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Chemistry • Class 12

Solutions - Class 12

Master Solutions & Colligative Properties through focused practice that strengthens conceptual understanding, problem-solving skills, and the ability to recognize common traps and misconceptions. Explore challenging questions designed to develop deeper reasoning and confident application of key ideas.

Overview

This chapter delves into the properties of solutions, including concentration terms, Raoult's Law, colligative properties, and their applications. It provides a comprehensive understanding of ideal and non-ideal solutions and the factors influencing solubility.

Why This Chapter Matters

  • The study of solutions is crucial for understanding chemical processes in industrial, biological, and environmental systems. From pharmaceuticals to chemical engineering, solutions play a key role in diverse applications.

Real-Life Applications

  • Understanding the principles behind saline solutions used in medical treatments.
  • Exploring the role of colligative properties in determining molecular masses.
  • Analyzing the behavior of solutions in environmental and industrial processes.

Skills You Will Learn

  • Calculating concentrations using various terms such as molarity and molality.
  • Understanding and applying Raoult's Law to ideal and non-ideal solutions.
  • Analyzing colligative properties and their applications.

Core Concepts to Master

Concentration Units Dependency

Molarity is temperature-dependent due to volume change; Molality and Mole Fraction are temperature-independent mass ratios.

Raoult’s Law Ideal vs Non-Ideal

Non-ideal deviations depend on whether solute-solvent interactions are weaker (positive) or stronger (negative) than pure components.

Azeotrope Boiling Point Logic

Minimum boiling azeotropes show large positive deviation; maximum boiling show large negative deviation from Raoult's Law.

Colligative Property Definition

Depends strictly on the total number of particles (ions/molecules) in solution, regardless of their chemical identity.

Vapor Pressure Lowering (Mole Fraction)

The relative lowering of vapor pressure equals the mole fraction of the solute, not the solvent.

Boiling Point Elevation (Solvent vs Solution)

Boiling point increases because vapor pressure decreases, requiring higher temperature to reach atmospheric pressure.

Freezing Point Depression (Pure Solvent)

Freezing occurs when solid and liquid phases have equal vapor pressure; solute lowers this equilibrium temperature.

Osmotic Pressure vs Diffusion

Osmotic pressure is the excess pressure applied to prevent solvent flow into the solution through a semi-permeable membrane.

Van’t Hoff Factor (i) Application

Always multiply colligative equations by 'i' for electrolytes to account for dissociation or association.

Degree of Dissociation/Association

Calculate 'i' using i = 1 + (n-1)α for dissociation and i = 1 + (1/n - 1)α for association.

Henry’s Law Constant (Kh) Trends

Higher Kh means lower gas solubility; Kh increases with temperature, explaining why gases are less soluble in hot water.

Solubility of Solids in Liquids

Dissolution is often endothermic; heating saturated solutions typically increases solubility per Le Chatelier’s principle.

Reverse Osmosis Dynamics

Requires external pressure greater than the osmotic pressure to force pure solvent out of the concentrated solution.

Isotonic, Hypertonic, Hypotonic

Comparison of osmotic pressures; water flows from low osmotic pressure (hypo) to high osmotic pressure (hyper) regions.

Molecular Mass Abnormalities

Calculated molar mass appears lower than actual for dissociation and higher for association (dimerization/polymerization).

Concept Collisions Used by Examiners

Competitive examinations rarely assess concepts in isolation. Instead, examiners intentionally combine multiple concepts from this and related chapters to create higher-order questions that test conceptual reasoning, analytical thinking, and problem-solving ability. The concept collision patterns below represent the combinations most frequently used while designing questions for this chapter.

Concentration Units Dependency
Amino Acid Zwitterion pH Sensitivity
Concentration Units Dependency
Nernst Equation Concentration Dependence
E° (M³⁺/M²⁺) Redox Potential
Concentration Units Dependency
Pseudo-First Order Kinetics
Stoichiometric Coefficient Division
Concentration Units Dependency
Schiff Base pH Dependence
Steric Hindrance (B-Strain)
Raoult’s Law Ideal vs Non-Ideal
Common Ion Effect on Solubility
Vapor Pressure Lowering (Mole Fraction)
Raoult’s Law Ideal vs Non-Ideal
Entropy of Phase Change
Enthalpy Definition
Raoult’s Law Ideal vs Non-Ideal
Finkelstein and Swarts Exchange
C-X Bond Polarization and Polarizability
Raoult’s Law Ideal vs Non-Ideal
Temperature Coefficient (Q10)
Graphical Slopes Analysis
Azeotrope Boiling Point Logic
Entropy of Phase Change
Spontaneity Criteria
Molecular Mass Abnormalities
Azeotrope Boiling Point Logic
Esterification Steric Hindrance
Ether Cleavage Patterns
Azeotrope Boiling Point Logic
Henry’s Law Constant (Kh) Trends
C-X Bond Polarization and Polarizability
Colligative Property Definition
Isotonic, Hypertonic, Hypotonic
Concentration Cells
Colligative Property Definition
KMnO₄ Redox pH Dependency
Degree of Dissociation (Alpha)
Vapor Pressure Lowering (Mole Fraction)
Electrode Potential Dependencies
Liquid Junction Potential
Vapor Pressure Lowering (Mole Fraction)
Henry’s Law Constant (Kh) Trends
Vapor Pressure Lowering (Mole Fraction)
Protein Denaturation Specificity
Vapor Pressure Lowering (Mole Fraction)
Reverse Osmosis Dynamics
Stoichiometric Coefficient Division
Boiling Point Elevation (Solvent vs Solution)
Hydrate and Ionization Isomerism
Coordination Isomerism
Boiling Point Elevation (Solvent vs Solution)
Molecular Mass Abnormalities
Basicity-Solvation Competition
Boiling Point Elevation (Solvent vs Solution)
Van’t Hoff Factor (i) Application
D-Glucose Anomeric Equilibrium
Freezing Point Depression (Pure Solvent)
Degree of Dissociation/Association
Inductive Effect Trends
Freezing Point Depression (Pure Solvent)
Hydroboration-Oxidation Regiochemistry
Degree of Dissociation/Association
Freezing Point Depression (Pure Solvent)
Pseudo-First Order Kinetics
Stoichiometric Coefficient Division
Freezing Point Depression (Pure Solvent)
Reducing Sugar Criteria
Epimerization vs Anomerization
Isotonic, Hypertonic, Hypotonic
Basicity-Solvation Competition
Osmotic Pressure vs Diffusion
Optical Isomerism Logic
Osmotic Pressure vs Diffusion
Protein Denaturation Specificity
Osmotic Pressure vs Diffusion
Pseudo-First Order Kinetics
Osmotic Pressure vs Diffusion
Standard Electrode Potential Sign Conventions
Van’t Hoff Factor (i) Application
Ammonolysis Complexity
Werner’s Theory Postulates
Van’t Hoff Factor (i) Application
E° (M2+/M) Anomalies
Molecular Mass Abnormalities
Van’t Hoff Factor (i) Application
Hydrate Stability vs. Carbonyl
Solubility of Solids in Liquids
Van’t Hoff Factor (i) Application
Molecular Mass Abnormalities
Amino Acid Zwitterion pH Sensitivity
Degree of Dissociation/Association
Basicity-Solvation Competition
Aniline Resonance Pitfalls
Degree of Dissociation/Association
Hydrate and Ionization Isomerism
Van’t Hoff Factor (i) Application
Degree of Dissociation/Association
KMnO₄ Redox pH Dependency
Steady State Approximation
Henry’s Law Constant (Kh) Trends
Electrolysis Product Prediction
Henry’s Law Constant (Kh) Trends
Gibbs Energy and Spontaneity
Henry’s Law Constant (Kh) Trends
Pseudo-First Order Kinetics
Henry’s Law Constant (Kh) Trends
Stoichiometric Coefficient Division
Henry’s Law Constant (Kh) Trends
Vapor Pressure Lowering (Mole Fraction)
Solubility of Solids in Liquids
Amino Acid Zwitterion pH Sensitivity
Van’t Hoff Factor (i) Application
Solubility of Solids in Liquids
Gibbs Energy and Spontaneity
Freezing Point Depression (Pure Solvent)
Solubility of Solids in Liquids
Hydrate Stability vs. Carbonyl
Van’t Hoff Factor (i) Application
Solubility of Solids in Liquids
Ligand Denticity Variations
Crystal Field Splitting (Octahedral)
Solubility of Solids in Liquids
Stoichiometric Coefficient Division
Rate Law Derivation from Mechanism
Reverse Osmosis Dynamics
Degree of Dissociation/Association
Kohlrausch Law Infinite Dilution
Reverse Osmosis Dynamics
Protein Denaturation Specificity
Peptide Bond Planarity
Reverse Osmosis Dynamics
Stoichiometric Coefficient Division
Rate Law Derivation from Mechanism
Isotonic, Hypertonic, Hypotonic
Corrosion as Electrochemical Process
Electrode Potential Dependencies
Isotonic, Hypertonic, Hypotonic
First Order Half-Life Independence
Osmotic Pressure vs Diffusion
Isotonic, Hypertonic, Hypotonic
Ligand Denticity Variations
Van’t Hoff Factor (i) Application
Isotonic, Hypertonic, Hypotonic
Protein Denaturation Specificity
Isotonic, Hypertonic, Hypotonic
Van’t Hoff Factor (i) Application
Degree of Dissociation/Association
Molecular Mass Abnormalities
Amino Acid Zwitterion pH Sensitivity
Inductive Effect Trends
Molecular Mass Abnormalities
Ether Cleavage Patterns
Oxidation State Traps
Molecular Mass Abnormalities
Hydrate and Ionization Isomerism
Crystal Field Splitting (Octahedral)
Molecular Mass Abnormalities
Schiff Base pH Dependence
Hydrate Stability vs. Carbonyl

