alat ulang abhs

8/18/2019 alat ulang abhs

1/201

C.1 Kolam Penampung bahan baku POME

Tekanan (P)

Temperatur (T)

Lama Pesediaan (t)

Asumsi :Pengaruh Temperatur terhadap densitas diabaikan

Laju Alir massa (F)

Faktor keaman

Menghitung kapasitas gudang bahan baku

Laju Alir volumetris

Volume bahan baku (Vb)

jumlah kolam direncanakan

Volume bahan baku (Vb)/kolam

volume keamanan kolam !"

menghitung dimensi kolam

Panjang

Lebar

Tinggi

rangkuman #pesi$kasi kolam bahan baku

kode %&'!'

tipe kolam terbuka berbentuk balok

bahan kontruksi dinding beton

volume !*+,

panjang -*.

lebar +*,

tinggi *,'

jumlah '!

C.3 Dekanter aulia

kondisi operasi

kondisi penimpanan p0' atm

laju alir massa ++++++*++

densittas campuran ,,.*,.1-2--

3aktu tinggal '*2

4aktor keaman !"

Menentukan dimensi tangki

5ensitas (6)


2/201


3/201


laju alir volumetrik !*!1+-!!-2,

volume bahan (Vb) .*11-,+1.+2

volume tangki '!*2,11!'1+

Volume silinder (Vs) '*1-

volume krucut '/ phi r


4/201


5/201

c/5t !*

L/5a !*1

?/5t !*!.

dimana

5a !*22-2'!, m

L !*'22,!112 m

; !*11!--.++- m@ !*'1!++. m

? !*'.1,''1m

Po!er Penagduk

n '*1

viskositas !*!+-.

rho ,+*+-2.'-,+',

5a !*22-2'!,

gc *

= ''.'*,2!.--

p 1P '!,*12.,.1+

Peren(anaan *aket Pemanas

T steam masuk !

T steam %eluar 2!

Bassa steam '!'*'1

Volume tutup ba3ah !*2!..12-'

volume cairan 2*+..--+.2

ketinggian ;airan dlm shell(8sh) *,2-'1211!.

5iameter luar tangki '*2.'-111,.

diameter dlm jaket '*2.'-111,.

Ash '1*22.+'!112

Ael *!.-.,1.

Luas Permukaan dindidng jaket(Aj) !

Tinggi jaket *.++',+!-

Lebar ?aket '*-.'-111,.

5iameter eki4alen jaket (5ej) !*!1,+2-+

Laju aliran steam *,2+.+'--

laju aliran massa steam persatuan luas +'!*++''1-+.

luas permukaan dinding

panjang pengaduk L !*'22,!112

lebar pengaduk ? !*'.1,''1

jarak pengaduk dr dsr tngki ; !*11!--.++-

tinggi larutan T *,2-'1211!.

rho ,+*+-2.'-,+',

viskositas +-*.

n ,!


6/201

k !*!.1

c !*2

=ej '*-1,1!.

?h +'!

asumsi tj !*!1

5j '*-2,!111,.

c*viskos/k -*''22-2hi +'*,2!.+1

hoi '1!!

C; +!*.'.,1-2121

=d !*!!1

hd !!

Cd *,!!'',.2,'

hot Duida cold Duida selisish

+. #hu rend4ah .2 '2

+. shu tinggi '+! '!.

1+LBT5 '*'.!.2,2.

A 11,*-,-!!--1

C%+ ,-T/0-

Tekanan (P)

Laju Alir >ahan

6 PEBLaju Alir volumetris ()

Laju Alir Ampas %eluar

6 Ampas

Laju Alir Filtrasi %eluar

Laju AlirVolumetrik keluar(out)

L

psilon

6 Ampas

Volume $ltrat (V)volume

Perhitungan Volume ;airan

@

A

A

@aktu Tinggal (G)


7/201

C.1 degumming aulia

kondisi operasi


laju alir massa 2+'*!-!

densittas ,*+,.+.1-,

3aktu tinggal '

4aktor keaman !"


laju alir volumetrik 2*2.12---!2

volume bahan (Vb) 2*2.12---!2

volume tangki .*!.'+-


volume krucut '/ phi r


8/201

3/da !*

c/5t !*

L/5a !*1

?/5t !*!.

dimana

5a !*2+.+.2'' m

L !*'2!.-'1 m; !*1+..-2!1. m

@ !*',22,-2 m

? !*'+1-m

Po!er Penagduk

n '*1

viskositas !*!+-.

rho ,*+,.+.1-,

5a !*2+.+.2''

gc *

= ''*.1.,1'+p 1

P '.!+*2.!1','

C.12 "a(uum dr#er aulia

kondisi operasi


laju alir massa +2!*!,!densittas campuran ,!-*111!.2'-

3aktu tinggal '

4aktor keaman !"


laju alir volumetrik +*.!+'11-'

volume bahan (Vb) +*.!+'11-'

volume tangki 1*-21!1.2.1

Volume silinder (Vs) *11

volume elipsiodal head (Vh) !*'!.

V atas 7 V ba3ah !*2'222222-5iameter tangki (5t) '*!''-

Tinggisilinder *,!22,+'!,

Tinggi head (8h) !*1!1-.+

Tinggi total (8t) +*11+.!,-,

menentukan tebal shell dan tebal head

tinggi cairan (8li9) *2'+1!.-'.

gravitasi ,*.

Ph '+-*1.


