Bab Iii_neraca Massa

III41

BAB III E!ACA E!ACA "A##A

BAB III NERASA MASSA Kapasitas %pe$asi Satuan panas T $e+e$ensi asis a"tu Satuan

: 13 130.000 to ton/tahun bi bioethanol 99 99,6. : 393.939,!1!0 "#/ha$i. : 330 ha$i/tahun & '( )a*/ha$i. : ""al. : '-. : 1 ha$i. : K#

Untu" "apasitas "apasitas 393939,!1!0 393939,!1!0 "# ipe$lu"an ipe$lu"an bahan ba"u A*pas A*pas tebu : 1.(9'.(00 "#. A-1. A-1. Rotar Rotary y Kni Knife fe Cutte Cutterr (C(C-1 113) Masuk Komosisi

Keluar Massa

Aliran !1"

Selulosa He*iselulosa i#nin Ash

Komosisi

Massa

Aliran !1"

2!6.(9(,! '61.120 361.160,! !3.2(,( 1.#$%.#&&

Selulosa He*iselulosa i#nin Ash

2!6.(9(,! '61.120 361.160,! !3.2(,( 1.#$%.#&&

A-%. A-%. 'am 'ammer mer Mil Milll (C(C-1 11#) Masuk Komosisi

Keluar Massa

Aliran !1"

Selulosa He*iselulosa i#nin TUGAS AKHIR 

Komosisi

Massa

Aliran !1"

2!6.(9(,! '61.120 361.160,!

Selulosa He*iselulosa i#nin

2!6.(9(,! '61.120 361.160,!

Pabrik Bioetanol Dari Ampas Tebu (Bagasse) dengan Proses Proses Hidrolisa Enzim dan Co-Fermentation Co-Fermentation

III4'

BAB III E!ACA "A##A Ash

!3.2(,( 1.#$%.#&&

Ash

!3.2(,( 1.#$%.#&&

A-3. resteamer Sre* Con+eyor (,-11) Masuk Keluar Komosisi Massa Komosisi Massa Aliran !1" Aliran !#" Selulose Selulose 2!6.(9(,! 2!6.(9(,! He*iselulose He*iselulose '61.120 '61.120 i#nin i#nin 361.160,! 361.160,! Ash Ash !3.2(,( !3.2(,( H'% 900.6(,631 1.(9'.(00 Aliran !%" Ai$ 5$oses 2(6.'00 Aliran !3" Stea*

1(.36(,631 %.3$%.$#/31

A-#.

%.3$%.$#/31

Reaktor retreatment (R-11&) Masuk

Komosisi Aliran !#" Selulose He*iselulose i#nin Ash H'%

Keluar Massa

2!6.(9(,! '61.120 361.160,! !3.2(,( 9006(,631

Komosisi Aliran !0" Selulose He*iselulose 7lose 8u$+u$al i#nin Ash

Massa

2!6.(9(,! 13.062,0990' '62.103,9!36 9(96,!22'1 361.160,! !3.2(,(

'.39'.96(,631 TUGAS AKHIR 

Pabrik Bioetanol Dari Ampas Tebu (Bagasse) dengan Proses Hidrolisa Enzim dan Co-Fermentation

III43

BAB III E!ACA "A##A '(.2((,1(6( Aliran !" Stea* Aliran !"

H'S%( H'%

9.9,!292 3.369.'0','!

1((.1'!,0(! 1.9'3.!'3,006 #.$0.$/03%

#.$0.$/03%

A-. las2 ank (4-1%1)

ahan *asu" Ko*posisi Aliran !0" Sellulosa He*iselulosa <7lose +u$+u$al li#nin ash H'%  H'S%(

>u*lah

8lash Tan" assa K#; 2!6(9(,!00 13062,099 '62103,9!( 9(96,!! 361160,!00 !32(,(00 3369'0','! 99,!26

#$0$/03%

ahan Kelua$ Ko*posisi Aliran !1&" ali$an Slu$$7 : Sellulosa He*iselulosa 7lose 8u$+u$al i#nin Ash H'% H'S%( Aliran !$" ali$an =apo$ : +u$+u$al H '% >u*lah

8lash Tan"   assa K#;

