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Gaseous propane \(\left(\mathrm{C}_{3} \mathrm{H}_{8}\right.\) ) at \(25^{\circ} \mathrm{C}, 1\) atm enters a reactor operating at steady state and burns with \(80 \%\) of theoretical air entering separately at \(25^{\circ} \mathrm{C}, 1 \mathrm{~atm}\). An equilibrium mixture of \(\mathrm{CO}_{2}, \mathrm{CO}, \mathrm{H}_{2} \mathrm{O}(\mathrm{g}), \mathrm{H}_{2}\), and \(\mathrm{N}_{2}\) exits at \(1227^{\circ} \mathrm{C}, 1 \mathrm{~atm}\). Determine the heat transfer between the reactor and its surroundings, in kJ per kmol of propane entering. Neglect kinetic and potential energy effects.

Short Answer

Expert verified
The heat transfer between the reactor and surroundings is -2137.93 kJ per kmol of propane entering.

Step by step solution

01

- Write the balanced chemical equation

The balanced combustion reaction of propane (\text{C}_3\text{H}_8) with theoretical air is: \[ \text{C}_3\text{H}_8 + 5\text{O}_2 + 5 \times 3.76 \text{N}_2 \rightarrow 3 \text{CO}_2 + 4 \text{H}_2\text{O} + 18.8 \text{N}_2 \] Note that each mole of oxygen is accompanied by 3.76 moles of nitrogen.
02

- Determine the amount of air used

Given that 80% of the theoretical air is used, calculate the actual moles of air: \[ \text{Actual air} = 0.80 \times \text{Theoretical air} = 0.80 \times (5 + 5 \times 3.76) = 18.8 \text{ moles}\]
03

- Identify reaction products

At equilibrium, not all products are completely burned, so we have \text{CO}_2, \text{CO}, \text{H}_2\text{O}(\text{g}), \text{H}_2, and \text{N}_2. We write the general form of the reaction: \[ \text{C}_3\text{H}_8 + 5O_2 + 18.8N_2 \rightarrow a\text{CO}_2 + b\text{CO} + c\text{H}_2\text{O} + d\text{H}_2 + 18.8\text{N}_2 \]
04

- Apply mass balance for each component

For Carbon: \[ 3 = a + b \] For Hydrogen: \[ 8 = 2c + 2d \] For Oxygen: \[ 10 = 2a + b + c \]
05

- Solve the system of equations

From step 4, solve the equations to find values for a, b, c, and d: \[ a = 3, b = 0, c = 4, d = 0 \] Hence, the products are 3 moles of \text{CO}_2, 4 moles of \text{H}_2\text{O}, and 18.8 moles of \text{N}_2.
06

- Calculate enthalpy changes

Use enthalpies at standard conditions (\text{kJ/mol}) for reactants and products. From standard enthalpy tables, we get: \( \text{C}_3\text{H}_8 : -103.85 \), O_2 : 0, \text{N}_2 : 0, \text{CO}_2 : -393.5, \text{H}_2\text{O (g)} : -241.82
07

- Calculate energy released (entry condition)

Calculate heat of formation reactants and products at 298.15K: \( \text{ΔH}_{298.15K}^{reactants} = (-103.85) + 0 + 0 = -103.85 \text{kJ/mol} \) \( \text{ΔH}_{298.15K}^{products} = 3(-393.5) + 4(-241.82) + 18.8(0) = -2241.78 \text{kJ/mol} \)
08

- Enthalpy change at standard state

\( \text{ΔH}_{298.15K} = (-2241.78) - (-103.85) = -2137.93 \text{kJ/mol} \)
09

- Heat transfer between reactor and surroundings

Given constant specific heat values, the heat transfer (Q) to the surrounding can be achieved from \( Q = ΔH_{reaction} - (\text{H products - H reactants}) \)

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Key Concepts

These are the key concepts you need to understand to accurately answer the question.

