Question 5.TC.3: Compression and Expansion of a Two Gases System A cylinder ......
Compression and Expansion of a Two Gases System
A cylinder is divided in two compartments with a mobile partition NM. The compartment in the left is limited by the fond of the cylinder and the partition NM (Fig.5-3). This compartment contains one mole of water vapor.
The compartment in the right is limited by the partition NM and a mobile piston AB. This compartment contains one mole of nitrogen gas (N_{2} ).
At first, the volumes and temperatures of the gases in two compartments are equal. The partition NM is well heat conductive. Its heat capacity is very small and can be neglected.
The specific volume of liquid water is negligible in comparison with the specific volume of water vapor at the same temperature.
The specific latent heat of vaporization L is defined as the amount of heat that must be delivered to one unit of mass of substance to convert it from liquid state to vapor at the same temperature. For water at T_{0} = 373 K, L = 2250 kJ/kg.
(1) Suppose that the piston and the wall of the cylinder are heat conductive, the partition NM can slide freely without friction. The initial state of the gases in the cylinder is defined as follows:
Pressure p_{1} = 0. 5 atm.; total volume V_{1} = 2V_{0} ; temperature T_{1} = 373 K.
The piston AB slowly compresses the gases in a quasi-static (quasi equilibrium) and isothermal process to the final volume V_{F} = V_{0} /4.
(a) Draw the P (V) curve, which is the curve representing the dependence of pressure P on the total volume V of both gases in the cylinder at temperature T_{1} • Calculate the coordinates of important points of the curve.
Gas constant: R = 8.31 J/(mol•K) or R = 0.0820 (L•atm.)/(mol•K); 1 atm. = 101. 3 kPa;
Under the pressure p_{0} = 1 atm. , water boils at the temperature T_{0} = 373 K.
(b) Calculate the work done by the piston in the process of gases compressing.
(c) Calculate the heat delivered to outside in the process.
(2) All conditions as in (1) except that there is friction between
partition NM and the wall of the cylinder so that NM displaces only when the difference of the pressures acting on its two opposed faces attains 0.5 atm. and over (assuming that the coefficients of static and kinetic friction are equal).
(a) Draw the p (V) curve representing the pressure p in the right compartment as a function of the total volume V of both gases in the cylinder at a constant temperature T_{1} .
(b) Calculate the work done by the piston in compressing the gases.
(c) After the volume of gases reaches the value V_{F}= V_{0} /4, piston AB displaces slowly to the right and makes a quasi-static and isothermal process of expansion of both substances (water and nitrogen) to the initial total volume 2V_{0} • Continue to draw in the diagram in question (2) (a) the curve representing this process.
Hint for (2)
Create a table like the one shown here and use it to draw the curves as required in (2) (a) and (2) (c).
Table–1–
(3) Suppose that the wall and the fond of the cylinder and the piston are heat insulator, the partition NM is fixed and heat conductive, the initial state of gases is as in (1). Piston AB moves slowly toward the right side and increases the volume of the right compartment until the water vapor begins to condense in the left compartment.
(a) Calculate the final volume of the right compartment.
(b) Calculate the work done by the gas in this expansion.
The ratio of isobaric heat capacity to isochoric one \gamma={\frac{C_{\rho}}{C_{V}}} for nitrogen is \gamma_{1}={\frac{7}{5}} an or water vapor \gamma_{2}={\frac{8}{6}}.
In the interval of temperature from 353 K to 393 K one can use the following approximate formula:
p = \rho_{0}\exp\!\left[-{\frac{\mu L}{R}}{\Big(}{\frac{1}{T}}-{\frac{1}{T_{0}}}{\Big)}\right]where T is boiling temperature of water under pressure p, μ its molar mass. p_{0}, L_{0} and T_{0} are given above.
Table–1–
| State | Left compartment | Left compartment | Total Volume |
Pressure on piston AB |
||
| Volume | Pressure | Volume | Pressure | |||
| initial | V_{0} | 0.5 atm. | V_{0} | 0.5 atm. | 2V_{0} | 0.5 atm. |
| 2 | ||||||
| 3 | ||||||
| . | ||||||
| . | ||||||
| . | ||||||
| . | ||||||
| . | ||||||
| final | 2V_{0} | |||||
(1) (a) The isotherm curve is shown in Fig. 5 – 4.
