REPORT OF
PROJECT SEMESTER TRAINING COMPLETED AT
G.H.T.P, LEHRA MOHABBAT WITH PROJECT- BOILER MAINTAINANCE
SUBMITTED IN PARTIAL PARTIAL FULFILLMENT FOR AWARD AWARD OF DEGREE OF
BACHELOR OF TECHNOLOGY IN MECHANICAL ENGINEERING BY
PARDEEP PA RDEEP SINGH (21003122)
MECHANICAL ENGINEERING SECTION YADA YA DAVINDRA VINDRA COLLEGE OF ENGINEERING ENGINEE RING PUNJABI UNIVERSITY, GURU KASHI CAMPUS, TALWANDI SABO 1!1302 (PUNJAB), INDIA MAY 201"
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ACKNOWLEDGEMENT A +$* *.7 5*.-6 & Er% D.S.BHU D.S.BHULLAR LLAR /5& +$*. '$66&. & =.$ +& G.H.T.P .P.. LEHRA MOHABB MOHABBAT AT% I /*6 5*.-4 $* $ *. ..+ .+ . G.H.T -4= = & Er. JASKARN U. $$ /5 /5&6 &6 += += *. *. I =. =.$ $/ /. . &= &=$$ $ $* *.. ..+ + *. 5 5* * * * * * 5 5 SINGH U. 44$.% I * .8 & 5 8*=6 /*6 5 /5&6 &.6*. 8*$$*+ &4 @=6&.6
-' &=$ +$*7 6 &=$ /&$-.+ &:$ *. 5'6 =6 4*5& 5 .$*6 &4 56 $*% M*.7 * '&6$6 87 5 +*: =6 4&& 4&$ 5&=+5% W /$ .+5. &. 5 '$** *6'6 &4 .+.$.+% A 5 +$*66 +$*66 $&& : : /$ 5 $* $* '&' '&' /5& 5 5' ' =6% T57 /$ /$ 5 *5. &'$*&$6, 5 654 I. 5*$+ *. &5$ /&$-. /5& '*. 5 /&$-.+ &4 * :*$7 &4 .6$=.6 *. 5 :*$&=6 5*.66 +&:$..+ 5$ &'$*&.% I /*6 5 .4&$* *- /5 5 /55 *=+5 =6 *.7 * .=*.6 &4 5 $*% I. 5 . I /&= - & +: * 8+ 5*.-6 & 5 /5& &4 5 G.H.T.P. LEHRA MOHABBAT 4*7 4&$ 5$ /5&5*$ 6=''&$ &/*$ 56 .*:&$ &4 &=$6%
BRIEF HISTORY OF GHTP E:$ /..+ +*' 8/. 5 '&/$ *. *. 6 *:**87 . 5 6* &4 P=.9*8 /*6 &. &4 5 8*6 $*6&.6 4&$ .:6*+.+ * 5$* '*. * L5$* M&5*88* D6% B*5.*% T5 &5$ 4*&$6 4*:&$.+ 5 .6**&. &4 56 5$* /$ &/ .* &6 *. 66 +.$*&. '$& *6 &'*$ & 57$& $ +.$*.+ 6*&., 6 +&& $*/*7 &..&. 4&$ 4*6 '$&7 & &* .$% T5 4&=.*&. &4 5 '*. /*6 * . 1>>! *. /*6 .* Gur G=$= $= H*$ H*$+&8 +&8. . Guru u Har Harg!" g!"#$ #$ T%& T%&r'a r'a(( P(a# P(a#)) % G= T5$* P*. 5*6 /& =.6 &4 6*+ I *5 &4 *'*7 210MW *. /& =.6 &4 6*+ II *5 &4 *'*7 2!0MW% T5 220KV6/5 7*$ *. 8&$ /*6 +5 =' 2. M*7 1>>< 87 Su*%$&+ S"#g% Ha#$a, M"#")&r Pu#/a! % T5 *= '&/$ &4 5 '*. 6
=6 . *+$==$ .=6$7 &* *. $=$* $4*&.% S*+ I T5 4$6 =. /*6 &66&. &. T5 6&. =. /*6 &66&. . &.
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1;10200? 3101200>
T5 '&/$ *:**87 4$& 5 '*. .&/ 6 202! &4 5 &* '&/$ $@=$. . P=.9*8% I 5*6 +&. * &.+ /*7 . =65$.+ '$&6'$7 . 5 6* 87 $+.+ * *$+ .=8$ .= 8$ &4 *+$ *+$ = == =$* $* '= '=' '.+ .+ 6 66 6,, & &$ $ . .= =6 6$ $* * & &.. .. & &.6 .6,, 100 100 $= $=$* $* $4*&., .$*6 '&7. '&.* $*87 *. '$&:. . &..=7 &4 6=''7 *. 676 :&*+ *. $&:* &4 '&/$ =6 & * +$* .% I 5*6 *6& & 4*6 :&'. & *8&= 3000 '$6&.6% T5 *. &'*.6 /5&6 5.&&+7 '*/ 5 /*7 &4 56 '*. *$ TA TAT TA H&.7/ BHEL . =$8. *. 8&$ &.$&% T5 4&&/.+ &.6$*&.6 5*: & 8 *. . * 84&$ 6&. &4 6 4&$ * '*. A:* ** *8 8 7 7 &4 4= 4= 6= 6=5 5 *6 & &* *%% A6 A65 5 6' 6'&6 &6* * 4* 4* 6 6%% S' S'** $@ $@=$ $ . .66% N*=$ &4 &4 *.% M& M&6 6 ' '&$ &$* *. . *:* *:* *8 *8 7 7 &4 &4 /* /*$$% A:* ** *8 8 7 7 &4 * *8& 8&$$% T$*. *.6' 6'&$ &$ 4* 4* 6 6%% P=8 P=8 S& S& 7 7 '$&8 '$&8 6 6 6= 6=5 5 *6 '& '&= = &. &.%% D D: :& &' '. . &4 &4 8* 8*-/ -/*$ *$ *$ *$**
GERNAL PROJECT INFORMAT I NFORMATION ION •
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B/. 12 12> - - *. *. 13 132 - - 6 6&.6 &. B* B*5.*, B*$.** R&* &. S* H+5/*7 N&% 12% H+56 +.$*&. =$.+ 200001 H H+5 +56 6 P%L% L%F F% =$ =$. .+ + M*$ M*$5, 5, 200 2001 1 L& L&/ /6 6 O O &.6 &.6= =' '& &. . =$ =$.+ .+ F8 F8,, 2001 2001 L&/6 D%M% /*$ *- =' =$.+ A=+=6, 2000 " " 2 21 210 MW "2 "20 0 MW (S S**+ I) •
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2 2!0 MW !00 MW (S*+ II) T&* C*'*7 >20 MW B*5.* B$*.5 O4 S$5. C*.* C&* 4$& N&$5 K*$*.'=$*% C&* 4 &4 C.$* C&* 4 L% A 6=86*$7 C&'*.7 &4 &* I.* L% L%D%O (L+5 D6 O) H%F%O (H*:7 F=$.* O) 210 MW *. 2!0MW 6.+ 65*4 $*&. =$8.6, *. &=' 3000 $' &=8 4&/ 5*=6, $5* 7' /5 .* '*$*$6 &4 1!0 -+6@%% A. !3!&C 2"< MVA, 1!%"MVA, 1;%! KV, 0%?! *+, !0 H, 3 '5*6, &=8 6*$ /& '&, H&$&.*, C7.$ $&&$ 7' S*+ I T5 4$6 =. /*6 &66&. &. 2>121>>< T5 6&. =. /*6 &66&. &. 1;101>>?
