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7/26/2019 Flow Diagram Sugar Plant-1
1/14
ukherji Associates Pvt. Ltd. BAGASS
Imbibition Water
49.92 t/h
80.00 Deg.C
!ugar "actor# Filter C!e
4.1" %&$.$
1&' (agasse 4".88 t/h 9$
)*+' t/da# t% &'e 2#.42
!ugarcane 1$0.00 t/h P)l % 2.00
P)l % 12.00 ()i*t % +0.00
Fi5re % 1".00 Fi5re % 4#.40
(a
1.+
Sgr 2.4
10.08 %&
1$.1" t/h (agasse ,ard
"9.88 t/h 24
Ecess bagasse B
#.## t/h 4.8+ %&
!team enera
!team Parame
Pre**re
Te7-er. +2
S/B
7/26/2019 Flow Diagram Sugar Plant-1
2/14
ukherji Associates Pvt. Ltd. BAGA
Imbibition Water
49.92 t/h
80.00 Deg.C
!ugar "actor# Filter C!e
4.1" %&$.
1&' (agasse 4".88 t/h 9$
)*+' t/da# t% &'e 2#.42
!ugarcane 1$0.00 t/h P)l % 2.00
P)l % 12.00 ()i*t % +0.00
Fi5re % 1".00 Fi5re % 4#.40
(a
1.
Sgr 2.
10.08 %&
1$.1" t/h (agasse ,ard
"9.88 t/h 24
Ecess bagasse B
"9.88 t/h 24.92 %&
Dr
7/26/2019 Flow Diagram Sugar Plant-1
3/14
(agasse asi0cation in !ugar Pant
Pant eisting data
Pl't &-&it t)' &r*hi'g/, )*+'Sgr &'e t&h 1&'
POL % 12
Fi5re % 1"
Po%er
P)er ge'erte, gr)** 7 1".49
I'ter'l &)'*7-ti)' -l't 7 +.12S-e&i& &)'*7-ti)' !/&r*hi'g "2
Net e6-)rt5le -)er 7 8."#
!ugar data
% ) &'e % 10.08
Sgr t)'/hr 1$.128
Pro$osed (agasse asi0cation
Bg**e
t 5g**e t)'/hr "9.8#2
()i*tre % % +0 r#er
LC= !&l/!g 1801 ()i*tre re7)e,
Dr 5g**e t)'/hr 19.9"$ t)'/hr
()i*tre t)'/hr 19.9"$ et L),
7/26/2019 Flow Diagram Sugar Plant-1
4/14
Bg**e
t 5g**e t)'/hr 24.92 asi0er
()i*tre % % 20 "or Po%er generati
LC= !&l/!g "241
Dr 5g**e t)'/hr 19.9"$ Lrge G*ier
et I' el 7 3).31)&
et I'-t t) g*ier )r B)iler G*ier Ther7l e
(: +".2$#41
et re7i'i'g )r -)er
7 40.$4$22
7/26/2019 Flow Diagram Sugar Plant-1
5/14
(agasse data
Bg**e % ) &'e % 2#.42
Bg**e t)'/hr 4".8#2POL % 2
()i*tre % +0 40 "0
5re % 4#.42
GC= !&l/!g 22#$ 2#"1 "18$
LC= !&l/!g 1801 2281 2#$1
Bg**e t) -r)&e** t)'/hr 2.4
Bg**e l)** t)'/hr 1.$
Bg**e t) &)ge' 5)iler t)'/hr "2.11
E6&e** 5g**e t)'/hr #.#$2
Bg**e -r)6i7te 'l*i* % =( "+.+ AS ".+
( +0 FC 10.+
Bg**e lti7te 'l*i* % C 2".2+ S 0
".2+ O 21
N 0.+ ( +0
A*h 2
!team boier data
B)iler Pre**re 5r 8#
S-erheter te7-ertre )& +20Ste7 &-&it t)'/hr #".8$
Ste7 ,i*tri5ti)' Process "eed hea condenser
C-&it t)'/hr ++.04 8.82 10
Pre**re 5r 2.+ 12 0.1
Te7-ertre )& 1"0 4+.8"
B)iler e;&ie'& )' LC= % 81
C)',e'*te retr' % 9+
Deert)r *te7 t)'/hr
24.92
20
"241
14.9+2 19.9"$
1900 4.984
7/26/2019 Flow Diagram Sugar Plant-1
6/14
on 2 (oier
40.48"2" 7
#$
!team out$ut
t t)'/hr
B)iler Pre**re 5r
as "ired Te7-ertre )&
E'thl-
"eed Inet
t
Te7-ertre
e'thl-
(o% do%n