9/201


10/201


11/201

dimana

5a !*1.2-++, m

L !*'+211,'' m

; !*+.2+1--' m

@ !*''-+-++, m

? !*''2++.m

Po!er Penagduk n '*1

viskositas !*!+-.

rho ,!2*'2+..-,2

5a !*1.2-++,

gc *

= ,--*-1.+,--+

p 1

P '!1.*.!,++2+


T steam masuk ! T steam %eluar 2!

Bassa steam ..*,'

Volume tutup ba3ah !*+''.2.1-!1

volume cairan +*,2+-1'-

ketinggian ;airan dlm shell(8sh) *2!1+,..22+

5iameter luar tangki '*+-.,''+

diameter dlm jaket '*+-.,''+

Ash '*!,+!,.,-

Ael *.!!-+

Luas Permukaan dindidng jaket(Aj) '12

Tinggi jaket *,-'.,-'++1

Lebar ?aket '*1-.,''+

5iameter eki4alen jaket (5ej) !*!2-2+11.

Laju aliran steam *1.2,..'1

laju aliran massa steam persatuan luas +21*!-11'-.-


panjang pengaduk L !*'+211,''

lebar pengaduk ? !*''2++.

jarak pengaduk dr dsr tngki ; !*+.2+1--'

tinggi larutan T *2!1+,..22+

rho ,!2*'2+..-,2

viskositas +-*.

n ,!

k !*!.1

c !*2

=ej '!*'-2!+-'.


12/201

?h +'!

asumsi tj !*!1

5j '*1211,''+

c*viskos/k -*''22-2

hi +-*+'',1.-

hoi '1!!

C; +1*,2!+.',-=d !*!!1

hd !!

Cd -*-!',




1+

LBT5 '*'.!.2,2.

A 1!-*-.1111+.22

C.3 penampungmetanol aulia

kondisi operasi


laju alir massa .2.*'!!

densittas campuran -.

3aktu tinggal '2.

4aktor keaman !"Menentukan dimensi tangki

laju alir volumetrik '*',++1!1+,

volume bahan (Vb) !!*!-2,!.

volume tangki 2!*!,,!-2,



V atas 7 V ba3ah !*2'222222-

5iameter tangki (5t) *!'+!21'!

Tinggisilinder 2*+!.'!!1

Tinggi head (8h) !*.!!1'2-2 Tinggi total (8t) .*!!1'2-1-


tinggi cairan (8li9) 2*+,1-'!

gravitasi ,*.

Ph +++''*

Pd *2

tebal didnidng silinder tangki

F !!!!


13/201

!*.1

; !*'1

r '*2!!-!11'

ts !*'''2'21-

tebal head

th !*''',-!'

C.) ettler aulia

kondisi operasi


laju alir massa +1+*+!

densittas campuran ,2*-2.1'3aktu tinggal

4aktor keaman !"


laju alir volumetrik +*2,.1'+,..,

volume bahan (Vb) ,*,-!,,---

volume tangki ''*-2+1,-



V atas 7 V ba3ah !*2'222222-

5iameter tangki (5t) '*2-1-!.+

panjang silinder +*..',--'1'

panjang head (Ph) !*+!2.'+-'

panjang total (Pt) 1*2,12,,-,


tinggi cairan (8li9) '*12'!+-1-

gravitasi ,*.

Ph ''2*!+

Pd '.*'


F !!!!

!*.1

; !*'1

r !*.'22.1+

ts !*'1,'1-.-.

tebal head

th !*'1,'2..!.2


14/201

perhitungan 3aktu tinggal

t '*,.+.-1''-.

C. tangki katalis aO

kondisi operasikondisi penimpanan p0' atm

laju alir massa +*-1!

densittas campuran '!

3aktu tinggal 2

4aktor keaman !"


laju alir volumetrik !*!!!-!+1

volume bahan (Vb) 2*-+22',-'.

volume tangki .*!,,+22

Volume silinder (Vs) '*1-volume elipsiodal head (Vh) !*'!.

V atas 7 V ba3ah !*2'222222-

5iameter tangki (5t) '*2+!..!'221

Tinggisilinder *.'-2!

Tinggi head (8h) !*+'!!!+'2

Tinggi total (8t) +*'!!!+'2


tinggi cairan (8li9) *',!2!!-

gravitasi ,*.

Ph 222!!*1,Pd 2*.!


F !!!!

!*.1

; !*'1

r !*.!++!!.

ts !*'-1..!1-!

tebal head

th !*'-1,!+21,

ran(angan pengaduk 5a/dt !*+

3/da !*

c/5t !*

L/5a !*1

?/5t !*!.

dimana

5a !*2121!222 m

L !*'2+!..!'22 m


15/201

; !*1+'+,!+1+, m

@ !*''-!+' m

? !*'2',!1.m

Po!er Penagduk

n '*1

viskositas !*.!'

rho '!5a !*2121!222

gc *

= '-'-*,-2,+!1

p 1

P +-.*'-'+,1'

C.31/eaktor Tranesterikasi aulia

kondisi operasi


laju alir massa 1+-*-1

densittas campuran ..,*!.2,+-1

3aktu tinggal '

4aktor keaman !"


laju alir volumetrik 1*,!12,,

volume bahan (Vb) 1*,!12,,

volume tangki -*!.-!-2-..Volume silinder (Vs) '*1-


V atas 7 V ba3ah !*2'222222-

5iameter tangki (5t) '*12,1.!!+

Tinggisilinder *','22!+!.

