a. 2.69 mol ![]() |
||
b. 0.208 mol ![]() |
||
c. 0.387 mol ![]() |
||
d. 0.004 mol ![]() |
a. S2 ![]() |
||
b. S3 ![]() |
||
c. S8 ![]() |
||
d. (S2)3 ![]() |
a. w = 11.7 kJ and ∆U = 11.7 kJ ![]() |
||
b. w = 11.9 kJ and ∆U = 0 ![]() |
||
c. w = 5.85 kJ and ∆U = -5.85 kJ ![]() |
||
d. w = 5.85 kJ and ∆U = 0 ![]() |
a. 5.83 bar ![]() |
||
b. 230 Torr ![]() |
||
c. 5.84 Torr ![]() |
||
d. There is not enough information provided to answer this question. ![]() |
a. 301.0 K ![]() |
||
b. 300.4 K ![]() |
||
c. 295.0 K ![]() |
||
d. None of the above answers is correct. ![]() |
a. 11.9 kg ![]() |
||
b. 119 g ![]() |
||
c. 238 g ![]() |
||
d. 14.6 kg ![]() |
a. 31.3 L ![]() |
||
b. 22.4 L ![]() |
||
c. 3170 L ![]() |
||
d. 0.0821 L ![]() |
a. 0.167 J ![]() |
||
b. 0.167 kJ ![]() |
||
c. 1.67 J ![]() |
||
d. 39.9 cal ![]() |
a. Cp (gas) > Cv (gas); Cp (solid) ≈ Cv (solid); and Cp (gas) >> Cp (solid) ![]() |
||
b. Cv (gas) ≈ Cv (solid) and Cp (liquid) ≈ Cv (liquid) ![]() |
||
c. Cv (gas) > Cv (liquid) > Cv (solid) and Cv > Cp in all phases ![]() |
||
d. Cp approaches a value of 0 as the sample temperature approaches 0 K but increases without bound as the sample temperature is increased. ![]() |
a. The Van der Waals ‘a’ parameter reflects the existence and strength of attractive intermolecular interactions in the gas, and the value of ‘a’ is always ≥0. ![]() |
||
b. The van der Waals ‘b’ parameter is related to the physical sizes of the constituent molecules (or atoms) of the gas. ![]() |
||
c. The magnitude of the ‘a’ parameter for N2(g) is expected to be greater than that for NH3(g). ![]() |
||
d. The magnitude of the ‘b’ parameter for Ar(g) is larger than that for He(g). ![]() |
a. Three solid bodies that are all in thermal equilibrium will have the same temperature. ![]() |
||
b. Gas molecules in motion tend to stay in motion in the absence of applied forces. ![]() |
||
c. Two material bodies that are separately in thermal equilibrium with a third body are in thermal equilibrium with each other. ![]() |
||
d. Molecules can be treated as non-interacting point-masses when contained in gaseous samples at very low pressures and number densities. ![]() |
a. The most probable value of a velocity component is equal to the most probable speed of the molecules in a dilute gas. ![]() |
||
b. The average kinetic energy of the molecules in a gas is independent of the molecular mass. ![]() |
||
c. The ratio of the most probable speed to the mean speed has the same value for all gases at all temperatures. ![]() |
||
d. Derivation of the ideal-gas equation-of-state from the kinetic-molecular theory of gases requires that the gas molecules be treated as non-interacting point masses. ![]() |
a. The molar heat capacities of He(g) and Ne(g) have identical values at T = 500 K. ![]() |
||
b. The average kinetic energy of the atoms in an He(g) sample is the same as the average kinetic energy of the atoms in an Ne(g) sample. ![]() |
||
c. The average speed of the atoms in an He(g) sample is the same as the average speed of the atoms in an Ne(g) sample. ![]() |
||
d. The average speed of the atoms in an He(g) sample is greater than the average speed of the atoms in an Ar(g) sample. ![]() |
a. The energy of a system always increases in any physical or chemical process. ![]() |
||
b. The energy of a system always decreases in any physical or chemical process. ![]() |
||