Balanced Chemical Equation
When dealing with chemical reactions, starting with a balanced equation is crucial. In the case of propane (\text{C}_3\text{H}_8) combustion, the balanced equation ensures that the reactants and products include all elements in the correct proportions. For propane burning with theoretical air, the equation is:
\[ \text{C}_3\text{H}_8 + 5\text{O}_2 + 5 \times 3.76 \text{N}_2 \rightarrow 3 \text{CO}_2 + 4 \text{H}_2\text{O} + 18.8 \text{N}_2 \] Here, each mole of oxygen (O_2) comes with 3.76 moles of nitrogen (N_2). This ensures the equation reflects real air composition and makes it simpler to analyze mass balance and enthalpy changes.
Mass Balance
In chemical processes, a mass balance ensures that the total mass of reactants equals the total mass of products. This balance provides insight into the quantities of different substances involved. For propane combustion at steady state:
\[ \text{C}_3\text{H}_8 + 5O_2 + 18.8N_2 \rightarrow a\text{CO}_2 + b\text{CO} + c\text{H}_2\text{O} + d\text{H}_2 + 18.8\text{N}_2 \] To solve this, we create equations based on the conservation of atoms for each element involved. For example:
- Carbon (C): \[ 3 = a + b \] - Hydrogen (H): \[ 8 = 2c + 2d \] - Oxygen (O): \[ 10 = 2a + b + c \] Solving these equations leads to values for a, b, c, and d. It helps us understand the amounts of different products formed during the reaction.
Enthalpy Change
Enthalpy change (\text{ΔH}) during a reaction refers to the heat absorbed or released. This is essential to determine whether the reaction is exothermic (releases heat) or endothermic (absorbs heat). For propane combustion, we use standard enthalpy values (\text{kJ/mol}) from tables:
- \text{C}_3\text{H}_8: -103.85
- \text{O}_2: 0
- \text{N}_2: 0
- \text{CO}_2: -393.5
- \text{H}_2\text{O (g)}: -241.82
By calculating the total enthalpy of reactants and products at standard conditions (298.15K), we find the enthalpy change of the reaction:
\[ \text{ΔH}_{298.15K} = (\text{ΔH products}) - (\text{ΔH reactants}) \] This gives us the energy change associated with the reaction, providing insight into the energy dynamics.
Heat Transfer Calculation
Heat transfer (\text{Q}) between the reactor and surroundings is a critical aspect of thermodynamic analysis. It represents the energy exchanged due to reaction enthalpy and temperature changes. Using the enthalpy change from the reaction and considering the reactor operates at steady state, we can calculate \text{Q}. This is done as follows:
\[ Q = ΔH_{reaction} - (\text{H products} - \text{H reactants}) \] By introducing the specific heat values and temperature differences, this equation quantifies how much heat is transferred to/from the reactor to its surroundings. Understanding \text{Q} helps in designing efficient reactors and ensuring energy optimization during the process.

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Most popular questions from this chapter

Using appropriate software, develop plots giving the variation with equivalence ratio of the equilibrium products of octane-air mixtures at \(30 \mathrm{~atm}\) and selected temperatures ranging from 1700 to \(2800 \mathrm{~K}\). Consider equivalence ratios in the interval from \(0.2\) to \(1.4\) and equilibrium products including, but not necessarily limited to, \(\mathrm{CO}_{2}, \mathrm{CO}, \mathrm{H}_{2} \mathrm{O}, \mathrm{O}_{2}, \mathrm{O}, \mathrm{H}_{2}, \mathrm{~N}_{2}\), \(\mathrm{NO}, \mathrm{OH}\). Under what conditions is the formation of nitric oxide (NO) and carbon monoxide (CO) most significant? Discuss.

Derive an expression for estimating the pressure at which graphite and diamond exist in equilibrium at \(25^{\circ} \mathrm{C}\) in terms of the specific volume, specific Gibbs function, and isothermal compressibility of each phase at \(25^{\circ} \mathrm{C}, 1 \mathrm{~atm}\). Discuss.

A mixture of \(1 \mathrm{kmol}\) of \(\mathrm{CO}\) and \(\frac{1}{2} \mathrm{kmol}\) of \(\mathrm{O}_{2}\) is held at ambient temperature and pressure. After 100 hours only an insignificant amount of \(\mathrm{CO}_{2}\) has formed. Why?

Estimate the equilibrium constant at \(2800 \mathrm{~K}\) for \(\mathrm{CO}_{2} \rightleftarrows \mathrm{CO}+\frac{1}{2} \mathrm{O}_{2}\) using the equilibrium constant at \(2000 \mathrm{~K}\) from Table A-27, together with the van't Hoff equation and enthalpy data. Compare with the value for the equilibrium constant obtained from Table A-27.

An isolated system has two phases, denoted by A and B, each of which consists of the same two substances, denoted by 1 and 2. The phases are separated by a freely moving, thin wall permeable only by substance 2 . Determine the necessary conditions for equilibrium.

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