2!6(9(,!00 13062,099 '62103,9!( 3203,669 361160,!00 !32(,(00 '2'923,!!' 99,!26

.29',91! 616.''!,(03 #$0$/03%

A-. Rotary 4rum ilter ('-1%3)

ASUK Aliran !1&" Selulosa He*iselulosa TUGAS AKHIR 

2!6(9(,! 13062,1

K?UAR Aliran !13" Ke Solis i< Selulosa 2!6(9(,! He*iselulosa 13062,0990'

Pabrik Bioetanol Dari Ampas Tebu (Bagasse) dengan Proses Hidrolisa Enzim dan Co-Fermentation

III4(

BAB III E!ACA "A##A Ash i#nin H'S%( H'% 8u$+u$al 7lose

!32(,( 361160,! 99,!! '2'92( 3203,669 '6210( #333$

Ash i#nin H'S%( H'% 8u$+u$al 7lose

!32(,( 361160,! 33,0'193' 110!9,1!'! 13,6!''2(2 9!6,2(!00 1%5#&/&5

Aliran !1%" Ke %=e$li*in#

Aliran !11"

H'%      

%#00$/#

H'S%( H'% 7lose 8u$+u$al 6A7

9'06,!(0( '9902(3,2!( '66112,'31 36!9,9!6932 3355/0

6A7

(61'(9!

6A7

(61'(92,93

A-5. 6+erlimin8 ank (R-1%&)

ASUK Aliran !1%" H'S%( H'% 7lose 8u$+u$al   Aliran !1#" i*e TUGAS AKHIR 

9'06,!(0( '9902(3,2!( '66112,'31 36!9,9!6932  

K?UAR Aliran !1" H'S%( H'% 7lose 8u$+u$al

0 1020!9!6,!6 '66112,'31 36!9,9!6932

G7psu* a%H

16213,'1!( 11'(,!2(661

23021,'390' Pabrik Bioetanol Dari Ampas Tebu (Bagasse) dengan Proses Hidrolisa Enzim dan Co-Fermentation

III4

BAB III E!ACA "A##A Ai$ p$oses

221!'(3,022

otal

111(202',1!

111(202',1!

A-0. Reai9ifiation ank (R-13&) "o*ponen "o*ponen *asu" *assa K#; "elua$ Aliran!1"

*assa K#;

Aliran!15"

<7lose

'66112,'3

<7lose

'66112,'3

+u$+u$al

36!9,9!2

+u$+u$al

36!9,9!2

H'% a%H;' aS%(.'H'%

1020!9!6,!60 11'(,!2

H'% aS%(.'H'%

10!0300',!'0 169266,6(3

16213,'1!

Aliran !1"

H'S%( H'% T%TA

1(!!,0 9(01,99!! 11%#%5/0

11%#%5/0

A-$. 'y9roylone ilter ('-1%$)

ASUK

K?UAR

Aliran !15"

Aliran !10"

H'%

'2222,10!

H'%

'2222,10!

7lose 8u$+u$al

'66011,0!33 36!!,103

7lose 8u$+u$al

'66011,0!33 36!!,103

G7psu*

(6'22(,193

G7psu*

'313,!2'96 3&%$55&/5$

Aliran !1$"

G7psu* TUGAS AKHIR 

(60(60,6(62

Pabrik Bioetanol Dari Ampas Tebu (Bagasse) dengan Proses Hidrolisa Enzim dan Co-Fermentation

III46

BAB III E!ACA "A##A

6A7

3(90'31,''

3(90'31,''

A-1&. an8ki Soli9s Mi: (-131)

ASUK Aliran !10" H'% 7lose 8u$+u$al G7psu*

10!0300',!' '66112,'31 36!9,9!6932 !(!,!33'16 11&530/00

Aliran !13"

Selulosa He*iselulosa Ash i#nin H'S%( H'% 8u$+u$al 7lose

  2!6(9(,! 13062,0990' !32(,( 361160,! 33,0'193' 110!9,1!'! 13,6!''2(2 9!6,2(!00 1%5#&/&5 1'33039!,9

K?UAR Aliran !%&" Selulosa He*iselulosa Ash i#nin H'S%( H'% 8u$+u$al 7lose G7psu*