c. The entropy of a system always increases in any spontaneous process. ![]() |
||
d. The energy of the universe (encompassing system + surroundings) is always conserved in any physical or chemical process. ![]() |
a. 1.56 kJ ![]() |
||
b. 1.40 kJ ![]() |
||
c. -1.56 kJ ![]() |
||
d. 0.62 kJ ![]() |
a. An isothermal process ![]() |
||
b. An isobaric process ![]() |
||
c. A diathermic process ![]() |
||
d. An adiabatic process. ![]() |
a. Process #1; ∆U = 0 ![]() |
||
b. Process #2; ∆U = 0 ![]() |
||
c. Process #2; ∆U > 0 ![]() |
||
d. Process #3; ∆U = 0 ![]() |
a. Endothermic, with |qnet | > |wnet| ![]() |
||
b. Exothermic, with qnet = wnet < 0 ![]() |
||
c. Endothermic, with qnet = -wnet ![]() |
||
d. Adiabatic, with qnet = 0 and wnet < 0 ![]() |
a. ∆U = -10 kJ and ∆S = 0 ![]() |
||
b. ∆U = 10 kJ and ∆S = 0 ![]() |
||
c. ∆U = 0 and ∆S = 10 J/K ![]() |
||
d. There is not enough information to determine the values of ∆U and ∆S. ![]() |
a. The change in the entropy of the system (∆S) ![]() |
||
b. The change in the Gibbs free energy of the system (∆G) ![]() |
||
c. The change in the internal energy of the system (∆U) ![]() |
||
d. The work done and heat exchanged during the process ![]() |
a. 4064 kJ/mol ![]() |
||
b. -895.4 kJ/mol ![]() |
||
c. -890.4 kJ/mol ![]() |
||
d. -885.4 kJ/mol ![]() |
a. ∆U = 0; q > 0; and ∆S = nR ln (Vfinal/Vinitial) ![]() |
||
b. ∆U > 0; q > 0; and ∆S = nR ln (Vfinal/Vinitial) ![]() |
||
c. ∆U = 0; q = 0; and ∆S = nR ln (Vfinal/Vinitial) ![]() |
||
d. ∆U = 0; q = 0; and ∆S = 0 ![]() |
a. w = 1.717 kJ; ∆U = 0; ∆S = 5.76 J/K ![]() |
||
b. w = -1.717 kJ; ∆U = -1.717 kJ; ∆S = 0 ![]() |
||
c. w = 0; ∆U = 1717 J; ∆S = 5.76 J/K ![]() |
||
d. w = -1717 J; ∆U = 0; ∆S = 5.76 J/K ![]() |
a. Pinitial = 292 bar and ∆H > 0 ![]() |
||
b. Pinitial = 292 bar and ∆H = 0 ![]() |
||
c. Pinitial = 225 bar and ∆H = 0 ![]() |
||
d. Pinitial = 292 bar and ∆H < 0 ![]() |
a. < 0 for nearly all gases. ![]() |
||
b. > 0 for nearly all gases. ![]() |
||
c. > 0 only for gases that exhibit ideal-gas P-V-T behavior. ![]() |
||
d. independent of the initial temperature and pressure of the gas undergoing the Joule-Thomson expansion process. ![]() |
a. -2801 kJ/mol ![]() |
||
b. 3455 kJ/mol ![]() |
||
c. 2801 kJ/mol ![]() |
||
d. 0 ![]() |
a. In cyclic thermodynamic processes, it is always true that the net changes in internal energy (∆U), entropy (∆S), and enthalpy (∆H) of a system are zero (i.e., ∆Unet = ∆Snet = ∆Hnet = 0). ![]() |
||
b. The entropy of a system always increases with an increase in temperature under either constant-volume or constant-pressure conditions. ![]() |
||
c. In reversible adiabatic processes, it is always true that ∆S = 0 and ∆U = w (work). ![]() |
||
d. An isothermal expansion of an ideal gas always gives ∆U > 0 and ∆S = 0. ![]() |
a. ηmax = 0.333; maximum net work from engine = 300 J ![]() |
||
b. ηmax = 0.667; maximum net work from engine = 900 J ![]() |
||
c. ηmax = 0.333; maximum net work from engine = 200 J ![]() |
||
d. ηmax = 0.667; maximum net work from engine = 600 J ![]() |
a. -242 kJ/mol ![]() |
||
b. -897 kJ/mol ![]() |
||
c. -185 kJ/mol ![]() |
||
d. 391 kJ/mol ![]() |
a. ∆rUo = -3230.7 kJ and w > 0 ![]() |
||
b. ∆rUo = -3230.7 kJ and w = 0 ![]() |
||
c. ∆rUo = -3228.2 kJ and w = 0 ![]() |
||
d. ∆rUo = -3227.0 kJ and w < 0 ![]() |
a. ∆H = -92.22 kJ; ∆S = -198.76 J/K; ∆G = -32.99 kJ ![]() |
||
