steam turbine balance

7/23/2019 Steam Turbine Balance

1/56

Case -MCR

HP Process

RB

Sweet water

XXX process xxx H

Deaerator

xxx procress xxx H

Case -I


2/56

HP Process

RB

Sweet water

XXX process xxx H

Deaerator

xxx procress xxx H

Case -II

HP Process

RB


3/56

Sweet water

XXX process xxx H

Deaerator

xxx procress xxx H

Case -III

HP Process

RB


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Sweet water

XXX process xxx H

Deaerator

xxx procress xxx H

Case -IV

HP Process

RB

Sweet water


5/56

XXX process xxx H

Deaerator

xxx procress xxx H

Case -V

HP Process

RB

Sweet water


6/56

XXX process xxx H

Deaerator

xxx procress xxx H


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P[bar] h[kJ/kg]

t[C] m[t/hr]

65 3368.7

HP header

480 174.4

Spray water header

16.553 3045.4

304.7 5.8

eader MP Header

1.01 57.4

!!.!8 5.!55

7 863.4

08.5 84.8!

eader LP Header

P[bar] h[kJ/kg]


8/56

t[C] m[t/hr]

65 3368.7HP header

480 15!.4

Spray water header

16.83 3058.3

310. 14.55

eader MP Header

0.!!1 581.4

!!.38 5.764

7 877.3

14.8 8.13

eader LP Header

P[bar] h[kJ/kg]

t[C] m[t/hr]


9/56

65 3368.7

HP header

480 16!.4

Spray water header

15.6!4 303!.8

301. !.3

eader MP Header

0.5!! 56!.4

85.! 3.041

7 868.3

10.7 10.06

eader LP Header

P[bar] h[kJ/kg]

t[C] m[t/hr]

65 3368.7

HP header

480 130.67


10/56

Spray water header

4.113 31!!

380.6 3.8

eader MP Header

0.606 600

86. 3.07

7 !1.6

30.6 68.6

eader LP Header

P[bar] h[kJ/kg]

t[C] m[t/hr]

65 3368.7

HP header

480 1!.4

Spray water header


11/56

3.83 31!6.5

37!.3 3.84

eader MP Header

0.4!6 603.5

81.15 .!

7 !13.4

31. 74.3

eader LP Header

P[bar] h[kJ/kg]

t[C] m[t/hr]

65 3368.7

HP header

480 114.4

Spray water header

0.408 3156.4

358.4 4.1


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eader MP Header

0.68 63.7

67.!5 0.8!

7 !15.3

3.1 73.34

eader LP Header


13/56

0.103 316.6

46.6 58.!

C"#$e#s"r


14/56

0.10 34.6

46.15 56.!7

C"#$e#s"r


15/56

0.077 344.!

40.84 34.!!

0.078 368

C"#$e#s"r


16/56

40.!! 35.

0.07 38!.3

3!.48 8.!!

C"#$e#s"r


17/56

0.06 48.3

36.31 15.!8

C"#$e#s"r


18/56

C"#$e#s"r


19/56

P"%er 31&180 k'

()rst stage 510580!4 k'h

*e+"#$ stage 67506!16 k'h

,h)r$ stage 518874 k'h

("rth stage 117153660 k'h

eat "%er 354.6833 k'

+)e#+ 0.!58168 2

P"%er 8&!0 k'

()rst stage 4!53!88! k'h

*e+"#$ stage 56740 k'h

Cooling Tower#2


20/56

,h)r$ stage 41348050 k'h

("rth stage 108!15588 k'h

eat "%er 3054.3301 k'

+)e#+ 0.!558!63 2

P"%er 6&0 k'()rst stage 4815!818 k'h

*e+"#$ stage 18885!50 k'h

,h)r$ stage 181045!75 k'h

("rth stage !8!!7!3.6 k'h

eat "%er 74!!.43 k'

+)e#+ 0.!5347454 2

Cooling Tower#2


21/56

P"%er 1!&060 k'

()rst stage 363!8784! k'h

*e+"#$ stage 16418348! k'h

,h)r$ stage 1563138! k'h

("rth stage 7!13! k'h

eat "%er 053.447 k'

+)e#+ 0.!4107541 2

Cooling Tower#2


22/56

P"%er 17&70 k'()rst stage 35!775!4 k'h

*e+"#$ stage 143306!74 k'h

,h)r$ stage 137344!5! k'h


eat "%er 18!10.8756 k'

+)e#+ 0.!3706!5 2

Cooling Tower#2


23/56

P"%er 13&660 k'

()rst stage 30!03010 k'h

*e+"#$ stage !5108 k'h

,h)r$ stage !887015 k'h


eat "%er 14783.!47 k'

+)e#+ 0.!4015!4 2

Cooling Tower#2


24/56

Cooling Tower#2


25/56

C"a +"#eer

C"a t/hr

eat)#g V k/kg

eat )# 0 k'

Metha#e 0 m3/$a


26/56

0 m3/hr

eat)#g V 4!6 kJ/m3

eat )# 0 k'

,P 9P:16 ;)ese ") ta#k ' 100&170

(ee$ %ater t/hr

eat)#g V kJ/kg

>'

(ee$ %ater ta#k

;earat"r


30/56

"tt"m ash ( ash


31/56

:;IV/0

a


32/56

$"s)#g


33/56

? 2

,P 19P)e ag

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