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Combined Nozzle and Blade Efficiency
( ) ( )0.931 0.836 0.778nb n bη η η = = =
Stage Efficiency
Assume an average loss from disk friction and fanning of 4% and from leakage of 1.5 %. Correcting for
tese effects gives!
( )( ) ( ) ( )1 " 0.778 1 0.04 0.015 0.735 st b Friction Fanning Leakage
η η η = − + = − + =
#et 0.73 st η = . $is is a rovisional value. &t 'ill (e modified as te design roceeds and more
recise information (ecomes availa(le.
Number of Stages
Ideal Available Energy to Blade
( )
( ) ( ) ( )
) ))
11406 "
39.5 ") ) 3).) 778
f s s m
m f
ft s Btu slbV h Btu lb
ft ft lblb∆ = = =
/
g g
g g
*se te ental+ at te given inlet conditions to te tur(ine and tat of te inlet to te condenser to get te
total isentroic dro in ental+!
( ) ( )1)93.7 9 0).9 390.8 " s mtotal h Btu lb∆ = − =
1.0465 R∞
= ,-eeat from a(ove gra
Trial Number of Stages, n
( ) ( ) ( )
( )
390.8 " 1.046510.35
39.5 "
m s total
m s
h R Btu lbn
h Btu lb
∞∆
= = =∆
/elect 10 stages ten correct for actual value of reeat!
( )1 1 0.73
1 1.0465 1 1 1.056510 0.)
R − = + − − =
Trial Isentropic Drop er Stage
1
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$e ental+ dro er stage is te total amount of actual ental+ cange in te tur(ine including te
reeat divided (+ te num(er of stages.
( ) ( )
( )
390.8 " 1.056541.3 "
10
m
s m
Btu lbh Btu lb∆ = =
$e trial value is 1.8 2tu"l(m greater tan 39.5 and 'ill cause a sligt increase in V 1 'ic 'ill (e
accounted for later.
Stage !e"eat, qr
ere 'e determine te amount of eat leak at eac stage.
( ) ( )41.3 1 0.73 11.15 "r s s st mq h h Btu lbη = ∆ − ∆ = − =
&f te desired final ressure ,0.491 sia is not reaced a ne' trial ∆h s and corresonding qr are found and
additional iterations run as needed. $o estimate te reuired cange divide te error in ental+ (+ te
num(er of stages and (+ te stage efficienc+ and ten add or su(tract tis uantit+ from ∆h s to get a ne'
trial value. After te correct value for ∆h s is found te final velocit+ triangles can (e constructed and
corresonding values calculated.
$e corrected value for V 1 is given (+!
( ) ( ) ( )1 )
) 41.3 " 778 3).)) 1438.49 "
m f
s s
f
Btu ft ft lb lb lbmV ft sh
Btu lb s
× ×= ∆ = =
× ×
( )11 0.965 1438.49 1387 "n sV ft sk V = = × =
from te velocit+ triangle W 1 is 873 ft"s and te (lade velocit+ coefficient is!
[ ] 916.0873,106,89).0 )"15
=−= − xk b
$is value is close enoug to te reviousl+ calculated value of 0.836. roceeding!
Total Internal #or$ er ound of Steam
mmr si lb Btulb Btuqhnw "5.301"15.113.41,10,, =−⋅=−∆⋅=
Internal Efficiency of t"e Turbine
301.5 " 0.7715390.8 "
mi
m
Btu lb Btu lb
η = =
%ec"anical &osses
Curc states te follo'ing roug rule for total mecanical losses including (earing friction and
gland um and governor resistances!
)
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ecanical loss in er cent at normal rating4 4
1.8"1000 5000 "1000kw
= = =
Assume a radiation loss of a(out 0.) % te com(ined mecanical and radiation losses amount to
a(out ) %.
Engine Efficiency, e
( ) ( )0.7715 0.98 0.756eη = =
Ideal Steam !ate
$e ideal steam rate reresents te mass of steam reuired to roduce a single kilo'att of o'er.