Tinggi head (8h) !*,,1-11'

Tinggi total (8t) *,,1-11'


tinggi cairan (8li9) *!1',22,.+'

gravitasi ,*.Ph 21,!*!

Pd !*+'


F !!!!

!*.1

; !*'1

r !*-.+-,'1'!

ts !*'2!.'!.,1


16/201

tebal head

th !*'2!,+++1'

Tebal Cone

Tc !*'2-.-!2!2

ran(angan pengaduk

5a/dt !*+

3/da !*c/5t !*

L/5a !*1

?/5t !*!.

dimana

5a !*2-.!. m

L !*'12,1.! m

; !*1'-,2,2- m

@ !*'11222+'2 m

? !*'!-1,!-m

Po!er Penagduk n +

viskositas !*.!'

rho ..,*!.2,+-1

5a !*2-.!.

gc *

= '-+,*1.!2.,

p 1

P .2'*.+,21..


T steam masuk !

T steam %eluar 2!

Bassa steam ..*,'

Volume tutup ba3ah !*1!1,!-2,'

volume cairan 1*,2+.-!--

ketinggian ;airan dlm shell(8sh) *-,!2,.'+

5iameter luar tangki '*1..!!+

diameter dlm jaket '*1..!!+

Ash '*.21.2!!!.

Ael *-.,+1'2-

Luas Permukaan dindidng jaket(Aj) '-,

Tinggi jaket *'.-2112,'

Lebar ?aket '*2..!!+

5iameter eki4alen jaket (5ej) !*!2',,.',

Laju aliran steam *-1.+.,+

laju aliran massa steam persatuan luas +1*++2-!-2



17/201

panjang pengaduk L !*'12,1.!

lebar pengaduk ? !*'!-1,!-

jarak pengaduk dr dsr tngki ; !*1'-,2,2-

tinggi larutan T *-,!2,.'+

rho ..,*!.2,+-1

viskositas +-*.

n +!k !*!.1

c !*2

=ej !*11!1+

?h +'!

asumsi tj !*!1

5j '*22,1.!!+

c*viskos/k -*''22-2

hi ++*+2!!21-.1

hoi '1!!

C; +*'.!!!2!1=d !*!!1

hd !!

Cd 1*1',+12.


+. #hu rend4ah '+! '!.

+. shu tinggi ',+ 1+

1+

LBT5 --*,!11!.

A ,'*1'!,'.,''

C.33 ettler -- aulia

kondisi operasi


laju alir massa 1+-*1

densittas campuran .--*.2!.13aktu tinggal '*1+11-,.-,

4aktor keaman !"


laju alir volumetrik 1*,--+1++!+

volume bahan (Vb) ,*.2!!+

volume tangki ''*!.2122+1



18/201


V atas 7 V ba3ah !*2'222222-

5iameter tangki (5t) '*2'.'!+--

panjang silinder +*.1+,!-+'

panjang head (Ph) !*+!+112',

panjang total (Pt) 1*22+11.2-menentukan tebal shell dan tebal head

tinggi cairan (8li9) '*+.++'.-'

gravitasi ,*.

Ph ''2!!*-

Pd '.*!


F !!!!

!*.1

; !*'1

r !*.!,!21',ts !*'1.-1''!.

tebal head

th !*'1.-2'.+!


t '*1+11-,.-,

L in

8 ++*2 in

ts !*1 in

A 11*-1 in

= '*.1.2'12+ in k'A/= '*-1!1'+. k

b -*.-1 in k2

P '.*! psi

teta '! derjat

jumlh buah

''12.*'- ib

#' '!!21!'-!*2!2+

C.3) 6ashing Tank aulia

kondisi operasi


laju alir massa 1,!*,

densittas campuran .,*-1+'.+,'

3aktu tinggal '


19/201

4aktor keaman !"


laju alir volumetrik 1*,.+.,2

volume bahan (Vb) 1*,.+.,2

volume tangki -*''+'2-11,


volume elipsiodal head (Vh) !*'!.V atas 7 V ba3ah !*2'222222-

5iameter tangki (5t) '*1-',!!1!!.

Tinggisilinder *'+.!'!!'1

Tinggi head (8h) !*,,-1'1

Tinggi total (8t) *,,-1'1',


tinggi cairan (8li9) *!12+-',1,

gravitasi ,*.

Ph 2-,*-'

Pd !*+tebal didnidng silinder tangki

F !!!!

!*.1

; !*'1

r !*-.1,1!1!+

ts !*'2'-2''

tebal head

th !*'2'.,-'22

Tebal Cone

Tc !*'2-,.!+!1.ran(angan pengaduk

5a/dt !*+

3/da !*

c/5t !*

L/5a !*1

?/5t !*!.

dimana

5a !*2.-2!!! m

L !*'1-',!!1!' m

; !*1'.--'21 m

@ !*'1-1!+!' m

? !*'!+2--+'2m

Po!er Penagduk

n +

viskositas !*.!'

rho .,*-1+'.+,'

5a !*2.-2!!!

gc *


20/201

= '-2'*'-,+-1

p 1

P .-'*+,,!2!2,',

C.3+ ettler --- aulia

kondisi operasi


laju alir massa ++12*,'!

densittas campuran ,+*,1,2-13aktu tinggal !*12.1!-!1.

4aktor keaman !"


laju alir volumetrik +*.'.+,'2-

volume bahan (Vb) *-,+2!,

volume tangki *.-1.-



V atas 7 V ba3ah !*2'222222-

5iameter tangki (5t) '*!-,!--1

panjang silinder *-!.1,.

panjang head (Ph) !*2,-12,.

panjang total (Pt) *--21,-'2+


tinggi cairan (8li9) !*.,,'.,-,++

gravitasi ,*.

