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ENSC 2213 Thermodynamics } sey
FINAL EXAM / 12-05-16
(5) Problem 1. It is your first day on the job wit! 4, a dry ice manufacturing
plant, and your superviser already needs you to uo an eme ey Calculation. In the dry ice
manufacturing plant 8 Ibmol of gaseous carbon dioxide at Ti = 493°R and p: = 320 Ibffin? is
compressed at constant pressure in a piston cylinder device. The work required for the
compression process is —2000 Btu. The final volume (V2) of the gas after the compression is a
key variable for the next processing step. Determine the final volume, V2 (in ft’). Do NOT
assume ideal gas behavior for the gaseous carbon dioxide.
We frdver(K-y) smu RR
~ Ib =
we _ -2000 BI. (77% FRE) 2. ae
Pe (3z6 Noe 2\( pay in gy)
Find Uf Using Cormpprest bi hy Chart
pa gn eZ) oe Teal
1 RT 27; nRT
BV. nS oy Ae
Where
Tp plang SAGES Oa = god
eee. a
) TB S4F'R nef © 9.244 0.3
Pr 320 yy. en
iA eS
0.4 atm) tT A atm) :
; x ¢ Fes a ee
a v4. A 1 with TR, = 0-4 ‘ 2
oo" ove BaD
(% omal Name) i 5)
WEY my inet
\szo BENG
_ 0.85
va nRy, =,
_
*
S,
eet f
3
3 f.2_ 33.77 Ft
ame = 9) \i2-ot0
Y, ~ Vi8-)
M2 sc 1%. 63 i
— ty
ENSC 2213 Thermodynamics Nam CXAM Key
FINAL EXAM / 12-05-16 ae
(25) Problem 2. A well-insulated steam turbine operates at steady state. Steam enters the turbine at
pi = 1600 lbffin? and T; = 1000°F. Twenty five percent (25%) of the steam entering is extracted
midway through the expansion process in the turbine at p2 = 160 Ibf/in* and T2 = 450°F. The rest
of the steam exits as saturated vapor at p3 = 1 Ibffin’, The turbine develops a power output of
9x10® Btu/hr. Assuming negligible kinetic and potential energy effects, determine the mass flow
rate of the steam entering the turbine (7m,), in Ibm/hr.
sTear
From (gus, YF PIASS Re teoo MFfin™ ©
, ‘ ‘ 0
221, = gl omy, Fa T = 1000 °F We 4x10 8
a m, = z |_—_——> fe he
2 r=
tA, = 0.25,
Ree Ont as 2 < 6.25), sah Vapor
: : : « TEAS Be ee):
dng - 1, - 25m, Seg wh ie pa tl
Be. = S0PF
For steady stah, ptrabatiy proces wrk, Axe g APE td),
reryy % (et law) reduces &
ire ape Beeps
Wi, Phy 1.28%) he — -% 25m, )hs
W. , (h, - 625h2- hy + 42543)
PN eis
eo 25h, — 2 "3
Bh. £, - 1246.1
wher Yrom Tabk A-¢& > fy, stt87+! 2 =
ree
Rhu /lom
Sega /2 A-tG: eg = 05.8 Bu
% Bh/h
a= tate z ao ie (0.15)(105-2)] Btu/lbm
Ass: Mo a ka: Neen rn
4,
Ai h-S3 624.
&
o ~ x19 Bli/hr
Po, = 4,514,961 bye eb
Mi =
ENSC 2213 Thermodynamics NA
oe a ae
a
NaMe_EXAM Key
ENSC 2213 Thermodynamics
FINAL EXAM / 12-05-16
(40) Problem 5. Consider an ideal ait-standard (variable specific heat analysis) Diesel cycle.
€ pl
‘essure and temperature at the beginning of the compression process are 94,9 kPa and
300 K, respectively. At the end of he
at addition process, the pressure is 7.2 MPa and the
temperature is 2150 K. For this cycle determine:
p
(a) The temperature at the beginning of the heat addition process (in K), 2 3
(b) The compression ratio, 4
(c) The cutoff ratio.
(d) The temperature at the beginning of the heat rejection process (in K), ‘
(e) The pressure at the beginning of the heat rejection process (in MPa).
Givin; T= 300K , Fe 44 KP
Tg: sok, R= 7.2MPa =
LA) For an Isenfropic process lene)
7200 mes 05.2
P. —oseniaes =
Mee AS a2 Bh \ AY. 1 Pa
Ly From able A-22 an = 360K
Fron Table A-22 wilh Rs los2 a> [T= 480K
ce From Tabi At @ Ty = Beg
&’) re Vr, ie 2), & aes
aves a2 aia, T -480K
\ From Tab A-z2r @ Te =
Coe eens
Ta
ONES Ae eo
ry _ 222 (2.175) = 22.4 ey
(d) Veg e % “ry ae. 2 ( bes from Table A~2% é =
Ts ao soX ane blaction
ae ee ee = t2.7 <> | 4
From Wake A-2L © 14 40 30
2b MPa
& 24.35 12 MP, es [ose MPs |
() We aN r= Benes u ( ¢)
3 ZS 3A
Feem Tb A-22 @ Taz 2is0 Kk
SS
>
EXAM K6EY
EENSC 2213 Thermodynamics NAME
FINAL EXAM / 12-05-16
(30) Problem. 6. gerant i vapor-compression
i ing fluid in an ideal vapor-co!
3 Refri it 134a is the working wld. in
refrigeration cycle operating under the following conditions:
Q
TS ig ee bist ht Meena dt camne att) if MAPe 1
ENSC 2213 Thermodynamics name. EXAM KE
FINAL EXAM / 12-05-16
(30) Problem 6, Refrigerant 134a is the working fluid in an ideal vapor-compression
refrigeration cycle operating under the following conditions:
Compressor inlet condition: Saturated vapor at 0.16 MPa
Condenser exit condition: Saturated liquid at 0.70 MPa
Refrigeration capacity: 3.5 tons
For this cycle determine:
(a) The mass flow rate of refrigerant (in kg/s).
(b) The power necessary to drive the compressor (in kW).
(c) The heat rejected by the condenser (in kW).
(d) The coefficient of performance.
\A) From & (0.3) = Qin
a
where from Table AN @ R= Ole MPA = 4G bar 6 Sak Mpéor
be Wig 2341 KS/ey 2 Si Sg = 0424S MT eg
Poem TC Asap @ RB = Pe = 9.7 Pa e (oary emer. lignid
hs: h3g = SUVS ‘Sieg
For thro MHlry gorg less Reta te Stns he Sd hes
Be ep (3.5 fms) 21) 1S min SS = 10,084 Ka.
(237. 47 SU.18) KT ic,
(6) ™% = hy A,)
peenteeg, | Tadic Ante ©. “le = fIMP. =7 bar g S2-S,= 0.4295 25
hag = 268.40 KT/e, (eh trterpalarvon)
HZ = 0.0814 KS (205.40 ~ 237.97) 82 =| 2489 KW |
2 a0 £s ( yx. [Baw
iS Qout ™ Cha hs)
Qo = 0.0F4 a (26% 40~€6.78) x ~ [4.4% Kw
a ee _ Ba - %o13) ‘i ==
his A, (26 ¢.40 ~ 237.97) KF), =[4.97 = 5]
W
M,
Ae