b. ∆H = 92.22 kJ; ∆S = 198.76 J/K; ∆G = 32.99 kJ ![]() |
||
c. ∆H = -46.11 kJ; ∆S = -99.38 J/K; ∆G = -16.49 kJ ![]() |
||
d. ∆H = -46.11 kJ; ∆S = -129.8 J/K; ∆G = -7.43 kJ ![]() |
a. An isothermal expansion, an adiabatic expansion, an isothermal compression, and an adiabatic compression ![]() |
||
b. An isothermal expansion, an isochoric expansion, an isothermal compression, and an isochoric compression ![]() |
||
c. An isentropic expansion, an isoenthalpic expansion, an isothermal compression, and an adiabatic compression ![]() |
||
d. An isobaric heating, an isothermal expansion, an isobaric cooling, and an isothermal compression ![]() |
a. The formation of ZnO(s) is an endothermic process. ![]() |
||
b. The formation of ZnO(s) is an exothermic process. ![]() |
||
c. No thermal energy is either taken up or given off in the formation process. ![]() |
||
d. None of the above answers is correct. ![]() |
a. Increasing the temperature of the hot reservoir (i.e., the heat source) will increase the efficiency of the engine. ![]() |
||
b. Decreasing the temperature of the cold reservoir (i.e., the heat sink) will increase the efficiency of the engine. ![]() |
||
c. A Carnot cycle is by definition a reversible cycle. ![]() |
||
d. Since the Carnot cycle is a cyclic process, the net work done is zero. ![]() |
a. ∆S = 16.97 J/K; the value of q depends on whether the process is carried out reversibly or irreversibly ![]() |
||
b. ∆S = 5.44 J/K; q = 1825 J ![]() |
||
c. ∆S = 11.53 J/K; q = 1825 J ![]() |
||
d. ∆S = 16.97 J/K; q = 1825 J ![]() |
a. ∆U = ∆H = ∆S = 0 ![]() |
||
b. ∆U = 0; ∆S = 15.88 J/K; and there is not enough information to determine ∆H ![]() |
||
c. ∆U = 0; ∆H = 0; ∆S = -15.88 J/K ![]() |
||
d. ∆U = 0; ∆H = 0; ∆S = 15.88 J/K ![]() |
a. ∆S > 13.3 J/K ![]() |
||
b. ∆S = 13.3 J/K ![]() |
||
c. ∆S < 13.3 J/K ![]() |
||
d. There is not enough information provided to answer this question. ![]() |
a. 26 J/K ![]() |
||
b. 0.8 J/K ![]() |
||
c. -12.6 J/K ![]() |
||
d. -0.8 J/K ![]() |
a. ∆vapS0 = 104.6 J/K-mol for methanol; ∆S(surroundings) = -104.6 J/K-mol ![]() |
||
b. ∆vapS0 = -104.6 J/K-mol for methanol; ∆S(surroundings) = 104.6 J/K-mol ![]() |
||
c. ∆vapS0 = 104.6 J/K-mol for methanol; ∆S(surroundings) = 0 ![]() |
||
d. ∆vapS0 = 550.2 J/K-mol for methanol; ∆S(surroundings) = 0 ![]() |
a. Vaporizing H2O(l) at 373 K and 1 bar pressure ![]() |
||
b. Melting H2O(s) at 273 K and 1 bar pressure ![]() |
||
c. Heating H2O(l) from 273 K to 373 K under a constant pressure of 1 bar ![]() |
||
d. Melting H2O(s) at 273.15 K and 1 bar pressure, and then heating the liquid water from 273.15 K to just short of the boiling point at 373.15 K under a constant pressure of 1 bar ![]() |
a. Tequil = 323 K and ∆Stot = 0 ![]() |
||
b. Tequil = 323 K and ∆Stot = 0.59 J/K ![]() |
||
c. Tequil = 323 K and ∆Stot = -0.59 J/K ![]() |
||
d. Tequil = 373 K and ∆Stot = 6.21 J/K ![]() |
a. 41.8 J/K-mol ![]() |
||
b. -17.5 J/K-mol ![]() |
||
c. -41.8 J/K-mol ![]() |
||
d. 24.2 kJ/mol ![]() |
a. Isothermal expansion from a volume of 5 L to a volume of 10 L ![]() |
||
b. Heating the gas from 300 K to 600 K under constant-volume conditions ![]() |
||
c. Isothermal expansion from a volume of 10 L to a volume of 15 L ![]() |
||
d. Reversible adiabatic expansion from a volume of 5 L to a volume of 10 L ![]() |
a. dS ≥ dq/T for all isothermal processes carried out reversibly or irreversibly at a constant temperature T. ![]() |
