Chapter 13 Gases, Vapors, Liquids, and Solids

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1 Chapter 13 Gases, Vapors, Liquids, and Solids Property is meaning any measurable characteristic of a substance, such as pressure, volume, or temperature, or a characteristic that can be calculated or deduced, such as internal energy. State and Equilibrium A system will possess a unique set of properties, such as temperature, pressure, density, and so on, at a given time, and thus is said to be in a particular state. A change in the state of the system results in a change in at least one of its properties. By equilibrium we mean a state in which there is no tendency toward spontaneous change. When a system is in equilibrium with another system, or the surroundings, it will not change its state unless the other system, or the surroundings, also changes. A phase is defined as a completely homogeneous and uniform state of matter. Liquid water would be a phase; ice would be another phase. Two immiscible liquids in the same container, such as mercury and water, would represent two different phases because the liquids have different properties Ideal Gas Law Calculations The Ideal Gas Law Under conditions such that the average distance between the molecules in a substance is great enough to neglect the effect of the intermolecular forces and the volume of the molecules themselves, a gas can be termed an ideal gas. More properly, an ideal gas is an imaginary gas that obeys exactly the following relationship pv = nrt 13.1 Where p = absolute pressure of the gas V = total volume occupied by the gas n = number of moles of the gas R = ideal gas constant in appropriate units T = absolute temperature of the gas Sometimes the ideal gas law is written as pv = RT 13.1a Where V is the specific volume (volume per mole or mass) of the gas. 155

2 Table 13.1 Common Standard Conditions for the Ideal Gas System T P V SI K kpa m 3 /kg mol Universal scientific 0.0 C 760 mm Hg liters/g mol Natural gas industry 60.0 F psia (15.0 C) ( kpa) ft 3 /lb mol American engineering 32 F 1 atm ft 3 /lb mol Example 13.1 Calculate the volume, in cubic meters, occupied by 40 kg of CO 2 at standard conditions. Solution Basis: 40 kg of CO 2 40 kg CO 2 1 kg mol CO m 3 CO 2 = 20.4 m 3 CO 2 ats.c. 44 kg CO 2 1 kg mol CO 2 Example 13.2 Find the value for the universal gas constant R for the following combinations of units: For 1 g mol of ideal gas when the pressure is in atm, the volume in cm 3, and the temperature in K. In many processes going from an initial state to a final state, you can use the ratio of ideal gas law in the respective states and eliminate R as follows (the subscript 1 designates the initial state, and the subscript 2 designates the final state) 156

3 13.2 Example 13.3 Calculate the volume occupied by 88 lb of CO 2 at a pressure of 32.2 ft of water and at 15 C Solution The final volume can be calculated via Equation 13.2 in which both R and n 1 /n 2 cancel out: Assume that the pressure is absolute pressure. 157

4 Another solution Chemical Engineering principles First Year/ Chapter Thirteen The same results can be obtained by using Eq The Gas Density The density of a gas is defined as the mass per unit volume and can be expressed in kilograms per cubic meter, pounds per cubic foot, grams per liter, or other units Example 13.4 What is the density of N 2 at 27 C and 100 kpa in SI units? Solution The Gas Specific Gravity The specific gravity of a gas is usually defined as the ratio of the density of the gas at a desired temperature and pressure to that of air (or any specified reference gas) at a certain temperature and pressure. 158

5 Example 13.5 Chemical Engineering principles First Year/ Chapter Thirteen What is the specific gravity of N 2 at 80 F and 745 mm Hg compared to air at 80 F and 745 mm Hg? Solution Note: for gases at the same temperature and pressure, the specific gravity is just the ratio of the respective molecular weights. Let A be one gas and B be another. Thus A p sp. gr. B p A B mol. wt. A T mol. wt. B T B A Ideal Gas Mixtures and Partial Pressure The partial pressure of gas; i defined by Dalton, p i, namely the pressure that would be exerted by a single component in a gaseous mixture if it existed by itself in the same volume as occupied by the mixture and at the same temperature of the mixture is 13.4 Where p i is the partial pressure of component i. If you divide Eq. (13.4) by Eq. (13.1), you find that

6 Where y i is the mole fraction of component i. Can you show that Dalton's law of the summation of partial pressures is true using Eq. 13.5? Although you cannot measure the partial pressure directly with an instrument, you can calculate the value from Eqs and/or Example 13.6 A flue gas analyzes 14.0% CO 2, 6.0% O 2, and 80.0% N 2. It is at 400 F and mm Hg pressure. Calculate the partial pressure of each component. Solution Use Eq, (13.5) p i = p t y i Basis: 1.00 kg (or lb) mol flue gas Component kg (or lb) mol p (mm Hg) CO O N Total On the basis of 1.00 mole of flue gas, the mole fraction y of each component, when multiplied by the total pressure, gives the partial pressure of that component Material Balances Involving Gases The only difference between the subject matter of previous chapters and this section is that here the amount of material flow can be specified in terms of p, V, and T rather than solely mass or moles. Example 13.7 The product gas analyzed 6.4% CO 2, 0.1% O 2, 39% CO, 51.8% H 2, 0.6% CH 4, and 2.1% N 2. It enters the combustion chamber at 90 o F and a pressure of 35 in. Hg, and is burned with 40% excess air (dry) which is at 70 o F and the atmospheric pressure of 29.4 in. Hg; 10% of the CO remains unburned. How many cubic feet of air are supplied per cubic foot of entering gas? How many cubic feet of product are produced per cubic foot of entering gas if the exit gas is at 29.4 in. Hg and 400 o F? 160

