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\(1-1 \mathrm{bm}\) of air at 10 psia and \(70^{\circ} \mathrm{F}\) is contained in a piston-cylinder device. Next, the air is compressed reversibly to 100 psia while the temperature is maintained constant. Determine the total amount of heat transferred to the air during this compression.

Short Answer

Expert verified
Answer: -95,175.8 J (The heat is removed from the air during the compression process).

Step by step solution

01

List the given information and assumptions.

Given information: - Initial pressure (P1) = 10 psia - Final pressure (P2) = 100 psia - Constant temperature (T) = 70°F Assumptions: - The air behaves as an ideal gas. - The compression is isothermal and reversible.
02

Convert units to SI.

We need to convert the given pressures and temperature from their current units to their SI units. There are several conversion factors, which include: 1 psi = 6894.76 Pa 1°F = 5/9(°C - 32) Converting the pressure and temperature values: P1 = 10 psia * (6894.76 Pa/1 psi) = 68,947.6 Pa P2 = 100 psia * (6894.76 Pa/1 psi) = 689,476 Pa T = (5/9) * (70°F - 32°F) = 21.11°C = 294.26 K Now, we have: P1 = 68,947.6 Pa P2 = 689,476 Pa T = 294.26 K
03

Calculate the initial and final volumes.

We are given that we have 1 bm (1 standard cubic meter) of air. Let's assume that the initial volume is V1, and the final volume is V2. Since the process is isothermal, the ideal gas law for the initial and final states can be written as: P1 * V1 = n * R * T P2 * V2 = n * R * T Since the number of moles (n) and the gas constant (R) are the same in both equations, we can write the relationship between P1, V1, P2, and V2 as: P1 * V1 = P2 * V2 From the given information, V1 = 1 m³. Therefore, we can solve for V2: V2 = (P1 * V1) / P2 = (68,947.6 Pa * 1 m³) / 689,476 Pa = 0.1 m³
04

Compute the work done during the compression.

As the compression is isothermal and reversible, the work done on the gas during the compression can be determined by the following equation: W = n * R * T * ln(V2/V1) We have P1 * V1 = n * R * T, which implies n * R = P1 * V1 / T. Substituting in the equation for work: W = (P1 * V1 / T) * T * ln(V2/V1) = P1 * V1 * ln(V2/V1) W = (68,947.6 Pa * 1 m³) * ln(0.1 m³/1 m³) = -95,175.8 J Note: Since the work value is negative, it implies that work is done on the gas during compression (as expected).
05

Determine the heat transfer.

For an isothermal process, the change in internal energy is zero. Thus, the first law of thermodynamics can be written as: ΔU = Q - W Since ΔU = 0, we can write: Q = W Therefore, the total amount of heat transferred to the air during this isothermal compression process is: Q = -95,175.8 J The heat transferred to the air is 95,175.8 J in the negative direction, which implies that the heat is actually being removed from the air during the compression process.

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Most popular questions from this chapter

The energy used to compress air in the United States is estimated to exceed one-half quadrillion \(\left(0.5 \times 10^{15}\right)\) kJ per year. It is also estimated that 10 to 40 percent of the compressed air is lost through leaks. Assuming, on average, 20 percent of the compressed air is lost through air leaks and the unit cost of electricity is \(\$ 0.13 / \mathrm{kWh}\), determine the amount and cost of electricity wasted per year due to air leaks.

Air is to be compressed steadily and isentropically from 1 atm to 16 atm by a two-stage compressor. To minimize the total compression work, the intermediate pressure between the two stages must be \((a) 3\mathrm{ atm}\) \((b) 4 \mathrm{atm}\) \((c) 8.5 \mathrm{atm}\) \((d) 9 \mathrm{atm}\) \((e) 12 \mathrm{atm}\)

The inner and outer glasses of a \(2-\mathrm{m} \times 2\) -m double-pane window are at \(18^{\circ} \mathrm{C}\) and \(6^{\circ} \mathrm{C}\), respectively. If the glasses are very nearly isothermal and the rate of heat transfer through the window is \(110 \mathrm{W}\), determine the rates of entropy transfer through both sides of the window and the rate of entropy generation within the window, in \(\mathrm{W} / \mathrm{K}\).

The compressors of a production facility maintain the compressed-air lines at a (gage) pressure of \(700 \mathrm{kPa}\) at \(1400-\mathrm{m}\) elevation, where the atmospheric pressure is \(85.6 \mathrm{kPa}\). The average temperature of air is \(15^{\circ} \mathrm{C}\) at the compressor inlet and \(25^{\circ} \mathrm{C}\) in the compressed-air lines. The facility operates \(4200 \mathrm{h} / \mathrm{yr},\) and the average price of electricity is \(\$ 0.12 / \mathrm{kWh}\). Taking the compressor efficiency to be 0.8 the motor efficiency to be \(0.93,\) and the discharge coefficient to be \(0.65,\) determine the energy and money saved per year by sealing a leak equivalent to a 3 -mm-diameter hole on the compressed-air line.

The polytropic or small stage efficiency of a compressor \(\eta_{\infty}, c\) is defined as the ratio of the actual differential work done on the fluid to the isentropic differential work done on the flowing through the compressor \(\eta_{\infty}, c=d h_{s} / d h\) Consider an ideal gas with constant specific heats as the working fluid undergoing a process in a compressor in which the polytropic efficiency is constant. Show that the temperature ratio across the compressor is related to the pressure ratio across the compressor by $$\frac{T_{2}}{T_{1}}=\left(\frac{P_{2}}{P_{1}}\right)^{\left(\frac{1}{\eta_{\infty, C}}\right)\left(\frac{R}{c_{p}}\right)}=\left(\frac{P_{2}}{P_{1}}\right)^{\left(\frac{1}{\eta_{\infty, C}}\right)\left(\frac{k-1}{k}\right)}$$

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