% 5l) ,)'
E'thl-
Pre**re
t
4et heat b# (oier
Net het
(oier e5cienc#
ON LC=
et i' t) 5)iler
Eile't BgSh)l, 5e
7/26/2019 Flow Diagram Sugar Plant-1
7/14
20
"$41
"241
7/26/2019 Flow Diagram Sugar Plant-1
8/14
Po%er
10.1$
t)'/hr ++.04
5r 2.+
)& 12#.4 $48.994#
!&l/!g $48.822+
t)'/hr +$.#422#
)& 10+
!&l/!g 10+.+
% "
!&l/!g 12#.8$+
Br 2.+
t)'/hr 1.#022$8
!&l/!g +4".99"4
!&l/hr 29941"99
! "481+.+8
% 8$
! 4048".2"
!g/hr 10#42.2"!g/hr 141"4.+2
7/26/2019 Flow Diagram Sugar Plant-1
9/14
(agasse asi0cation in !ugar Pant
Pant eisting data
Pl't &-&it t)' &r*hi'g/, )*+'
Sgr &'e t&h 1&'
POL % 12
Fi5re % 1"
Po%er
P)er ge'erte, gr)** 7 1".49
I'ter'l &)'*7-ti)' -l't 7 +.12
S-e&i& &)'*7-ti)' !/&r*hi'g "2
Net e6-)rt5le -)er 7 8."#
!ugar data
% ) &'e % 10.08
Sgr t)'/hr 1$.128
Pro$osed (agasse asi0cation
Bg**e
t 5g**e t)'/hr "9.8#2
()i*tre % % +0 r#er
LC= !&l/!g 1801 ()i*tre re7)e,
Dr 5g**e t)'/hr 19.9"$ t)'/hr
()i*tre t)'/hr 19.9"$ et L),
7/26/2019 Flow Diagram Sugar Plant-1
10/14
Bg**e
t 5g**e t)'/hr 24.92 asi0er
()i*tre % % 20 6n# 7or Po%er gen
LC= !&l/!g "241
Dr 5g**e t)'/hr 19.9"$ S7ll G*ier
et I' el 7 3).31
et I'-t t) B)iler G*ier Ther7l e
(: 4".+2
et re7i'i'g )r -)er
7 +0."9 4".+2
7/26/2019 Flow Diagram Sugar Plant-1
11/14
(agasse data
Bg**e % ) &'e % 2#.42
Bg**e t)'/hr 4".8#2
POL % 2
()i*tre % +0 40 "0
5re % 4#.42
GC= !&l/!g 22#$ 2#"1 "18$
LC= !&l/!g 1801 2281 2#$1
Bg**e t) -r)&e** t)'/hr 2.4
Bg**e l)** t)'/hr 1.$
Bg**e t) &)ge' 5)iler t)'/hr "2.11
E6&e** 5g**e t)'/hr #.#$2
Bg**e -r)6i7te 'l*i* % =( "+.+ AS ".+
( +0 FC 10.+
Bg**e lti7te 'l*i* % C 2".2+ S 0
".2+ O 21
N 0.+ ( +0
A*h 2
!team boier data
B)iler Pre**re 5r 8#
S-erheter te7-ertre )& +20
Ste7 &-&it t)'/hr #".8$Ste7 ,i*tri5ti)' Process "eed hea condenser
C-&it t)'/hr ++.04 8.82 10
Pre**re 5r 2.+ 12 0.1
Te7-ertre )& 1"0 4+.8"
B)iler e;&ie'& )' LC= % 81
C)',e'*te retr' % 9+
Deert)r *te7 t)'/hr
24.92
20
"241
14.9+2 19.9"$
1900 4.984
7/26/2019 Flow Diagram Sugar Plant-1
12/14
eration
#$
!team out$ut
t t)'/hr
7 B)iler Pre**re 5r
(agasse 0red Te7-ertre )&
E'thl-
"eed Inet
t
Te7-ertre
e'thl-
(o% do%n
% 5l) ,)'
E'thl-
Pre**re
t
4et heat b# (oier
Net het
(oier e5cienc#ON LC=
et i' t) 5)iler
Eile't Bg
Sh)l, 5e
7/26/2019 Flow Diagram Sugar Plant-1
13/14
20
"$41
"241
7/26/2019 Flow Diagram Sugar Plant-1
14/14
Po%er
12.$0
t)'/hr ++.04
5r 2.+
)& 12#.4 $48.994#
!&l/!g $48.822+
t)'/hr +$.#422#
)& 10+
!&l/!g 10+.+
% "
!&l/!g 12#.8$+
Br 2.+
t)'/hr 1.#022$8
!&l/!g +4".99"4
!&l/hr 29941"99
! "481+.+8
% 80
! 4"+19.48
!g/hr 11+4#.9
!g/hr 11+4#.9