||
b. dS ≥ dqrev/T for any reversible process carried out at a constant temperature T. ![]() |
||
c. dS ≥ 0 for all spontaneous processes occurring in any kind of system. ![]() |
||
d. dG ≤ 0 for a spontaneous process occurring in an isolated system. ![]() |
a. The reaction must be endothermic. ![]() |
||
b. The reaction must be exothermic. ![]() |
||
c. The total entropy of the reacting chemical system and its surroundings must increase. ![]() |
||
d. The standard entropy change, ∆rS0, for the chemical reaction must be ≥ 0. ![]() |
a. For a closed system, ∆S can never have a negative value. ![]() |
||
b. For a reversible process in a closed system, ∆S must be zero. ![]() |
||
c. For an adiabatic process in a closed system, ∆S cannot have a negative value. ![]() |
||
d. For an adiabatic process in a closed system, ∆S must be zero. ![]() |
a. Calorimetry involves the measurement of heat transfer during a physical or chemical process. ![]() |
||
b. According to the third law of thermodynamics, the entropies of all perfectly crystalline substances must be the same at the absolute zero of temperature (i.e., at T = 0 K). ![]() |
||
c. For any given change of state, the work done by a system in an irreversible process is always greater than that in a reversible process. ![]() |
||
d. The Joule-Thompson effect relates to the temperature change occurring in a gas during an isenthalpic expansion of the gas. ![]() |
a. 15.03 J/K ![]() |
||
b. -15.03 J/K ![]() |
||
c. 150.3 J/K ![]() |
||
d. 198.1 J/K ![]() |
a. 143.4 J/K-mol ![]() |
||
b. 1.43 J/K-mol ![]() |
||
c. 1550 J/K-mol ![]() |
||
d. -143.4 J/K-mol ![]() |
a. The Nernst heat theorem ![]() |
||
b. The equipartition-of-energy principle ![]() |
||
c. The formulation and analysis of the Carnot cycle and heat engine ![]() |
||
d. The Heisenberg uncertainty principle ![]() |
a. The entropy of the universe always increases in a spontaneous change-of-state process. ![]() |
||
b. The energy of the universe always remains constant in any change-of-state process. ![]() |
||
c. The entropy of a system always decreases with a decrease in the temperature of the system. ![]() |
||
d. The entropy of any chemically pure substance approaches a value of zero as the temperature of the substance approaches a value of 0 K, and at T = 0 K, S = 0. ![]() |
a. Solid water (ice) melts at 1 bar pressure and a temperature of 0oC. ![]() |
||
b. Solid water (ice) melts at 1 bar pressure and a temperature of 5oC. ![]() |
||
c. Liquid water is vaporized at 1 bar pressure and a temperature of 105oC. ![]() |
||
d. Liquid water is vaporized at 1 bar pressure and a temperature of 95oC. ![]() |
a. 2.1 kPa ![]() |
||
b. 21 atm ![]() |
||
c. 2.24 Pa ![]() |
||
d. 2.24 bar ![]() |
a. Calcite is more stable; ∆rG0 = -1.04 kJ/mol ![]() |
||
b. Aragonite is more stable; ∆rG0 = 1.04 kJ/mol ![]() |
||
c. Aragonite is more stable; ∆rG0 = -1.04 kJ/mol ![]() |
||
d. Calcite is more stable; ∆rG0 = 1.04 kJ/mol ![]() |
a. It will increase its value. ![]() |
||
b. It will decrease its value. ![]() |
||
c. It will have no effect on its value. ![]() |
||
d. There is not enough information provided to answer this question. ![]() |
a. 5.7 kJ ![]() |
||
b. -479 J ![]() |
||
c. -5.70 kJ ![]() |
||
d. 479 J ![]() |
a. -54.3 kJ ![]() |
||
b. -60.1 kJ ![]() |
||
c. -43.2 kJ ![]() |
||
d. 12.2 kJ ![]() |
a. The temperature is raised from 500 K to 600 K. ![]() |