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0.1 GERNAL PROJECT INFORMATION
F"g. 2.1 G.H.T.P. THERMAL PLANT PRACTICAL OVERVIEW
3101200>
GERNAL PROCESS OF POWER GENERATION I. 5 +.$* '$&66 &4 '&/$ +.$*&. * +.$*.+ =. &4 5$* '*. &.666 &4 8&$ =., * =$8. =. /5 *66&$6 * +.$*&$ =. $*.64&$$ *. &5$ @='.6 * *$$*.+ & &'$* *6 &'.*$7 '*$6 &4 * &' &.&5 6% T5 &* $*:6 87 &.:7&$ 8 4$& 5 &* 5*..+ '*. & 5 8&$ 8=.-$6 4$& /5$ 6 4 .& '=:$.+ 6 /55 +$. 5 &* . & '&/$% T56 '&/$ &* 6 *$$ 4$& 5 87 6$* &4 *$ 4*. & 5 8&$ 8=$.$6, /5$ 6 8&/. . & 5 4=$.* *. 8=$.6 - * +*6% A 4&$ $*=+5 4*. '$&:6 *&.* &.$&*8 4*$ & 5 8=$.$6 & *666 &8=6&.% T5 '$&= &4 &8=6&. *$ =6 *. *65% T5 *65 4*6 & 5 8&& &4 5 8&$ *. 6 '$&*7 6= & 5 *65 6.+ '6% T5 =6 6 *$$ . 5 4= +*66 & 5 '$'*&$ /5$ 6 $* 87 5+5 :&*+ $&6% T5 =6 6 5. &.:7 & 6.+ &+&.6 &$ $&: 87 $& 4&$ 6*% T5 *$ 4: +*66 '*66 :* *. .= $*=+5 4*. & 5 5.7%
T5 5* $*6 87 8=$..+ 6 *86&$8 87 &.+ .+56 &4 =8.+ /55 4$& 5 8&$ /*6% I.6 5 =86, $7 '=$ /*$ -.&/. *6 8&$ 4 /*$ 6 &.:$ 87 5 5* . & 6* * 5+5 '$*=$ *. '$66=$% T5 6* 6 6='$5* . 4=$5$ =86 *. '*666 & 5+5 '$66=$ =$8. 8*6 *- 5 =$8. $&*&.% A4$ '*66.+ 5$&=+5 5 HP =$8. 5 6* 6 5. $=$. & 5 8&$ 4&$ $5*.+ 84&$ '*66.+ . & 5 .$* '$66=$ =$8. *. 4$& 5$ & &/ '$66=$ =$8. &=' & 5 =$8. 65*4 6 5 $&&$ &4 +.$*&$, * *$+ 7.$* $&*+. 6& 5* /5. 5 =$8. $&&$ $&*6 5 +.$*&$ $&*6 /5 % T5 +.$*&$ $&&$ .&6 . 5 6*&$ /55 &.666 &4 *$+ &6 &4 &''$ 8*$ . /55 $7 6 '$&= 87 5 $&*&. &4 5 *+. 4 $* 87 5 $&&
%$T5 $7 '*666 5 6*&$ /..+ & 5 $*.64&$$ /55 .$*66 6 :&*+ 6& 5* *. 8 $*.6 &:$ 5 '&/$ .6 . & 5 +$ 676% M*./5, 5 6* /55 5*6 5*=6 6 =64= .$+7 . =$..+ 5 =$8. 8*6 6 =$. 8*- . & /*$ . 5 &..6$ & 8 =6 *+*. . 5 8&$% B4&$ .$.+
5 8&$ * 5 &.&$ 5 /*$ '=' 87 &..6* $*&. '='6, 5* . LP 5*$, *$* . $*% I.$*6 . '$66=$ 87 5 8&$ 4 '=' *. 5* 4=$5$ . HP 5*$6% T5 /*$ 5$&=+5 5 &.&$ & 5 6* $=, 5. =' 5$&=+5 5 4=$.* /* =8.+ 84&$ $=$..+ & 5 6* $=+ 4&$ 6* &'$*&.% T5 6* *:6 5 $=+ *. 6 5* 4=$5$ . 5 6='$ 5*$ &. 56 /*7 & 5 HP =$8.% T5 C&..6$ &.*.6 =8.+6 5$&=+5 /55 5 & /*$ 6 &.6*.7 '='%
T%&r'a( P(a#) Pr3&
F"g. 4.1
COAL HANDLING PLANT 5
RECIEPT AND WEGHTMENT OF COAL6
C&* * GHTP $: 4$& C.$ C&* L *. E*6$. C&* 4 L &4 C&* I.* 866 '&$*. &* 4$& C5.*% O. $:.+ &*, 6 /+5 &. 5 $&. . &&. W*7 B$+% T5$ *$ 2 .=8$6 I. &&. /*7 8$+6% B&5 *. 8 '= .& 6$: * * % T5 6' &4 5 $*. =6 8 66 5*. 10 K5$% A4$ /+5. 5 $*- 6 : .& @=* 8*56 &.66.+ &4 *8&= 1! /*+&.6 . *5 8*5 4&$ =.&*.+%
F"g. 7.1
5 WEGON TIPPLER A4$ :*&. . 8*5 5 /*+&. 6 6. & 5 /*+&. ''$% H$ 5 &* 6 =.&* 4$& 5 /*+&. /5 5 5' &4 /*+&. ''$% T''$ 6 6+. *6 * /*7 5* / 4 5 /*+&. . *67 /*7% I. 56 5.6, * '*4&$ 6 = &= &4 5 6 &4 /*+&. -.&/. *6 ''$ *8% I 6 4 =' /5 5 5' &4 * 6$:& &&$ &...+ /5 * +*$ 8&% T5* +*$ 8& 6 &.. & * 65*4 5* 5*6 * +*$ **5 & , 6 &.. & * 5*.6 /5 ''$ *8% W5. 5 &*. 6 +:., 5 6$:& &&$ &'$*6 5 5.6% I 46 5 *8 *. =.&*6 5 /*+&.% T5 &* +&6 &. 5 A'$&. $&=+5 5 5&''
%$F"g. 7.8WEGON TIPPLER
5
COAL CONVEYOR6 C&* &.:7&$6 *$ =6 & &: &* *$&=. 44.7% C&* *$$:.+ 87 $*. *. 8 6&- 4&$ *$ =6 &$ *-. 6$*+5 & 5 &* 8=.-$6% CHP &.$& $&& /5 $& &.$& 676 5'6 & .6=$ 5* 5 &.:7&$6 *- 5 &* & 5 $+5 8=.-$6%
F"g. 7.0
5
CONVEYING SYSTEM6 A !&() 3#+&9r &.666 &4 /& &$ &$ '=76, /5 * &..=&=6 &&' &4 *$* 5 &.:7&$ 8 5* $&*6 *8&= 5% O. &$ 8&5 &4 5 '=76 *$ '&/$, &:.+ 5 8 *. 5 *$* &. 5 8 4&$/*$% T5 '&/$ '=7 6 * 5 $: '=7 /5 5 =.'&/$ '=7 6 * 5 $% T5 /5 &4 5 8 . G%H%T%P% 6 2000%
5
CRUSHER HOUSE6
C&* =.&* 87 5 /*+&. ''$ 6 *$$ & $=65$ 5&=6 5$&=+5 &.:7&$6 4&$ $=65.+% T5$ *$ /& 7'6 &4 $=65$ . G%H%T%P% *6 +:. 8&/ 5
R)ar9 !r&a*&r :;r"'ar9 3ru%&r<.
Rotary Breakers are used in the primary and secondary reduction of ROM coal and in the separation of rock and mine refuse. This is accomplished through the tumbling action of the rotating drum, which lifts and drops the feed material repeatedly until the coal breaks down and exits the drum through the screen plate perforations while the rock and refuse moe through and are re!ected at the discharge end.
F"g. 7.2 ROTARI BREAKER
TECHANICAL DATA Type roller mounted
"
#$%&$
%$'eight
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($ MT
)apacity
"
*+MT-hr
Material input sie
"
+mm
Material output sie
"
#$+mm
Motor rating 2#+ olt 3os.
5
"
#/ 01, "
R"#g gra#u(a)r :&3#$ar9 3ru%&r<
F"g. 7.4RING GRANULATOR
$
TECHANICAL DATA T7'
TRM!"
C*'*7
1000T5$
M*$* .'= 6
300 (*)
M*$* &='= 6
2!
M&&$ $*.+
<3
N&6%
2
T5 $=65$ 5&=6 *&&*6 5 65*$+ .6 &4 5 &.:7&$ "A, "B $:.+ .6 &4 &.:7&$ !A, !B *. &.:7&$
5
STACKING = RECLAIMING6
F"g. 7.7 COAL STACKING AREA
I. &* 6*-.+ *$* $=65 &* 6 6&$ 4&$ $+.7 (/5. .& &* &6 & '&/$ '*.)% H$ * &. &4 &* 6 6&$ /5 5 5' &4 * 5*:7 *5. -.&/. *6 )a3*&r % I &.*.6 * 8=- /5, /5. .& &* &6 & 5 '*. 5. 87 5 $:$6 $: 56 8=- /5 $* 5 &* *. & 5 8=.-$6%
7.>STACKER
5
TROLLEY6
T''$ $&7 6 =6 & 4 5 8=.-$6 /5 &* &.+ &. 5 &.:7&$ 4$& 5 &* 5*..+ '*.% T5$ *$ 4&=$ $&76 . GHTP * 5 5+5 &4 !3 %
F"g. 7.? TROLLEY 5
BUNKER6 I 6 * :$7 8+ 7.$* $=% I 6 =6 & 6&$ 5 &* /55 &6 4$& 5 CHP% I 5*.+ * 5 5+5 &4 !3 '* $+5 *8&: 5 $*/ &* 4$ *. &.. /5 87 * *$+ *% P'% 0ard coal and brown
coal are the main energy carriers in coal45red power plants. 6eliered by ship or by train, the coal is unloaded into bunkers up to 7 m high. The coal is transported from these bunkers to the stockpiles of the power plant ia oer ground or underground coneyor belt systems. 8dditional coneyor belts feed, often ia intermediate bunkers, purlerier mills where the coal is conerted into a 5ne dust for subse9uent combustion in the furnace. Reliable leel measurement guarantees uninterrupted feeding of the furnaces and point leel sensors preent oer5lling in the bunkers.
