Download Assignment 9 with Solutions for Introduction to Thermodynamics | ME 205 and more Assignments Thermodynamics in PDF only on Docsity! PROBLEM 5.43
5.43 A refrigeration cycle operating between two reservoirs receives energy Qe trom a cold
reservoir at Te = 274 K and rejects energy Gy to a hot reservoir at Tj; = 315 K. For each of the
following cases determine whether the cycle operates reversibly, operates irreversibly, or is
impossible:
KNOWN: A rettigeration cycle operates between two reservoirs with specified temperatures.
FIND: Whether cach of four cycles operates reversibly, operates irreversibly, or is impossible.
SCHEMATIC AND GIVEN DATA:
\ |
x.
{| Retrigeration [| Mace
1] Cycle '
| t !
oo dg = 205K
Cold Reservoir
ENGINEERING MODEL:
1. The contrel volume detined by the dashed line on the accompanying diagram undergoes a
refrigeration cyele.
ANALYSIS:
The meximuro coefficient of performance for a refrigeration cycle operating between two i
reservoirs is
279K _~ 6,875
. SISK-275K
PROBLEM 5.43 (Continued)
Coefficient of performance for any refrigeration cycle is
ede
(a) Given Qe = 1000 KI, Meyae = 80 kJ, the coefficient of performance determined using these
energy data is
|
{
i
i
tb) Given Qc = 1200 kJ, Gu = 2000 1, cycle work can be determined trom i
Woyte = Qu— Qc = 2000 kJ - 1200 kd = 800 kT i
\
|
The coefficient of performance determincd using these energy data is
1200K _ | 5 :
800k)
cle operates irreversibly.
(c) Given Qu = 1575 XJ, Myete = 200 KJ, heat transfer associated with the cold reservoir can be
determined from
Weyee = Qi - Oc + Qe = Qu— Weycte = 1575 kJ — 200 KI = 1375 kd é
‘The coefficient of performance determined using these energy data is
Since B= = 6.875, the evele operates reversibly. an
(d) Given f= 6, the cycie is irreversible.
Since 8=6 < Bou = 6.875, the cycle vperates irreversibly. —§ <———-—~
PRoGLEM 5.54
AL stendy state, « retrigeration cycle uperating between
hot and cold reservoirs at 300 K and 274 K, respectively,
qmbves citeryy by heat transfer {rom the wold seservoie c
4 rate of 600 kW,
(2) If the eyele's eoctficient of performance és 4, determine
the power input required, in kW.
©) Determine the mioimuni thcoreticul power required, in
KW, for any such eyete,
dvaursts:
5 - = Qe. Gooxw = 1SDKWW
ESS ap se = Se 2 Ga0KW -
mo PES Bo +
&)
S fais Geof Te Soften yy
BS Rudy => Waue? Here 27 PEE ]< ycle
wf 25K ] & Weyete
bone (28)
Ca)
ce)
By Weycle BSG. SRN
PROBLEM 5.67
5.67 By supplying energy at an average rate of 24,000 kJ/h, a heat pump maintains the
temperature of a dwelling at 20°C, If electricity costs 8.5 cents per kW-h, determine the
minimum theoretical operating cost for each day of operation if the heat pump receives
energy by heat transfer from.
(a) the outdoor air, at -7°C.
(6) the ground, at 5°C.
KNOWN: ‘A heat pump maintains the temperature within 2 dwelling under known
conditions.
FIND: Determine the minimum theoretical operating cost for each day of operation if the
heat pump receives energy by heat transfer from the outdoor air, at -7°C; and the ground
ar sec,
SCHEMATIC AND GIVEN DATA:
000 ki/h
W,
oyele
! Heat pump
, cycle
CoStacenicity = 8.5 cents/k Wh
ENGENEERING MODEL:
(1) ‘The system shown on the accompanying diagram undergoes a heat pump cycle in
steady state.
(2) The dwelling’s interior acts as the hot reservoir.
(3) The outdoor air and ground act as the cold reservoirs in parts a and b, respectively.
PROBLEM 5.67 (Continued)
ANALYSIS:
The coefficient of performance for the heat pump is less than, or equal to, the coefficient
of performance for a reversible heat pump operating between reservoirs at Te and Th. i
Then with Eq. 5.6 on a time rate basis and Eq. 5.11 we get. i
Vows 2
KI gare
(Fy 7) _ 28000 O95K—T)) ay 4
oe OT T 293K 3600s! is
“7, By
a)
‘The corresponding minimum theoretical operating cost for each day of operation is as
follows.
, 24h |$0.085|
2:
527 | Ae saoes °
Use Eqs. (1) and (2) to determine the minimum theoretical operating cust for each day of
operation if the heat pump receives energy by heat mansfer from different cold reservoirs.
(a) For a cold reservoir af To-7°C=266 K,
re)
24,000— (293K — 266K)
Woe RW cae
293K 3600sf 5 KI
‘oute =
8
30. a
1.254 —
KW: 5 = $1.25iday
s=(ocrsuw| #2 00)
(b) For a cold reservoir at 5°C=278 K,
kJ
34,000-— (293K -278K) th law
Woe 2- | 1 = 0.341 kW
ee 293K. 3600s; KS]
bos
$2 (034kw)—| 24 h [50.085] =$0.70/day _
I day KW
1. Owing to effects of irreversibilities, the daily operating cost of an actual heat purp
providing the specified heating will be significantly greater than the calculated
minimum values.