Ph .'1!*.!

Pd '-*+-


F !!!!

!*.1

; !*'1

r !*1,1'.-22

ts !*'+2.',,,.

tebal head

th !*'+2.2'2


21/201


t !*12.1!-!1.

C.4 "a(uum dr#er aulia

kondisi operasi


laju alir massa ++12*,!

densittas campuran .1*,,!+2+1!'

3aktu tinggal '

4aktor keaman !"


laju alir volumetrik 1*'.,+2!+

volume bahan (Vb) 1*'.,+2!+

volume tangki 2*2-1.,



V atas 7 V ba3ah !*2'222222-

5iameter tangki (5t) '*-2-.1-

Tinggisilinder +*!','11.

Tinggi head (8h) !*++!,+2

Tinggi total (8t) +*2.'-+.+


tinggi cairan (8li9) *-'122!-!'.gravitasi ,*.

Ph '!,2*-2

Pd '*'


F !!!!

!*.1

; !*'1

r !*22..'.,2

ts !*'1--',---

tebal headth !*'1--2'-1+


22/201

C.45 penampung biodiesel aulia

kondisi operasi


laju alir massa +2.*-!!

densittas campuran .1'*!2'+-1,.1

3aktu tinggal '2.

4aktor keaman !"


laju alir volumetrik 1*'2,.2

volume bahan (Vb) .2*..!+!!-'

volume tangki '!*+.2!12+.!,



V atas 7 V ba3ah !*2'222222-

5iameter tangki (5t) *.-'-22,..

Tinggisilinder -*2-+1,-1 Tinggi head (8h) !*,1,,+'-+-

Tinggi total (8t) ,*1,,+'-+2,


tinggi cairan (8li9) -*+2''-2,'+

gravitasi ,*.

Ph 2,*

Pd 2*'!


F !!!!

!*.1; !*'1

r '*,'.1..+,+

ts !*+!...21.

tebal head

th !*+!,+',,!.

C.4) hold Tank aulia

kondisi operasi


laju alir massa .+,*2+!

densittas campuran .2+*+2'!!,!-,


23/201

3aktu tinggal '

4aktor keaman !"


laju alir volumetrik !*,..1+.-!2

volume bahan (Vb) !*,..1+.-!2

volume tangki '*'-,+1.++-

Volume silinder (Vs) '*1-volume elipsiodal head (Vh) !*'!.

V atas 7 V ba3ah !*2'222222-

5iameter tangki (5t) !*.21+22.

Tinggisilinder '*--!+,-2

Tinggi head (8h) !*'1..''1,

Tinggi total (8t) *'1..''1,


tinggi cairan (8li9) '*2-,!-12.-

gravitasi ,*.

Ph '++*22Pd '.*++


F !!!!

!*.1

; !*'1

r !*+'-2'.+

ts !*'++,-2+

tebal head

th !*'++1-1..

C.4) ,lash drum aulia

kondisi operasi


laju alir massa .+,*2+!

densittas campuran .2+*+2'!!,!-,3aktu tinggal '

4aktor keaman !"


laju alir volumetrik !*,..1+.-!2

volume bahan (Vb) !*,..1+.-!2

volume tangki '*'-,+1.++-



24/201


V atas 7 V ba3ah !*2'222222-

5iameter tangki (5t) !*-22-2,.!2

Tinggisilinder *!!'.!,+'.

Tinggi head (8h) !*','2.'-+1

Tinggi total (8t) *2.1+++'

menentukan tebal shell dan tebal headtinggi cairan (8li9) *',-,-'2.+

gravitasi ,*.

Ph '.!+*!1

Pd ',*!1


F !!!!

!*.1

; !*'1

r !*.2+,!

ts !*'+',!+-tebal head

th !*'+',!,,','

C.4) ,lash drum -- aulia

kondisi operasi

kondisi penimpanan p0' atmlaju alir massa +-+*..!

densittas campuran ,+*,,'2.++!2

3aktu tinggal '

4aktor keaman !"


laju alir volumetrik !*1!2'+

volume bahan (Vb) !*1!2'+

volume tangki !*2!++212!.



5iameter tangki (5t) !*2'1+++'1

Tinggisilinder '*.+!2-++

Tinggi head (8h) !*'1.2!2!+

Tinggi total (8t) *'+-+!+.+1'


tinggi cairan (8li9) '*-!+.,11,2

gravitasi ,*.


25/201

Ph '1-+.*.+

Pd '.*2.


F !!!!

!*.1

; !*'1

r !*!2--'!-ts !*'.2-'2--

tebal head

th !*'.-'1+'+

C.5) ,lash drum lll aulia

kondisi operasi


laju alir massa +1*-!!

densittas campuran .,.*'2!'1+,2+

3aktu tinggal '

4aktor keaman !"


laju alir volumetrik !*+.1'!-,

volume bahan (Vb) !*+.1'!-,

volume tangki !*1.'1Volume silinder (Vs) *11


V atas 7 V ba3ah !*2'222222-

5iameter tangki (5t) !*2!1,,21,

Tinggisilinder '*.'--..,1.-

Tinggi head (8h) !*'1'+.+'

Tinggi total (8t) *'!-1-.1


tinggi cairan (8li9) '*2.'-,+-

gravitasi ,*.Ph '+.'+*,

Pd '.*1


F !!!!

