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    Name: October 26th, 2005

    EGEE 301 - Thermodynamics and Flid !echanics

    Final E"am on Thermodynamics

    115 mintes

    #$ %&0'( )ircle the choice that *i+es the best anser to the estions

    1. A common battery is

    (i) an adiabatic system(ii) a closed system

    (iii) an open system

    2. Density of a substance is(i) an extensive property

    (ii) an intensive property(iii) a molar property

    3. The molar entropy

    (i) an extensive property(ii) an intensive property

    (iii) a molar property

    4. Volume is

    (i) an extensive property(ii) an intensive property(iii) a molar property

    5. Which temperature in Celsius and ahrenheit is the same

    (i) -30 degrees

    (ii) -40 degrees

    (iii) -50 degrees

    !. "f #olume is fi$ed% based on the ideal &as la'

    (i) P1/P2= 1/2

    (ii) P1!P2= 1!2(iii) P1/P2= 2/1

    (. )ne mol of an ideal &as at temperature of *+C and pressure of 1 bar occupies

    (i) 22"# 103cm3

    (ii) 24"# 103cm3

    (iii) 2$"3 103cm3

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    ,. "f pressure is -ero% the compressibility factor /0 should be

    (i) 0(ii) 1

    (iii) 10

    . "f the reduced temperature and #olume are 1% the reduced pressure of the #an der

    Waals &as is

    (i) 0(ii) 1

    (iii) 2

    1*. The molar heat capacity is

    (i) an extensive property

    (ii) an intensive property

    (iii) none o% t&e above

    11. The internal ener&y is

    (i) a %'nction o% state(ii) a %'nction o% process

    (iii) none o% t&e above

    12. The standard pressure for presentin& thermodynamic properties is

    (i) 0"1 Pa

    (ii) 1 atm

    (iii) 10 psi

    13. Wor is

    (i) a %'nction o% state(ii) a %'nction o% process

    (iii) none o% t&e above

    14. A small #ariation of the enthalpy% d% is

    (i) a per%ect di%%erential

    (ii) an imper%ect di%%erential

    (iii) bot& o% t&e above

    15. A small #ariation of heat% d% is

    (i) a per%ect di%%erential(ii) an imper%ect di%%erential

    (iii) bot& o% t&e above

    1!. The 'or done on a system by en#ironment is

    (i) positive

    (ii) negative

    (iii) eit&er positive or negative

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    1(. The heat released by a system to uni#erse is

    (i) positive(ii) negative

    (iii) eit&er positive or negative

    1,. CVis

    (i) larger t&an p

    (ii) smaller t&an p(iii) e*'al to p

    1. Cp of an ideal monatomic &as is

    (i) (5/2)+(ii) (3/2)+

    (iii) (#/2)+

    2*. "n an isochoric process heat euals(i) ent&alpy

    (ii) entropy(iii) internal energy

    21. A chemical reaction% 'hich has a positi#e 6r$n% is called

    (i) exot&ermic(ii) endot&ermic

    (iii) none o% t&e above

    22. The enthalpy of formation of 2&0 is

    (i) , 0

    (ii) 0(iii) = 0

    23. "f Cp is constant then 7T87To

    (i) = p ln(/o)

    (ii) = p ( . o)

    (iii) = p (/o)

    24. or a re#ersible heat en&ine

    (i) 11= 22

    (ii) 1/1= 2/ 2(iii) 1/ 1= 2/ 2

    25. The efficiency of an ideal heat en&ine is defined as

    (i) =1-2/1

    (ii) =1-2/1

    (iii) bot& o% t&e above

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    2!. d9T is

    (i) a per%ect di%%erential

    (ii) an imper%ect di%%erential(iii) bot& o% t&e above

    2(. de7 can be(i) ,0

    (ii) 0

    (iii) bot& o% t&e above

    2,. di7 can be

    (i) 0

    (ii) 0(iii) bot& o% t&e above

    2. "f the absolute temperature approaches -ero% then

    (i) 0(ii) 0

    (iii) 0

    3*. The combined 1stand 2nd:a's of thermodynamics for re#ersible and closed

    systems 'ithout chemical reactions0 can be e$pressed as

    (i) d = d6 7 d(ii) d = - Pd8 7 d

    (iii) d = d 7 Pd8

    31. "t is possible to determine the absolute #alue of

    (i) ent&alpy

    (ii) entropy(iii) none o% t&e above

    32. The heat capacity of a substance can be

    (i) , 0

    (ii) 0

    (iii) = 0

    33. "f entropy of a system is decreasin&% the order in the system

    (i) is increasing

    (ii) is decreasing(iii) is not c&anging

    34. At euilibrium% the entropy production achie#es

    (i) minim'm

    (ii) 9ero

    (iii) bot& o% t&e above

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    35. or the same substance