F"g. 7.@ COAL BUNKER
RAW COAL FEEDER I. GHTP L5$* M&5*88* RC F$ *$ =6 4&$ &.$& 5 C&* *. 56 4$ 4 5 &* & B&/ 6 *. B&/ 6 *$ G$.$ 5 C&* *. C&.:$ .& '&/$ 65*'% T$*.6'&$ &* 4$& RC B=.-$ & &* 87 8 &.:7&$ 5*:.+ $: &&$ &.. /5 7.*$: & &.$& 5 &* 4% RC B=.-$ ; .&6% &. 4&$ *5 RC 4$ 4*8$* 4$& 65 * 5*:.+ *'*7 &4 ;!0 T&.6 *''$&% 5*: 8. '$&:%
F"g. 7.1 RAW COAL FEEDER RC F$ *$ ; 4&$ *5 =. " RC 4$ /&$- * * *. 2 6 6*. 87 '&6&.% I. GHTP 5 RC F$ 6 &.$& 5 &* 87 * &.:7&$ 8 *. 6 &'$* 87 3 '5*6 $ &&
%$5
COAL FEEDER6
T5 :*$*8 6' &* 4$ 46 &* 4$& 5 8=.-$6 & 5 % I =66 * &.:7&$ & &: &* 5$&=+5 * 4 +*' * * '$67 &.$& 6'% V*$7.+ 5 6' &.$&6 5 *&=. &4 &* 6='' & 5 8&$6% T56 *$ '$6&. 86 &4 @='. 5* 5*: & &: * *&=.6 &4 &*% T57 *. &: ;!0 T&.6 *''$&% &4 &* . *. 5&=
%$
F"g. 7.11 3a( &&$ 9. COAL PULVERISING SYSTEM A GHTP B&/ M6 5*: 8. .6* 4&$ '=:$.+ 5 $*/ &*% C&* &4 *= 6 &4 2! 6 $: . R*/ C&* B=.-$6 4$& Ca( Ha#$("#g P(a#)% F$& 5 B=.-$, 56 &* 6 4 .& 5 5$&=+5 R*/ C&* F$% T5 4 & 5 &* *. 8 &.$& 87 $+=*.+ 5 6' &4 5 F$% I. '*. &* 2" B&/ 6 *$ =6 *5 =. =6 &.7 " B&/ 6 *. 2 B&/ M6 *$ 6*. 87 '&6&. S&, * &. " B&/ M6 *$ R=...+ C&.&.%
T7' &4 P=:$6$ BOWL MILL C&* '=:$.+ *'*7 M&&$
#RP?03, 3;%> T&.5$, 3"0KW, ;%;KV
PARTS OF BOWL MILL
5
MILL BASE6
T56 6 5 &/6 '&6&. &4 *. &.*.6 $: 676 %% /&$ 65*4, & &&$ *6 *. '*$6% T5 +*$ H&=6.+ 6 */*76 4 /5 =8$*&. & 84&$ 5 '=:$ 6 '= .& &'$*&.% L: &4 5 & *. 8 5- 4$& 5 & : +*=+ '$&: &. 5 8*6% C&$$ : 6 .* &.7 /5 5 6 % F&$ &&.+ 5 & /5 6 . &'$*&., T=8 7' /*$ &&$ 5*: 8. .6* . 5 G*$ H&=6.+%
5
MILL SIDE6
T56 '&$&. 6 9=6 *8&: 5 8*6 *. &.*.6 6 .$6, S$*''$ *6687 *. T$*' $&. 6'&= 65*$+ *$$*.+. :*. /5 *6687% H* '$*$7 *$ .$6 5 6 5&=6.+ 8&/ 5 B&/% A.7 $*' $&., 6&. % $&' . 56 '&$&. *. *$ 6$*'' & 5 $*' $&. 65*$+ 6'&= 4&$ '.+ . 5 M R9 B%
5
MILL OUTLET ASSEMBLY6
T56 '&$&. &.*.6 *664$ :.=$ *. 4&$ $+=*&$% M 65*$+ :*: *6687 6 &.. * 5 &' &4 56 '&$&. 4$& /5$ 5 '=:$ &* 6 *+. & *5 &4 4&=$ &* .&6 * &. :*&.%
5
SEPARATOR BODY ASSEMBLY6
T56 '&$&. 6 9=6 *8&: 5 6 5&=6.+ *. 56 6 5 '&$&. /5$ &* 6 '=:$% M*. '*$6 &4 56 *6687 *$ B&/, J&=$.* *6687, G$..+ R& A6687 B= $.+ 6+.6, .$6, I..$ &., *664$ *6687, S'*$*&$ 8&7 .$ *6687 *. .$ 4 ''% T5 G$..+ R&6 & .& $&* 4 5 66 6 '7% W5. 5 $*/ &* 4$& .$ 4 '' &6 . 8/. 5 G$..+ R&6 *. $:&:.+ 8&/, *=66 5 $&6 & =$. *. 5=6, 5 &* +6 '=:$%
F"g. 17.18 S&;ara)r
F"g. >.1 BOWL MILL
MILL LUBRICATION
I. &* '=:$ 676 8&/ 6 =6 & '=:$ 5 &*% I. 56 676 = & 5 4$&. . 5 *.+ '*$6 6*$6 $&6% T& .* 5* 44 5 =8$*. 6 &.% I 6 &. . 5 64 $&*.+ $&$ *. =.$ 5 8&/ '*, 8*$.+6 *$ *6& '$&: 5$ & .* 5 %
F"g. >.8 MILL LUBRICATION SYS.
COAL TRANSFER SYSTEM TO BOILER
F"g. >.0 COAL PATH TO BOILER PARTS OF COAL TRASPOTATION TO THE BOILER6
COAL BUNKER
COAL FEEDER
BOWL MILL
TRANSFER PIPE
5
FURNANCE
DM PLANT
RAW WATER TREATMENT
T5 @=*7 &4 /*$ . 4&$ .=6$6 '.6 ='&. 6 .. =6% U$* 5+5 '=$7 W*$ 6 $@=$ 4&$ 5+5 '$66=$ 6* +.$*.+ 676% T5 /*$ '=$6 *. $6= . 6$&=6 &'$*.+ '$&86 *=6 87 '&6 4&$*&.% C&$$&6&. &4 *% F&*.+ . 6* +.$*.+ $& 8&&+* 4&.+ /&& $&$*&. . &&.+ /*$ 676%
T5 *:$*+ $*/ /*$ @=*7 * GHTP L5$* M&5*88* 6 *6 8&/
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100''
30
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!0
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30'' *6 C* &3
20
T&* H*$.66 12''
120'' *6 C* &3
<0
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13"'' *6 C* &3
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M*+.6= H*$.66 "0''
"0'' *6 C* &3
20
D66&: S*
!'' *6 C* &3
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C&&* S*
1''
12''
T&* 66&: S&6 *6 6=5 200''
200''
1!0
T&* 6=6'. S&6 !0''
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30
Water Treatment Consists of:
5
CLARIFICATION6
I 6 * '$&66 *'' & 6=$4* /*$ 4&$ $&:* &4 6=6'. 6&6, 4.$ 6&6 /55 *''*$6 *6 =$87, &&$ &5$ &&* *$*6% T56 '$&666 .&$'&$* &*+=*&. 4&=*&. 6.*&. *5 6 * 6. '$&=$ /55 *.* $*. $@=$.6 & .6=$ 5 6$ $6=6% A GHTP L5$* M&5*88* / *$ 5*:.+ &. .&% *$4$ 5*:.+ *'*7 3?00 M 5$ 4&$ &&.+ /*$ 676 *. * 1?0 M35$ 6=+ 8*.- 4&$ 5 &'$*&. &4 D%M% P*.% 3
F"g. ?.1 CLARIFIER
DM PLANT I. GHTP L5$* M&5*88* &.7 &. DM P*. 6 =6 4&$ $*/ /*$ &.:$ 5 DM W*$ *. 56 /*$ 6 =6 . 8&$ 8*=6 5 /*$ 6 :$7 '=$ *. 56 /*$ PH @=*7 6 :$7 6=*8 4&$ 6*% T5 /*$ 6 5 * =' . 66 *. 8&$ &'= 6 4$ 4$& &$$&6&.%
F"g. ?.8 DM PLANT OVER VIEW
'a*& u; DM a)&r !9 GHTP
BOILER FEED PUMP E*5 '=' 6 &.666 &4 * FA IB 47 B)&r Pu'; , $7 $: 4$& &. . &4 5 65*4 &4 *. $* $:.+ &&$, *. * FK 7D 0 B"(&r F&&$ Pu'; $:. 4$& &''&6 . &4 5 &&$ 65*4 5$&=+5 * :*$*8 6' Tur! Cu;("#g )9;& R17K.1 % T5 $: 6 $*.6 . *5 *=6 5$&=+5 * 6'*$ 7' 48 &='.+ *5 &='.+ 8.+ .&6 . * 6' 4*8$*&. +=*$%
F"g. @.1 BOILER FEED PUMP
5
BOILER FEED PUMP6
A 8&$ 4 /*$ '=' 6 * FK7D0 7' &4 '=' =6 & '=' 4 /*$ .& * 6* 8&$ % T5 /*$ *7 8 4$657 6='' &$ $=$..+ &..6* '$&= *6 * $6= &4 5 &..6*&. &4 5 6* '$&= 87 5 8&$% T56 '='6 *$ .&$*7 5+5 '$66=$ =.6 5* =6 6=&. 4$& * &..6* $=$. 676 *. *. 8 &4 5 .$4=+* '=' 7' &$ '&6: 6'*. 7'%
T5 FK7D0 TYPE B"(&r F&&$ Pu'; 6 * 6 6*+ H&$&.* .$4=+* '=' &4 8*$$ *6.+ 6+.% I.$ 6*+ *' &44 6 '$&: 4&$ PRDS *. R5*$ 6'$*7 4$& 2. 6*+%
F"g. @.8 GENREL LEYOUT OF FEED PUMP
TECHANICAL DATA OF BOILER FEED PUMP
P=' 7' N&% &4 6*+6 D$&. &4 $&*&.