!*.1

; !*'1

r !*!,2+.21

ts !*'-,,.!2'-


26/201

tebal head

th !*'.!!'1

C.5 Tanki gliserol aulia

kondisi operasi


laju alir massa +'*'!!

densittas campuran .,1

3aktu tinggal -

4aktor keaman !"


laju alir volumetrik !*+-!1!-,

volume bahan (Vb) *.-2!'''-volume tangki +!*21'++'+!.



V atas 7 V ba3ah !*2'222222-

5iameter tangki (5t) *.'!.+1

Tinggisilinder 1*2!+-2.21

Tinggi head (8h) !*-!11,2!.'

Tinggi total (8t) -*!11,2!.'


tinggi cairan (8li9) 1*+2+11!--gravitasi ,*.

Ph +-,-*.+

Pd *.


F !!!!

!*.1

; !*'1

r '*+!1'','2

ts !*!+1-+,+,

tebal headth !*!+,!!+1


27/201

'*!! atm NO

!*!! c 1

*!! hari - jam 2

3

4

,,.*,, %g/m 5

++++++*+! kg/jam

!*!

+++*,! m/jam

!*+, m

'!*!! kolam

!*1 m

.+*,! m

-*. m '

+*, m '

*,' m '2,

NO

T0! c 1

kg/jam 2

kg/m 3

jam 4

5


28/201

m/jam

m

m

5t

5t

5t

m '--*2!,+.2+ inm

m

m

m

m/s

pa '*+2 psi

psi

m ..*.!+-+'. in

in

in

T0! c

kg/jam

kg/m

jam


29/201

m/jam

m

m

5t .*11-,+1.+2

'*-''1.,'2,

m 2,*.-1!2--2 inm !*!+!!,!

m

m

m

m/s

pa '*!' psi

psi

m +*2+-1.. in

in

in

in

kg/jam *+ ib/mnit '+1*,,+. ib/jam

kg/m '2*'+.,+ ib/4t

4t/jam

in !* m

rpm

4t '1*+ m

ib/jam *+ ib/mnit

hp

hp ' hp

' jam *++- ib/menit

2!menit


30/201

' m '2*'1 ib/4t

1*'+2- 4

NO

T02! c 1

kg/jam 2

kg/m 3

jam 4

5

6

m/jam

m

m 5iamter tingggi

5t '

5t

5t

m 21*-!,+2,1. in 1*+-1-.,

m ''*+'.,,!2 in '!*,1'1.

m '2*+-2-. in '*2.,+-

m '2+*-2-. in '*2.,+-

m

m/s

pa +*1 psi

psi

m *.1+-+-2+ in

in !*1 !*!!21 m

in


31/201

rps

kg/m*s

kg/m

m

4t/s

j/s *.-2'!.'.hp

celcius .2 F

celcius '+! F

kg/jam

m

m

m ,*-+-22+ 4t

m 1*1'-+1122.+ 4t

m 1*1'-+1122.+ 4t

m '2, 4t

m 4t

4t

m ''*'! 4t

m 1*. 4t

m !*-

4t

ib/jam*4t

m !*1+-1-.,'- 4t

m

m

m

kg/m 1.*.2.! ib/4t

kg/m*s ''1*2-2 ib/4t*hr

rpm


32/201

m !*'2+!+'1 4t

m 1*.!.-'-+ 4t

btu*/hr*4t*F

btu*/hr*4t*F

btu*/hr*4t*F

* atm

22..*++%g/jam

,+*+-2.'-,+', %g/m-*!,22222'-m/jam 1!*2'2+Ft/jam

++-*- kg/jam NO

'!..*1'+1!,,kg/m 1

2+'*!-kg/jam 2

2*2',.-1+,m/jam 3

' in !*!1+ m 4

!*2-1!.,'2 5

2!! %g/m 6

2*2',.-1+,m/jam-*!,22222'-m/jam

'-!*',,,.,!+ m 2!'+*-,1 Ft/jam

!*, NO

&!*'!-.'1.-+2 1

!*',+2m 2

+ jam '++! menit 3


33/201

4

5

6

NO

T0! c 1

kg/jam 2

kg/m 3

jam 4

5

6

m/jam

m

m

5t 2*2.12---!2

'*-'11+'

m 2*.'2+-+!- in

m !*'-,'.+2-

m

m

m

m/s

pa +*! psi

psi

m '*,!2.-!+ inin

in


34/201

rps

kg/m*s

kg/m

m

4t/s

j/s *+',!+,'.hp

NO

T02! c 1

kg/jam 2kg/m 3

jam

m/jam

m

m 5iamter tingggi

5t '

5t

5tm 1'*,'!.1 in +*2,!,

m '1*2.-!.12 in '*.!-.

m '*.!--1-' in '*!2--

m '-,*!'.1,,, in '+*,+'.

m

m/s

pa +*22 psi


35/201

psi

m 1*2'+11'+2 in

in !*1 !*!!21 m

in

NO

T02! c 1kg/jam 2

kg/m

jam

m/jam

m

m 5iamter tingggi

5t '

5t5t

m '+*,-'-'-' in '*+-2++

m ++*,'1',,1'+ in *-+,

m *-+,,. in !*'',''

m 1*+!'!22!,, in +*22-12

m

m/s

pa *-2 psi

psi

m -*+.1.221.12 in

in !*1 !*!!21 m

in


36/201

NO

T02! c 1

kg/jam 2

kg/m 3

jam 4

5

m/jam

m

m 5iamter tingggi

5t '