    (i) (solid) (gas)

    (ii) (solid) , (gas)(iii) (solid) : (gas)

    3!. The enthalpy of e#aporation should be(i) , 0

    (ii) 0

    (iii) 0

    3(. "f the number of microstates W0 is 1**% the molar entropy is

    (i) ;"314 < mol-1-1

    (ii) 1>"15 < mol-1-1(iii) 3;"2> < mol-1-1

    3,. The chemical potential is

    (i) an extensive property(ii) an intensive property

    (iii) none o% t&e above

    3. Affinity is

    (i) a %'nction o% state

    (ii) a %'nction o% process(iii) none o% t&e above

    4*. "f affinity is ne&ati#e% the reaction can proceed

    (i) to t&e rig&t

    (ii) to t&e le%t

    (iii) bot& o% t&e above

    41. Diffusion of molecules is due to

    (i) a concentration gradient(ii) a c&emical potential gradient

    (iii) a gravitation gradient

    42. The internal ener&y is a thermodynamic potential if

    (i) ? 8 = constant

    (ii) ? 8 = constant

    (iii) ? P = constant

    43. "f temperature and #olume are constant% the thermodynamic potential is

    (i) @elm&olt9%ree energy(ii) entropy

    (iii) ibbs %ree energy

    44. The chemical potential of the i8th component is

    5

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    (i) (AB/ACi)?8

    (ii) (A/ACi)?p

    (iii) bot& o% t&e above

    45. The chemical potential of a pure substance is

    (i) t&e molar ibbs %ree energy(ii) t&e molar ent&alpy

    (iii) t&e molar entropy

    4!. The chemical reaction affinity is

    (i) (A/AD)?8

    (ii) (A@/A D)?p

    (iii) bot& o% t&e above

    4(. The partial molar entropy is

    (i) (A/ACE)?8

    (ii) (A/ACE)?P(iii) (A/ACE)?

    4,. The partial molar enthalpy can be

    (i) ,0

    (ii) 0

    (iii) bot& o% t&e above

    4. "f pressure is close to -ero% the fu&acity approaches

    (i) 0(ii) 1

    (iii) t&e press're

    5*. "f temperature approaches *% the isochoric heat capacity of a pure solid approaches

    (i) 0

    (ii) + (iii) 3+

    51. "f temperature is uite hi&h% the isochoric heat capacity of a pure solid approaches

    (i) 0(ii) +

    (iii) 3+

    52. or a #an der Waals &as% C+and C+%ideal are

    (i) e*'al

    (ii) not e*'al(iii) slig&tly di%%erent

    53. "ce and 'ater are in euilibrium if

    (i) @(ice) = @(Fater)

    $

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    (ii) (ice) = (Fater)

    (iii) G(ice) = G(Fater)

    54. At room temperature and atmospheric pressure% the stable phase of 2) is

    (i) @2H(g)

    (ii) @2H(l)(iii) @2H(s)

    55. At atmospheric pressure and temperature of 3* o% the stable phase of 2) is

    (i) @2H(g)

    (ii) @2H(l)

    (iii) @2H(s)

    5!. At temperature of 125oC% the saturated pressure of 'ater is about

    (i) 0"5 bar

    (ii) 1"0 bar

    (iii) 1"5 bar

    5(. At temperatures and pressures abo#e the critical point

    (i) gas p&ase can not be li*'e%ied

    (ii) gas p&ase can be li*'e%ied

    (iii) gas p&ase can be slig&tly li*'e%ied

    5,. )n a saturated #apor cur#e% d;9dT could be ne&ati#e if

    (i) I@vapori9 , 0 and I8vapori9 , 0

    (ii) I@vapori9 , 0 and I8vapori9 0(iii) I@vapori9 0 and I8vapori9 , 0

    5. "f pressure is *., bar% 'ater 'ill boil at temperature

    (i) , 100 o

    (ii) 100 o

    (iii) : 100o

    !*. The de&ree of freedom in the triple point of 'ater is

    (i) 0

    (ii) 1(iii) 2

    !1. The de&ree of freedom in the critical point of 'ater is

    (i) 0

    (ii) 1

    (iii) 2

    !2. An a-eotropic solution

    (i) can be separated to tFo components 'sing distillation

    (ii) can not be separated to tFo components 'sing distillation

    #

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    (iii) can be partially separated to tFo components 'sing distillation