Exam Coverage

Understand how this chapter is tested across major competitive examinations.

JEE Advanced

India · Competitive Exam · Undergraduate

JEE Main

India · Competitive Exam · Undergraduate

BITSAT

India · Competitive Exam · Undergraduate

NEET-UG

India · Competitive Exam · Undergraduate

IISER Aptitude Test (IAT)

India · Competitive Exam · Undergraduate

NEST

India · Competitive Exam · Undergraduate

NSEC

India · Olympiad · High School

AP Chemistry

United States · Curriculum · Advanced Placement

A-Level Chemistry

United Kingdom · Curriculum · Advanced Level

IB Chemistry HL

International · Curriculum · IB Diploma

Singapore A-Level Chemistry

Singapore · Curriculum · Advanced Level

Cambridge International A-Level Chemistry

International · Curriculum · Cambridge

International Chemistry Olympiad (IChO)

International · Olympiad · International

Practice Questions

Strengthen your understanding by solving carefully selected questions from this chapter.

50 Questions
1

A redox half-cell is prepared at 298 K298\text{ K} by mixing 50 mL50\text{ mL} of 0.40 M \ceFe2(SO4)30.40\text{ M } \ce{Fe_2(SO_4)_3} and 50 mL50\text{ mL} of 0.10 M \ceFeSO40.10\text{ M } \ce{FeSO_4}. In this highly concentrated electrolyte medium, the solution exhibits significant non-ideal behavior. The single-ion activity coefficients are determined to be γ\ceFe3+=0.01\gamma_{\ce{Fe^{3+}}} = 0.01 and γ\ceFe2+=0.10\gamma_{\ce{Fe^{2+}}} = 0.10. Given the standard reduction potential E\ceFe3+/Fe2+∘=0.770 VE^\circ_{\ce{Fe^{3+}/Fe^{2+}}} = 0.770\text{ V} and 2.303RTF=0.059 V\frac{2.303 RT}{F} = 0.059\text{ V}, calculate the actual reduction potential of this half-cell. (Given: log⁡2=0.301\log 2 = 0.301, log⁡5=0.699\log 5 = 0.699)

2

An aqueous buffer solution at 298 K298\text{ K} is prepared by dissolving 0.144 mol0.144\text{ mol} of a neutral amino acid zwitterion (\ceHA±\ce{HA^\pm}) and 0.144 mol0.144\text{ mol} of its sodium salt (\ceNaA\ce{NaA}) in water, along with an inert non-electrolyte. The total mass of the resulting solution is exactly 2000 g2000\text{ g} and the mass of the water solvent is 1.00 kg1.00\text{ kg}. The density of the solution is 1.250 g mL−11.250\text{ g mL}^{-1}.

The thermodynamic acid dissociation constant for the zwitterion is pKa2=9.60pK_{a2} = 9.60. Assuming the Debye-Hückel limiting law applies, what is the pHpH of this buffer solution?

(Given: Debye-Hückel constant A=0.50 L1/2 mol−1/2A = 0.50\text{ L}^{1/2}\text{ mol}^{-1/2} at 298 K298\text{ K}. The limiting law is log⁡γi=−Azi2Ic\log \gamma_i = -A z_i^2 \sqrt{I_c}, where IcI_c is the ionic strength in molarity).

3

The acid-catalyzed hydrolysis of ethanoic anhydride in a non-ideal dioxane-water mixture follows second-order kinetics (first-order with respect to each reactant):

\ce(CH3CO)2O+H2O−>[H+]2CH3COOH\ce{(CH3CO)2O + H2O ->[H^+] 2CH3COOH}

At 300 K300\text{ K}, a reaction mixture is prepared with initial concentrations [\ce(CH3CO)2O]0=0.12 M[\ce{(CH3CO)2O}]_0 = 0.12\text{ M} and [\ceH2O]0=1.2 M[\ce{H2O}]_0 = 1.2\text{ M}. The initial rate law is expressed as −d[\ce(CH3CO)2O]dt=kobs[\ce(CH3CO)2O]-\frac{d[\ce{(CH3CO)2O}]}{dt} = k_{\text{obs}}[\ce{(CH3CO)2O}], where kobs=3.6×10−4 s−1k_{\text{obs}} = 3.6 \times 10^{-4}\text{ s}^{-1}.

An identical mixture (containing the same initial moles of all components) is reacted at 330 K330\text{ K}. Due to the non-ideal nature of the solvent, heating from 300 K300\text{ K} to 330 K330\text{ K} causes a 20%20\% increase in the total volume of the solution.

Given that the activation energy for the true second-order rate constant is Ea=3300Rln⁡(3) J mol−1E_a = 3300 R \ln(3)\text{ J mol}^{-1} (where RR is the universal gas constant), what is the initial rate of appearance of ethanoic acid at 330 K330\text{ K}?

4

A student attempts to synthesize the Schiff base of 2,2,4,4-tetramethyl-3-pentanone using an aqueous solution of methanamine at 298 K. To maximize the yield, the total analytical concentration of methanamine is increased to 5.0 M. However, the yield of the imine remains negligible at both pH = 2.0 and pH = 4.5. Which of the following statements correctly identifies the primary chemical principles responsible for this failure?

5

An aqueous system is prepared at 298 K298 \text{ K} by mixing exactly 50.0 moles50.0 \text{ moles} of \ceH2O(l)\ce{H2O(l)}, 0.40 moles0.40 \text{ moles} of a completely soluble 1:1 strong electrolyte \ceNX\ce{NX}, and 0.50 moles0.50 \text{ moles} of a sparingly soluble 1:1 salt \ceMX\ce{MX}. The final volume of the aqueous solution is exactly 1.0 L1.0 \text{ L}. Given that the solubility product of \ceMX\ce{MX} at 298 K298 \text{ K} is Ksp=5.0×10−2K_{sp} = 5.0 \times 10^{-2}, what is the exact relative lowering of vapor pressure (ΔPP∘\frac{\Delta P}{P^\circ}) of the solution? Assume ideal behavior for all dissolved species.