FK;30 ; (S) A. &- /6 (V/ 4$& $:. .) B&$ F W*$ 1;1%3&C >0;%1 K+= "
L@= '=' S=&. '$*=$ S'% W% A 6=% T'% D6+. 4&/ D44$.* 5* M., RC 4&/ E44.7 S' I.'= '&/$ I.$ 6*+ 4&/
G*$ M* C&%, U%K% D&=8 5$=6, CK $*.+ ?1!>2KP2KP
T%ru) !&ar"#g6 M*.=4*=$$ T7' S
Cu;("#g !&)&&# H9$rau("3 3u;("#g ;u';6 M*.=4*=$$ T7'
B5*$* F&$+ L%, I.* HBS 1000?#
Cu;("#g !&)&&# H9$rau("3 3u;("#g M)r6 M*.=4*=$$ T7' T7'
B5*$* F&$+ L%, I.* HBS 3;00?
V&5 T=$8& GMBH *. C&% R 1; K% 1
B%H%E%L% SCIM
H9$rau("3 3u;("#g6 M*.=4*=$$ T7'
Dr"+& ')r6 M*.=4*=$$ T7'
R*.+ S' E$* S=''7
"000 -W 1"?! $' ;%; -V, 3'5*6, !0 H
BOILER FEED BOOSTER PUMP T5 B&&6$ 6 * 6.+ 6*+ 5&$&.* ** 6' *6.+ 7' 5*:.+ 5 6=&. *. 65*$+ 8$*.56 &. 5 *6.+ 8&& 5*4 5=6 *&/.+ 5 '=' .$.*6 & 8 $&: /5&= 6=$8.+ 5 6=&. *. 65*$+ '' /&$- &4 5 *+.. 8/. 5 '=' *. &&$% T5 '=' 65*4 6 6* * 5 $: . *. .&. $: . 87 5*.* 6*6 /55 *$ 4=65 87 * 6=''7 &4 *$4 /*$% T5 $&*.+ *6687 6 6=''&$ 87 '*. /5 * . 9&=$.* 8*$.+ *. **7 &* 87 * G*$ &=8 .+ '* 5$=6 8*$.+
A''*&. B&&6$ '='6 *$ =6 & *$ 5 $@=$.6 &4 B&$ 4 '='6 6=&.% T57 *$ $:. 87 5 *. BFP $: &&$ /55 5*6 65*4 .6&.6 &. 8&5 .6%
D6+. 4*=$6
H&$&.* 6.+ 6*+ &.6$=&.
A*7 6' *6.+ (:&= 7')
D&=8 6=&. '$
L&/ NPSH $@=$.
T.+ '* 7' 5$=6 8*$.+
M5*.* 6*6
TECHANICAL DATA OF BOOSTER PUMP
T7' &4 '=' :&=
S.+
6*+,
7' /5 H&$&.* 6' *6.+
N&% &4 '='6 $@=$ '$ *5 =$8& 6
21
R* 6'
1"?3 $'
D6+. 4&/
"
H* :&'
103
E44.7
I.'= '&/$
1"; -/
D$&. &4 $&*&. &4 5 '=' &- /6
&&$ 6) T7' &4 9&=$.* 8*$.+6 8=65 8*$.+ N&% &4 8*$.+6 5$=6 T7' &4 =8$*&. =8$*&. S=&. T'% NPSH $@=$ T7' &4 &='.+ &='.+ &4 *'5$*+ 6+. M5*.* S* T7' !03 M*.=4*=$$ S*& F8 &='.+ T7' M*.=4*=$$ L% T5$=6 8*$.+ T7' M*.=4*=$$
A. (V/
4$&
B*88
.
2 9&=$.* 1 8*$.+ F&$ O
1;0%?& C ;%00 F8
"%2!
D=$* *
HB"1"0# B5*$ F&$+
?1122KP2KP
MS G*$
PTO
B&$ 4 '=' *-6 6=''7 &4 /*$ 4$& D*$*&$ *. 6=''6 & B&$ D$= *+*.6 5 '&6: '$66=$ . 5 $=, 5 6=''7 &4 /*$ 6 $+=* 87 ::6 4 *.4& 6*&. *. 6&&' =8 &4 5 '='% F &.$& 6=&. 5*6 M*. . B7'*66 . L&/ &* .
(100) (100) (30)
S&&' =8 :*$*&. 6 4$& 30 & 100
STEAM GENERATOR T5 6* +.$*&$ 6 &4 $**., $5*, .*=$* $=*&. 6.+ $=, $7 8&& *. 6&=&&$ 7' =., 6+. 4&$ 4$.+ &* *6 5 '$.'* 4= *. 5 HFO & 4$.+ *'*7 6 @=:*. & 22%! 8&$ MCR% "LDO 8=$.$6 *$ *'*8 4&$ <%! 8&$ MCR 5* .'=% AS '$ *7&= *$$*.+. 5 6 *$ &* 8/. B&$ *. ESP6% T5 &' 4=$.* 6&. 6 &4 4=6&. / /* 7' *$$*.+ *6 * +*6 *. '$66=$ +5 .:&'% T5 . 6 /* 6&. 6 &:$ /5 /*$ && 4. / /*6% T5 *= 4= +*6 :&7 . 5 '$66=$ '*$ 676 6 & 10 12 6% A 100 8&$ MCR &*%
F"g. 1.1 STEAM GENRATOR
A 5 5*$6 . 5 '$66=$ '*$ 676 *$ '$&: /5 .66*$7 5*. 5&6 *. 5*. 5&6 '*6 *$$*.+.% A 5*$6 *$ &* &=6 5 +*6 '*5, ' 4&$ 5 &.&$ . *. .$* 5*$6 /55 *$ &* . 5 &/ +*6 '$*=$ 6&. . 2. '*66% T5 &' '$66=$ '*$6 *$ 6=6'. 4$& 5 8&$ 6$==$* 6 $&&4 6&.6 *. *$$*.+ 4&$ 4$ '*.6&. &/./*$%
F"g. 1.8 STEAM GENRETOR DETAIL DEGINE
BOILER B&$ =6 . 5 5$* '&/$ '*. 6 /*$ =8, .$.* &8=6&., &* 8*6% T5 5+5 &4 8&$ 6 * GHTP 6 STAGE1 6 .*$ *8&= !; *. STAGE2 6 ;1% 5
6* = 6 &* * 5 5+5 &4 !" * STAGE1 *. !> * STAGE2%
5
SUPERHEATER 6
M&6 &4 5 &$. 8&$6 *$ 5*:.+ 6='$ 5*$ *. $5*$ *$$*.+.% S='$5*$ 6 * &'&.. &4 * 6*+.$*.+ =. . /55 6*, *4$ 5*6 4 5 8&$ $=, 6 5* *8&: 6 6*=$*&. '$*=$% T5 *&=. &4 6='$5* * & 5 6* 6 .4=. 87 5 &*&., *$$*.+., *. *&=. &4 6='$ 5*$ 6=$4* .6*, *6 / *6 5 $*.+ &4 5 8&$% T5 6='$ 5*$ *7 &.66 &4 &. &$ &$ 6*+6 &4 =8 8*.-6 *$$*.+ & 44:7 $*.64$ 5* 4$& 5 '$&=6 &4 &8=6&.% S='$ 5*$6 *$ *664 *6 &.:&., $**. &$ &8.*&. &4 56%
5
REHEATER 6
S& &4 5 5* &4 6='$5* 6* 6 =6 & $&* 5 =$8. /5$ &66 6& &4 6 .$+7% R5*$ 6 *6& 6* 8&$ &'&.. . /55 5* 6 * & 56 .$*'$66=$ 6*, /55 5*6 +:. =' 6& &4 6 .$+7 . '*.6&. 5$&=+5 5 5+5'$66=$ =$8.% T5 6* *4$ $5*.+ 6 =6 & $&* 5 6&. 6* =$8. /5$ 5 5* 6 &.:$ & 5*.* .$+7% T56 5*.* .$+7 6 =6 & $=. 5 *$.*&$, /55 6 &=' & =$8., 5$ 87 +.$*.+ $* .$+7%
5
ECONOMISER 6
F= +*66 &.+ &= &4 5 8&$ *$$7 & &4 5*% F=.&. &4 &.&6$ 6 & $&:$ 6& &4 5 5* 4$& 5 5* *$$ */*7 . 5 4= +*66 =' 5 5.7 *. = 4&$ 5*.+ 5 4 /*$ & 5 8&$% I 6 '* . 5 '*66*+ &4 4= +*66 . 8/. 5 4$& 5 8&$ *. 5 .$7 & 5 5.7% T5 =6 &4 &.&6$ $6=6 . 6*:.+ . &* &.6='&., .$*6 . 6*.+ $* *. 5+5 8&$ 44.7 8= .6 $* .:6. *. .$*6 . *..*. &66 *. 4&&$ *$* $@=$ 4&$ 5 '*.% T56 6 =6 . * &$. '*.6% I. 56 * *$+ .=8$ &4 6* *$ 5. /* =86 *$ '* 8/. /& 5*$6% F /*$ .$6 5 =8 5$&=+5 &. 5*$ *. *:6 5$&=+5 5 &5$% T5 4= +*66 4&/ &= 6 5 =86 =6=*7 . &=.$ 4&/%
5
AIR PREHEATER 6
T5 $*..+ 5* &4 4= +*66 6 = 87 *$ '$5*$% I 6 * : =6 . 6* 8&$6 & $*.64$ 5* 4$& 5 4= +*66 & 5 &8=6&. *$ 84&$ 5 *$ .$6 5 4=$.*% A6& -.&/. *6 *$ 5*$ *$5*.+ 676% I 6 .& 65&/. . 5 *7 &=% B= 6 -' * * '* .*$ 87 /5$ 5 *$ .$6 . & 5 8&$% T5 '=$'&6 &4 5 *$ '$5*$ 6 & $&:$ 5 5* 4$& 5 4= +*6 4$& 5 8&$ & '$&: 8&$ 44.7 87 8=$..+ /*$ *$ /55 .$*66 &8=6&. 44.7, *. $=.+ =64= 5* &6 4$& 5 4=%
5
DEAERATOR 6
A 6* +.$*.+ 8&$ $@=$6 5* 5 8&$ 4 /*$ 65&= 8 :& &4 *$ *. &5$ 66&: +*66, '*$=*$7 &$$&6: &.6, . &$$ & *:& &$$&6&. &4 5 *% G.$*7, '&/$ 6*&.6 =6 * D*$*&$ & '$&: 4&$ 5 $&:* &4 *$ *. &5$ 66&: +*66 4$& 5 8&$ 4 /*$% A D*$*&$ 7'*7 .=6 * :$*, & *$*&. 6&. &=. &. &' &4 * 5&$&.* 7.$* :66 /55 6$:6 *6 5 *$* 8&$ 4 /*$ 6&$*+ *.-% T5$ *$ *.7 44$. 6+.6 4&$ * D*$*&$ *. 5 6+.6 / :*$7 4$& &. *.=4*=$$ & *.&5$% T5 *9*. *+$* '6 * 7'* &.:.&.* D*$*&$% I4 &'$* '$&'$7, &6 D*$*&$ *.=4*=$$6 / +=*$*. 5* &7+. . 5 *$* /*$ / .& < ''8 87 /+5 :.4 3'=L<.