2!6(9(,! 13062,0990' !32(,( 361160,! 33,0'193' 10!1(09',3( 3203,669'11 '62103,9!36 !(!,!33'16

1'33039!,9

A-11. Reaktor 'i9rolisa (R-1#&)

ASUK Aliran !%1" TUGAS AKHIR 

K?UAR Aliran !%3" Pabrik Bioetanol Dari Ampas Tebu (Bagasse) dengan Proses Hidrolisa Enzim dan Co-Fermentation

III42

BAB III E!ACA "A##A Selulosa He*iselulosa Ash i#nin H'S%( H'% 8u$+u$al 7lose G7psu* Aliran !%%"

2!6(9(,! 13062,0990' !32(,( 361160,! 390,999029( '26!201,0' 3203,669'11 '62103,9!36 '313,!2'96 #%01&/#$  

Selulase H'%

12'9,!96 33((9!3,211

6A7

26(2''(,'6

Selulosa He*iselulosa Ash i#nin H'S%( H'% 8u$+u$al 7lose G7psu* Selulase Glu"osa

2!6(9,(! 13062,099 !32(,( 361160,! 390,999029 6030'',6( 3203,669'1 '62103,9!( '313,!2'6 12'9,!96 2!602,(1'

26(2''(,'6

A-1%. Rotary 4rum ilter ('-%%%)

ASUK

K?UAR

Alitan !%3"

Aliran !%"

Selulosa He*iselulosa Ash i#nin H'S%( H'% 8u$+u$al TUGAS AKHIR 

2!6(9,(! 13062,0990' !32(,( 361160,! 33,0'193' 1023(30,' 3203,669'11

Selulosa He*iselulosa Ash i#nin H'S%( H'% 8u$+u$al

2!6(9,(! 13062,099 !32(,( 361160,! 0,136!!6( 1'0,1!269 1,(361'0!3

Pabrik Bioetanol Dari Ampas Tebu (Bagasse) dengan Proses Hidrolisa Enzim dan Co-Fermentation

III4!

BAB III E!ACA "A##A 7lose G7psu* Selulase Glu"osa

'62103,9!36 !(!,!33'16 12'9,!96 2!602,(112 1%3#1%0/0#

Aliran !%#"

H'%

103,21'3 !(!,!33'16 12'9,!96 30(,9231' 0&/013

Aliran !%#"

'(69'',26!

 

6A7

7lose G7psu* Selulase Glu"osa

H'% H'S%( 7lose Glu"osa 8u$+u$al

1(!13(,61

131993,! 3',!!0(6 '62000,(1' 2!6'0',(39 320','3309 1#%5$3/0

1(!13(,6

A-13. an8ki Sterilisasi (M-%%#)

ASUK

K?UAR

Aliran !%"

Aliran !%5"

H'% H'S%( 7lose Glu"osa 8u$+u$al

131993,!3 3',!!0( '62000,(1'3 2!6'0',(3! 320','33091

H'% H'S%( 7lose Glu"osa 8u$+u$al

131993,! 3,'!!0(6 '6200,0(1' 2!6'0,'(39 320,''3309 1#%5$/30

Aliran !%0"

 

TUGAS AKHIR 

H'% H'S%( 7lose

11!29!',' 312,96(1 '(0300,321

Pabrik Bioetanol Dari Ampas Tebu (Bagasse) dengan Proses Hidrolisa Enzim dan Co-Fermentation

III49

BAB III E!ACA "A##A Glu"osa 8u$+u$al

 

202!',19 333',0092! 1%03111#/#

6A7

1#%5$3/0

1#%5$3/0

A-1#. an8ki Starter (R-%3&)

Masuk 

Keluar

Aliran !%5"

Aliran !"

ahan *asu" Aliran !%$" 5ena*bahan H 35%( Aliran !3&" 5ena*bahan @H(;'S%(  Aliran !31" io*ass

1('629,3! 991,1'013'3   991,1'013'3   991,1'013'3

  1#%0%/5#&

TUGAS AKHIR 

%' Aliran!3%"

