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A natural gas containing 82.0 mole \(\% \mathrm{CH}_{4}\) and the balance \(\mathrm{C}_{2} \mathrm{H}_{6}\) is burned with \(20 \%\) excess air in a boiler furnace. The fuel gas enters the furnace at \(298 \mathrm{K}\), and the air is preheated to 423 \(\mathrm{K}\). The heat capacities of the stack-gas components may be assumed to have the following constant values: $$\begin{aligned}\mathrm{CO}_{2}: & C_{p}=50.0 \mathrm{J} /(\mathrm{mol} \cdot \mathrm{K}) \\ \mathrm{H}_{2} \mathrm{O}(\mathrm{v}): & C_{p}=38.5 \mathrm{J} /(\mathrm{mol} \cdot \mathrm{K}) \\\\\mathrm{O}_{2}: & C_{p}=33.1 \mathrm{J} /(\mathrm{mol} \cdot \mathrm{K}) \\ \mathrm{N}_{2}: & C_{p}=31.3 \mathrm{J} /(\mathrm{mol} \cdot \mathrm{K})\end{aligned}$$ (a) Assuming complete combustion of the fuel, calculate the adiabatic flame temperature. (b) How would the flame temperature change if the percent excess air were increased? How would it change if the percentage of methane in the fuel increased? Briefly explain both of your answers.

Short Answer

Expert verified
The adiabatic flame temperature would be found by utilizing a heat balance equation, taking into account the molecular composition of the gas and the number of moles of each component in the reacting gases along with their respective heat capacities. Changes in the percentage of excess air and the composition of the fuel would affect the flame temperature - increasing excess air decreases the flame temperature and increasing methane in the fuel increases the flame temperature.

Step by step solution

01

Calculate the moles of fuel

First, find the number of moles of CH4 and C2H6 in one mole of the gas. Since the fuel contains 82.0 mole% CH4 and the remainder is C2H6, there are 0.82 moles of CH4 and 0.18 moles of C2H6.
02

Perform Stoichiometric Calculations

Use the chemical equations to find the number of moles of oxygen required for complete combustion. For CH4, the equation is \(CH4 + 2O2 \rightarrow CO2 + 2H20\). Thus, each mole of CH4 requires 2 moles of O2 for combustion. Similarly, the equation for C2H6 is \(2C2H6 + 7O2 \rightarrow 4CO2 + 6H20\). So, each mole of C2H6 requires 7/2 moles of O2 for combustion. Given that 20\% excess air is used, calculate the number of moles of O2 supplied. 1 mole of air is 21 mol% O2 and 79 mol% N2.
03

Calculate the stack-gas composition

Calculate the moles of each gas in the combustion products or stack gas. For complete combustion, all carbon in the fuel goes to CO2 and all hydrogen goes to H2O. Oxygen in excess of the stoichiometric requirement exits as O2. The balance of the air, N2, also exits unchanged.
04

Apply the heat balance equation

Apply the heat balance equation (adiabatic flame, no heat loss or gain, \(\sum \Delta H_{reactants} = \sum \Delta H_{products}\)). The contribution of each component to \(\Delta H_{products}\) is (number of moles) \(\times (Cp)\) \(\times (T - T_{reference})\). Equate heat produced by combustion of reactants (there is no energy change for incoming air as its components are also in the stack gas). Set this equal to the heat capacity of the stack gas multiplied by the temperature rise, and solve for the flame temperature, \(T\).
05

Discuss the effect of increasing the percentage of excess air

Increasing the percentage of excess air would decrease the flame temperature. This is because the excess air, primarily nitrogen, absorbs some of the heat generated during combustion, but does not participate in the reaction. Hence, more excess air causes more heat to be absorbed, lowering the flame temperature.
06

Discuss the effect of increasing the percentage of methane in the fuel

Increasing the percentage of methane (CH4) in the fuel would increase the flame temperature. This is because methane has a higher heat of combustion than C2H6, such that for each mole of methane burned, more heat is produced than for a mole of C2H6. Thus, greater methane percentage leads to a higher flame temperature.

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Key Concepts

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

Adiabatic Flame Temperature
In the context of combustion analysis, the adiabatic flame temperature is essential. It refers to the temperature a flame reaches under the assumption that no heat is lost to the surroundings. The temperature depends on several factors, such as the type of fuel used and the amount of excess air introduced.