F"g. 1.0 DEAERATOR
TECHANICAL DATA OF BOILER
F=$.* W* S76 J&.
O%D%
N&%
T7'6 &4
F$&. W*
;3%!
1?1
F=6&.
R*$ W*
;3%!
1?1
F=6&.
;3%!
131
F=6&.
;3%!
2;
F. /
S W* ('$ 6)
E. W* ('$ 6)
F=$.* W5
13?;?
F=$.*
10!>2
F=$.* :&= (A''$&%)
!200 3
F=$.* *$* 44: '$&9
2100 2
R5*$
F$&.
R*$
N&% &4 *6686
!>
!>
N&% &4 .*6687
;
;
T=8 O%D%
M*$*
!""
!"3%;
;0%3"
""%!"
SA213T11 ( Q C$ MO ) SA213T22 ( 2 C$ MO ) SA20> T1 ( Q MO ) SA 213 T>1
FILLING CAPACITY B&$ D$= E&.&6$ W*$ W* S='$ H*$6 R5*$ W*$ $@=$ 4&$ .&$* +5 =' F&$ H7$&6* 6
3! T&. 2! T&. 130 T&. >! T&. !0 T&. 1>0 T&. 33! T&.
SUPER HEATER D6$'&.
F=$.* R&&4 /
B*- '*66 R&&4
B*- '*66 4$&.
O%D%
N&%
!1%0
120
""%! ""%!
T7' F. 120
>?
B*- '*66 R*$
""%!
B*- '*66 S('$ 6)
""%!
;;
B*- '*66 .('$ 6)
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1<
M*$* 4&$ *8&: MO)
C*$8&. S (!*210 GC), SA20>T1(Q SA
120>(U''$L&/$)
210
G
%$C*$8&.
6
ECONOMIER
N&% &4 *6686
O%D% 6
1"! N&% ""%!
DRUM
M*$* C*$8&.
I%D%
1<
BOILER PARAMETERS
S='$5*$ &= S* 4&/ (MCR)
;>0
TH$
S* P$66=$ * SH% O=
1!! K+C2(G)
S* '$*=$ * SH% O=
!"0 C
R5*$ &= 6* 4&/
!><%! TH$
S* '$66=$ * RH% I. K+C2(G)
3<%;
S* '$66=$ * RH% O= C2(G)
3;%1
S* '$*=$ * RH% I.
3"2& C
S* '$*=$ * RH% O=
!"0& C
F /*$ '$*=$ .$.+ &.&6$
2"3& C
A8. *$ '$*=$
"0& C
K+
BOILER AIR AND GAS SCHEME
A$ 4&/ 6 $@=$ . 8&$ *.7 4&$ /& '=$'&66
F&$ 5 &8=6&. &4 4= . 4=$.* 56 *$ 6 * 6&.*$7 *
%$
F&$ $7.+ *. $*.6'&$*&. &4 '=:$ &* & 5 4=$.* 4$& 5 * P$*$7 A$ F*.%
S&3#$ar9 A"r S&.*$7 *$ 6 6='' 87 /& 4&$6 $*4 4*.6 *$ +:. 8&/
FORCED DRAUGHT :FD< FAN6 E*5 =. 65* 5*: /& 4&$ $*=+5 4*.6% T5 4*.6 $*/ /*$ *$ 4$& 5 &' &4 5 8&$ 5&=6 5$&=+5 *$+ *$ 5*$6 8&.+ 5 '$*$7 *. 6&.*$7 *$ =6 4&$ 5 8&$ &8=6&. '$&66% T5 *$ 5*$ /*$6 5 .&.+ *$ 87 $*.64$$.+ 5* .$+7 4$& 5 &=+&.+ 4= +*66
F"g. 11.1
INDUCED DRAUGHT :ID< FAN6 T/& .= $*=+5 4*.6 $*/ +*66 &= &4 5 8&$% T5 +*6 5*6 *$*7 '*66 5$&=+5 5 *$ 5*$6 *. '$'*&$6 84&$ 5*6 $*5 56 4*.6% T5 5* 4$& 5 4= +*66 &$ 6&- 6 =6 . 5 *$ 5*$6 & 5* =' 5 '$*$7 *. 6&.*$7 *$
F"g. 11.8
TECHANICAL DATA
T7' &4 &'$*&. N&% &4 4*.6 87)
C&..=&=6 3 '$ 8&$(2$=...+, 1 6*.
T7' &4 &'$*&. O$.*&. C*'*7 T&* 5* :&' T'% &4 = S' M&&$ P&/$ E$ 6=''7 S'
F= G*6 E5*=6 H&$&.* 230 M36 3!0 1!0& C >>0 $'
1300 -W ;%; -V >>0 $'
PRIMARY AIR FAN6 E*5 =. 65* 5*: /& '$*$7 *$ 4*.6% A$ & 8&/ 5 &* 4$& 5 & 5 8&$, * 5 '$*$7 *$, 6 6='' 87 * *$+ 4*. $:. 87 * :*$*8 6' &&$% W5. /5 * 6$* &4 *$ 5 '&/$ &* 85*:6 &$ - * +*6 5*. * 6&% P$*$7 *$ &6 /& 9&86 5*.+ 5 &* '&/$ *. 6&.7 4.+ .& 5 4=$.* 5$&=+5 ''.6 PARTS OF PA FAN6
S*&$ R&&$ C&='.+ D$: L&' 676
TECHANICAL DATA
T7' &4 &'$*&.
C&..=&=6
N&% &4 F*.6
T/& '$ 8&$
M= 5*.
A&6'5$
O$.*&.
