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13.10 A sample of dried feedlot manure is being tested for use as a fuel. The mass analysis of the sample is \(42.7 \%\) carbon, \(5.5 \%\) hydrogen \(\left(\mathrm{H}_{2}\right), 31.3 \%\) oxygen \(\left(\mathrm{O}_{2}\right), 2.4 \%\) nitrogen \(\left(\mathrm{N}_{2}\right)\), \(0.3 \%\) sulfur, and \(17.8 \%\) noncombustible ash. The sample is burned completely with \(120 \%\) of theoretical air. Determine (a) the balanced reaction equation. (b) the air-fuel ratio on a mass basis.

Short Answer

Expert verified
Balanced combustion equation and air-fuel ratio calculation based on the 120% excess air assumption.

Step by step solution

01

Write the combustion equation

Start by writing the general combustion equation for a hydrocarbon with the given mass percentages. We assume 1 kg of dried feedlot manure as the basis. The equation for complete combustion will look like this:
02

Convert mass percentages to mass in kg

Convert the percentages to masses by assuming 1 kg of feedstock:
03

Convert masses to moles

Next, convert the masses of each element to moles.
04

Sum the moles of air required theoretically

Calculate the total moles of air required for complete combustion on theoretical basis.
05

Implement 120% excess air

Adjust for 120% excess air by multiplying the moles of air by 1.2.
06

Write the balanced reaction equation

Include the adjusted moles of O2 in the balanced combustion equation. The balanced reaction equation is: Combustion equation including all elements along with 120% excess air.
07

Calculate the mass basis air-fuel ratio

Finally, calculate the air-fuel ratio by using the balanced equation and mass basis.

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Key Concepts

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

Introduction to Mass Analysis in Combustion Reactions
Mass analysis is a crucial step when dealing with combustion reactions. It involves determining the mass fractions of different components in a fuel. This is particularly important for understanding the energy potential and combustion characteristics of the fuel. In our problem, the dried feedlot manure was analyzed, and its mass composition was found to be: 42.7% carbon, 5.5% hydrogen, 31.3% oxygen, 2.4% nitrogen, 0.3% sulfur, and 17.8% noncombustible ash.
By assuming a basis of 1 kg of dried feedlot manure, we can convert these percentages into masses. For instance, 42.7% of carbon in 1 kg becomes 0.427 kg of carbon.
Converting mass percentages to actual masses enables us to further work with moles, which simplifies the computation of the combustion process and air requirements.
Understanding Theoretical Air Requirement
Theoretical air is the precise amount of oxygen needed for complete combustion of a given amount of fuel. It ensures that all the combustible elements in the fuel react fully with oxygen.
For our dried feedlot manure sample, we need to calculate the moles of oxygen required to combust each of the fuel's components: carbon, hydrogen, sulfur, and others.
The concept of theoretical air is foundational because it helps in determining how much oxygen (and therefore air) is necessary for complete combustion. This is also crucial in the design and optimization of combustion systems to ensure efficiency.
  • Example: To combust 1 mole of carbon, 1 mole of oxygen is needed. For hydrogen, 0.5 moles of O2 per mole of H2.
  • The total moles of oxygen needed are summed up to calculate the total air required theoretically.
Creating the Balanced Reaction Equation
A balanced reaction equation accounts for all atoms of reactants converting to products, ensuring mass conservation. For combustion reactions, this means accurately representing the conversion of fuel and oxygen to products like CO2, H2O, SO2, etc.
Starting from the masses and converting these to moles, we can structure the balanced combustion equation systematically. By including all the components like carbon, hydrogen, oxygen, sulfur, and adjusting for the air added, we get a complete picture of the combustion process.
In our problem, once the theoretical oxygen requirements were multiplied by 1.2 to account for 120% theoretical air, the balanced equation was formed incorporating the requisite excess oxygen. This follows the combustion principle that excess air helps ensure complete combustion of all fuel components.
Calculating the Air-Fuel Ratio
The air-fuel ratio (AFR) is a critical parameter in combustion reactions. It describes the amount of air needed per unit mass of fuel. The AFR ensures the correct proportioning of air to fuel, impacting combustion efficiency and emissions.
To determine the AFR on a mass basis, we use the balanced reaction equation from our previous step. The mass of air required includes oxygen as well as nitrogen (since air is roughly 21% O2 and 79% N2 by volume).
  • First, calculate the mass of oxygen from the balanced equation.
  • Then, convert this to the total air mass by considering the air composition (multiply the mass of O2 by about 4.76).

The final step involves dividing the total air mass by the mass of fuel to get the air-fuel ratio. For our example, this ratio provides insight into how much air is needed to completely combust 1 kg of dried feedlot manure, ensuring efficient and clean combustion.

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Most popular questions from this chapter

13.1 A vessel contains a mixture of \(60 \% \mathrm{O}_{2}\) and \(40 \% \mathrm{CO}\) on a mass basis. Determine the percent excess or percent deficiency of oxygen, as appropriate.

13.35 The energy required to vaporize the working fluid passing through the boiler of a simple vapor power plant is provided by the complete combustion of methane with \(110 \%\) of theoretical air. The fuel and air enter in separate streams at \(25^{\circ} \mathrm{C}, 1 \mathrm{~atm}\). Products of combustion exit the stack at \(150^{\circ} \mathrm{C}\), \(1 \mathrm{~atm}\). Plot the mass flow rate of fuel required, in \(\mathrm{kg} / \mathrm{h}\) per MW of power developed by the plant versus the plant thermal efficiency, \(\eta\). Consider \(\eta\) in the range \(30-40 \%\). Kinetic and potential energy effects are negligible.

13.61 An inventor has developed a device that at steady state takes in liquid water at \(25^{\circ} \mathrm{C}, 1 \mathrm{~atm}\) with a mass flow rate of \(4 \mathrm{~kg} / \mathrm{h}\) and produces separate streams of hydrogen \(\left(\mathrm{H}_{2}\right)\) and oxygen \(\left(\mathrm{O}_{2}\right)\), each at \(25^{\circ} \mathrm{C}, 1\) atm. The inventor claims that the device requires an electrical power input of \(14.6 \mathrm{~kW}\) when operating isothermally at \(25^{\circ} \mathrm{C}\). Heat transfer with the surroundings occurs, but kinetic and potential energy effects can be ignored. Evaluate the inventor's claim.

13.60 Streams of hydrogen \(\left(\mathrm{H}_{2}\right)\) and oxygen \(\left(\mathrm{O}_{2}\right)\), each at \(1 \mathrm{~atm}\), enter a fuel cell operating at steady state and water vapor exits at \(1 \mathrm{~atm}\). If the cell operates isothermally at (a) \(300 \mathrm{~K}\), (b) \(400 \mathrm{~K}\), and (c) \(500 \mathrm{~K}\), determine the maximum theoretical work that can be developed by the cell in each case, in kJ per kmol of hydrogen flowing, and comment. Heat transfer with the surroundings takes place at the cell temperature, and kinetic and potential energy effects can be ignored.

7\. When applying the energy balance to a reacting system, why is it essential that the enthalpies of each reactant and product be evaluated relative to a common datum?

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