V_{\circ}={\frac{R T_{1}}{P_{1}}}={\frac{8.31\times373}{0.5\times1.013\times10^{5}}}=0.0612\,{\mathrm{m}}^{3}=61.2\,{\mathrm{dm}}^{3}.(b) The process of compressing can be divided into 3 stages:
\begin{array}{l}{{(\rho_{1},\ 2V_{0})\rightarrow(2\rho_{1},\ V_{0})\rightarrow\left(2\rho_{1},\ \frac{V_{0}}{2}\right)\rightarrow\left(4\rho_{1},\ \frac{V_{0}}{4}\right).}}\end{array} \qquad(\,1\,)\qquad\qquad(2)\qquad\qquad(3)\qquad\qquad(4)The work in each stage can be calculated as follows:
{ A}_{12}=-\int_{2V_{0}}^{V_{0}}p \,\mathrm{d}V= 2R T_{1}\int_{V_{0}}^{2V_{0}}\ \frac{\mathrm{d}V}{V}=2R T_{1}\ln2=4297\,J\,,A_{23}=2p_{1}\Bigl(V_{0}-\frac{V_{0}}{2}\Bigr)=R T_{1}=3100\,\mathrm{J},
A_{34}=-\int_{\frac{1}{4}V_{0}}^{\frac{1}{4}V_{0}}p^{′}\mathrm{d}V=R T_{1}\int_{\frac{1}{4}V_{0}}^{\frac{1}{2}V_{0}}\frac{\mathrm{d}V}{V}=R T_{1}\ln2=2149\,\mathrm{J}.
The total work of gases compressing is
A=A_{12}+A_{23}+A_{34}=9545\;\mathrm{J\cong9.55~kJ.} (1)
(c) In the second stage 23, all the water vapor (one mole) condenses. The heat Q’ delivered in the process equals the sum of the work A and the decrease ΔU of internal energy of one mole of water vapor in the condensing process.
Q^{\prime}=\Delta U+A_{12}+A_{23}+A_{34}.One can remark that ΔU + A_{23} is the heat delivered when one mole of water vapor condenses, and equals 0.018 x L. Thus
{ Q}^{\prime}=\Delta U+A_{11}+A_{23}+A_{34}=0.\,018\times L+A_{11}+A_{34}=46.946\ { J}\cong47\ { kJ}. (2)
(2) The process of compression (2) (a) and expansion (2) (c) of gases can be divided into several stages. The stages are limited by the following states:
Table–2–
(a) See Fig. 5 – 5 below.
(b) The work A_{P} done by the piston in the process of compressing the gases equals the sum of the work A calculated in (1) and the work done by the force of friction. The latter equals O. 5 atm. × V_{0} = p_{1} V_{0} (the force of kinetic friction appears in the process 234 during which the displacement of the partition NM corresponding to a variation V_{0} of volume of the left compartment). Then, we have:
A_{p}=A+p_{1}V_{\displaystyle0}=9545+8.31\times373=12\,645\,\mathrm{J}\cong12.65\,\mathrm{k}\mathrm{J}.(c) In process 89 the pressure in the left compartment is always larger than the pressure in the right one (with a difference of 0.5 atm. ). If p denotes the pressure in the right compartment, the pressure in the left one will be p + 0. 5 atm.
Let V be the total volume in process 89, we have
\frac{R T_{1}}{p}+\frac{R T_{1}}{p+0.5}=Vwith V=2V_{0}={\frac{2R T_{1}}{0.5}} , p can be defined by \frac{R T_{1}}{p}+\frac{R T_{1}}{p+0.5}=\frac{2R T_{1}}{0.5}.
This is equivalent to:
p+0.5+ p=4p\cdot(p+ 0.5)\,,p={\frac{1}{\sqrt{8}}}={\frac{\sqrt{2}}{4}}=0.35\;\mathrm{atm.}.
The pressure in the right compartment is p = 0.35 atm ..
The volume of the right compartment is {\sqrt{2}}V_{\mathrm{0}}\,.
The pressure in the left compartment is p + 0. 35 = 0. 85 atm. .
The volume of the left compartment is (2-\sqrt{2}\,)V_{\mathrm{0}}.
(3) (a) Apply the first law of thermodynamic for the system of two gases in the cylinder:
\delta q=\mathrm{d}U+\delta A. (3)
In an element of process in which the variations of temperature and volume are respectively dT and dV:
\delta q=0;\;\mathrm{d}U=(C_{V_{1}}+C_{V_{2}})\mathrm{d}T=\Big(\frac{R}{\gamma_{1}-1}+\frac{R}{\gamma_{2}-1}\Big)\mathrm{d}T;\delta A\,=\,p\cdot\,\mathrm{d}V.