||
b. The pressure is increased from 10 bar to 12 bar. ![]() |
||
c. An inert (unreactive) gas is pumped into the reaction mixture under constant-volume conditions. ![]() |
||
d. Hydrogen (H2) gas is added to the mixture at constant pressure. ![]() |
a. 2478 J ![]() |
||
b. -2478 kJ ![]() |
||
c. 12.22 kJ ![]() |
||
d. There is not enough information provided to answer this question. ![]() |
a. 275 K ![]() |
||
b. 396 K ![]() |
||
c. 479 K ![]() |
||
d. 301 K ![]() |
a. 2.3 x 10-3 ![]() |
||
b. 1.1 ![]() |
||
c. 3.8 x 102 ![]() |
||
d. There is not enough information provided to answer this question. ![]() |
a. -116 kJ ![]() |
||
b. -24.9 kJ ![]() |
||
c. 24.9 kJ ![]() |
||
d. There is not enough information provided to answer this question. ![]() |
a. Keq = 0.462 at 25oC; ∆rH0 = 40.1 kJ ![]() |
||
b. Keq = 0.046 at 25oC; ∆rH0 = 21.2 kJ ![]() |
||
c. Keq = 0.003 at 25oC; ∆rH0 = -40.1 kJ ![]() |
||
d. Keq = 0.023 at 25oC; ∆rH0 = -40.1 kJ ![]() |
a. 1842 ![]() |
||
b. 46.4 ![]() |
||
c. 18.4 ![]() |
||
d. 12.6 ![]() |
a. 2.5 x 10-5 bar ![]() |
||
b. 5.0 x 10-3 bar ![]() |
||
c. 0.2 bar ![]() |
||
d. There is not enough information provided to answer this question. ![]() |
a. ∆Hm < 0; ∆Gm < 0 ![]() |
||
b. ∆Hm < 0; ∆Gm = 0 ![]() |
||
c. ∆Hm < 0; ∆Gm > 0 ![]() |
||
d. ∆Hm > 0; ∆Gm = 0 ![]() |
a. 104.6 kJ/K-mol ![]() |
||
b. 104.6 J/K-mol ![]() |
||
c. -104.6 J/K-mol ![]() |
||
d. There is not enough information provided to answer this question. ![]() |
a. An increase in the total pressure of the reaction mixture, with temperature held constant ![]() |
||
b. An increase in the temperature of the reaction mixture, with total pressure held constant ![]() |
||
c. A decrease in the total pressure of the reaction mixture, with temperature held constant ![]() |
||
d. A simultaneous increase in temperature and increase in pressure ![]() |
a. 47.6oC ![]() |
||
b. 27.3oC ![]() |
||
c. 25.2oC ![]() |
||
d. 22.7oC ![]() |
a. 35.1 J/K-mol ![]() |
||
b. 35.1 J/mol ![]() |
||
c. 295 J/K-mol ![]() |
||
d. -35.1 J/K-mol ![]() |
a. 4.73 kJ ![]() |
||
b. 9.46 kJ ![]() |
||
c. -4.73 kJ ![]() |
||
d. -2.85 kJ ![]() |
a. 237 kJ ![]() |
||
b. -237 kJ ![]() |
||
c. 237 J ![]() |
||
d. -116 kJ ![]() |
a. 1.03 x 10-8 bar ![]() |
||
b. 1.06 x 10-16 bar ![]() |
||
c. 0.65 bar ![]() |
||
d. 0.81 bar ![]() |
a. 0.843 bar ![]() |
||
b. 7.78 x 10-38 bar ![]() |
||
c. 6.05 x 10-75 bar ![]() |
||
d. 8.05 x 10-5 bar ![]() |
a. 0.99 bar ![]() |
||
b. 15.7 bar ![]() |
||
c. 6.4 x 10-4 bar ![]() |
||
d. 6.4 x 10-2 bar ![]() |
a. ∆Am < 0; ∆Gm = 0 ![]() |
||
b. ∆Am > 0; ∆Gm = 0 ![]() |
||
c. ∆Am = 0; ∆Gm = 0 ![]() |
||
d. ∆Am < 0; ∆Gm < 0 ![]() |
a. Increase ![]() |
||
b. Decrease ![]() |
||
c. Not change ![]() |
||
d. There is not enough information provided to answer this question. ![]() |
a. The molar entropy (Sm) ![]() |
||
b. The molar enthalpy (Hm) ![]() |
||
c. The molar Gibbs free energy (Gm) ![]() |
||
d. The molar volume (Vm) ![]() |
a. Greater than ![]() |
||
b. Equal to ![]() |
||
c. Less than ![]() |
||
d. There is not enough information provided to answer this question. ![]() |
a. 0.13 J/K-mol ![]() |
||
b. 129.7 J/K-mol ![]() |
||
c. -129.7 J/K-mol ![]() |
||
d. There is not enough information provided to answer this question. ![]() |
a. -30.7 kJ/mol ![]() |
||
b. 30.7 kJ/mol ![]() |
||
c. 70.6 kJ/mol ![]() |
||
d. -12.6 kJ/mol ![]() |