    !3. "n the composition trian&le center% the molar fractions of all three components are

    (i) e*'al

    (ii) di%%erent

    (iii) 9ero

    !4. "n i&ure (.1* if 7: < *.5 :; the system has

    (i) more vapor t&an li*'id(ii) more li*'id t&an vapor

    (iii) abo't t&e same amo'nt o% vapor and li*'id

    !5. "n a first8order phase transition% #olumes of both phases are

    (i) e*'al

    (ii) not e*'al

    (iii) sero

    !!. "n a first8order phase transition the molar =ibbs ener&ies of both phases are

    (i) e*'al(ii) not e*'al

    (iii) 9ero

    !(. The acti#ity coefficient can be

    (i) positive

    (ii) negative

    (iii) eit&er positive or negative

    !,. >ased on the enry?s la'% if the partial pressure of C)2in air is increasin& its

    concentration in a lae 'ater is

    (i) increasing

    (ii) decreasing

    (iii) not c&anging

    !. >ased on the @aoults la'% the partial pressure of 'ater abo#e an aueous solution

    is

    (ii) larger t&an t&e partial press're above p're Fater(ii) smaller t&an t&e partial press're above p're Fater

    (iii) abo't t&e same

    (*. The enthalpy of formation of Ba0 is

    (i) , 0

    (ii) = 0(iii) 0

    (1. The ionic stren&th of 1 mol &81Cu7)4a0 solutions is

    (i) 1mol Eg-1

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    (ii) 2 mol Eg-1

    (iii) 4 mol Eg-1

    (2. "f the solubility product% spis 1*81*% the salt solubility

    (i) 10-3mol Eg-1

    (ii) 10-5

    mol Eg-1

    (iii) 10-10mol Eg-1

    (3. "n a dilute electrolyte solutions if the electrolyte concentration is decreasin& the

    acti#ity coefficient is

    (i) increasing

    (ii) decreasing

    (iii) in not c&anging

    (4. The chemical reaction #elocity is

    (i) + %/+r

    (ii) + r- +%(iii) +%- +r

    (5. The rate constant% i% depends on

    (i) temperat're

    (ii) concentration

    (iii) bot& temperat're and concentration

    (!. The rate constant of an elementary reaction is of the 1storder can be obtained

    plottin&

    (i) JKL vs" time

    (ii) ln JKL vs" time

    (iii) 1/JKL vs" time

    ((. The rate constant of an elementary reaction is of the 2ndorder can be obtained

    plottin&

    (i) JKL vs" time

    (ii) ln JKL vs" time

    (iii) 1/JKL vs" time

    (,. The euilibrium constant depends on

    (i) temperat're

    (ii) concentration

    (iii) temperat're and concentration

    (. "f the =ibbs free ener&y of a reaction is ne&ati#e% the euilibrium constant is

    (i) , 1

    (ii) = 1

    (iv) 1

    >

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    ##$ %10'( )alclate the Gibbs .ree ener*y %/Gor"n(, enthaly /or"n, and entroy

    /or"nchan*es, as ell as the eilibrim constant %( at 25o) and 1 bar .or the

    methane combstion reaction, )4%*( 2 O2%*( )O2%*( 22O%l($

    Iorxn= 2 Io

    %J@2H? lL 7 Io

    %JH2? gL - Io%J@4? gL . 2 I

    o%JH2? gL = - ;1;"3 E< mol

    -1

    I@orxn= 2 I@o

    %J@2H? lL 7 I@o

    %JH2? gL - I@o%J@4? gL . 2 I@

    o%JH2? gL = - ;>0"4 E< mol

    -1

    Iorxn= (I@o

    rxn - Io

    rxn)/ = 241"; < mol-1-1

    = exp (-Iorxn/(+)) = 1"3>

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