When calculating it, one needs to apply the principle of conservation of energy. This means that the total enthalpy of reactants must equal the total enthalpy of products. During combustion, the heat from burning is used to raise the temperature of gases produced. Thus, properly determining the temperature involves knowing both the specific heat capacities of the products and the amount of thermal energy released.
  • An accurate measure of the adiabatic flame temperature is critical as it influences the efficiency of processes like power generation and heating.
  • Higher flame temperatures typically indicate more efficient combustion and energy release.
  • Variables like air preheat and ambient temperature significantly impact the final temperature.
Stoichiometric Combustion
Stoichiometric combustion involves a perfect balance between fuel and oxygen, ensuring all fuel is burned with no leftover oxygen. In our scenario, this concept helps calculate the precise amount of oxygen required for burning methane (\(\mathrm{CH}_{4}\)) and ethane (\(\mathrm{C}_{2}\mathrm{H}_{6}\)).

For methane, the reaction can be written as: \(\mathrm{CH}_{4} + 2\mathrm{O}_{2} \rightarrow \mathrm{CO}_{2} + 2\mathrm{H}_{2}\mathrm{O}\). This equation shows that each mole of methane requires 2 moles of oxygen. Similarly, ethane needs \(\dfrac{7}{2}\) moles of \(\mathrm{O}_{2}\) for every mole of \(\mathrm{C}_{2}\mathrm{H}_{6}\), as expressed by \(2\mathrm{C}_{2}\mathrm{H}_{6} + 7\mathrm{O}_{2} \rightarrow 4\mathrm{CO}_{2} + 6\mathrm{H}_{2}\mathrm{O}\).
  • In stoichiometric combustion, efficiency peaks because all fuel is used for energy production without wasting resources.
  • It forms the basis for determining the right amount of excess air needed in industrial settings.
  • Skillfully managing combustion around these principles ensures minimal emissions and energy losses.
Excess Air in Combustion
Using excess air in combustion impacts the system's temperature and efficiency. It refers to the amount of air supplied beyond the stoichiometric requirement. In our example, there's a 20% excess air used, implying more oxygen than is theoretically required.

While adding some excess air ensures thorough combustion by ensuring complete reaction with the fuel, too much excess air can cool down the reaction. That's because the extra nitrogen in the air, which does not react, absorbs energy without contributing to the combustion process.
  • Adding excess air is a common practice in industrial combustion due to its safety cushion, preventing the formation of harmful pollutants like carbon monoxide.
  • Optimal excess minimizes energy losses while ensuring full combustion.
  • However, an increase in excess air leads to a lower adiabatic flame temperature, highlighting the trade-off that must be managed.
Methane Combustion
Combusting methane is a crucial concept in this analysis. Methane (\(\mathrm{CH}_{4}\)) is a simple hydrocarbon with a high energy content, making it an efficient fuel choice.

Its combustion reaction is straightforward, producing carbon dioxide (\(\mathrm{CO}_{2}\)) and water (\(\mathrm{H}_{2}\mathrm{O}\)). This reaction releases a significant amount of heat energy, contributing to a higher potential flame temperature compared to heavier hydrocarbons like ethane (\(\mathrm{C}_{2}\mathrm{H}_{6}\)).
  • Methane's high heat of combustion is beneficial in generating more heat per mole, leading to higher energy efficiency when used in engines or heating systems.
  • Its combustion tends to produce fewer carbon-based pollutants, making it an environmentally friendly fuel compared to other fossil fuels.
  • When methane composition in fuel increases, the adiabatic flame temperature also increases, enhancing the combustion efficiency of the system.

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Most popular questions from this chapter