a. For a one-component system, the maximum number of phases that can coexist in equilibrium is three. ![]() |
||
b. When three phases coexist in equilibrium in a one-component system, one of the phases must be a gas, one must be a liquid, and one must be a solid. ![]() |
||
c. For a one-component system, the most stable phase at a given T and P is the phase with the lowest Gm (molar Gibbs free energy). ![]() |
||
d. For a pure substance, the vapor pressure of the solid is equal to the vapor pressure of the liquid at the triple-point temperature. ![]() |
a. It is impossible for four phases of a single pure substance to coexist at equilibrium. ![]() |
||
b. The maximum number of phases that can coexist in a system composed of four components is equal to six. ![]() |
||
c. The Clausius-Clapeyron equation can be used in the characterization of solid-liquid phase equilibria. ![]() |
||
d. Two phases at equilibrium must have the same pressure. ![]() |
a. It will be higher. ![]() |
||
b. It will be lower. ![]() |
||
c. It will be the same. ![]() |
||
d. There is not enough information provided to answer this question. ![]() |
a. The vapor pressure of the solution will exhibit negative deviations from Raoult’s law behavior. ![]() |
||
b. The vapor pressure of the solution will be less than ½(PA* + PB*) when species A and B are present in equimolar amounts (where PA* and PB* denote the vapor pressures of pure liquid A and pure liquid B, respectively). ![]() |
||
c. The vapor pressure of the solution will exhibit positive deviations from Raoult’s law behavior. ![]() |
||
d. If the mole-fraction of species A (XA) is much larger than the mole-fraction of species B (XB), then the vapor pressure of B will follow Henry’s law behavior. ![]() |
a. 0.166 Torr ![]() |
||
b. 1.02 L-atm ![]() |
||
c. 985 Torr ![]() |
||
d. 985 Torr/mol ![]() |
a. The chemical potential of A in solution is always less than the chemical potential of pure liquid A (at fixed values of pressure and temperature). ![]() |
||
b. Additions of more solute to the solution will always lower the chemical potential of the solvent. ![]() |
||
c. Additions of a nonvolatile solute to the solution will always lower the vapor pressure of the solution. ![]() |
||
d. At any given temperature, the vapor pressure of the solution will always be less than the vapor pressure of the pure solvent. ![]() |
a. 1683 J ![]() |
||
b. -1683 J ![]() |
||
c. -1282 J ![]() |
||
d. 440 J ![]() |
a. -1.39 kJ/mol ![]() |
||
b. 0 ![]() |
||
c. 1.39 kJ/mol ![]() |
||
d. There is not enough information provided to answer this question. ![]() |
a. 0.075 atm ![]() |
||
b. 0.115 atm ![]() |
||
c. 0.224 atm ![]() |
||
d. 0.008 atm ![]() |
a. a(toluene) = 0.3399; a(benzene) = 0.6914; γ(toluene) = 1.03; γ(benzene) = 1.03 ![]() |
||
b. a(toluene) = 0.77; a(benzene) = 0.23; γ(toluene) = 1.11; γ(benzene) = 0.89 ![]() |
||
c. a(toluene) = 0.46; a(benzene) = 0.54; γ(toluene) = 0.79; γ(benzene) = 0.93 ![]() |
||
d. There is not enough information provided to answer this question. ![]() |
a. 0.69 bar ![]() |
||
b. 0.012 atm ![]() |
||
c. 6.9 atm ![]() |
||
d. 69 Pa ![]() |
a. 5.55oC ![]() |
||
b. 11.1oC ![]() |
||
c. 2.47oC ![]() |
||
d. There is not enough information provided to answer this question. ![]() |
a. 4.31 atm ![]() |
||
b. 4.31 x 105 Pa ![]() |
||
c. 12.4 bar/mol ![]() |
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d. 4.31 x 104 atm ![]() |
