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Grade 11 Chemistry Effective Homework 2: Industrial Production of Sulfuric Acid | Brief Solutions
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1 Main reason to purify furnace gas before the contact-process converter.
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2 Choose incorrect statements about sulfuric-acid manufacture.
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3 Choose correct statements from the converter and heat-exchanger diagram.
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4 Which sulfur-dioxide oxidation condition is not industrially appropriate?
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5 Which operation is explained by Le Chatelier's principle?
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6 Choose correct operation-and-reason pairs in sulfuric-acid manufacture.
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7 Choose the incorrect statement about temperature, pressure and recycling in SO2 oxidation.
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8 Methyl-formate synthesis conversion-temperature curve: choose incorrect statements.
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9.1 Pyrite-to-sulfuric-acid process: choose the incorrect statement.
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9.2 Two other functions of concentrated sulfuric acid in apparatus B, besides mixing gases.
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Dry the gas; observe bubbles to monitor and regulate gas flow.
9.3 Why temporarily remove the burner when the catalyst becomes red hot, besides catalyst activity?
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The exothermic reaction sustains heating; excessive temperature shifts equilibrium backward and lowers SO2 conversion.
9.4 D produces a white precipitate while fuchsin in E still decolorizes. Choose the solution in D.
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10.1 Combine CO2-to-CO conversion and methanol synthesis: find overall enthalpy and the equilibrium expression.
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$-49\ \mathrm{kJ\,mol^{-1}}$;$K=\dfrac{c(\mathrm{CH_3OH})c(\mathrm{H_2O})}{c(\mathrm{CO_2})c^3(\mathrm{H_2})}$
10.2 At constant volume, choose correct statements for $\mathrm{CO_2+H_2\rightleftharpoons CO+H_2O}$.
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10.3 How does the graph show that equilibrium has not been reached at $240^\circ\mathrm C$?
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Actual CO2 conversion is below the equilibrium value at that temperature.
10.4 Why does equilibrium CO2 conversion fall from $220$ to $240^\circ\mathrm C$?
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Exothermic methanol formation dominates in this range, and heating shifts its equilibrium backward.
10.5 Why does actual methanol selectivity fall with heating in this range?
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Heating favors the endothermic CO-forming reaction, increasing the CO share of carbon products.
10.6 Choose measures that improve equilibrium conversion of CO2 to methanol.
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10.7 Which curve represents the methanol mole fraction among carbon products?
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10.8 Directly making methanol and oxygen from CO2 and water has $\Delta H=676.48$ kJ/mol. Assess thermodynamic feasibility.
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It is not spontaneous under the stated thermodynamic model: $\Delta H>0$ and $\Delta S<0$, hence $\Delta G>0$. An external energy input is required.
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