V$* 6=&. 5&$&.* :$7
F*. C*'*7
<0 M36
T&* 5* :&'
1210
S'
1"?0 $'
T'$*=$
!0& C
M&&$
12!0 -W
P&/$
8&&
E$ 6=''7
;%; -V
S'
1"?0 $'
B"(&r ("g%)-u; B&$ +5=' *.6 5 6*$.+ &4 5 8&$ &$ 4*.+ 5 4=$.*% T5$ *$ /& 7'6 &4 8&$ +5 =' 676%
C& +5='
H& +5='
5
C($ ("g%)-u;
W5. 5 8&$ 6*$6 =' *-6 * *% '$*=$% A 56 4$6 L%D%O(+5 6 &) 6 +:. & 5 4=$.* /5 5+5 '% 6*% T5 $*6&. & +: 5 6* 6 5* 8*=6 * *% T'% 5 6* &4 L%D%O% 6 5*$% 6& & @=47 5 & 6* 6 +:. & % T5 & 6 6. & 5 4=$.* /5 5 5' 4 & +=.6% N*$ 5 ' &4 5 & +=. * +5$ &$ 6'*$- '=+ 6 '$&:% W5. 5 & 6 4 & 5 4=$.* 5. +5$ 6 +. *. & *56 5 4$ *. 6*$6 8=$..+% A4$ '$&'$ 8=$..+ 5 H%F%O%(H& 4=$.* &) 6 4 & 5 4=$.* *. H%F%O% 6 6&''% A4$ 5* 5 '=:$ &* 6 4 & 5 4=$.* *. &8=6&. 6*$6%
5
H) ("g%)-u;
W5. 5 8&$ 6*$ =' *-6 '* *4$ * $' *6 5* 5 '% &4 5 8&$ 6 6=44. & 6-' 5 4$6 6' &4 H%F%O% *. $7 L%D%O% 6 =6 & +5 =' 5 8&$%
S'*$- '=+ '$&:6 5 .* +.&.% L+5 D6 & 6 5. 4 & 5 8=$.$ *. *56 4$
T56 6 4&&/ 87 5*:7 4=$.* & (HFO)
O. * 6*8 4* 6 6*865 5 &**$ 6 8&/. 5$&=+5 5 8=$.$ /5$ +56 6'&.*.&=67
T5 & *$ 5. 65= &44% B=$.$ '&6&., &* 4&/ *. *$ 4&/ *$ &.$& & *5: 6$ &='= &4 '$*=$, '$66=$ *. 4&/ *. 5. 5 $7
A 4= &='= ",000 MW '&/$ 6*&. *. 8=$. &$ 5*. !0,000 &.6 &4 &* * *7
STEAM TURBINE I. GHTP L5$ M&5*88* 210MW *. 2!0MW 6.+ 65*4 $*&. =$8.6, T*. C&='.+ 3000 R%P%M% &=8 4&/ 5*=6, $5* 7' /5 .* '*$*$6 &4 1!0 K+6@%% *. !3!&C% A 6* =$8. 6 * 5*.* : 5* $*6 5$* .$+7 4$& '$66=$ 6*, *. &.:$6 .& $&*$7 &&.% I6 &$. *.46*&. /*6 .:. 87 S$ C5*$6 P*$6&.6 . 1??"%
F"g. 18.1 STEAM TURBINE
T5 4$6 : 5* *7 8 *664 *6 * 6* =$8. /*6 &$ 5*. * &7, 5 *66 A&', 6$8 . 5 16 .=$7 87 H$& &4 A*.$* . R&*. E+7'% A 5&=6*. 7*$6 *$, * 6* =$8. /5 '$** *''*&.6 /*6 .:. . 1!!1 87 T*@ *D. . O&*. E+7', /5& 6$8 *6 * '$ &:$ 4&$ $&*.+ * 6'% A.&5$ 6* =$8. : /*6 $* 87 I**. G&:*.. B$*.* . 7*$ 1;2>% A 6* =$8. 6 * 5*.* : 5* $*6 5$* .$+7 4$& '$66=$ 6*, *. &.:$6 .& =64= 5*.* /&$-%
I 5*6 *&6 &'7 $'* 5 $'$&*.+ '6&. 6* .+. '$*$7 8*=6 &4 6 +$*$ 5$* 44.7 *. 5+5$ '&/$&/+5 $*&% A6&, 8*=6 5 =$8. +.$*6 $&*$7 &&., 6 '*$=*$7 6= & 8 =6 & $: *. $* +.$*&$ *8&= ?0 &4 * $ +.$*&. . 5 /&$ 6 87 =6 &4 6* =$8.6% I &6. $@=$ * .-*+ 5*.6 & &.:$ $'$&*.+ & $&*$7 &&.% T5 6* =$8. 6 * 4&$ &4 5* .+. 5* $:6 =5 &4 6 '$&:. . 5$& 7.* 44.7 5$&=+5 5 =6 &4 =' 6*+6 . 5 '*.6&. &4 5 6* (*6 &''&6 & 5 &. 6*+ . 5 W* .+.), /55 $6=6 . * &6$ *''$&*5 & 5 * $:$68 '$&66%
H"g% Pr&ur& Tur!"#& H+5 '$66=$ 6* * !;0C *. 1;0-6 '$66=$ '*666 5$&=+5 5 5+5 '$66=$ =$8.% T5 5*=6 6* 4$& 56 6&. 6 $=$. & 5 8&$ 4&$ $5*.+ 84&$ 8.+ =6 . 5 . 6&. &4 5 =$8. 6% T5 8*6 . 5 5+5 '$66=$ =$8. *$ 5 6*6 &4 * 5 =$8. 8*6 56 6 8*=6 5 .&.+ 6* 5*6 :$7 5+5 .$+7 *. &='6 * &/ :&=% T5 8*6 *$ 4 & * 65*4 *. *6 5 6* 56 5 8*6 *=66 5 65*4 & $&*
I#)&r'&$"a)& Pr&ur& Tur!"#&
O. *:.+ 5 8&$ R5*$, 6* .$6 5 .$* '$66=$ =$8. * !;0C *. "0 -6 '$66=$ (1 -6 1"%22 '6 )% F$& 5$ 5 6* +&6 6$*+5 & 5 . 6&. &4 5 =$8. 6% T5 6* 5*6 '*. *. 5*6 66 .$+7 /5. .$6 56 6&., 6& 5$ 5 =$8. 8*6 *$ 8++$ 5*. 5&6 . 5 5+5 '$66=$ =$8.% T5 8*6 *$ 4 & * 65*4 *. *6 5 6* 56 5 8*6 *=66 5 65*4 & $&*
L Pr&ur& Tur!"#& F$& 5 .$* '$66=$ =$8.6, 5 6* &..=6 6 '*.6&. . 5 5$ &/ '$66=$ =$8.6% T5 6* .$.+ 5 =$8.6 6 * 300C *. ; -6 '$66=$% T& + 5 &6 /&$- &= &4 5 6*, 5*=6 '$66=$ 6 -' :$7 &/, 9=6 !0 8*$ *8&: * &' :*==% T5 ' 6' &4 5 *$+6 8*6 /5 5 65*4 6'...+ * 3,000 $:&=&.6 '$ .= 6 2,000 -'5
B"(&r R&%&a)&r
A4$ '*..+ 5$&=+5 5 5+5 '$66=$ =$8. 5 5*=6 6* 6 $=$. & 5 8&$ * 3;0C *. "0 -6 '$66=$ 4&$ $5*.+ 84&$ 8.+ =6 . 5 .$* '$66=$ =$8.
T5 R5*$ $5*6 5 6* 4$& * '$*=$ &4 3;0C 8*- & !;0C
TECHANICAL DATA
M*-
B%H%E%L%
T7' &4 =$8.
H&$&.* 7'
N&% &4 C7.$
T5$ (3)
S* 6 =6
D$7 S*
C&&*.
W*$ H7$&+.
G*6 P$66=$
3%!K+C S@
STAGEI
STAGEII
R* &= '=
210 MW
2!0 MW
R* S'
3000 R%P%M%
3000 R%P%M%
I. S* P$66=$
1!0 K+2
1!0 K+2
I. S* T'$*=$
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F"g. 18.8M$&r# )&a' )ur!"#& g&#&ra)r r a 3a( "r&$ )&a' ;(a#)
F"g.18.0 HP AND IP CASING
CONDENSER S=$4* &..6$ 6 5 &&.7 =6 $ 4&$ * /*$&& 65 *. =8 5* 5*.+$ .6* &. 5 5*=6 6* 4$& 5 6* =$8.6 5* $: 5 $* +.$*&$6 . 5$* '&/$ '*.6% T56 6=$4* &..6$6 *$ 5* 5*.+$6 /55 &.:$ 6* 4$& 6 +*6&=6 & 6 @= 6* * * '$66=$ 8&/ *&6'5$ '$66=$%
5 PURPOSE6 I. 5$* '&/$ '*.6, 5 '$*$7 '=$'&6 &4 * 6=$4* &..6$ 6 & &..6 5 5*=6 6* 4$& * 6* =$8. * *6 &/ * '$66=$ *6 '&668 *. & &8*. '=$ /*$ ($4$$ & *6 6* &..6*) 6& 5* *7 8 $=6 . 5 6* +.$*&$ &$ 8&$ *6 8&$ 4 /*$% T5 6* =$8. 64 6 * : & &.:$ 5 5* . 6* & 5*.* /&$-% T5 44$. 8/. 5 .5*'7 &4 5 . 6* & * =$8. *. 5 .5*'7 &4 5 5*=6 6* $'$6.6 5 5* /55 6 &.:$ & 5*.* /&$-% T5$4&$, 5 *$+$ 5 .5*'7 44$. 8/. . 6* *. 5*=6 6*, 5 5+5$ 6 5 *&=. &4 /&$- :$ 87 5 =$8.% C&..6.+ 5 5*=6 6* &4 * =$8. * * '$66=$ 8&/ *&6'5$ '$66=$ .$*66 5* .5*'7 44$. *. 5$4&$ .$*66 5 /&$- &='= &4 =$8.% T5 /*$&& 6=$4* &..6$6 =6 &. 5 6* =$8. 5*=66 . *$+ '&/$ '*.6 =6=*7 &'$* * *. *86&= '$66=$ &4 *8&= 3! & "0 H+ /55 6 4*$ 8&/ 5 7'* *&6'5$ '$66=$ &4 <;0 H+% M&6 &4 5 5* 8$* 87 &..6.+ 5 5*=6 6* 6 $*.64$$ & *. *$$ */*7 87 5 &&.+ = (/*$ &$ *$) =6 87 5 6=$4* &. .6
%$F"g. 10.8 C#$&#&r 5
SHELL6