6

An aqueous solution of ethanol (\ce{C2H5OH}) exhibits a positive deviation from Raoult's Law, forming a minimum-boiling azeotrope at a specific liquid mole fraction xEx_E and temperature TazT_{az} under a constant pressure PP. Let ΔHvap,sys\Delta H_{vap, sys} and ΔSvap,sys\Delta S_{vap, sys} represent the integral enthalpy and entropy of vaporization of the azeotropic mixture. Let γE\gamma_E and γW\gamma_W be the activity coefficients of ethanol and water in the liquid phase, and PE∘P_E^\circ and PW∘P_W^\circ be their respective pure component vapor pressures at TazT_{az}. Assuming the vapor phase behaves ideally, which of the following sets of thermodynamic relations is strictly valid during the reversible, isobaric vaporization of this azeotrope?

7

At 298 K, 37.0 g of 1-chlorobutane (Molar mass = 92.5 g/mol) is mixed with 36.9 g of anhydrous tetrabutylammonium iodide (TBAI, Molar mass = 369 g/mol). The system undergoes an in-situ Finkelstein-type exchange:

\ceC4H9Cl(l)+TBAI(solv)<=>C4H9I(l)+TBACl(solv)\ce{C4H9Cl(l) + TBAI(solv) <=> C4H9I(l) + TBACl(solv)}

The equilibrium constant for this reaction at 298 K is Kc=1.0K_c = 1.0. Unlike the classic Finkelstein reaction, all ammonium salts remain completely dissolved as non-volatile, undissociated ion pairs in the homogeneous liquid phase. Assuming the final liquid mixture of haloalkanes behaves as an ideal solution, what is the total vapor pressure of the system at equilibrium?

(Given at 298 K: P\ceC4H9Cl∘=100P^\circ_{\ce{C4H9Cl}} = 100 Torr, P\ceC4H9I∘=30P^\circ_{\ce{C4H9I}} = 30 Torr)

8

Two volatile liquids, \ce{A} and \ce{B}, form a non-ideal solution exhibiting a positive deviation from Raoult's law. At 300 K300\text{ K}, the vapor pressures of pure \ce{A} and pure \ce{B} are 300 Torr300\text{ Torr} and 100 Torr100\text{ Torr}, respectively. A student incorrectly assumes that the mixture behaves ideally and that the vapor pressures of both pure liquids follow a temperature coefficient Q10=2Q_{10} = 2 (i.e., vapor pressure doubles for every 10 K10\text{ K} rise in temperature). Experimentally, the mixture forms a minimum-boiling azeotrope at 330 K330\text{ K} with a liquid mole fraction of \ce{A}, xA=0.5x_A = 0.5. Calculate the magnitude of the difference between the true mole fraction of \ce{A} in the vapor phase (yA,truey_{A, \text{true}}) at the azeotropic point and the vapor mole fraction of \ce{A} (yA,calcy_{A, \text{calc}}) calculated by the student at 330 K330\text{ K} for the same liquid composition.

9

Two volatile liquids, \ce{A} and \ce{B}, form a minimum boiling azeotrope at Taz=324 KT_{az} = 324 \text{ K} and 1 atm1 \text{ atm}. The azeotropic mixture has a mole fraction of \ce{A}, xA=0.6x_A = 0.6. The pure liquids \ce{A} and \ce{B} have boiling points TA=340 KT_A = 340 \text{ K} and TB=390 KT_B = 390 \text{ K} at 1 atm1 \text{ atm}, respectively. The enthalpies of vaporization of pure \ce{A} and pure \ce{B} are 30.6 kJ mol−130.6 \text{ kJ mol}^{-1} and 35.1 kJ mol−135.1 \text{ kJ mol}^{-1}, respectively, and can be assumed to be independent of temperature. The enthalpy of mixing to form 1 mole1 \text{ mole} of the liquid azeotrope from pure liquids \ce{A} and \ce{B} at 324 K324 \text{ K} is ΔHmix=+1.62 kJ mol−1\Delta H_{\text{mix}} = +1.62 \text{ kJ mol}^{-1}. Assuming the vapor phase behaves as an ideal gas mixture, what is the entropy of vaporization (ΔSvap\Delta S_{\text{vap}}) of 1 mole1 \text{ mole} of the azeotropic mixture at its boiling point?

10

An equimolar gaseous mixture of four halomethanes, \ce{CH3F}, \ce{CH3Cl}, \ce{CH3Br}, and \ce{CH3I}, is equilibrated with a minimum-boiling azeotropic mixture of ethanol and water at 320 K320\text{ K} and 1 atm1\text{ atm}. Let KH(F)K_{H(F)}, KH(Cl)K_{H(Cl)}, KH(Br)K_{H(Br)}, and KH(I)K_{H(I)} be their respective Henry's Law constants in this solvent system. Given that the dipole moments (μ\mu) of the halomethanes follow the order \ce{CH3Cl} > \ce{CH3F} > \ce{CH3Br} > \ce{CH3I}, which of the following correctly identifies the order of their Henry's Law constants and the dominant physical factor dictating this trend?

11

An open reactive distillation apparatus is charged with an equimolar liquid mixture of 2,2-dimethylpropanoic acid, 2-methylpropan-2-ol, and 1-butoxybutane. The mixture is heated to 80∘C80^\circ\text{C} in the presence of a catalytic amount of concentrated \ce{H2SO4}. Let restr_{est} be the rate of esterification, rdehydr_{dehyd} be the rate of alcohol dehydration, and rcleavr_{cleav} be the rate of ether cleavage. It is observed that the liquid-vapor equilibrium composition alters significantly over time due to the rapid evolution of a gas G\textbf{G}, violating the assumption of a static azeotrope. Which of the following represents the correct order of initial reaction rates and the identity of G\textbf{G}?

12

An aqueous solution is prepared by dissolving 0.08 mol0.08\text{ mol} of \ceKMnO4\ce{KMnO4} and 0.03 mol0.03\text{ mol} of \ceNa2S2O3\ce{Na2S2O3} in 1 kg1\text{ kg} of pure water. The solution is allowed to react completely at 298 K298\text{ K} in a neutral medium. After the reaction is complete, the solid precipitate formed is filtered off. Assuming complete dissociation of all soluble electrolytes and neglecting any change in the mass of water, what is the depression in freezing point (ΔTf\Delta T_f) of the resulting filtrate?

(Given: KfK_f of water = 1.86 K kg mol−11.86\text{ K kg mol}^{-1})

13

A concentration cell is constructed at 298 K as follows:

\ceAg(s)∣AgCl(s)∣NaCl(aq,m1)∣∣NaCl(aq,m2),Na2SO4(aq,m3)∣AgCl(s)∣Ag(s)\ce{Ag(s) | AgCl(s) | NaCl(aq, m_1) || NaCl(aq, m_2), Na2SO4(aq, m_3) | AgCl(s) | Ag(s)}

The two half-cell solutions are separated by a salt bridge. It is given that the two solutions are perfectly isotonic. Assume ideal van't Hoff factors for osmotic pressure (i\ceNaCl=2i_{\ce{NaCl}} = 2, i\ceNa2SO4=3i_{\ce{Na2SO4}} = 3) and that the Debye-Hückel limiting law is valid for calculating the activity coefficients of individual ions.

If m3>0m_3 > 0, which of the following statements correctly describes the cell potential (EcellE_{\text{cell}}) and the relationship between the single-ion activity coefficients of chloride (γ\ceCl−,1\gamma_{\ce{Cl^-}, 1} and γ\ceCl−,2\gamma_{\ce{Cl^-}, 2}) in the two half-cells?

