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Formaldehyde may be produced in the reaction between methanol and oxygen: $$2 \mathrm{CH}_{3} \mathrm{OH}(\mathrm{l})+\mathrm{O}_{2}(\mathrm{g}) \rightarrow 2 \mathrm{HCHO}(\mathrm{g})+2 \mathrm{H}_{2} \mathrm{O}(\mathrm{l}): \quad \Delta H_{\mathrm{r}}^{\circ}=-326.2 \mathrm{kJ}$$ The standard heat of combustion of hydrogen is $$\mathrm{H}_{2}(\mathrm{g})+\frac{1}{2} \mathrm{O}_{2}(\mathrm{g}) \rightarrow \mathrm{H}_{2} \mathrm{O}(\mathrm{l}): \quad \Delta \hat{H}_{\mathrm{c}}^{\circ}=-285.8 \mathrm{kJ} / \mathrm{mol}$$ (a) Use these heats of reaction and Hess's law to determine the standard heat of the direct decomposition of mcthanol to form formaldchyde: $$\mathrm{CH}_{3} \mathrm{OH}(\mathrm{l}) \rightarrow \mathrm{HCHO}(\mathrm{g})+\mathrm{H}_{2}(\mathrm{g})$$ (b) Explain why you would probably use the method of Part (a) to determine the heat of the methanol decomposition reaction experimentally rather than carrying out the decomposition reaction and measuring \(\Delta H_{f}^{\circ}\) directly.

Short Answer

Expert verified
(a) The standard heat of the direct decomposition of methanol to form formaldehyde is \( \Delta H_{decomp}^\circ = 40.1 kJ/mol \). (b) The indirect method using Hess's law is safer and more manageable than conducting a direct experiment to measure the heat of methanol decomposition.

Step by step solution

01

Determine the Heat of Methanol Decomposition

The given reaction \[2 CH_{3}OH(l) + O_{2}(g) \rightarrow 2 HCHO(g) + 2 H_{2}O(l): \quad \Delta H_{r}^\circ = -326.2 kJ\]defines the production of formaldehyde and water from methanol and oxygen. Let's rearrange it to match the reaction asked in part (a):\[CH_{3}OH(l) \rightarrow HCHO(g) + H_{2}O(l): \quad \Delta H_{r}^\circ = -326.2 kJ / 2\]Subtract the combustion of hydrogen from the new equation:\[CH_{3}OH(l) \rightarrow HCHO(g) + H_{2}O(l) - [H_{2}(g) + \frac{1}{2} O_{2}(g) \rightarrow H_{2}O(l)]\]This simplifies to:\[CH_{3}OH(l) \rightarrow HCHO(g) + H_{2}(g)\]Using Hess's Law:\[\Delta H_{decomp}^\circ = \Delta H_{r}^\circ - \Delta H_{c}^\circ = -326.2 kJ / 2 - (-285.8 kJ/mol) = 40.1 kJ/mol\]
02

Discuss the Advantages of the Indirect Method

Conducting an actual lab experiment to measure the heat of methanol decomposition can be a challenging and dangerous task. It may not be feasible due to unpredictable conditions or hazards associated with decomposition reactions. By using Hess's law, we can indirectly determine energy changes using known heats of other chemical reactions under standard conditions. This avoids messing with difficult chemicals or reactions directly, making it safer and more manageable.

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Key Concepts

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

Standard Heat of Combustion
The standard heat of combustion, denoted by \( \Delta \hat{H}_{c}^\circ \), is a fundamental concept in thermochemistry. It refers to the heat energy released when one mole of a substance combusts completely with oxygen under standard conditions. Standard conditions generally mean at a pressure of 1 bar and a specific temperature, usually 25°C.

To put it simply, it's like measuring how much energy you'd get if you set a mole of a substance on fire in a controlled setting. For example, the standard heat of combustion of hydrogen describes the energy released when hydrogen gas is combined with oxygen to produce liquid water, and it holds immense relevance when dealing with chemical reactions involving hydrocarbons.