a. PT = 7.219 kPa; Xtoluene = 0.643 (in vapor) ![]() |
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b. PT = 6.006 kPa; Xtoluene = 0.643 (in vapor) ![]() |
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c. PT = 6.006 kPa; Xtoluene = 0.357 (in vapor) ![]() |
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d. There is not enough information provided to answer this question. ![]() |
a. 107.5 g/mol ![]() |
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b. 6.602 g/mol ![]() |
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c. 73.3 g/mol ![]() |
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d. 57.9 g/mol ![]() |
a. 36.1 g/mol ![]() |
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b. 72.2 g/mol ![]() |
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c. 36.1 kg/mol ![]() |
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d. 18.1 g/mol ![]() |
a. A 0.01 M aqueous solution of BaCl2 ![]() |
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b. A 0.1 M aqueous solution of CaCl2 ![]() |
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c. A 0.1 M aqueous solution of sucrose ![]() |
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d. A 0.1 M aqueous solution of KCl ![]() |
a. Pure liquid water ![]() |
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b. A 0.01 M aqueous solution of NaHCO3 ![]() |
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c. A 12 M solution of sulfuric acid ![]() |
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d. A 0.1 M aqueous solution of glucose ![]() |
a. A 0.01 M aqueous solution of NaCl ![]() |
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b. A 0.01 M aqueous solution of BaCl2 ![]() |
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c. A 0.01 M aqueous solution of KBr ![]() |
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d. A 0.01 M aqueous solution of FeCl3 ![]() |
a. The molar entropy of a substance is an extensive property. ![]() |
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b. The molar entropy of a substance always increases with an increase in temperature. ![]() |
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c. The molar entropy of a molecular gas depends on the molar mass of the constituent molecules. ![]() |
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d. The entropy of a molecular system depends on the spacings between the rotational and vibrational energy levels of the constituent molecules. ![]() |
a. 446.9 J/K-mol ![]() |
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b. 53.8 J/K-mol ![]() |
||
c. There is no difference. ![]() |
||
d. There is not enough information provided to answer this question. ![]() |
a. 2.50 x 10-17 ![]() |
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b. 3.75 x 10-17 ![]() |
||
c. 1.67 x 10-17 ![]() |
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d. 1.67 x 1017 ![]() |
a. 1115 ![]() |
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b. 1.115 ![]() |
||
c. 10.15 s-1 ![]() |
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d. 10.15 J ![]() |
a. 9 ![]() |
||
b. 6.74 x 10-24 ![]() |
||
c. 4.03 x 10-24 ![]() |
||
d. 6.743 ![]() |
a. 2.41 x 108 ![]() |
||
b. 1.45 x 1032 ![]() |
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c. 1.45 x 1032 J/m3 ![]() |
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d. 2.41 x 108 kJ/molecule ![]() |