Calcium chloride is a salt used in a number of food and medicinal applications and in brine for refrigeration systems. Its most distinctive property is its affinity for water. in its anhydrous form it efficiently absorbs water vapor from gases, and from aqueous liquid solutions it can form (at different conditions) calcium chloride hydrate \(\left(\mathrm{CaCl}_{2} \cdot \mathrm{H}_{2} \mathrm{O}\right)\) dihydrate \(\left(\mathrm{CaCl}_{2} \cdot 2 \mathrm{H}_{2} \mathrm{O}\right)\) tetrahydrate \(\left(\mathrm{CaCl}_{2} \cdot 4 \mathrm{H}_{2} \mathrm{O}\right),\) and hexahydrate \(\left(\mathrm{CaCl}_{2} \cdot 6 \mathrm{H}_{2} \mathrm{O}\right)\) You have been given the task of determining the standard heat of the reaction in which calcium chloride hexahydrate is formed from anhydrous calcium chloride: $$\mathrm{CaCl}_{2}(\mathrm{s})+6 \mathrm{H}_{2} \mathrm{O}(\mathrm{l}) \rightarrow \mathrm{CaCl}_{2} \cdot 6 \mathrm{H}_{2} \mathrm{O}(\mathrm{s}): \quad \Delta H_{\mathrm{r}}^{\circ}(\mathrm{k} \mathrm{J})=?$$ By definition, the desired quantity is the heat of hydration of calcium chloride hexahydrate. You cannot carry out the hydration reaction directly, so you resort to an indirect method. You first dissolve 1.00 mol of anhydrous \(\mathrm{CaCl}_{2}\) in \(10.0 \mathrm{mol}\) of water in a calorimeter and determine that \(64.85 \mathrm{kJ}\) of heat must be transferred away from the calorimeter to keep the solution temperature at \(25^{\circ} \mathrm{C}\). You next dissolve 1.00 mol of the hexahydrate salt in 4.00 mol of water and find that 32.1 kJ of heat must be transferred to the calorimeter to keep the temperature at \(25^{\circ} \mathrm{C}\). (a) Use these results to calculate the desired heat of reaction. (Suggestion: Begin by writing out the stoichiometric equations for the two dissolution processes.) (b) Calculate the standard heat of reaction in \(\mathrm{kJ}\) for \(\mathrm{Ca}(\mathrm{s}), \mathrm{Cl}_{2}(\mathrm{g})\) and \(\mathrm{H}_{2} \mathrm{O}\) reacting to form \(\mathrm{CaCl}_{2}\) (aq, \(r=10\) ). (c) Speculate about why the standard heat of reaction in forming calcium chloride hexahydrate cannot be measured directly by reacting the anhydrous salt with water in a calorimeter.

A gaseous fuel containing methane and ethane is burned with excess air. The fuel enters the furnace at \(25^{\circ} \mathrm{C}\) and 1 atm, and the air enters at \(200^{\circ} \mathrm{C}\) and 1 atm. The stack gas leaves the furnace at \(800^{\circ} \mathrm{C}\) and 1 atm and contains 5.32 mole\% \(\mathrm{CO}_{2}, 1.60 \%\) CO, \(7.32 \%\) O \(_{2}, 12.24 \% \mathrm{H}_{2} \mathrm{O}\), and the balance \(\mathrm{N}_{2}\). (a) Calculate the molar percentages of methane and ethane in the fuel gas and the percentage excess air fed to the reactor. (b) Calculate the heat (kJ) transferred from the reactor per cubic meter of fuel gas fed. (c) A proposal has been made to lower the feed rate of air to the furnace. State advantages and a drawback of doing so.

A methanol-synthesis reactor is fed with a gas stream at \(220^{\circ} \mathrm{C}\) consisting of 5.0 mole\% methane, \(25.0 \%\) CO, \(5.0 \% \mathrm{CO}_{2},\) and the remainder hydrogen. The reactor and feed stream are at \(7.5 \mathrm{MPa}\). The primary reaction occurring in the reactor and its associated equilibrium constant are $$\begin{array}{l}\mathrm{CO}+2 \mathrm{H}_{2} \rightleftharpoons \mathrm{CH}_{3} \mathrm{OH} \\\K=\frac{y_{\mathrm{CH}, \mathrm{OH}} y_{\mathrm{H}_{2}}}{y_{\mathrm{CO}} y_{H_{2}}^{2} P^{2}}=\exp \left(\begin{array}{c}21.225+\frac{9143.6}{T}-7.492 \ln T \\ +4.076 \times 10^{-3} T-7.161 \times 10^{-8} T^{2}\end{array}\right)\end{array}$$ where \(T\) is in kelvins. The product stream may be assumed to reach equilibrium at \(250^{\circ} \mathrm{C}\). (a) Determine the composition (mole fractions) of the product stream and the percentage conversions of CO and \(\mathrm{H}_{2}\). (b) Neglecting the effect of pressure on enthalpies, estimate the amount of heat (kJ/mol feed gas) that must be added to or removed from (state which) the reactor. (c) Calculate the extent of reaction and heat removal rate (kJ/mol feed) for reactor temperatures between \(200^{\circ} \mathrm{C}\) and \(400^{\circ} \mathrm{C}\) in \(50^{\circ} \mathrm{C}\) increments. Use these results to obtain an estimate of the adiabatic reaction temperature. (d) Determine the effect of pressure on the reaction by evaluating extent of conversion and rate of heat transfer at \(1 \mathrm{MPa}\) and \(15 \mathrm{MPa}\). (e) Considering the results of your calculations in Parts (c) and (d), propose an explanation for selection of the initial reaction conditions of \(250^{\circ} \mathrm{C}\) and \(7.5 \mathrm{MPa}\).