14

Two aqueous solutions are prepared at 298 K298 \text{ K} using 1.0 kg1.0 \text{ kg} of water each:

Solution A: 0.10 mol0.10 \text{ mol} \ce{HCl} Solution B: 0.10 mol0.10 \text{ mol} \ce{HCl} and 1.80 mol1.80 \text{ mol} Sucrose (\ce{C12H22O11})

The solutions are placed in separate open beakers inside a sealed desiccator and allowed to reach thermodynamic equilibrium via isothermal solvent vapor transfer. Assume ideal behavior for all solutes (γ=1\gamma = 1) and complete dissociation of \ce{HCl}.

After equilibrium is established, the two solutions are used to construct the following concentration cell with a liquid junction:

Pt(s)∣\ceH2(g,1 bar)∣Solution Beq⋮Solution Aeq∣\ceH2(g,1 bar)∣Pt(s)Pt(s) | \ce{H2}(g, 1 \text{ bar}) | \text{Solution B}_{eq} \vdots \text{Solution A}_{eq} | \ce{H2}(g, 1 \text{ bar}) | Pt(s)

Given the transport number of \ce{Cl^-} is t−=0.20t_- = 0.20 (assume constant across the junction) and 2.303RTF=0.060 V\frac{2.303 RT}{F} = 0.060 \text{ V} at 298 K298 \text{ K}. What is the measured electromotive force (EcellE_{cell}) of this cell?

15

An aqueous solution of \ce{K4[Fe(CN)6]} has a molality of 0.40 mol kg−10.40 \text{ mol kg}^{-1}. To purify the water via reverse osmosis at 300 K300 \text{ K}, a minimum applied pressure of 39.28 bar39.28 \text{ bar} is required to overcome the osmotic pressure. Assume the solution follows the exact thermodynamic relation for real solutions: Π=−RTVmln⁡(xsolvent)\Pi = -\frac{RT}{V_m} \ln(x_{\text{solvent}}), where VmV_m is the molar volume of pure water (0.018 L mol−10.018 \text{ L mol}^{-1}). Given: R=0.083 L bar K−1 mol−1R = 0.083 \text{ L bar K}^{-1} \text{ mol}^{-1}, e−0.0284=0.9720e^{-0.0284} = 0.9720, and moles of water in 1 kg=55.55 mol1 \text{ kg} = 55.55 \text{ mol}. Calculate the percentage degree of dissociation (α\alpha) of the complex in this solution.

16

A volatile gas \ce{G} is dissolved in water at 298 K298\text{ K} under a constant partial pressure PG=760 TorrP_G = 760\text{ Torr}. The ideal Henry's law constant for \ce{G} in pure water is KH∘=7.6×105 TorrK_H^\circ = 7.6 \times 10^5\text{ Torr}. To this solution, a non-volatile, fully dissociating strong electrolyte \ce{Ca(NO3)2} is added such that its molality is 2.0576 mol kg−12.0576\text{ mol kg}^{-1}. Due to the 'salting-out' effect, the chemical potential of the solvent decreases, which increases the activity coefficient (γG\gamma_G) of the dissolved gas. The apparent Henry's law constant becomes KH=KH∘⋅γGK_H = K_H^\circ \cdot \gamma_G. If γG\gamma_G is thermodynamically linked to the vapor pressure lowering of the solvent such that γG=P\ceH2O∘P\ceH2O\gamma_G = \frac{P^\circ_{\ce{H2O}}}{P_{\ce{H2O}}}, calculate the new equilibrium mole fraction of gas \ce{G} (xG′x_G') in the solution. (Assume the amount of dissolved gas is negligible compared to the solvent and \ce{Ca(NO3)2}, and the molar mass of water is 18 g mol−118\text{ g mol}^{-1}).

17

A multimeric globular protein (Mw=2.56×105 g/molM_w = 2.56 \times 10^5 \text{ g/mol}) consists of 8 identical non-covalently linked subunits. At low concentrations, it exists entirely in its native folded octameric state. However, when 256 g256 \text{ g} of this protein is dissolved in 900 g900 \text{ g} of water at 298 K298 \text{ K}, the high concentration induces complete denaturation. The protein fully dissociates into its 8 unfolded monomeric peptide chains. Furthermore, due to the exposure of previously buried hydrophobic and hydrophilic residues, each unfolded monomeric chain strongly binds 250250 molecules of water in its primary hydration shell, effectively removing them from the bulk solvent (these bound water molecules do not contribute to the vapor pressure). Given that the vapor pressure of pure water at 298 K298 \text{ K} is 24.00 Torr24.00 \text{ Torr}, calculate the vapor pressure lowering (ΔP\Delta P) of this solution. (Assume the unfolded chains act as ideal independent kinetic particles and the molar mass of water is 18.0 g/mol18.0 \text{ g/mol}).

18

A 34.2 g34.2 \text{ g} sample of sucrose (\ceC12H22O11\ce{C12H22O11}) is dissolved in 100.0 g100.0 \text{ g} of water. A trace amount of an acid catalyst is added, and the solution is heated until the inversion of sucrose is complete. The resulting monosaccharides undergo mutarotation and reach their respective anomeric equilibria. For D-glucose, the equilibrium mixture contains 36%36\% α\alpha-anomer and 64%64\% β\beta-anomer. For D-fructose, the equilibrium mixture contains 70%70\% β\beta-pyranose, 20%20\% β\beta-furanose, and 10%10\% α\alpha-furanose. Assuming the trace acid contributes negligibly to the molality, what is the boiling point elevation (ΔTb\Delta T_b) of the final solution? (KbK_b for water = 0.52 K kg mol−10.52 \text{ K kg mol}^{-1}, Molar mass of sucrose = 342 g mol−1342 \text{ g mol}^{-1}, Molar mass of water = 18 g mol−118 \text{ g mol}^{-1})

19

An organic base \ce{B} (molar mass = 100 g mol−1100 \text{ g mol}^{-1}) is studied in two different solvents to understand its solvation thermodynamics.

Experiment 1: 10.0 g10.0 \text{ g} of \ce{B} is dissolved in 100 g100 \text{ g} of benzene (Kb=2.53 K kg mol−1K_b = 2.53 \text{ K kg mol}^{-1}). The boiling point of the solution is elevated by 1.518 K1.518 \text{ K}. In benzene, \ce{B} undergoes partial dimerization due to intermolecular hydrogen bonding.

Experiment 2: 10.0 g10.0 \text{ g} of \ce{B} is dissolved in 100 g100 \text{ g} of water (Kb=0.52 K kg mol−1K_b = 0.52 \text{ K kg mol}^{-1}). The boiling point elevation is observed to be 0.5252 K0.5252 \text{ K}. In water, \ce{B} acts as a weak monobasic amine.

Experiment 3: 0.05 mol0.05 \text{ mol} of anhydrous \ce{HCl} gas is dissolved in the aqueous solution from Experiment 2 (assume no change in the mass of the solvent and no volume change).

Assuming the molarity of the aqueous solution is approximately equal to its molality, calculate the dimerization equilibrium constant (KdK_d) of \ce{B} in benzene, the base ionization constant (KbK_b) in water, and the new boiling point elevation (ΔTb′\Delta T_b') of the solution in Experiment 3.

20

A 2.665 g2.665 \text{ g} sample of a mixture containing two hydrate isomers of \ceCrCl3⋅6H2O\ce{CrCl3 \cdot 6H2O}, Isomer X (pale green) and Isomer Y (dark green), is dissolved in 100 g100 \text{ g} of water at 298 K298 \text{ K}. The boiling point of this solution is found to be 100.1456∘C100.1456^\circ\text{C} at 1 atm1 \text{ atm}. If the entire solution is treated with excess \ceAgNO3(aq)\ce{AgNO3(aq)}, what mass of \ceAgCl(s)\ce{AgCl(s)} will precipitate?