5t

5t

m 1-*-!!+' in +*.!.2

m ''1*+!!2.++ in ,*2'2-+

m '+*+1!.111 in '*!!,

m '++*1!.111 in '*!!,

m

m/spa *2- psi

psi

m .*.1!'-''!1 in

in !*1 !*!!21 m

in


37/201

rps

kg/m*s

kg/m

m

4t/s

j/s '*+',+'!-+'1hp '*--+2

celcius .2 Fcelcius '+! F

kg/jam

m

m

m .*1+.',..+2 4t

m +*.1!!.,', 4t

m +*.1!!.,', 4t

m '! 4t

m 2 4t

4t

m ,*-1 4t

m 1* 4t

m !*-

4t

ib/jam*4t

m !*+.!.2'.1' 4t

m

m

m

kg/m 12*12,,' ib/4t

kg/m*s ''1*2-2 ib/4t*hr

rpm


38/201

m !*'2+!+'1 4t

m 1*'2+++.1!, 4t

btu*/hr*4t*F

btu*/hr*4t*F

btu*/hr*4t*F

NO

T02! c 1

kg/jam 2

kg/m

jam

m/jam

m

m 5iamter tingggi

5t '

5t

5t

m '2*!,+21 in '!*1!-

m 1*!-.+,1' in '*!!21+

m '*1!,.''12 in *21.'.m '1*!,.''12 in 2*1.'.

m

m/s

pa 2*++ psi

psi


39/201

m 2*!',2'2 in

in !*1 !*!!21 m

in

A

NO

T0! c 1

kg/jam 2

kg/m 3 jam

m/jam

m

m

5t ' >

5t

5t NO

m 2+*!2--+.!+1 in 1

m ',*!++'+ 2

m '2*!'2,-!'' 3

m +*-''.'2

m

m/s

pa '*-, psi

psi

m *!.-+! in

in

in


40/201

jam

NO

T02! c 1

kg/jam 2

kg/m 3

jam

m/jam

m

m 5iamter tingggi

5t ' 5t

5t

m 2+*2!'.21', in 1*.++,

m ',*!--!+ in '!*-22,

m '2*'1!+22 in '*+1.2

m '2'*1!+22 in '*+1.2

m

m/s

pa ,*22 psipsi

m *!!2,2 in

in !*1 !*!!21 m

in


41/201

rps

kg/m*s

kg/mm

4t/s

j/s 1*.2,+1-12 -*2.

NO

T02! c 1

kg/jam 2

kg/m 3

jam 4

5

6

m/jam

m

m 5iamter tingggi5t '

5t

5t

m 2'*-,++!-, in 1*'+,11

m '*1...+'+2 in '!*,,!-

m '1*++.2!1'. in '*.-.+

m '1+*+.2!1'. in '*.-.+

m

m/spa *.2 psi

psi

m !*.,-'!21 in

in !*1 !*!!21 m


42/201

in

rps

kg/m*s

kg/m

m

4t/s

j/s '*'11-'!2hp '*+++'+

celcius .2 F

celcius '+! F

kg/jam

m

m

m ,*'1+-.,,2, 4t

m 1*','!'2!'. 4t

m 1*','!'2!'. 4t

m '+, 4t

m , 4t

4t

m '!*++ 4t

m 1*1 4t

m !*-

4t

ib/jam*4t


43/201

m !*1'+,11!2' 4t

m

m

m

kg/m 11*1!!'--'+ ib/4t

kg/m*s ''1*2-2 ib/4t*hr

rpm

m !*'2+!+'1 4t

m 1*+--2'.!2!. 4t

btu*/hr*4t*F

btu*/hr*4t*F

btu*/hr*4t*F

A

NO

T0! c 1

kg/jam 2

kg/m 3 jam 4

.''!*!! 5

6

m/jam 7

m

m

5t '


44/201

5t

5t

m 2*-!1-'- in >

m ','*''-'2,.

m '1*,2+!-. NO

m *,-!!!,+ 12

m 3

m/s 4

pa '*2. psi

psi

m '*.1.2'12 inin

in

jam

!*1'*'-'

!*!1

NO

T02! c 1

kg/jam 2

kg/m 3

jam 4


45/201

5

6

m/jam 7

m

m 5iamter tingggi

5t '

5t5t

m 2'*..121,., in 1*'1-'.

m '*--'',2. in '!*'+.

m '1*+-'+'+,2 in '*.,.1

m '1+*-'+'+,2 in '*.,.1

m

m/s

pa *.. psi

psi

m !*,+.,, in

in !*1 !*!!21 m

in

rps

kg/m*s

kg/m

m

4t/s


46/201

j/s '*'2.!-2!.-hp '*+2!.1

A

NO

T0! c 1

kg/jam 2

kg/m 3 jam +*'''.+1menit 4

5

6

m/jam 7

m

m

5t '

5t

5t

m +*+.'-,+.+ in >

m '-*++..+1

m '!*2!',.-' NO

m '+.*2.++-. 1

2

m 3

m/s 4

pa '*'. psi

psi

m '*+!2,-+ in

in

in


47/201

jam

NO

T02! c 1

kg/jam 2

kg/m 3

jam 4

m/jam

m

m 5iamter tingggi

5t '