On the other hand, pV=RT. (4)
One can deduce the differential equation for the process:
\Bigl(\frac{R}{\gamma_{1}-1}+\frac{R}{\gamma_{2}-1}\Bigr)\mathrm{d}T+p·\mathrm{d}V=0or
\frac{\mathrm{d}T}{T}+\frac{(\gamma_{1}-1)\,(\gamma_{2}-2)}{\gamma_{1}+\gamma_{2}-2}\,\frac{\mathrm{d}V}{V}=0. (5)
By putting
K=\frac{(\gamma_{1}-1)\,(\gamma_{2}-1)}{\gamma_{1}+\gamma_{2}-2}=\frac{2}{11} (6)
after integrating (5), we have
T V^{\kappa}={\mathrm{const.}} (7)
The condensing temperature of water vapor under the pressure 0. 5 atm. is also the boiling temperature T’ of water under the same pressure. By using the given approximate formula, we obtain
\frac{1}{T^{\prime}}-\frac{1}{T_{0}}=\left(-\frac{R}{\mu L}\right)\ln\frac{p}{p_{0}}.• If we consider p approximatively constant (with relative deviation
about {\frac{20}{373}}\approx5\%) T’ can be easily found, and
T’ = 354K.
The volume V′ of the right compartment at temperature T’ can be
calculated as follows:
= 81.6\ dm^{3}=0.0816\,{\mathrm{m}}^{3}\cong0.08\,{\mathrm{m}}^{3}.
(b) The work done by the gas in the expansion is
A=-\,\Delta U=(C_{V_{1}}+C_{V_{2}})\,(\,T_{0}-T^{\prime})= \Bigl(\frac{R}{\gamma_{1}-1}+\frac{R}{\gamma_{2}-2}\Bigr)(373-354)
= \left(\frac{5}{2}R+\frac{6}{2}R\right)\times19=868\,\mathrm{J}\cong9\times10^{2}\,\mathrm{J}.
• If we consider the dependence of water vapor pressure p on temperature T’ , we must resolve the transcendental equation
\frac{1}{T^{\prime}}-\frac{1}{T_{0}}=\left(-\frac{R}{\mu L}\right)\ln\frac{1}{2}\,\frac{T^{\prime}}{T_{0}}=\frac{R}{\mu L}\mathrm{ln}\,2-\frac{R}{\mu L}\mathrm{ln}\,\frac{T^{\prime}}{T_{0}}.This equation can be reduced to a numerical one:
{\frac{1}{T^{\prime}}}-{\frac{1}{373}}=1.422\times10^{-4}-2.052\times10^{-4}\ln{\frac{T^{\prime}}{373}}.
By giving T’ different values 354, 353, 352 and choosing the one which satisfies this equation, we find the approximate solution:
T’ = 353 K.
With this value of temperature, the volume of the right compartment is
V^{\prime}=V_{\mathrm{\scriptscriptstyle{0}}}\Bigl(\frac{373}{353}\Bigr)^{{{{\frac{11}{2}}}}}\,=\,1.35V_{\mathrm{\scriptscriptstyle{0}}}=0.082\,{\mathrm{m}}^{2}\cong0.08\,{\mathrm{m}}^{3}.(c) The work done by the gas in the expansion is
A={\frac{11}{2}}R\times20=914\,{J}\cong9\times10^{2}\,{ J}.
Table–2–
| State | Left compartment | Left compartment | Total Volume |
Pressure on piston (atm.) |
||
| Volume | Pressure (atm.) |
Volume | Pressure (atm.) |
|||
| 1 | V_{0} | 0.5 | V_{0} | 0.5 | 2V_{0} | 0.5 |
| 2 | V_{0} | 0.5 | 0.5V_{0} | 1 | 1.5V_{0} | 1 |
| 3 | 0.5V_{0} | 1 | \frac{V_{0}}{3} | 1.5 | \frac{5}{6}V_{0} | 1.5 |
| 4 | 0 | 1 | \frac{V_{0}}{3} | 1.5 | \frac{V_{0}}{3} | 1.5 |
Cont.
| State | Left compartment | Left compartment | Total Volume |
Pressure on piston (atm.) |
||
| Volume | Pressure (atm.) |
Volume | Pressure (atm.) |
|||
| 5 | 0 | 1.5 | \frac{V_{0}}{4} | 2 | \frac{V_{0}}{4} | 2 |
| 6 | 0 | 1.5 | \frac{V_{0}}{3} | 1.5 | \frac{V_{0}}{3} | 1.5 |
| 7 | 0 | 1 | V_{0} | 0.5 | V_{0} | 0.5 |
| 8 | 0.5V_{0} | 1 | V_{0} | 0.5 | 1.5V_{0} | 0.5 |
| 9 | (2-{\sqrt{2}})V_{0} | \frac{{\sqrt{2}}+2}{4} | {\sqrt{2}}V_{0} | \frac{\sqrt{2}}{4} | 2V_{0} | {\frac{\sqrt{2}}{4}}\approx0.35 |