(Assume the boiling point of pure water is 100.000∘C100.000^\circ\text{C} at 1 atm1 \text{ atm}, 100%100\% ionization of the complex salts, ideal behavior, and no aquation of the inner coordination sphere. Given: Kb(\ceH2O)=0.52 K kg mol−1K_b(\ce{H2O}) = 0.52 \text{ K kg mol}^{-1}, Molar mass of \ceCrCl3⋅6H2O=266.5 g mol−1\ce{CrCl3 \cdot 6H2O} = 266.5 \text{ g mol}^{-1}, Molar mass of \ceAgCl=143.5 g mol−1\ce{AgCl} = 143.5 \text{ g mol}^{-1})

21

When 2.44 g2.44 \text{ g} of benzoic acid (\ceC6H5COOH\ce{C6H5COOH}) is dissolved in 100 g100 \text{ g} of benzene (\ceC6H6\ce{C6H6}), the freezing point of the solution is depressed by 0.6144 K0.6144 \text{ K}. Assuming benzoic acid undergoes dimerization in benzene, calculate the equilibrium constant KmK_m (in kg mol−1\text{kg mol}^{-1}) for the dimerization process.

(Given: KfK_f for benzene =5.12 K kg mol−1= 5.12 \text{ K kg mol}^{-1}, Molar mass of benzoic acid =122 g mol−1= 122 \text{ g mol}^{-1})

22

An alkene XX (\ce{3-methylbut-1-ene}) is subjected to hydroboration-oxidation using \ce{B2H6}/THF followed by alkaline \ce{H2O2} to yield a major organic product YY. Exactly 7.0 g7.0\text{ g} of XX is completely converted to YY, and the entire yield of YY is dissolved in 250 g250\text{ g} of benzene. The freezing point of the resulting solution is depressed by 1.6384 K1.6384\text{ K}. Assuming YY undergoes partial dimerization in benzene due to intermolecular hydrogen bonding, identify the IUPAC name of YY and its percentage of dimerization. (Given: KfK_f for benzene = 5.12 K kg mol−15.12\text{ K kg mol}^{-1}, atomic masses: C=12, H=1, O=16)

23

A 33.3 g33.3 \text{ g} sample of a non-reducing tetrasaccharide (\ceC24H42O21\ce{C24H42O21}, molar mass = 666 g mol−1666 \text{ g mol}^{-1}) is dissolved in 100.0 g100.0 \text{ g} of water. The solution is subjected to complete hydrolysis using a catalytic amount of an insoluble solid acid resin, which is subsequently filtered off. The solution is then allowed to stand at 298 K298 \text{ K} until mutarotation equilibrium is reached.

The specific rotation of pure α\alpha-D-glucose is +112∘+112^\circ and pure β\beta-D-glucose is +19∘+19^\circ. The final equilibrium mixture exhibits a specific rotation of +52.6∘+52.6^\circ.

Assuming ideal behavior, what is the freezing point depression (ΔTf\Delta T_f) of the final equilibrium solution?

(Given: KfK_f of water = 1.86 K kg mol−11.86 \text{ K kg mol}^{-1}, Molar mass of water = 18 g mol−118 \text{ g mol}^{-1})

24

Pentaamminechloridocobalt(III) chloride, \ce{[Co(NH3)5Cl]Cl2}, undergoes a pseudo-first-order aquation reaction in water to form pentaammineaquacobalt(III) chloride, \ce{[Co(NH3)5(H2O)]Cl3}. A solution is prepared by dissolving 0.10 mol0.10 \text{ mol} of \ce{[Co(NH3)5Cl]Cl2} and 0.05 mol0.05 \text{ mol} of \ce{NaCl} in 1.0 kg1.0 \text{ kg} of water at 298 K298 \text{ K}. The half-life of the aquation reaction at this temperature is 69.3 min69.3 \text{ min}. Assuming ideal behavior and complete ionization of all ionic species, what is the theoretical freezing point of the solution corresponding to its composition after 138.6 min138.6 \text{ min}? (Given: KfK_f for water is 1.86 K kg mol−11.86 \text{ K kg mol}^{-1})

25

A biochemist is investigating the osmotic pressure (π\pi) of a tetrameric protein solution at 300 K300\text{ K}. In its native folded state, the protein behaves as an ideal solute with a molar mass Mnative=1.0×105 g mol−1M_{native} = 1.0 \times 10^5\text{ g mol}^{-1}. Upon the addition of a chemical denaturant, the protein completely dissociates into four identical unfolded monomeric chains. The osmotic pressure is measured against a dialysate containing the exact same concentration of denaturant, ensuring only the protein contributes to the measured π\pi.

Due to the massive increase in the hydrodynamic radius and excluded volume upon unfolding, the denatured monomers exhibit non-ideal behavior. The osmotic pressure of such macromolecular solutions follows the virial expansion: πC=RT(1M+BC)\frac{\pi}{C} = RT \left( \frac{1}{M} + BC \right) where CC is the protein concentration in g L−1\text{g L}^{-1}, MM is the molar mass of the kinetic solute particle, and BB is the second virial coefficient. For the denatured state, B=3.6×10−5 L mol g−2B = 3.6 \times 10^{-5}\text{ L mol g}^{-2}.

Calculate the ratio of the osmotic pressure of the denatured state to the native state (πdenπnat\frac{\pi_{den}}{\pi_{nat}}) at a protein concentration of C=10 g L−1C = 10\text{ g L}^{-1}.

26

An aqueous solution contains 0.10 M0.10\text{ M} of a weak monoacidic base BB (pKb=4.52pK_b = 4.52). The pH of this solution is adjusted by adding a negligible volume of concentrated \ce{H2SO4}. At what pH will this solution become isotonic with a 0.1375 M0.1375\text{ M} aqueous solution of glucose at 298 K298\text{ K}?

(Assume \ce{H2SO4} dissociates completely into \ce{2H+} and \ce{SO4^{2-}}, and the solutions behave ideally. Given: log⁡2=0.30\log 2 = 0.30, log⁡3=0.48\log 3 = 0.48)

27

An aqueous solution of the trisaccharide raffinose (\ceC18H32O16\ce{C18H32O16}) is placed in an osmotic cell at 300 K300\text{ K}. In the presence of a dilute acid catalyst, raffinose undergoes a pseudo-first order hydrolysis to yield equimolar amounts of D-glucose, D-fructose, and D-galactose. The initial osmotic pressure of the solution, due solely to raffinose, is 1.50 atm1.50\text{ atm}. If the pseudo-first order rate constant for the hydrolysis is k=2.0×10−3 s−1k = 2.0 \times 10^{-3}\text{ s}^{-1}, what is the initial rate of change of the osmotic pressure, (dπdt)t=0\left( \frac{d\pi}{dt} \right)_{t=0}, of the solution? (Assume ideal behavior and that the volume of the solution remains constant).

28

Consider the following concentration cell operating at 298 K298\text{ K}:

\ceAg(s,P1)∣Ag+(aq,0.1M,P1)∣∣Ag+(aq,0.01M,P2)∣Ag(s,P2)\ce{Ag(s, P_1) | Ag+(aq, 0.1 M, P_1) || Ag+(aq, 0.01 M, P_2) | Ag(s, P_2)}

The left compartment is maintained at a standard pressure P1=1 barP_1 = 1\text{ bar}. To completely halt the flow of electrons (i.e., Ecell=0E_{\text{cell}} = 0), a specific hydrostatic pressure P2P_2 is applied to the right compartment.