T5 65 6 5 &..6$6 &=$&6 8&7 *. &.*.6 5 5* 5*.+$ =86% T5 65 6 4*8$* 4$& *$8&. 6 '*6 *. 6 644. *6 . & '$&: $+7 4&$ 5 65% W5. $@=$ 87 5 6 6+., .$* '*6 *$ .6* & 6$: *6 8*44 '*6 5* '$&: 5 6$ 4&/ '*5 &4 5 &..6.+ 6*% T5 '*6 *6& '$&: 6=''&$ 5* 5' '$:. 6*++.+ &4 &.+ =8 .+56% A 5 8&& &4 5 65, /5$ 5 &..6* &6, *. &= 6 .6*% I. 6& 6+.6, * 6=' (&4. $4$$ & *6 5 5& /) 6 '$&:% C&..6* 6 '=' 4$& 5 &= &$ 5 5& / 4&$ $=6 *6 8&$ 4 /*$% F&$ &6 /*$&& 6=$4* &..6$6, 5 65 6 =.$ :*== =$.+ .&$* &'$*.+ &.&.6%
5
VACUUM SYSTEM6 5
VACCUM SYSTEM
S5* *+$* &4 * 7'* .9&$ &$ 9&$% F&$ * 6*9 9&$, 5 &: 4= 6 6*% T5 .$.* :*== . 5 65 &4 * /*$&& 6=$4* &..6$ 6 &6 &&.7 6='' 87 *. *.*. 87 *. $.* 6*9 9&$ 676% S=5 *. 9&$ 676 =66 6* *6 5 &: 4= & $&: *.7 .&.&..6*8 +*66 5* *7 8 '$6. . 5 6=$4* &..6$% T5 V.=$ 44, /55 6 * '*$=*$ *6 &4 B$.&=6 @=*&., *''6 & 5 &'$*&. &4 6*9 9&$6% M&&$ $:. 5*.* :*== '='6, 6=5 *6 @= $.+ 7' :*== '='6, *$ *6& =6 4&$ 56 6$:
5
TUBE SHEETS6
A *5 . &4 5 65, * 6 65 &4 6=44. 5-.66 6 '$&:, /5 5&6 4&$ 5 5*.+$ =86 & 8 .6$% T5 . . &4 *5 =8 6 *6& 8 &=5 4&$ 6$*. .$7 &4 /*$% T56 6 & *:& 6 * 5 =8 .6 +:.+ $6 & $&6&., *. & $= 4&/ 4$&.% T& *- *$ &4 .+5/6 '*.6&. &4 5 =86, 6& 6+.6 *7 5*: '*.6&. 9&.6 ('* 6 8&/6) 8/. 5 65 *. 5 =8 656 *&/.+ 5 *$ & &: &.+=.*7%
5
TUBES6
G.$*7 5 =86 *$ * &4 6*.66 6, &''$ *&76 6=5 *6 8$*66 &$ 8$&., ='$& .-, &$ *.= '..+ &. :*$&=6 $$*% T5 =8 .+56 $*.+ =' & *8&= !! 4 (1< ) 4&$ &$. '&/$ '*.6, '..+ &. 5 6 &4 5 &..6$% T5 &=$ *$ &4 5 &..6$ =86 7'*7 $*.+6 4$& 3" .5 (1> ) & 11" .5 (32 ), 8*6 &. &..6$ &&.+ /*$ 4$&. &.6$*&.6 *. &:$* &..6$ 6%
5
COOLING WATER INLET AND OUTLET6 E*5 . &4 5
&..6$ 65 6 &6 87 * 8& &:$ $4$$ & *6 * /*$ 8&, &.. & 5 =8 65 &$ &..6$ 65 87 * 4*.+% T5 /*$ 8& 6 =6=*7 '$&: /5 *.5&6 &. 5.+ &:$6 & *&/ '$& .6'&. *. *..+% T5 . *. &= /*$ 8&6 *6& 5*: 4*.+6 4&$ &...+ & 5 . *. &= /*$ .6% T57 *6& 5*: 6*, :*: *$ :.6 * 5 &' &4 5 8&6 *. :*: $*.6 * 5 8&& &4 5 8&6 4&$ =6 =$.+ '$& *..*. 65=&/.6%
CONTROL VALVE C#)r( +a(+& *$ :*:6 =6 /5. .=6$* '*.6 *. 6/5$ & &.$& &'$*.+ &.&.6 6=5 *6 '$66=$, '$*=$, @= : *. 4&/ $* 87 4=7 &$ '*$*7 &'..+ &$ &6.+ . $6'&.6 & 6+.*6 $: 4$& &.$&$6 5* &'*$ * 6 '&. & * '$&66 :*$*8 /5&6 :*= 6 '$&: 87 .'.. 6.6&$6 5* &.&$ 5*.+6 . 6=5 &.&.6%
C&.$& :*:6 *$ *. .+$* '*$ &4 5 5=.$6 (&$ :. 5&=6*.6) &4 &.$& &&'6 ./&$- &+5$ . .=6$* '*.6 & '$&= 5$ :*$&=6 . '$&=6% A &.$& :*: 6 '*$ &4 *. *6687 5* 7'*7 .=6 * :*: 8&7 (*. 6 .$.* '*$6), *. *=*&$ & '$&: 5 &: '&/$ 4&$ &'..+ *. &6.+ 5 :*:, *. * :*$7 &4 *&.* *66&$6 6=5 *6 '&6&.$6, $*.6=$6, *.=* &'$*&$6 *. 6/56% T5 &: '&/$ '$&: 87 5 *=*&$6 *7 8 $*, 57$*= &$ '.=*%
F"g. 10.2 SCHEMATIC DIAGRAM OF CONVENTIONAL CONTROL VALVE WITH A PNEUMATIC ACTUATOR
A''*&.6
C&.$& :*:6 *$ =6 . .=6$6 6=5 *6 '$&= $4..+, 5* *. '$&5* *.=4*=$.+, .=*$
'&/$
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4=
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I. 6=5 .=6$6, &.$& :*:6 *$ *. 66.* &'&.. &4 5 6766 =6 & &.$& '&$*. &'$*&.* '*$*$6 - '$66=$, '$*=$, @= :6 *. 4&/ $*6%
P$66=$ &.$& :*:6 *7 8 =6 & $= @= &$ +*6 '$66=$6 &$ 57 *7 8 =6 & *.*. * 8*-'$66=$ (%%, * '$66=$ ='6$* &4 5 :*:)% T57 *7 *6& 8 =6 & *.*. * '$66=$ 44$. 8/. /& '&.6 . * '$&66%
T'$*=$ &.$& :*:6 *$ =6 & *.*. @= &$ +*6 '$*=$6 /5. '$&66 :666 &$ & &.$& 5 5* $*.64$ /5. 5* 5*.+$6 *. '$&66
5*$6 &$ 4=$.*6%
L: &.$& :*:6 *$ =6 & *.*. @= :6 /5. * 6$ $*.+ . '$&66 :666 &$ *.-6% I. 6& *66, 57 *7 *6& 8 =6 & *.*. :6 &4 6& '*$6%
F&/ &.$& :*:6 *$ =6 & &.$& 5 :&=$ &$ *66 4&/ $* &4 @=6 *. +*66% T57 *7 *6& 8 =6 & *.*. * 6$ $*& 8/. /& 4&/6, . /55 *6 57 *$ '*$ &4 /5* 6 * * flow ratio controller %
POWER GENRETOR
G.$*&. 6 5 '$&66 &4 +.$*.+ $ .$+7 4$& &5$ 4&$6 &4 .$+7% E$&*+. HYPERLINK 5'.%/-'*%&$+/-E$&*+.X.=&. HYPERLINK 5'.%/-'*%&$+/-E$&*+.X.=&..=&., /5$ *. $* +.$*&$ , 7.*& &$ *$.*&$ $*.64&$6 -. .$+7 (.$+7 &4 &&.) .& $7, 56 6 &6 =6 4&$ 4&$ +.$*.+ $7, 6 8*6 &. F*$**76 */, *. 8 '$. 87 6'7 $&*.+ * *+. /5. &6 &&' &4 * &.=.+ *$* (%+% C&''
F"g. 10.1 POWER GENERATOR ASSEMBELED WITH TERBINE
T5 '&/$ +.$* 87 5 +.$*&$ &4 STAGE1 6 . 1!%
COOLING TOWERS
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
F"g. 12.1 WORKING OF COOLING TOWER
F"g. 12.8 COOLING TOWER AT GHTP LEHRA MOHABBAT
COOLING WATER SYSTEM T5 &* &&.+ /*$ $@=$. 4&$ $=...+ /& .=8$ =.6 (210 MW *5) * G=$= H*$+&8. T5$* P*. , L5$* M&5*8* 6 6='' 87 5 .*- '=' 5&=6% T5 $*/ /*$ 6 *-. 4$& 5 S$ 5. *.* 6$8=&$ $=...+ 9=6 .*$87 5 '*. *$* *. 6&$ . 5 6&$*+ '&.% T5 '&. * *6 /*$ $6$:&$ =$.+ 5 '$& 5 *.* 6 =.$ 65= &/. 4&$ *..*. '=$'&6 &$ &5$/6% N&$*7, =$87 &4 $*/ /*$ 6 8/. 1!0200 $', /55 .$*66 & "00 !00 '' =$.+ $*.7 6*6&.% I. &$$ & 6$&7 *+* *. 8*$* . 5 $*/ /*$, 5&$.*&. * 5 .*- '=' 5&=6 6 &. *6 '$ $@=$.% T5 /*$ 4$& '&. 6 *-. & 5 *$4$ /5 5 '='6 .6* . 5 .*- '=' 5&=6%
5
CLARIFIERS6
T5 8*6 '=$'&6 &4 *$4$ 6 & $&: &$ & '$'* 5 =.6$: '=$6 '$6. . $*/ /*$ /55 &*+=*6 87 '=.+ *= *. 6 &/. * 5 8&& &4 *$4$6 . 5 4&$ &4 6=+ /55 6 4=$5$ $&: /5 5 5' &4 6=+.+ :*:6 '$&: 4&$ 5 '=$'&6 %T5 @=*.7 &4 *= 6 $+=* '..+ ='&. 5 =$87 &4 $*/ /*$% T5 $=*.+ /*$ $@=$ 4&$ 5 C%W P='6 I6 P$'*$ I. 5 C*$4$ NO%1% O. 6 &&. 6$: *$4$ (*'*7 3?00 3 5$%)% T5 /*$ 4$& 5 *$4$6 6 $*.64$$ & 5 *$ / O4 D%M% '*. 5 *$4 /*$ 4$& 5 *$ /6 6 =6 4&$ 5 4&&/.+ 44$. '=$'&66
F&$ *-=' &4 5 $=*.+ /*$ . 5 C%W P='%
F&$ :*$&=6 6$:6 . 5 '*.
