Flow Diagram Sugar Plant-1

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    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

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    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

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    (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),

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    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

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    (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

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    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

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    20

    "$41

    "241

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    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

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    (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),

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    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

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    (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

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    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

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    20

    "$41

    "241

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    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