5t

5t

m 1*22-+.-1+ in +*..12

m '1-*,..+22 in '*'212,

m '*'212.-'.. in '*!,-'+'

m '.+*',2!2+ in '1*1,,-

mm/s

pa +*1' psi

psi

m 2*'-+-- in

in !*1 !*!!21 m

in


48/201

NO

T02! c 1

kg/jam 2

kg/m 3

jam

m/jam

m

m 5iamter tingggi

5t '

5t

5t

m '1'*!2,+,'+ in '*1.,'

m !*'.,.2, in 1*'-.1m -*-2--.2 in *'+-.'

m --*2--.2 in '*+-.'

m

m/s

pa ,*! psi

psi

m -1*1+-+21- in

in !*1 !*!!21 m

in

NO

T02! c 1

kg/jam 2

kg/m 3


49/201

jam 4

5

m/jam

m

m 5iamter tingggi

5t ' 5t

5t

m *,,2,!+' in *.!-.

m 2-*,,.2!.', in 1*222'11

m .*+,,2!+ in !*-!.2,

m .+*,,2!+ in -*!.2,+

m

m/s

pa *!2 psipsi

m '2*,,.+21!1 in

in !*1 !*!!21 m

in

NO

T02! c 1

kg/jam 2

kg/m 3 jam 4

5

m/jam

m

m 5iamter tingggi

5t '


50/201

5t

5t

m !*'.2!'!11. in *1'11!'

m ,!*11.!'2- in -*1+21!

m -*1+21!2,+ in !*2..-1

m '!1*21'!2,1 in .*.!+1

m

m/s

pa *2 psi

psi

m '1*!,!!1-, in

in !*1 !*!!21 m

in

NO

T02! c 1kg/jam 2

kg/m 3

jam 4

m/jam

m

m 5iamter tingggi

5t '

5t5t

m +*'11'+1 in *!',+

m -*+2122-+ in 2*!..!

m 2*!..!!2' in !*1!+

m .+*1++.1- in -*!+1-

m

m/s


51/201

pa *. psi

psi

m '*!--2!2' inin !*1 !*!!21 m

in

NO

T02! c 1

kg/jam 2

kg/m

jam

m/jam

m

m 5iamter tingggi5t '

5t

5t

m *.11+2',. in '*,.-,1

m -'*122-.1, in 1*,2.1-

m 1*,2.121+,+ in !*+,2,..

m .*+,,,'2, in 2*,1-.

m

m/spa *'1 psi

psi

m ''*,--'!,, in

in !*1 !*!!21 m


52/201

in

NO

T02! c 1

kg/jam 2

kg/m

jam

m/jam

mm 5iamter tingggi

5t '

5t

5t

m ''!*2.,-+2. in ,*',,'1

m '*--,+,2 in '.*+,.

m -*21,-+2- in *!+,-,

m -2*1,-+2- in *!+,-,

mm/s

pa 2*,1 psi

psi

m 11*',+.-, in

in !*1 !*!!21 m

in


53/201

densitas 998.9857677323

Komponen V (m3/jam)

C3H5(OOC)3 4!339.555 9"7.34" 4.783

#O4 8.889 1!82" ".""5

$mp%&ities 29.333 932 "."31

COOH 66.667 87".415 "."77

H2O 439!999.956 1!""" 44"

'ota 444!444.4"" 5!529.755 444.896

densitas 998.9857677323

Komponen V (m3/jam)

C3H5(OOC)3 4!339.555 9"7.34" 4.783

#O4 8.889 1!82" ".""5

$mp%&ities 29.333 932 "."31

COOH 66.667 87".415 "."77

H2O 439!999.956 1!""" 44"

'ota 444!444.4"" 5!529.755 444.896

(*+/jam)

,ensitas(K+/m3)

(*+/jam)

,ensitas(K+/m3)


54/201


55/201


56/201


57/201


58/201

densitas 942.4768179419

Komponen V (m3/jam)

C3H5(OOC)3 4!317.86" 9"7.34" 4.759

#O4 8.84" 1!82" ".""5

$mp%&ities 29.19" 932 "."31

COOH 66.33" 87".415 "."76

H2O 2!2"".""" 1!""" 2

Ca-entonite 66.22" 2!6"" "."25

'ota 6!688.44" 8!129.755 7."97

densitas 1"88.53145"99"3

Komponen V (m3/jam)

C3H5(OOC)3 21.59" 9"7.34" "."24

#O4 "."4" 1!82" "."""

$mp%&ities 29.19" 932 "."31

(*+/jam)

,ensitas(K+/m3)

(*+/jam)

,ensitas(K+/m3)


59/201

COOH ".33" 87".415 "."""

H2O 33".""" 1!""" "

Ca-entonite 66.22" 2!6"" "."25

'ota 447.37" 8!129.755 ".411

densitas 933.4984835379

Komponen V (m3/jam)

C3H5(OOC)3 4!296.27" 9"7.34" 4.735

#O4 8.8"" 1!82" ".""5

COOH 66.""" 87".415 "."76

H2O 1!87".""" 1!""" 2

'ota 6!241."7" 4!597.755 6.686

(*+/jam)

,ensitas(K+/m3)


60/201

densitas 9"7.555"286172

Komponen V (m3/jam)

C3H5(OOC)3 4!272.79" 9"7.34" 4.7"9

COOH 65.67" 87".415 "."75H2O 19.63" 1!""" "."2

'ota 4!36"."9" 2!777.755 4.8"4

(*+/jam)

,ensitas(K+/m3)


61/201

densitas 18"9.67614392"1

Komponen V (m3/jam)

2so4 ".644 1!84".""" "."""2o "."13 1!""".""" "."""