F&$ 4$ 4+5.+ '=$'&6%
T5 /*$ 4$& *. *$4$ .&%1 &6 & 6=+ 8*.- /5$ 4=$5$ *=
&6.+ 6 &. *. 56 /*$ 6 =6 & '$'*$ D%M% /*$ . D%M% '*.%
5 C("#g a)&r 9)&'6 T5$ *$ ; N&% '='6 . 5 C%W% '=' 5&=6 4&$ 8&5 5 =.6, 5$ '='6 4&$ *5 =.% O= &4 5$ '='6, 2 N&% '='6 4&$ *5 =. 5*:.+ *'*7 !0 *5 *$ $=. *. &. .=8$ '='6 *6 *6 6*.87% T5 ''.+ &4 5 6*. 87 '='6 5*6 8. &. . 6=5 * *..$ 5* 5 6*.87 '=' *. 8 =6 4&$ 5 &5$ =. *6& %T5 '*$=*$6 &4 5 C%W% '='6 .6* * G%H%T%P% L5$* M&5*8* *$ *6 =.$ M*.=4*=$$ T7'
M6, J&7 L% W ', 4&/, :$* .&. $**8 '=' $7 &=' /5 E$ &&$ $:%
D6+. &4 5 +*.6 5*6 8. '$&: 5* =$.+ 6*$ =', .= /*$ '*666 *&.+ /5 5 65*4% M&$&:$, 5 $* &&$ &4 5 '=' 5*6 8. -' &. * 6'*$* 4&&$ %% 6=44. '*$&. 6 '$&: 6& 5* /*$ &6 .& 4* &. 5 &&
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B&$ *=*$6 &&.+ 676% T5 6&=$ &4 =$8. *=*$6 &&.+ 676 6 =$8. *=*$7 C%W% '='6 (TACW P='6) *. 4&$ 8&$ *=*$7 &&.+ 676, 6 8&$ *=*$7 C%W% '='6%
5
T%& TACV Pu';6 T5$ *$ /& .&% TACW '='6 &. '='6 6 4&$ 100 *'*7 *. &5$ 6 6*. 87% T56 '='6 *- 6=&. 4$& =' 6$* &4 &..6$ *. 5 *4$ $&=.+ 5 /*$ 4$& :*$&=6 &&$6 65*$+ .& 5& /*$ =..% T5 '*$=*$6 &4 56 '='6 *$ *6 =.$
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HYDROGEN GAS PLANT H7$&+. G*6 * GHTP L5$* M&5*88* 6 =6 5 R&&$% T5 *7 &.6='&. &4 H7$&+. +*6 6 3 & " 7.$ *''$&*7 /55 6 %N3% T5 H7$&+. P*. 6 6+. & '$&= 57$&+. +*6 * 5 $* &4 10 N35$% *. O7+. G*6 * 5 $* &4 ! N35$% 5 &7+. +*6 +.$* 6 :. & 5 *&6'5$%
PROCESS DESCRIPTION 5
ELECTROLYSERS 6
H7$&+. *. &7+. +*6 6 '$&= 87 4.+ $ =$$. & $&7 6% T5$ *$ 1" 6 *$$*.+ . /& 8*.-6 &4 < 6 *5 . 6$6% A 6*7 =$$. &4 2000 A'6% I6 '*66 +$*=*7 5$&=+5 5 6% T5
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
5
LOW PRESSURE GAS HOLDER :LPGH< 6
T5 H7$&+. G*6 S&$ . * L&/ '$66=$ 4&*.+ $&&4 7' +*6 5&$% W*$ 6* 5*6 8. '$&:.+ 8/. /& *.-6 & 5- +*6 *-*+% T5 4&*.+ $&&4 6 8**. 87 &=.$ /+56%
5
HYDROGEN GAS COMPRESSER 6
H7$&+. G*6 C&'$66&. 6 &. 87 $'$&.+ &'$66&$% T5 &'$66&$6 &'$66 5 57$&+. +*6 4$& 0 & !0 / & 1!0 -+2% T5 57$&+. +*6 6 6=- 4$& 5 &/ '$66=$ +*6 5&$ :* -.&- &= $= 5*:.+ 6$ '*6 4&$ -.&-.+ &= /*$ $&'6 *. &5$ =.6$*8 '*$6% T5 &'$66 +*6 6 '*66 5$&=+5 4$6 * * '$66=$ &4 1!0 -+2%
5
PURIFIER AND DRYING UNIT 6
H7$&+. G*6 6 '=$4 87 $&:.+ 5 $*6 &4 O7+. . 5 D&& '=$4$ 87 '*66.+ 5 6* 5$&=+5 * 8 &4 '**= **76% I. 5 '$6. &4 56 **76, 57$&+. *. &7+. $*6 $* & 4&$ /*$ :*'&$6% T5 $*&. 6 &5$ *. 5 5* 6& '$&= $*66 5 '$*=$ &4 5 +*6% H. 5 +*6 &.+ &= &4 5 '=$4$ 6 && *. 5. '*66 5$&=+5 5 +*6 $7$% P=$4 +*6 6 '*66 5$&=+5 5 /. 8 $+.$*: $7$ =. & *86&$8 &6=$ &.*. . 5 +*6 & +: *&6'5$ / '&. &4 ;0 +% C%
5
HYDROGEN STORAGE CYLINDERS THROUGH MANIFOLDS 6
F$& $7$ 5 +*6 6 *.*7 4&$ 5 / '&. *. 57$&+. '=$7% A4$ &.4$*&. &4 H7$&+. P=$7 &4 >>%> *. / '&. ;0 +% C, 5 +*6 6 6&$ . 7.$6 5$&=+5 57$&+. 4.+ *.4&6 * 1!0 -+2
PRESTART-UP CHECK LIST
E$&7 L: . C
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SPECIFICATION 5
5
HYDROGEN GAS INLET CONDITION6
S$:
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HYDROGEN GAS OUTLET CONDITION6
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COMPRESSORS HOUSE
I. GHTP L5$* M&5*88* " C&'$66&$ H&=66% I. &'$66&$ 5&=6 /& 7'6 &'$66&$6 *$ =6 INSTRUMENT COMPRESSOR *. SERVICE AIR COMPRESSOR% P$.'* &4 * BOP C&'$66&$% T/& 7.$6 *$ '&6&. &. 5$ 6 &4 $*.-*6 4*.+ *5 &5$ 8.+ $:. 87 6* C$*.- 65*4 /5 5 /& $*.-6 * 1?0& 5 $'$&*.+ 5*.6 . 5 /& 7.$6 / */*76 5*: &:.6 *7 &''&6 & *5 &5$ 5=6 '*$.+ '$4 7.* 8**. .& 5 676% T5 B**. &''&6 '6&. &'$66&$6 *$ 5$ 6.+ 6*+ 6+. /5$ .'= '$66=$ 4&$ 8&5 5 7.$ *$ 6* P1 (*&6'5$ '$66=$) 6& *6& 5 &='= '$66=$6 P2 &$ /& 6*+ 6+. /5$ 5 &='= '$66=$ &4 * /& 6*+ &'$66&$ P3 / 8 5+5$ 5*. 5* &4 * &$$6'&..+ 6.+ 6*+ &'$66&
%$5 F&a)ur&6
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5
S$: *$ &'$66&$6
INSTRUMENT COMPRESSOR6 T5 .6$=. &'$66&$6 *$ :$7
'&$*. &'$66&$ 8*=6 * 5 .6$=.6, :*:6 *$ &'$* 87 56 &'$66&$% E*5 =. 5*: 2 .6$=. &'$66&$6 &. 6 $=...+ *. 6&. 6 6*. 87 &.&. /5. $=...+ &'$66&$ 6&' 5. . !. 6&. .6$=. &'$66&$ 6 6*$% W5. 56 &'$66&$ 6 6&' /&$-.+ 5. =.$ !. '*. 6 $' * 5 .6$=. 6&' /&$-.+% T56 &'$66&$ *$ 6 && *. &'$66 *$ '$66=$ 6 <%28*
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SERVICE AIR COMPRESSOR6
T5 S$: *$ &'$66&$ *$ =6 4&$ *..+, *. &5$ '=$'&6% S$: *$ &'$66&$6 *$ 6*$ & .6$=. *$ &'$66&$% T5 6$: *$ &'$66&$6 *. .6$=. *$ &'$66&$6 8&5 *$ &.. /5 &&. :*: *. /5. .6$=. *$ &'$66&$6 *$ 6&' /&$-.+ 5*. &&. :*: 6 *=&* &'. =$.+ !. *. 6$: *$ &'$66&$ *- 5 &'$66 *$ & 5 .6$=. *$ &'$66&
%$TECHANICAL DATA OF AIR COMPRESSOR
R&$ L%P% C7.$ H%P% C7.$
S$&- C&'$66&$ S' F$ *$ :$7 P6&. D6'*. S=&. P$66=$ W&$-.+ P$66=$ L=8 & P$66=$ T&* &&.+ /*$ T&* /+5 &4 &'$66&$ O:$* .6&. &4 &'$66&$
"<0 2;! 1!0 ;2! $' 2!%00 3. 32%3? 3. 0%>;! -+2 ?%?0 -+2 2 & " -+2 200 %'%% "000 -+ L.+5 3200 W5 2?00
H+5
2010
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