UNIVERSITY OF TORONTO FACULTY OF APPLIED SCIENCE AND ENGINEERING TERM TEST 2 17 MARCH First Year APS 104S

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UNIERSIY OF ORONO Please mark X to indicate your tutorial section. Failure to do so will result in a deduction of 3 marks. U 0 U 0 FACULY OF APPLIED SCIENCE AND ENGINEERING ERM ES 7 MARCH 05 U 03 U 04 U 05 U 06 U 07 U 08 U 09 First Year U 0 U APS 04S U INRODUCION O MAERIALS AND CHEMISRY Exam ype B Examiners: G. Azimi, C Chin,. Mirkovic, J. Nogami Q /0 Q /0 NAME: Last First Q3 /0 Q4 /0 Q5 /0 SUDEN NO: otal /00 INSRUCIONS: his is a ype B examination. Only non-programmable calculators are allowed. Answer all 5 questions. All work is to be done on the pages of this booklet. When answering the questions include all the steps of your work on these pages and then fill the answer in the respective boxes. For additional space, you may use the back of the preceding page. Do not unstaple this exam booklet. A Formula Sheet and the periodic table are attached to the end of this exam booklet; if you wish, you may tear-off these sheets only. Exam papers filled out in pencil will not be eligible for regrading. Page of

Name: QUESION : Ideal Gas Law (0 pts) 0 g of propane (C 3 H 8 ) is in a L container at 5 C. a) what is the pressure in the container (in atm), assuming that propane behaves like an ideal gas? [ pts] b) assuming an der Waals behavior, recalculate the pressure (a = 9.39 L atm mol - and b=0.0905 L/mol) [4 pts] c) calculate the exact number of moles of oxygen needed to burn all the propane according to: C! H! + 5O! = 3CO! + 4H! O (g) [ pts] Page of

Name: d) If we add the exact number of moles of O from part c) into the same L container, and assuming the reaction in part c) takes place completely, calculate the final pressure in the vessel assuming: ideal gas behavior the temperature rises to 50 C water remains as water vapor [5 pts] e) recalculate the answer in part d) if you start with only half the amount of oxygen calculated in part c), and also calculate (in addition to the total pressure) the partial pressures and mole fractions of all the remaining gasses. [7 pts] Page 3 of

Name: QUESION : First Law of hermodynamics (0 pts) A quantity of 0.45 mol of neon is confined in a container at 3.5 atm and 98 K and then allowed to expand under three different conditions. (a) In the first process, the gas expands adiabatically and reversibly to.00 atm. Calculate the final temperature and the work done. [6 pts] (b) In the second process, the gas expands adiabatically against a constant pressure of.00 atm. Calculate the final temperature and the work done. [6 pts] (a) In the third process, the gas expands isothermally and reversibly until its volume reaches the same value as the final volume in part (a). Determine the value of the final volume and the final pressure of this reversible isothermal expansion. [4 pts] (d) On a P- diagram, sketch the paths described in (a) and (c). In which process was more work performed? On the diagram, shade the area that represents the difference in the work done in process (a) and process (c) [4 pts] Page 4 of

Name: QUESION 3: First Law of hermodynamics (0 pts) (a) he density of liquid water at 00 C is 0.9584 g/cm 3, and that of steam at the same temperature is 0.000596 g/cm 3. If the enthalpy of evaporation of water at atmospheric pressure is 40.63 kj/mol, what is ΔU? How much work is done by the system during the evaporation process? Hint: Consider calculating molar volumes first. [5 pts] (b) Would you expect for the fusion process (ice to water) the difference between ΔU and ΔH to be larger or smaller than the one calculate in (a) for the vaporization process? Explain. [3 pts] (c) How much heat is required to heat moles of water (ice at -0 C) to gasous water vapour at 0 C? Sketch the process on a temperature vs heat graph. [6 pts] Given: ΔH fusion =6. 0 kj/mol, ΔH vapourization = 40.67 kj/mol, ice water vapour CP =.J/gK CP = 4.8J/gK CP =.08J/gK (d) A chunk of ice at 70 K, weighing 30 grams, is dropped into 300 g of liquid water at 300 K. Determine the final temperature of the system once equilibrium has been reached. Use any constants that you need from parth (c). [6 pts] Page 5 of

