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Formaldehyde is produced commercially by the catalytic oxidation of methanol. In a side reaction, methanol is oxidized to \(\mathrm{CO}_{2}\) $$\begin{array}{l}\mathrm{CH}_{3} \mathrm{OH}+\mathrm{O}_{2} \rightarrow \mathrm{CH}_{2} \mathrm{O}+\mathrm{H}_{2} \mathrm{O} \\\\\mathrm{CH}_{3} \mathrm{OH}+\mathrm{O}_{2} \rightarrow \mathrm{CO}_{2}+2 \mathrm{H}_{2} \mathrm{O}\end{array}$$ A mixture containing 55.6 mole \(\%\) methanol and the balance oxygen enters a reactor at \(350^{\circ} \mathrm{C}\) and \(1 \mathrm{atm}\) at a rate of \(4.60 \times 10^{4} \mathrm{L} / \mathrm{s}\). The reaction products emerge at the same temperature and pressure at a rate of \(6.26 \times 10^{4} \mathrm{L} / \mathrm{s} .\) An analysis of the products yields a molar composition of \(36.7 \% \mathrm{CH}_{2} \mathrm{O}, 4.1 \% \mathrm{CO}_{2}\) \(14.3 \% \mathrm{O}_{2},\) and \(44.9 \% \mathrm{H}_{2} \mathrm{O} .\) The required reactor cooling rate is calculated to be \(1.05 \times 10^{5} \mathrm{kW}\) (a) Is the calculated cooling rate correct for the given stream data? (b) The stream data cannot be correct. Prove it.

Short Answer

Expert verified
After calculating energetics, if the calculated cooling rate doesn't match with the \(1.05 \times 10^5 kW\), then the given cooling rate is incorrect. And if calculated moles of \(O_2\) for both reactions don't match with the moles in the input stream, the stream data is incorrect.

Step by step solution

01

- Calculation of Mole flows

First calculate the mole flows of the key substances involved in the reaction. The molar flow of the incoming methanol is calculated as \(0.556 \times \frac{4.60 \times 10^{4}\,L/s}{24.47\,L/mol}\), where 24.47 is the molar volume in liters under standard conditions (1 atm, 25 Celsius). Similarly, get the molar flows of \(CH_2O\), \(CO_2\), and \(H_2O\) from the exit gas stream.
02

- Application of Energy Balance

To verify the cooling rate, apply the energy balance principle on the system. This amounts to the fact that total energy coming into system should equate the total energy going out of it. Make use of appropriate heats of formation and combustion to calculate energetics of the incoming methanol, the desired reaction outcome, and the side reaction. Here, remember reactions are exothermic and heat will be released. Based on these findings, compare the energetics with the given cooling rate.
03

- Application of Molar Balance

To prove the inaccuracy in the stream data, apply the molar balance principle on \(O_2\), being a key reactant. Calculate the total moles of \(O_2\) needed for both the main and the side reactions. Match it with the moles of \(O_2\) in the input stream. If it doesn't match, then the stream data is shown to be incorrect.

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Key Concepts

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

Catalytic Oxidation
Catalytic oxidation is a fundamental chemical process whereby a catalyst accelerates the oxidation of a substance. In our context, the commercial production of formaldehyde from methanol is under scrutiny. To understand the reaction, picture the catalyst as a facilitator that doesn't change itself but makes it easier for reactants, in this case, methanol (\( \text{CH}_3\text{OH} \) and oxygen (\( \text{O}_2 \) to convert into products: formaldehyde (\( \text{CH}_2\text{O} \) and water (\( \text{H}_2\text{O} \) in the main reaction, and carbon dioxide (\( \text{CO}_2 \) and water in the side reaction.

It's important to understand that not all of the methanol turns into formaldehyde; some of it is fully oxidized into water and carbon dioxide. This is typical in such processes where multiple reactions can occur, and managing these side reactions is vital for efficiency and safety. Catalysts must be carefully selected to favor the main reaction and minimize undesired byproducts while operating under specific conditions of temperature and pressure.

When interacting with the catalyst, these molecules break and form new bonds to generate the desired and side products. In industrial processes, this is heavily monitored and optimized to ensure maximum yield and minimum waste.
Energy Balance
The energy balance is a cornerstone of chemical engineering and reaction analysis, ensuring that the energy entering a system (like our reactor) equals the energy exiting. This reflects the conservation of energy principle. In the context of the exercise, this involves comparing the heat released by the reaction (exothermic in nature) with the reactor's cooling rate.

Every chemical substance involved in a reaction possesses a certain amount of stored energy, commonly referred to as enthalpy. When reactions occur, this enthalpy changes, and energy is either absorbed or released. In our scenario, the enthalpies of formation and combustion provide us with the energy changes of methanol conversion to formaldehyde and the side reaction leading to carbon dioxide. To confirm if the reactor's cooling rate aligns with the stream data, we compare the energy released (sum of the exothermic reactions' energy) with the cooling rate provided. The calculated cooling rate should ideally match the sum of the heat of reaction of the products and the enthalpies of the inflowing and outflowing streams if the energy balance is maintained.
Mole Flows
Mole flows are a reflection of the amount of a substance in terms of its molecular count per time unit, which is crucial for quantifying chemical reactions. In our problem, the mole flow calculations help us understand how much reactant is being converted and whether the product stream data is accurate.