(3396,(((9(

H'% 7lose Glu"osa io*ass

131993,!3 (9(1,6193( (9',!6!321 !!!1,126((

'H%H

(('2,2'93

H3%%H H'S%( 8u$+u$al

13,!110!6 3,'!!0( 320,''33091 13!'6,'9 1#%0%/5#&

Pabrik Bioetanol Dari Ampas Tebu (Bagasse) dengan Proses Hidrolisa Enzim dan Co-Fermentation

III410

BAB III E!ACA "A##A A-1. an8ki ermentor (R-1&)

Masuk 

Keluar

Aliran !%0"

Aliran !"

ahan *asu"

!263!',(3

Aliran !33"

!3,6(902'(9

H'% 7lose

2960',26 309!1,!'32

!,(302(

Glu"osa io*ass

'!(0!,9('2 (3!600,((0(

!,(302(

'H%H

'90'21,!(!'

H3%%H H'S%( 8u$+u$al

10'0,9'2!!2 390,2(26'6' 3201,'!2366

anti +oa*

!3,6(902'(9

 

5ena*bahan H35%( Aliran !%$" 5ena*bahan @H(;'S%(

'311(,6396

Aliran !3"

Anti +oa* Aliran !31"

%'

 

  000155/&%

000155/&%

A-1. Rotary 4rum ilter ('-31%)

ASUK Aliran !3" H'% 7lose Glu"osa

2960',26 309!1,!'32 '!(0!,9('2

K?UAR Aliran !3" H'% 7lose Glu"osa

(191,06!9 16,9!112016 1,209213!

io*ass

(3!600,((0(

'H%H

19,09!301

'H%H

'90'21,!(!'

H3%%H

0,9216(!

H3%%H

10'0,9'2!!2

H'S%(

0,'1(1691!

TUGAS AKHIR 

Pabrik Bioetanol Dari Ampas Tebu (Bagasse) dengan Proses Hidrolisa Enzim dan Co-Fermentation

III411

BAB III E!ACA "A##A H'S%( 8u$+u$al anti +oa*

390,2(26'6' 3201,'!2366 !3,6(902'(9

8u$+u$al anti +oa* io*ass

033&%/#%3

',0'!629(96 0,0(!(!1( (3!600,((0( ##%$0/###0

Aliran !35" Aliran !30"

H'%  

  !22'0,0!!0!

   

6A7

!((02!',11

H'% 7lose Glu"osa

26(3131,33! 3096(,!('! '!393,3212!

'H%H

'9011',2(99

H3%%H H'S%( 8u$+u$al anti +oa*

10'0,36!31 390,33(21 3699,'!6!2 !3,603''(3 5$$55$/& !((02!',11

A-15. 4istilasi I (4-1&) Masuk Komosisi Massa Aliran !30" H'% 7lose Glu"osa 'H%H 3H!%3 H3%%H TUGAS AKHIR 

2!.9'2,(12 6,3!! 3.303,(13 (!.03,69 '.1!,(! !'1,1'0

Keluar Komosisi Massa Aliran !3$" ; 4istilat H'% '.((6,(3 'H%H (6.999,!' 3H!%3 0 H3%%H 0,'1 (9.((6,3(0

Pabrik Bioetanol Dari Ampas Tebu (Bagasse) dengan Proses Hidrolisa Enzim dan Co-Fermentation

III41'

BAB III E!ACA "A##A Anti+oa*

1,((6 Aliran !#&" ;  Bottom H'% 7lose Glu"osa 'H%H 3H!%3 H3%%H Anti+oa*  131.335/1

26.(!0,!2( 6,3!! 3.303,(13 1.0(,02!   '.1!,(! !'0,90 1,((6 !1.!91,126 131.335/1

A-10. Moleular Sie+e (4-15&) < (4-10&) Komosisi Aliran !3$" ; 4istilat

assa K#;

Komosisi Aliran !#%" ; an8ki enamun8

'H%H K;

(12((!,('61

'H%H

H'% HK;

19!(!,000

H'%

H3%%H

0,0003

assa K#;

393939.!1!0 19!(,!00

H3%%H

0,0003

Aliran !#1"

,umla2

TUGAS AKHIR 

(32'96,(31(

'H%H

'30!,60!11

H'%

12!63,'0(

,umla2

(32'96,(31(

Pabrik Bioetanol Dari Ampas Tebu (Bagasse) dengan Proses Hidrolisa Enzim dan Co-Fermentation