Name: Question 4: hermochemistry A table (4.) with thermodynamic data is provided. he heat of combustion for formaldehyde (CH O) is -33 kj (mol - CH O) at the standard state (98.5 K, bar, products and reactants are both in the gas phase). a) Determine the heat of formation for formaldehyde (CH O) at standard state. [5 pts] b) he heat of reaction for the reverse Water-Gas-Shift reaction (98.5 K, bar) is: 0 CO (g) +H (g) à H O (l) +CO (g) Δ H RXN = 88kJ (mol - ) Determine the heat of reaction for the following reaction at standard state: CH O (g) à CO (g) +H (g) Show your work. [5 pts] c) Determine the heat of combustion (in kj (mol - CH O)) for formaldehyde at 500 K. [4 pts] Page 6 of

Name: d) Using Bond Enthalpy able (Bond Dissociation Energies for the various bonds listed below), estimate the heat of reaction for the following reaction at the standard state. [4 pts] H O C H C O + H H e) he heat capacity for CO (liquid) is HIGHER LOWER than CO (gas) (circle one) [ pts] able 4. hermodynamic Data Heat of formation at standard 0 state, Δ Hf ( kjmol ) 98.5 K, bar Heat Capacity at constant pressure, C P ( Jmol K ) *independent of temperature CO (g) -08 37 H O (g) -4 33 H O (l) -86 75 O (g) 0 9 CH O Not given for this problem 34 H (g) 0 Page 7 of

Name: Question 5: Entropy i) In a process taking place inside a system,.5 mole of a monoatomic ideal gas is expanded adiabatically from 500 C and 5 bar to a final pressure of bar. Calculate ΔS system, ΔS surroundings, and ΔS universe for the following conditions: a) if the process is reversible; [3 pts] b) if the process is irreversible and expansion is made against vacuum. [4 pts] c) if the process is irreversible and the work produced is 6000 J; [4 pts] ii) Are the following statements true or false? [4 pts] Check one F he entropy of a system cannot increase in any adiabatic process... ΔS (universe) for melting ice to water at 0 C is ZERO. It is possible to have the efficiency of the Carnot cycle equal to. In a process, «graphite» is transformed to «diamond». ΔS for this process is negative. Page 8 of

Name: iii) a) Calculate the change in the entropy when 0 g of solid mercury (Hg(s)) at -50 C and bar transforms to gaseous mercury at its boiling point. Below are the required thermodynamic data (specific heat capacities, C p,m, are independent of temperature): [3 pts] ΔH fusion =.33 kj/mol ΔH vaporization = 59. kj/mol C p, m Hg(s) = 8. J/mol.K C p,m Hg(liq) = 7.9 J/mol.K Melting temperature = -39 C Boiling temperature = 357 C b) Using the thermodynamic data provided in part (a), sketch a qualitative graph of the molar entropy of mercury (Hg) as a function of temperature in the range of 0 to 700 K at constant pressure. [ pts] Page 9 of

Name: FORMULAE & CONSANS (You may tear these sheets off.) R = 8.345 J K - mol - = 0.080574587 L atm K - mol - = 0.08345 L bar K- mol- atm = 0.35 kpa =.035 bar = 4.696 psi = 760 orr = 760 mmhg NA = 6.0 x 0 3 mol - k = 8.6 x 0-5 e/k e =.60 x 0-9 J (K) = ( o C) + 73.5 K F = 9.6485309 0 4 C mole - e =.607733 0-9 C SP: 73.5K, atm SAP: 98.5K, bar L atm = 0.35 J Idea gas equation of state: P = nr an der Waals equation of state: nr an P = ( nb) First law, closed systems ΔU = q + w du = dq +dw dw= Pextd du = ncv,md For an isothermal reversible process (ideal gas): nr P Wrev = d = nr ln = nr ln P Adiabatic reversible process ( ideal gas): γ γ P = P C (γ ) (γ ) [( γ )/ γ ] [( γ )/ γ ] = P = P C P = γ H U + P dh = ncp,md For ideal gases, Cp,m=Cv,m+R Solids, Liquids, Cp,m = Cv,m G H S dqreversible ds For a process at constant temperature ΔG= ΔH-ΔS υi: stoichiometric coefficient Assuming no phase change, constant Cp ΔH rxn = Συi*ΔH f,i + ΔCp*(-5 C) ΔCp = Συi*Cp,i Efficiency = w /q in ε(ideal) = C / H For solids or liquids: Phase transition ΔS trans ΔH = trans trans = + Δ d f ΔS ( ) ΔS ( ) C ΔS = nc Pln (change in at const P) P i Standard entropy of the reaction ΔS rxn = Συi*Sm i S = nc! ln nr ln P! P! f ΔS = nrln f ΔS = nc ln i i (isothermal) (change in at const ) S = nc! ln + nr ln!! =!! = P! P!!!/!!!/!! Page 0 of

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