Understanding this concept is crucial because it underpins the energy changes involved in chemical reactions and allows us to calculate unknown reaction enthalpies, as shown in Hess's Law calculations.
Methanol Decomposition
Methanol, a simple alcohol, can break down into formaldehyde and hydrogen gas, a reaction that can be studied through methanol decomposition. This process is particularly interesting because it has various applications in industrial chemistry. As such, getting an accurate measurement of the energy changes associated with methanol decomposition is vital not only for theoretical studies but also for practical implications in synthesis and energy production.

In educational settings, decomposing methanol provides a tangible example for students to grasp the intricacies involved in chemical process calculations. It's like taking apart a toy to see what's inside; by breaking down methanol, you learn about the bonds formed and broken in the reaction, and it's a perfect segue into the discussion of reaction energetics and applications of Hess's Law.
Thermochemical Calculations
Thermochemical calculations are the bread and butter of understanding the energy aspects of chemical reactions. Think of it as accounting, but instead of money, you're counting how much heat energy goes in and out of a chemical system. By foraying into this field, you delve into quantifying the heat absorbed or released during reactions. This is done by employing known values, such as the standard heats of combustion and formation.

To perform these calculations accurately, the law of conservation of energy is applied to the reaction. Since energy cannot be created or destroyed, the total energy of the system must remain constant. Thermochemical equations are balanced not only for mass in terms of atoms but also for energy. This dual balancing act provides precise insights into the energetic feasibility and the conditions necessary for a reaction to occur.
Chemical Reaction Energy Changes
Every chemical reaction involves a change in energy. This change can either be absorbed from the surroundings (endothermic), or released to the surroundings (exothermic). These energy changes are the 'give and take' of the chemical world. They're incredibly important because they determine whether a reaction will occur spontaneously and what energy might be harnessed for use in other applications.

For instance, the decomposition of methanol is a process that, while not energetically complex, highlights the importance of tracking these changes meticulously. In a classroom or an industrial setting, understanding how much energy a reaction requires or releases is paramount for safety, efficiency, and predictive purposes. This knowledge forms the basis of designing chemical processes, selecting materials, and in the case of explosive reactions, taking appropriate safety measures.

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Most popular questions from this chapter

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.

Ethylene oxide is produced by the catalytic oxidation of ethylene: $$\mathrm{C}_{2} \mathrm{H}_{4}(\mathrm{g})+\frac{1}{2} \mathrm{O}_{2}(\mathrm{g}) \rightarrow \mathrm{C}_{2} \mathrm{H}_{4} \mathrm{O}(\mathrm{g})$$ An undesired competing reaction is the combustion of ethylene to \(\mathrm{CO}_{2}\) The feed to a reactor contains \(2 \mathrm{mol} \mathrm{C}_{2} \mathrm{H}_{4} / \mathrm{mol} \mathrm{O}_{2} .\) The conversion and yield in the reactor are respectively \(25 \%\) and \(0.70 \mathrm{mol} \mathrm{C}_{2} \mathrm{H}_{4} \mathrm{O}\) produced/mol \(\mathrm{C}_{2} \mathrm{H}_{4}\) consumed. A multiple- unit process separates the reactor outlet stream components: \(\mathrm{C}_{2} \mathrm{H}_{4}\) and \(\mathrm{O}_{2}\) are recycled to the reactor, \(\mathrm{C}_{2} \mathrm{H}_{4} \mathrm{O}\) is sold, and \(\mathrm{CO}_{2}\) and \(\mathrm{H}_{2} \mathrm{O}\) are discarded. The reactor inlet and outlet streams are each at \(450^{\circ} \mathrm{C}\), and the fresh feed and all species leaving the separation process are at \(25^{\circ} \mathrm{C}\). The combined fresh feedrecycle stream is preheated to \(450^{\circ} \mathrm{C}\). (a) Taking a basis of 2 mol of ethylene entering the reactor, draw and label a flowchart of the complete process (show the separation process as a single unit) and calculate the molar amounts and compositions of all process streams. (b) Calculate the heat requirement ( \(k J\) ) for the entire process and that for the reactor alone. Data for gaseous ethylene oxide $$\begin{aligned}\Delta \hat{H}_{\mathrm{f}}^{\prime} &=-51.00 \mathrm{kJ} / \mathrm{mol} \\ C_{p}[\mathrm{J} /(\mathrm{mol} \cdot \mathrm{K})] &=-4.69+0.2061 T-9.995 \times 10^{-5} T^{2} \end{aligned}$$ where \(T\) is in kelvins. (c) Calculate the flow rate \((\mathrm{kg} / \mathrm{h})\) and composition of the fresh feed, the overall conversion of ethylene, and the overall process and reactor heat requirements (kW) for a production rate of \(1500 \mathrm{kg} \mathrm{C}_{2} \mathrm{H}_{4} \mathrm{O} /\) day. Briefly explain the reasons for separating and recycling the ethylene-oxygen stream. (d) One of the attributes of this process defined in the problem statement is extremely unrealistic. What is it?