( )
( )
34138.73 "
390.8
mm
Btu lb ISR lb kWh
kWh Btu
/= =/
Bra$e Steam !ate
$e (rake steam rate corrects te ideal steam rate for te inefficiencies of te engine ,tur(ine.
( )8.73 " " 0.756 11.55 "m me BSR ISR lb kWh lb kWhη = = =
Turbine %ass 'lo( !ate
( ) ( )
( )
11.55 500016.04 "
3600
m
m
lb kWhm lb s
kWh s= =&
3
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%ollier Diagram
A ollier cart or an h s diagram offers a uniue descrition of te termod+namic interactions occurring
'itin te tur(ine. $e condition line details te termod+namic state rogression and is usuall+ dra'n
suerimosed on te ollier cart. &n order to construct tis cart it is useful to detail te state at eac ofte various stages. $is is most easil+ acieved (+ constructing a ta(le of te stage roerties.
$o construct te ta(le and from tere te ollier cart one must understand o' te termod+namic state
canges (et'een stages. All te ertinent information as alread+ (een determined. &t is siml+ a uestion
of organiation. $e state ta(le for te eamle in rogress is given on te follo'ing age. *sing a ta(ular
format 'e roceed in turn for eac stage to su(tract ∆h s from te entrance ental+ and ten add (ack te
reeat to determine te stage end oint. $e needed termod+namic state roerties including secific
volume are found as te rocess roceeds. &nitiall+ te state is fied and set (+ te inlet steam ressureand temerature. &t is ossi(le to determine te entro+ of te steam directl+. $en as te steam flo's
troug te first stage nole it goes troug an isentroic eansion. &t is ere tat te ental+ of te
fluid dros. $e amount of ental+ cange at eac stage is considered constant and as alread+ (een
determined. :no'ing te ne' value of te ental+ and assuming isentroic eansion it is ossi(le to
determine te ressure at te end of te nole.
/team ten flo's across te vanes on te 'eel 'ere it is reeated due to friction. $is rocess occurs
under constant ressure or iso(aric conditions. $us te increase in energ+ due to te eating is added tote revious value of te ental+. $e constant ressure assumtion fies te state and te resulting value
of entro+ can (e determined at te entrance to te nole for te net stage. $is rocedure is continued
and te values are ta(ulated until te total num(er of stages as (een comleted.
;nce te values of te ental+ and te entro+ are determined at eac stage it is ossi(le to lot tese
values on te ollier cart. $ese lotted values create te condition line and indicate te state
rogression of te steam troug te various tur(ine stages. $e aroriate ollier cart for tis eamle
is given on age 14. <</ 'ill roduce a roert+ lot automaticall+. $e ta(ulated ental+ and entro+
values can ten (e suerimosed on te lot using te =;verla+ lot> otion in te lot menu.
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5
Stage artEnt"alpy)BT*+lbm
Entropy)BT*+lbm-!
ressure)psia
1
?ole1)93.70
41.30 ,∆htrial
1.680 150
@eel1)5).40
11.15 ,qB 100.5
) N
1)63.55
41.30
1.69) B
W 1))).)3
11.15
B 65.0
3
N 1)33.40
41.30
1.705 B
W 119).10
11.15
B 40.9
4
N 1)03.)5
41.30
1.719 B
W 1161.95
11.15
B )4.5
5
N 1173.1041.30
1.734 B
W 1131.80
11.15
B 14.0
6 N
114).95
41.30
1.751 B
W 1101.65
11.15
B 7.8)
7
N 111).8041.30
1.768 B
W 1071.50
11.15
B 4.07
8
N 108).65
41.30
1.786 B
W 1041.3511.15
B ).10
9
N 105).50
41.30
1.806 B
W 1011.)0
11.15
B 1.0)
10 N
10)).35
41.30
1.8)6 B
W 981.0511.15
B 1.00 ,ing
<nd oint B 99).)0 1.847
$ermod+namic state ta(le for te stages of te steam tur(ine.
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ollier cart ,h-s diagram so'ing energ+ distri(ution 'itin te tur(ine.
6