid are the same at wich some other molecules of this component leaves the liquid to the gas mixture.
Some principles are common to systems like this:
- at a fixed set of pressure and temperature conditiions there exist a set of relationships for equilibrium,
- in a system in equilibrium, the net diffusion of components across the interface is zero,
- if the system is not in equilibrium the diffusion of components across the inteface will bring it to a condition of equilibrium.
Equilibrium diagrams for constant pressure
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Hereon, we will refer mainly to the gas component soluble in the liquid and ommit the other components in the gas mixture (being those insoluble or very little). In some other texts, the soluble gas component is also referred as A.
For a given set of solubility data: concentration, temperature and pressure; the fractions of the gas component x and y in the liquid phase and gas mixture, respectively, need to be calculated. Since the concentration of the gas component in the liquid phase is given in the solubility data as,
\dfrac{m_{gc}}{m_{lp}}=\dfrac{mass\, of \, gas\, component}{mass\, of\, liquid\, phase} Eq. (03)
the fraction x can be calculated by using the following relationship,
x=\dfrac{m_{gc}/M_{gc}}{m_{gc}/M_{gc}+m_{lp}/M_{lp}} Eq. (04)
where M and m are the molecular weight and mass of the gas component gc and liquid phase lp. For the fraction y in the gas mixture, the relationship of this with the partial pressure can be used. This is,
p_{gc}=p_t\,y Eq. (05)
where p_{gc} is the partial pressure exerted by the gas component in the mixture and p_t is the total pressure. You should recall that Eq. (05) makes sense only if the gas mixture behaves as an ideal gas (which is a rough approximation).
Now, if the total pressure p_t remains constant the temperature can be varied so that plots of the mole fraction of the soluble gas comoponent in the gas mixtures y vs the mole fraction of the soluble gas component in the liquid x can be given from the solubility data.
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Fig. 02 Equilibrium diagram of y vs x for constant pressure. |
Equilibrium diagrams for constant temperature
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A similar plot to that sketch in Fig. 02 can also be built for constant temperature and varying pressure.
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Fig. 03 Equilibrium diagram of y vs x for constant temperature. |
The most significant change is the effect of increasing temperature and pressure. The process to follow is just the same as in the prevous section and sample solubillity data is presented in the post: Gas absorption: General commments.
This is the end of the post. I hope you find it useful.
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Ildebrando.
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