Given: RTln⁡10=5700 J mol−1RT \ln 10 = 5700\text{ J mol}^{-1} Partial molar volume of \ceAg+(aq)\ce{Ag+(aq)}, Vˉ\ceAg+=67 cm3 mol−1\bar{V}_{\ce{Ag+}} = 67\text{ cm}^3\text{ mol}^{-1} Molar volume of \ceAg(s)\ce{Ag(s)}, V\ceAg=10 cm3 mol−1V_{\ce{Ag}} = 10\text{ cm}^3\text{ mol}^{-1} 1 bar=105 Pa1\text{ bar} = 10^5\text{ Pa}

Assuming the liquids and solids are incompressible, what is the required pressure P2P_2?

29

Compartments A and B of equal volume are separated by a specialized chiral semipermeable membrane. Initially, Compartment A contains a 0.15 M0.15\text{ M} aqueous solution of fully dissociated racemic 1-phenylethylammonium chloride, denoted as (±)−M+Cl−(\pm)-M^+Cl^-. Compartment B initially contains pure water. The chiral membrane is perfectly permeable to water, the (S)−M+(S)-M^+ enantiomer, and Cl−Cl^- ions, but is completely impermeable to the (R)−M+(R)-M^+ enantiomer due to stereospecific binding interactions. The system is allowed to reach thermodynamic equilibrium at 300 K300\text{ K}, with external pressure applied to maintain constant and equal volumes in both compartments. What is the osmotic pressure difference (Δπ=πA−πB\Delta \pi = \pi_A - \pi_B) required to maintain this equilibrium? (Given: R=0.082 L atm K−1 mol−1R = 0.082\text{ L atm K}^{-1}\text{ mol}^{-1})

30

A 0.10 M0.10 \text{ M} aqueous solution of a neutral α\alpha-amino acid (with pKa1=2.00pK_{a1} = 2.00 and pKa2=9.00pK_{a2} = 9.00) is prepared at 300 K300 \text{ K}. The osmotic pressure of this initial solution is 2.46 atm2.46 \text{ atm}, indicating ideal behavior and that the amino acid exists almost entirely as a single-particle zwitterion.

To 1.0 L1.0 \text{ L} of this solution, a small volume of highly concentrated aqueous \ce{HCl} is added to adjust the pH exactly to 2.002.00. Assuming the volume of the solution remains unchanged at 1.0 L1.0 \text{ L}, what is the new osmotic pressure of the solution at 300 K300 \text{ K}?

(Given: R=0.082 L atm K−1mol−1R = 0.082 \text{ L atm K}^{-1} \text{mol}^{-1}, assume all species behave ideally)

31

A 3d transition metal MM is unique in its series for possessing a positive standard reduction potential (EM2+/M∘>0E^\circ_{M^{2+}/M} > 0). An aqueous solution is prepared by dissolving 0.1 mol0.1\text{ mol} of its chloride salt, \ce{MCl2}, in 1 kg1\text{ kg} of water. To this solution, 0.5 mol0.5\text{ mol} of \ce{KCN} is added, resulting in the evolution of a toxic gas that escapes completely, and the formation of a stable, tetrahedral mononuclear complex of MM. Assuming 100% dissociation of all soluble salts and ideal behavior, what is the depression in freezing point (ΔTf\Delta T_f) of the final solution? (KfK_f of water = 1.86 K kg mol−11.86\text{ K kg mol}^{-1})

32

A 1.0 kg1.0\text{ kg} aqueous solution contains a total of 0.10 moles0.10\text{ moles} of a mixture of two octahedral \ce{Co(III)} ammine complexes: a yellow complex PP and a green complex QQ. Both complexes are synthesized exclusively from anhydrous \ce{CoCl3} and \ce{NH3}. The boiling point of this solution is 100.1352∘C100.1352^\circ\text{C} at 1 atm1\text{ atm}.

When excess \ce{AgNO3(aq)} is added to this solution, WW grams of \ce{AgCl(s)} precipitate is formed. Assuming 100%100\% ionization of the complexes and ideal behavior, what is the value of WW?

(Given: KbK_b for water = 0.52 K kg mol−10.52\text{ K kg mol}^{-1}, Molar mass of \ce{AgCl} = 143.5 g mol−1143.5\text{ g mol}^{-1}, Boiling point of pure water = 100.0000∘C100.0000^\circ\text{C})

33

An amount WW of Mohr's salt, \ce(NH4)2Fe(SO4)2⋅6H2O\ce{(NH4)2Fe(SO4)2 \cdot 6H2O}, is dissolved in 94.6 g94.6\text{ g} of water at 298 K298\text{ K}. The resulting solution exhibits a boiling point elevation of 1.30 K1.30\text{ K}. Assuming complete dissociation of the double salt into its constituent ions, what is the value of WW?

(Given: KbK_b for water =0.52 K kg mol−1= 0.52\text{ K kg mol}^{-1}, Molar mass of Mohr's salt =392 g mol−1= 392\text{ g mol}^{-1})

34

An unknown aromatic amine XX (molecular formula \ce{C7H9N}) is dissolved in water to form a 0.10 M0.10 \text{ M} solution at 300 K300 \text{ K}. The osmotic pressure of this solution is measured to be 2.46 atm2.46 \text{ atm} (Use R=0.082 L atm K−1mol−1R = 0.082 \text{ L atm K}^{-1} \text{mol}^{-1}). When XX is treated with \ce{NaNO2 / HCl} at 0−5∘C0-5^\circ\text{C} followed by alkaline β\beta-naphthol, an intense orange-red dye is formed.

A student incorrectly assumes that the nitrogen lone pair in XX is fully localized (ignoring its resonance with the aromatic ring) and assigns it a hypothetical base dissociation constant Kb=1900K_b = \frac{1}{900}.

Based on this flawed assumption, what is the student's calculated osmotic pressure (πcalc\pi_{\text{calc}}), and what is the true identity of XX?

35

A 2.665 g2.665 \text{ g} sample of a hydrate isomer of \ceCrCl3⋅6H2O\ce{CrCl3 \cdot 6H2O} (Molar mass = 266.5 g mol−1266.5 \text{ g mol}^{-1}) is dissolved in water and passed through a cation-exchange resin in the \ceH+\ce{H+} form. The effluent requires 20.0 mL20.0 \text{ mL} of 1.0 M NaOH1.0 \text{ M NaOH} for complete neutralization. A separate 0.10 m0.10 \text{ m} aqueous solution of this specific isomer exhibits a degree of dissociation α=0.85\alpha = 0.85. Assuming no hydrolysis of the complex cation, what is the freezing point of this 0.10 m0.10 \text{ m} solution? (Given: KfK_f for water = 1.86 K kg mol−11.86 \text{ K kg mol}^{-1})

36

A redox reaction between \ceKMnO4\ce{KMnO4} and a weak acid reductant \ceHA\ce{HA} (Ka=2.0×10−5K_a = 2.0 \times 10^{-5}) proceeds in an acidic medium containing \ceHCl\ce{HCl}. The proposed mechanism involves the formation of a transient \ceMn(VI)\ce{Mn(VI)} intermediate:

Step 1: \ceMnO4−+HA−>[k1]MnO42−+HA∙+\ce{MnO4- + HA ->[k_1] MnO4^{2-} + HA^{\bullet+}} (slow) Step 2: \ceMnO42−+H+−>[k2]Mn3++Products\ce{MnO4^{2-} + H+ ->[k_2] Mn^{3+} + \text{Products}} (fast)

An electrochemical half-cell is prepared at 298 K298 \text{ K} containing 0.05 M \ceKMnO40.05 \text{ M } \ce{KMnO4}, 0.05 M \ceMn2+0.05 \text{ M } \ce{Mn^{2+}}, 0.1 M \ceHA0.1 \text{ M } \ce{HA}, and 1.0×10−3 M \ceHCl1.0 \times 10^{-3} \text{ M } \ce{HCl}.