To calculate mole flows for this problem, we began by determining the methanol mole flow entering the reactor based on its given percentage and the volumetric flow rate. After that, we analyzed the product stream to get the mole flows for each product formed. Through these figures, it’s possible not only to gain insight into the reaction progress but also to apply a molar balance. A molar balance involves verifying if the number of moles of reactants equals the number of moles of products considering both the main and side reactions.

By establishing the mole flow for oxygen, we can compare it against the amounts required for the reactions. If the necessary oxygen for the reactions exceeds what's available in the stream, then we can conclude that there's an error in the given stream data. This essential concept allows chemical engineers to validate reaction feasibility, optimize processes, and troubleshoot production issues.

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Most popular questions from this chapter

A culture of the fungus aspergillus niger is used industrially in the manufacture of citric acid and other organic species. Cells of the fungus have an ultimate analysis of \(\mathrm{CH}_{1,79} \mathrm{N}_{0.2} \mathrm{O}_{0.5}\), and the heat of formation of this species is necessary to approximate the heat duty for the bioreactor in which citric acid is to be produced. You collect a dried sample of the fungus and determine its heat of combustion to be \(-550 \mathrm{kJ} / \mathrm{mol} .\) Estimate the heat of formation \((\mathrm{kJ} / \mathrm{mol})\) of the dried fungus cells.

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.

Use Hess's law to calculate the standard heat of the water-gas shift reaction $$\mathrm{CO}(\mathrm{g})+\mathrm{H}_{2} \mathrm{O}(\mathrm{v}) \rightarrow \mathrm{CO}_{2}(\mathrm{g})+\mathrm{H}_{2}(\mathrm{g})$$ from each of the two sets of data given here. (a) \(\mathrm{CO}(\mathrm{g})+\mathrm{H}_{2} \mathrm{O}(\mathrm{l}) \rightarrow \mathrm{CO}_{2}(\mathrm{g})+\mathrm{H}_{2}(\mathrm{g}): \quad \Delta H_{\mathrm{r}}^{\circ}=+1226 \mathrm{Btu}\) $$\mathrm{H}_{2} \mathrm{O}(\mathrm{l}) \rightarrow \mathrm{H}_{2} \mathrm{O}(\mathrm{v}): \quad \Delta \hat{H}_{\mathrm{v}}=+18,935 \mathrm{Btu} / \mathrm{lb}-\mathrm{mole}$$ $$\begin{aligned}&\text { (b) } \mathrm{CO}(\mathrm{g})+\frac{1}{2} \mathrm{O}_{2}(\mathrm{g}) \rightarrow \mathrm{CO}_{2}(\mathrm{g}): \quad \Delta H_{\mathrm{r}}^{\circ}=-121,740 \mathrm{Btu}\\\&\mathrm{H}_{2}(\mathrm{g})+\frac{1}{2} \mathrm{O}_{2}(\mathrm{g}) \rightarrow \mathrm{H}_{2} \mathrm{O}(\mathrm{v}): \quad \Delta H_{\mathrm{r}}^{\circ}=-104,040 \mathrm{Btu} \end{aligned}$$

A gas stream consisting of \(n\) -hexane in methane is fed to a condenser at \(60^{\circ} \mathrm{C}\) and 1.2 atm. The dew point of the gas (considering hexane as the only condensable component) is \(55^{\circ} \mathrm{C}\). The gas is cooled to \(5^{\circ} \mathrm{C}\) in the condenser, recovering pure hexane as a liquid. The effluent gas leaves the condenser saturated with hexane at \(5^{\circ} \mathrm{C}\) and 1.1 atm and is fed to a boiler furnace at a rate of \(207.4 \mathrm{L} / \mathrm{s}\), where it is burned with \(100 \%\) excess air that enters the furnace at \(200^{\circ} \mathrm{C}\). The stack gas emerges at \(400^{\circ} \mathrm{C}\) and 1 atm and contains no carbon monoxide or unburned hydrocarbons. The heat transferred from the furnace is used to generate saturated steam at 10 bar from liquid water at \(25^{\circ} \mathrm{C}\). (a) Calculate the mole fractions of hexane in the condenser feed and product gas streams and the rate of hexane condensation (liters condensate/s). (b) Calculate the rate at which heat must be transferred from the condenser (kW) and the rate of generation of steam in the boiler ( \(\mathrm{kg} / \mathrm{s}\) ).

Methane at \(25^{\circ} \mathrm{C}\) is burned in a boiler furnace with \(10.0 \%\) excess air preheated to \(100^{\circ} \mathrm{C}\). Ninety percent of the methane fed is consumed, the product gas contains \(10.0 \mathrm{mol} \mathrm{CO}_{2} / \mathrm{mol} \mathrm{CO},\) and the combustion products leave the furnace at \(400^{\circ} \mathrm{C}\). (a) Calculate the heat transferred from the furnace, \(-\dot{Q}(\mathrm{kW}),\) for a basis of \(100 \mathrm{mol} \mathrm{CH}_{4}\) fed/s. (The greater the value of \(-\dot{Q}\), the more steam is produced in the boiler.) (b) Would the following changes increase or decrease the rate of steam production? (Assume the fuel feed rate and fractional conversion of methane remain constant.) Briefly explain your answers. (i) Increasing the temperature of the inlet air; (ii) increasing the percent excess air for a given stack gas temperature; (iii) increasing the selcctivity of \(\mathrm{CO}_{2}\) to \(\mathrm{CO}\) formation in the furnace; and (iv) increasing the stack gas temperature.

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