Methane is burned completely with 40\% excess air. The methane enters the combustion chamber at \(25^{\circ} \mathrm{C},\) the combustion air enters at \(150^{\circ} \mathrm{C},\) and the stack gas \(\left[\mathrm{CO}_{2}, \mathrm{H}_{2} \mathrm{O}(\mathrm{v}), \mathrm{O}_{2}, \mathrm{N}_{2}\right]\) exits at \(450^{\circ} \mathrm{C} .\) The chamber functions as a preheater for an air stream flowing in a pipe through the chamber to a spray dryer. The air enters the chamber at \(25^{\circ} \mathrm{C}\) at a rate of \(1.57 \times 10^{4} \mathrm{m}^{3}(\mathrm{STP}) / \mathrm{h}\) and is heated to \(181^{\circ} \mathrm{C}\). All of the heat generated by combustion is used to heat the combustion products and the air going to the spray dryer (i.e., the combustion chamber may be considered adiabatic). (a) Draw and completely label the process flow diagram and perform a degree- of-freedom analysis. (b) Calculate the required molar flow rates of methane and combustion air (kmol/h) and the volumetric flow rates \(\left(\mathrm{m}^{3} / \mathrm{h}\right)\) of the two effluent streams. State all assumptions you make. (c) When the system goes on line for the first time, environmental monitoring of the stack gas reveals a considerable quantity of CO, suggesting a problem with either the design or the operation of the combustion chamber. What changes from your calculated values would you expect to see in the temperatures and volumetric flow rates of the effluent streams [increase, decrease, cannot tell without doing the calculations]?

Formaldehyde is produced by decomposing methanol over a silver catalyst: $$\mathrm{CH}_{3} \mathrm{OH} \rightarrow \mathrm{HCHO}+\mathrm{H}_{2}$$ To provide heat for this endothermic reaction, some oxygen is included in the feed to the reactor, leading to the partial combustion of the hydrogen produced in the methanol decomposition. The feed to an adiabatic formaldehyde production reactor is obtained by bubbling a stream of air at 1 atm through liquid methanol. The air leaves the vaporizer saturated with methanol and contains \(42 \%\)methanol by volume. The stream then passes through a heater in which its temperature is raised to \(145^{\circ} \mathrm{C} .\) To avoid deactivating the catalyst, the maximum temperature attained in the reactor must be limited to \(600^{\circ} \mathrm{C}\). For this purpose, saturated steam at \(145^{\circ} \mathrm{C}\) is metered into the air-methanol stream, and the combined stream cnters the reactor. A fractional methanol conversion of \(70.0 \%\) is achicved in the reactor, and the product gas contains 5.00 mole\% hydrogen. The product gas is cooled to \(145^{\circ} \mathrm{C}\) in a waste heat boiler in which saturated steam at 3.1 bar is generated from liquid water at \(30^{\circ} \mathrm{C}\). Several absorption and distillation units follow the waste heat boiler, and formaldehyde is ultimately recovered in an aqueous solution containing 37.0 wt\% HCHO. The plant is designed to produce 36 metric kilotons of this solution per year, operating 350 days/yr. (a) Draw the process flowchart and label it completely. Show the absorption/distillation train as a single unit with the reactor product gas and additional water entering and the formaldehyde solution and a gas stream containing methanol, oxygen, nitrogen, and hydrogen leaving. (b) Calculate the operating temperature of the methanol vaporizer. (c) Calculate the required feed rate of steam to the reactor \((\mathrm{kg} / \mathrm{h})\) and the molar flow rate and composition of the product gas. (d) Calculate the rate ( \(\mathrm{kg} / \mathrm{h}\) ) at which steam is generated in the waste heat boiler. (e) Enough saturated steam was added to the feed to the reactor to keep the reactor outlet temperature at \(600^{\circ} \mathrm{C}\). Explain in your own words (i) why adding steam lowers the outlet temperature, and (ii) the cconomic drawbacks of higher and lower outlet temperatures.

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