Given: k1=4.0×10−2 M−1s−1k_1 = 4.0 \times 10^{-2} \text{ M}^{-1}\text{s}^{-1} k2=1.0×103 M−1s−1k_2 = 1.0 \times 10^3 \text{ M}^{-1}\text{s}^{-1} E\ceMnO4−/Mn2+∘=1.51 VE^\circ_{\ce{MnO4- / Mn^{2+}}} = 1.51 \text{ V} 2.303RTF=0.06 V\frac{2.303 RT}{F} = 0.06 \text{ V}, log⁡2=0.30\log 2 = 0.30.

Assuming the system is at a steady state for \ceMnO42−\ce{MnO4^{2-}} and the weak acid equilibrium is established instantaneously, determine the steady-state concentration of \ceMnO42−\ce{MnO4^{2-}} and the instantaneous reduction potential (EredE_{red}) of the \ceMnO4−/Mn2+\ce{MnO4- / Mn^{2+}} couple.

37

A gaseous reactant \ce{A} is continuously bubbled through an aqueous solution containing 0.20 M0.20 \text{ M} of reactant \ce{B} at 298 K298 \text{ K}. The partial pressure of \ce{A(g)} above the solution is maintained constant at 0.60 bar0.60 \text{ bar}. The Henry's law constant for \ce{A} in water at 298 K298 \text{ K} is given as KH=12.0 bar L mol−1K_H = 12.0 \text{ bar L mol}^{-1}.

The overall reaction is: \ce2A(aq)+3B(aq)−>A2B3(aq)\ce{2A(aq) + 3B(aq) -> A2B3(aq)}

The proposed mechanism for this reaction is: Step 1: \ce{2A(aq) <=> A2(aq)} \quad (Fast equilibrium, Kc=4.0 L mol−1K_c = 4.0 \text{ L mol}^{-1}) Step 2: \ce{A2(aq) + B(aq) -> A2B(aq)} \quad (Slow, k1=2.5×10−2 L mol−1 s−1k_1 = 2.5 \times 10^{-2} \text{ L mol}^{-1} \text{ s}^{-1}) Step 3: \ce{A2B(aq) + 2B(aq) -> A2B3(aq)} \quad (Fast)

Assuming ideal behavior, what is the initial rate of disappearance of \ce{B}?

38

An advanced electrochemical cell is designed to study the thermodynamics of 'bubble-free' water electrolysis at 298 K298\text{ K}. Two inert platinum electrodes are immersed in an aqueous buffer solution of pH=2.0pH = 2.0.

During steady-state electrolysis, the products exist entirely as dissolved gases before any bubbles can form. The local concentration of dissolved hydrogen at the cathode is maintained at 1.0×10−4 M1.0 \times 10^{-4}\text{ M}, and dissolved oxygen at the anode is 1.0×10−5 M1.0 \times 10^{-5}\text{ M}.

The Henry's Law constants for the gases in water at 298 K298\text{ K} are KH(\ceH2)=1.0×10−3 M bar−1K_H(\ce{H2}) = 1.0 \times 10^{-3}\text{ M bar}^{-1} and KH(\ceO2)=1.0×10−3 M bar−1K_H(\ce{O2}) = 1.0 \times 10^{-3}\text{ M bar}^{-1}.

Given the standard electrode potential E\ceO2(g)/H2O∘=1.23 VE^\circ_{\ce{O2(g)/H2O}} = 1.23\text{ V} and 2.303RTF=0.06 V\frac{2.303 RT}{F} = 0.06\text{ V}.

Calculate the minimum theoretical applied voltage (VminV_{min}) required to sustain this electrolysis.

39

A closed vessel of total volume 2.0 L2.0\text{ L} contains 1.0 L1.0\text{ L} of an aqueous solution of a reactive substrate \ce{S} at an initial concentration of 10.0 M10.0\text{ M}. The remaining 1.0 L1.0\text{ L} is filled with a reactive gas \ce{G} at an initial partial pressure of 2.0 atm2.0\text{ atm}. The gas \ce{G} dissolves in the aqueous phase and reacts with \ce{S} according to the elementary bimolecular reaction: \ceG(aq)+S(aq)−>Products\ce{G(aq) + S(aq) -> Products} Given:

  • Rate constant k=0.1 L mol−1 min−1k = 0.1\text{ L mol}^{-1}\text{ min}^{-1}.
  • Henry's law constant for \ce{G} in water is KH=5.55×103 atmK_H = 5.55 \times 10^3\text{ atm} (defined as PG=KHχGP_G = K_H \chi_G, where χG\chi_G is the mole fraction of \ce{G} in the solution).
  • The dissolution of \ce{G} is rapid and maintains phase equilibrium at all times.
  • The temperature is constant, and RT=25 L atm mol−1RT = 25\text{ L atm mol}^{-1}.
  • The concentration of water is 55.5 M55.5\text{ M} and remains constant.
  • The volume of the solution remains exactly 1.0 L1.0\text{ L}.

Calculate the time required for the partial pressure of gas \ce{G} in the vessel to drop to 0.25 atm0.25\text{ atm}. (Assume the concentration of \ce{S} remains effectively constant).

40

At 298 K298\text{ K}, the vapor pressure of pure liquid A is 150 Torr150\text{ Torr} and that of pure liquid B is 400 Torr400\text{ Torr}. When a small amount of B is dissolved in A to form a dilute solution, the solvent A follows Raoult's Law, whereas the volatile solute B follows Henry's Law with a Henry's Law constant KH=1900 TorrK_H = 1900\text{ Torr}. If the vapor phase in equilibrium with the solution contains B at a mole fraction of 0.40.4, what is the total vapor pressure of the system?

41

A saturated aqueous solution of cerium(III) sulfate, \ce{Ce2(SO4)3}, is prepared at 320 K320 \text{ K} in 1 kg1 \text{ kg} of water. The excess un-dissolved solid is rapidly filtered off at 320 K320 \text{ K}. The filtrate is then cooled to determine its freezing point. Assuming ideal behavior and complete dissociation of the salt, what is the freezing point depression (ΔTf\Delta T_f) of this filtrate?

Given: Solubility of \ce{Ce2(SO4)3} at 300 K=2.0×10−2 mol kg−1300 \text{ K} = 2.0 \times 10^{-2} \text{ mol kg}^{-1} ΔHsol∘=−138.28 kJ mol−1\Delta H^\circ_{\text{sol}} = -138.28 \text{ kJ mol}^{-1} (assume independent of temperature) Kf for water=1.86 K kg mol−1K_f \text{ for water} = 1.86 \text{ K kg mol}^{-1} R=8.314 J K−1mol−1R = 8.314 \text{ J K}^{-1} \text{mol}^{-1} ln⁡2=0.693\ln 2 = 0.693

42

Solid \ce{Ni(OH)2} is added to an aqueous solution containing 0.31 M0.31\text{ M} of the bidentate ligand ethylenediamine (en) at 298 K298\text{ K}. The system reaches equilibrium. Given the solubility product of \ce{Ni(OH)2} is Ksp=4.0×10−15K_{sp} = 4.0 \times 10^{-15} and the overall formation constant of the complex \ce{[Ni(en)3]^{2+}} is β3=1.0×1018\beta_3 = 1.0 \times 10^{18}, calculate the solubility of \ce{Ni(OH)2} in this solution. (Assume no volume change upon addition of solid and ignore the basicity of ethylenediamine).