7 Solution Chemical Engineering principles First Year/ Chapter Thirteen This is a steady state problem with reaction. The system is the gases in combustion chamber. Basis: 100 lb mol gas The entering air can be calculated from the specified 40% excess air, the reactions for complete combustion are The moles of oxygen required are listed in Figure E13.7. The excess oxygen is Total moles of air in are = 310 lb mol Degree of freedom: Five unknowns exit, the five products. You can make four element balances You can calculate: Hence the problem has zero degrees of freedom. 161

8 Make element balances Chemical Engineering principles First Year/ Chapter Thirteen The solution of these equations is The total moles exiting sum to lb mol. If you prefer the species balances The degrees of freedom are zero. Solution of these equations gives the same results as the element balances, as expected. Finally, we can convert the lb mol of air and product into the volumes requested: 162

9 Example 13.8 Gas at 15 o C and 105 kpa is flowing through an irregular duct. To determine the rate of flow of the gas, CO 2 from a tank was passed into the gas stream. The gas analyzed 1.2% CO 2 by volume before and 3.4% CO 2 by volume after, addition. The CO 2 left the tank, was passed through a rotameter, and was found to flow at the rate of m 3 /min at 7 o C and 131 kpa. What was the rate of flow of the entering gas in the duct in cubic meters per minute? Solution This is an open, steady state system without reaction. The system is the duct. Figure E13.8 is a sketch of the process. Assume that the entering and exit gases are at the same temperature and pressure. 163

10 Take as a basis 1 min m 3 of CO 2 at 7 o C and 131 kpa. The gas analysis is in volume percent, which is the same as mole percent. We do not know F and P, but can make two independent component balances, CO 2 and "other", hence the problem has zero degrees of freedom. Note that the "other" is a tie component. The solution of Equations (a) and (c) gives F = 5.17 m 3 /min at 15 o C and 105 kpa P = m 3 /min at 15 o C and 105 kpa Check : By Equation (b) 5.17 (0.012) = (0.034)(P) P = The equation checks out to a satisfactory degree of precision. Problems 1. Calculate the volume in ft 3 of 10 lb mol of an ideal gas at 68 F and 30 psia. 2. A steel cylinder of volume 2 m 3 contains methane gas (CH 4 ) at 50 C and 250 kpa absolute. How many kilograms of methane are in the cylinder? 3. What is the value of the ideal gas constant R to use if the pressure is to be expressed in atm, the temperature in Kelvin, the volume in cubic feet, and the quantity of material in pound moles? 4. Twenty-two kilograms per hour of CH 4 are flowing in a gas pipeline at 30 C and 920 mm Hg. What is the volumetric flow rate of the CH 4 in m 3 per hour? 5. What is the density of a gas that has a molecular weight of kg/kg mol at 300 K and 1000 kpa? 6. What is the specific gravity of CH 4 at 70 F and 2 atm compared to air at S.C.? 164

11 7. A gas has the following composition at 120 F and 13.8 psia. Component Mol % N 2 2 CH 4 79 C 2 H 6 19 (a) What is the partial pressure of each component? (b) What is the volume fraction of each component? 8. (a) If the C 2 H 6 were removed from the gas in problem 7, what would be the subsequent pressure in the vessel? (c) What would be the subsequent partial pressure of the N 2? 9. A furnace is fired with 1000 ft 3 per hour at 60 o F and 1 atm of a natural gas having the following volumetric analysis: CH 4 : 80%, C 2 H 6 : 16%, O 2 : 2%, CO 2 : 1%, and N 2 : 1%. The exit flue gas temperature is 800 o F and the pressure is 760 mm Hg absolute; 15% excess air is used and combustion is complete. Calculate the: (a) Volume of CO 2 produced per hour. (b) Volume of H 2 O vapor produced per hour. (c) Volume of N 2 produced per hour. (d) Total volume of flue gas produced per hour. 10. A flue gas contains 60% N 2 and is mixed with air to cool it. If the resulting mixture flows at a rate of ft 3 /hr and contains 70% N 2, what is the flow rate of the flue gas? State all your assumptions concerning the temperatures and pressures of the gas streams. 11. Two tanks containing N 2 at the following conditions sit next to each other After the two tanks are connected and reach equilibrium, the conditions in the combined tanks are 700 kpa and 35 o C. What was the pressure in Tank B? Answers: ft kg

12 m 3 /hr kg/m 3 Chemical Engineering principles First Year/ Chapter Thirteen (lb CH 4 /ft 3 at 70 F and 2 atm)/ (lb air/ ft 3 at S.C.) 7. N 2, 0.28 psia; CH 4, 10.9 psia; C 2 H 6, 2.62 psia 8. (a) psia at 2 ft 3 and 120 F; (b) 0.28 psia at 2 ft 3 and 120 F 9. (a) 2735 ft 3 /hr; (b) 5034 ft 3 /hr; (c) ft 3 /hr; (d) ft 3 /hr, all at the exit temperature and pressure ft 3 /hr kpa. Supplementary Problems (Chapter Thirteen): Problem 1 166

13 Problem 2 Problem 3 167

14 Problem 4 168

15 Problem 5 169

16 170

17 171

18 Problem 6 172

19 Problem 7 173

20 174

21 Problem 8 175

22 176

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