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.

Methane and \(30 \%\) excess air are to be fed to a combustion reactor. An inexperienced technician mistakes his instructions and charges the gases together in the required proportion into an evacuated closed tank. (The gases were supposed to be fed directly into the reactor.) The contents of the charged tank are at \(25^{\circ} \mathrm{C}\) and 4.00 atm absolute. (a) Calculate the standard internal energy of combustion of the methane combustion reaction. \(\Delta \hat{U}_{c}^{\circ}(\mathrm{kJ} / \mathrm{mol}),\) taking \(\mathrm{CO}_{2}(\mathrm{g})\) and \(\mathrm{H}_{2} \mathrm{O}(\mathrm{v})\) as the presumed products. Then prove that if the constant-pressure heat capacity of an ideal-gas species is independent of temperature, the specific internal energy of that species at temperature \(T\left(^{\circ} \mathrm{C}\right)\) relative to the same species at \(25^{\circ} \mathrm{C}\) is given by the expression $$\hat{U}=\left(C_{p}-R\right)\left(T-25^{\circ} \mathrm{C}\right)$$ where \(R\) is the gas constant. Use this formula in the next part of the problem. (b) You wish to calculate the maximum temperature, \(T_{\max }\left(^{\circ} \mathrm{C}\right),\) and corresponding pressure, \(P_{\max }(\text { atm }),\) that the tank would have to withstand if the mixture it contains were to be accidentally ignited. Taking molecular species at \(25^{\circ} \mathrm{C}\) as references and treating all species as ideal gases, prepare an inlet-outlet internal energy table for the closed system combustion process. In deriving expressions for each \(\dot{U}_{i}\) at the final reactor condition \(\left(T_{\max }, P_{\max }\right),\) use the following approximate values for \(C_{p_{i}}\left[\mathrm{k} J /\left(\mathrm{mol} \cdot^{\circ} \mathrm{C}\right)\right]: 0.033 \mathrm{for} \mathrm{O}_{2}, 0.032\) for \(\mathrm{N}_{2}, 0.052 \mathrm{for} \mathrm{CO}_{2},\) and \(0.040 \mathrm{for} \mathrm{H}_{2} \mathrm{O}(\mathrm{v}) .\) Then use an energy balance and the ideal-gas equation of state to perform the required calculations. (c) Why would the actual temperature and pressure attained in a real tank be less than the values calculated in Part (a)? (State several reasons.) (d) Think of ways that the tank contents might be accidentally ignited. The list should suggest why accepted plant safety regulations prohibit the storage of combustible vapor mixtures.

Methanol vapor is burned with excess air in a catalytic combustion chamber. Liquid methanol initially at \(25^{\circ} \mathrm{C}\) is vaporized at 1.1 atm and heated to \(100^{\circ} \mathrm{C}\); the vapor is mixed with air that has been preheated to \(100^{\circ} \mathrm{C},\) and the combined stream is fed to the reactor at \(100^{\circ} \mathrm{C}\) and 1 atm. The reactor effluent emerges at \(300^{\circ} \mathrm{C}\) and 1 atm. Analysis of the product gas yields a dry-basis composition of \(4.8 \% \mathrm{CO}_{2}\) \(14.3 \% \mathrm{O}_{2},\) and \(80.9 \% \mathrm{N}_{2}\) (a) Calculate the percentage excess air supplied and the dew point of the product gas. (b) Taking a basis of 1 g-mole of methanol burned, calculate the heat ( \(k\) J) needed to vaporize and heat the methanol feed, and the heat (kJ) that must be transferred from the reactor. (c) Suggest how the energy economy of this process could be improved. Then suggest why the company might choose not to implement your redesign.

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