43

An α\alpha-amino acid has pKa1=2.0pK_{a1} = 2.0 and pKa2=9.0pK_{a2} = 9.0. The intrinsic solubility of its zwitterionic form (HA±HA^\pm) in pure water at 300 K300\text{ K} is S0=0.05 MS_0 = 0.05\text{ M}. An excess of the solid amino acid is added to water, and the solution is titrated with concentrated \ceHNO3\ce{HNO3} until the equilibrium pH of the solution reaches 2.02.0. Assuming the volume change upon adding \ceHNO3\ce{HNO3} is negligible, what is the osmotic pressure of the resulting saturated solution at 300 K300\text{ K}? (Given: R=0.082 L atm K−1 mol−1R = 0.082\text{ L atm K}^{-1}\text{ mol}^{-1})

44

Solid \ceA\ce{A} (Molar mass = 150 g mol−1150 \text{ g mol}^{-1}) is added in excess to a solvent at 298 K298 \text{ K}. The saturation solubility of \ceA\ce{A} in this solvent is 3.0 g L−13.0 \text{ g L}^{-1}. To this saturated solution, reactant \ceB\ce{B} is added such that its initial concentration is 0.50 mol dm−30.50 \text{ mol dm}^{-3}. The overall reaction is: \ce3A(aq)+2B(aq)−>P(aq)\ce{3A(aq) + 2B(aq) -> P(aq)} The proposed mechanism for this reaction is: Step 1: \ce2A(aq)+B(aq)−>[k1]I(aq)\ce{2A(aq) + B(aq) ->[k_1] I(aq)} (Slow) Step 2: \ceI(aq)+A(aq)+B(aq)−>[k2]P(aq)\ce{I(aq) + A(aq) + B(aq) ->[k_2] P(aq)} (Fast) Given the rate constant for the slow step is k1=4.0×10−2 dm6 mol−2 s−1k_1 = 4.0 \times 10^{-2} \text{ dm}^6 \text{ mol}^{-2} \text{ s}^{-1}, what is the initial rate of disappearance of \ceB(aq)\ce{B(aq)} in mol dm−3 s−1\text{mol dm}^{-3} \text{ s}^{-1}?

45

At 340 K340\text{ K}, 47.4 g47.4\text{ g} of potash alum (\ceKAl(SO4)2⋅12H2O\ce{KAl(SO4)2 \cdot 12H2O}) is completely dissolved in 177.0 g177.0\text{ g} of anhydrous chloral (\ceCCl3CHO\ce{CCl3CHO}). Chloral reacts quantitatively with the released water of crystallization to form chloral hydrate, which acts as the sole liquid solvent. Assuming complete dissociation of the inorganic salt and ideal behavior of the resulting solution, what is the relative lowering of vapor pressure of the system? (Given molar masses in g/mol\text{g/mol}: \ceK=39\ce{K}=39, \ceAl=27\ce{Al}=27, \ceS=32\ce{S}=32, \ceO=16\ce{O}=16, \ceH=1\ce{H}=1, \ceC=12\ce{C}=12, \ceCl=35.5\ce{Cl}=35.5)

46

Due to significant ion-pair formation, a 0.05 M0.05 \text{ M} aqueous solution of the coordination complex pentaamminechloridocobalt(III) chloride exhibits incomplete dissociation at 300 K300 \text{ K}. The solution is placed in a reverse osmosis chamber separated from pure water by a semipermeable membrane. The resistance of this solution, measured in a conductivity cell with a cell constant of 1.2 cm−11.2 \text{ cm}^{-1}, is 200Ω200 \Omega. Given the limiting molar conductivities: λ∞(\ce[Co(NH3)5Cl]2+)=160 S cm2 mol−1\lambda^\infty(\ce{[Co(NH_3)_5Cl]^{2+}}) = 160 \text{ S cm}^2 \text{ mol}^{-1} and λ∞(\ceCl−)=70 S cm2 mol−1\lambda^\infty(\ce{Cl^-}) = 70 \text{ S cm}^2 \text{ mol}^{-1}. Assuming the Arrhenius theory of electrolytic dissociation is valid for the apparent degree of dissociation, what is the minimum external pressure that must be applied to the solution to initiate reverse osmosis? (Use R=0.082 L atm K−1 mol−1R = 0.082 \text{ L atm K}^{-1} \text{ mol}^{-1})

47

In an industrial reverse osmosis (RO) plant, an aqueous solution of a reactive pollutant \ce{A} (bulk concentration Cb=10 mol m−3C_b = 10 \text{ mol m}^{-3}) is processed at 298 K298 \text{ K}. The RO membrane perfectly rejects \ce{A} (R=100%R = 100\%). Due to concentration polarization, a boundary layer exists at the membrane surface with a mass transfer coefficient km=1.0×10−5 m s−1k_m = 1.0 \times 10^{-5} \text{ m s}^{-1}. The steady-state water flux through the membrane is Jw=2.0×10−5 m s−1J_w = 2.0 \times 10^{-5} \text{ m s}^{-1}.

At the membrane surface, \ce{A} undergoes a first-order degradation reaction \ceA−>B\ce{A -> B} with a surface rate constant ks=1.0×10−5 m s−1k_s = 1.0 \times 10^{-5} \text{ m s}^{-1}. This reaction occurs exclusively at the membrane surface.

Assuming steady-state film theory, what is the rate of degradation of \ce{A} per unit membrane area (r′′r'')?

(Note: ee is the base of the natural logarithm)

48

A 40 g L−140 \text{ g L}^{-1} aqueous solution of a monomeric globular peptide (M=5,000 g mol−1M = 5,000 \text{ g mol}^{-1}) is subjected to purification via Reverse Osmosis (RO) at 298 K298 \text{ K}. In its native state, the peptide behaves as an ideal solute. However, under the extreme hydraulic pressure at the RO membrane surface, the peptide undergoes localized denaturation. While the rigid planarity of the peptide bonds (ω≈180∘\omega \approx 180^\circ) is preserved, the unfolding exposes hydrophobic residues, causing the peptide to quantitatively aggregate into stable pentamers. Furthermore, the extended conformation of the denatured chains interacts non-ideally with the solvent, characterized by a second virial coefficient A2=4.9×10−5 L mol g−2A_2 = 4.9 \times 10^{-5} \text{ L mol g}^{-2}. Given RT=25 L atm mol−1RT = 25 \text{ L atm mol}^{-1}, calculate the effective osmotic pressure (π\pi) exerted by the protein at the membrane surface.

49

An aqueous solution is prepared by dissolving WW grams of a weak monobasic acid \ce{HA} (molar mass =120 g mol−1= 120 \text{ g mol}^{-1}) in water to make 500 mL500 \text{ mL} of solution at 298 K298 \text{ K}. This solution is found to be isotonic with a 0.06 M0.06 \text{ M} aqueous solution of glucose at the same temperature. Given the acid dissociation constant KaK_a of \ce{HA} is 2.5×10−32.5 \times 10^{-3} at 298 K298 \text{ K}, determine the value of WW.

50

A globular metalloprotein exists as a tetramer (Mw=60,000 g mol−1M_w = 60,000 \text{ g mol}^{-1}). In its native folded state, the tetramer completely sequesters 44 molecules of a non-electrolyte cofactor and 22 formula units of \ceFe2(SO4)3\ce{Fe2(SO4)3} deep within its hydrophobic core. These sequestered species are tightly bound and do not contribute to the initial osmotic pressure.

An aqueous solution is prepared by dissolving 15.0 g15.0 \text{ g} of this protein in 500 mL500 \text{ mL} of water at 300 K300 \text{ K}. Under severe osmotic stress, the protein completely denatures, dissociating into its 44 monomeric chains and releasing all sequestered species into the aqueous medium. The released \ceFe2(SO4)3\ce{Fe2(SO4)3} undergoes complete ionization.

Assuming the volume remains constant, what is the osmotic pressure of the solution after complete denaturation? (Given: R=0.082 L atm K−1 mol−1R = 0.082 \text{ L atm K}^{-1} \text{ mol}^{-1})

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