'ota ".657 "."""

(*+/jam)

,ensitas(K+/m3)


62/201

densitas 9"6.1643887962

Komponen V (m3/jam)

C3H5(OOC)3 4!274.787 9"7.34" 4.711

COOH 65.67" 87".415 "."75

CH3OH 13.""" 728 "."18

H20O4 ".644 1!84".""" "."""

H2O ".14" 1!""" "."""

'ota 4!354.241 5!345.755 4.8"5

(*+/jam)

,ensitas(K+/m3)


63/201


64/201

densitas 18"9.67614392"1

Komponen V (m3/jam)

2so4 ".644 1!84".""" "."""

2o "."13 1!""".""" "."""

'ota ".657 "."""

(*+/jam)

,ensitas(K+/m3)


65/201

viskositas !*.!'

densitas 9"6.542

Komponen x i x.i

C3H5(OOC)3 4!274.8"" 9"7.34" 98.42 893.""4"28

COOH 3.28" 87".415 "."8 ".696332

COOCH3 65.51" 85".42 1.51 12.841342'ota 4!343.59" 9"6.542

densitas 946.912

Komponen x i x.i

CH3OH 5.84" 782 56.8" 44417.6"

H20O4 ".64" 1!84" 6."4 11113.6"

H2O 4.17" 1!""" 39.16 3916".""

'ota 1".65" 946.912

(*+/jam)

(*+/jam)


66/201

densitas 2!"73.5""

Komponen x i x.i

CH3OH 5.84" 2!13" 95."" 2"235".""

H20O4 ".64" 1!""" 5."" 5""".""

'ota 6.48" 2!"73.5""

(*+/jam)


67/201

densitas 889."286943275

Komponen V (m3/jam)

C3H5(OOC)3 4!274.787 9"7.34" 4.711

COOH 3.284 87".415 ".""4

CH3OH 846.4"8 782 1."82

NaOH 4".61" 2!13" "."19

COOCH3 65.5"" 873 "."75

H2O 1".687 1!""" "."11

'ota 5!247.275 6!562.755 5.9"2

(*+/jam)

,ensitas(K+/m3)


68/201


69/201

viskositas !*.!'

densitas 851.914

Komponen x i x.i

C3H5(OOC)3 85.496 9"7.34" 1.94 17.6"2396

COOH 3.284 87".415 "."7 ".6"929"5

CH3OH 17.384 782 ".39 3."498C3H5(OH)3 19.842 895 ".45 4."275

COOCH3 4!279.921 85".42 97."9 825.672778

NaOH 1.828 213" "."4 ".852

H2O ".481 1!""" "."1 ".1

'ota 4!4"8.234 851.914

(*+/jam)


70/201

densitas 9"3.758

Komponen x i x.i

CH3OH 368.925 782 43.97 34384.54C3H5(OH)3 421."86 895 5".19 4492"."5

NaOH 38.78 213" 4.63 9851.25

H2O 1".2"" 1!""" 1.22 122".""

'ota 838.991 9"3.758

densitas 892.3754183491

Komponen V (m3/jam)

C3H5(OOC)3 85.496 9"7.34" "."94

COOH 3.284 87".415 ".""4

CH3OH 17.384 782 "."22

C3H5(OH)3 19.84 895 "."22

(*+/jam)

(*+/jam)

,ensitas(K+/m3)


71/201

NaOH 1.83" 2!13" ".""1

COOCH3 4!279.92" 873 4.9"3

H2O 882.64" 1!""" ".883

'ota 5!29".393 5.928


72/201


73/201

densitas 853.99"43645"1

Komponen Densitas (kg/m3) V (m3/jam)

C3H5(OOC)3 85.5"" 9"7.34 "."94

COOH 3.3"" 87".42 ".""4

COOCH3 4279.92 85".42 5."33

H2O 88.21" 1!""" "."88

'ota 4!456.93" 5.219

(*+/jam)


74/201

densitas 851."614375985

Komponen V (m3/jam)

C3H5(OOC)3 85.5"" 9"7 "."94

COOH 3.28" 87" ".""4

COOCH3 4!279.92" 85" 5."35

'ota 4!368.7"" 5.133

densitas 864.4613""9"79

Komponen V (m3/jam)

CH3OH 374.76" 782 ".479

H2O 14.6"" 1!""" "."15

NaOH 38.25" 2!13" "."18

(*+/jam)

,ensitas(K+/m3)

(*+/jam)

,ensitas(K+/m3)


75/201

C3H5(OH)3 421.1"" 895 ".471

N20O4 ".93" 1!656 ".""1

'ota 849.64" ".983

densitas 864.4613""9"79

Komponen V (m3/jam)

CH3OH 374.76" 782 ".479

H2O 14.6"" 1!""" "."15

NaOH 38.25" 2!13" "."18C3H5(OH)3 421.1"" 895 ".471

N20O4 ".93" 1!656 ".""1

'ota 849.64" ".983

(*+/jam)

,ensitas(K+/m3)


76/201

densitas 942.92916844"6

Komponen V (m3/jam)

H2O 14.6"" 1!""" "."15 NaOH 38.25" 2!13" "."18

C3H5(OH)3 421.1"" 895 ".471

N20O4 ".93" 1!656 ".""1

'ota 474.88" ".5"4

(*+/jam)

,ensitas(K+/m3)


77/201

densitas 898.16"1549634

Komponen V (m3/jam)

H2O 14.6"" 1!""" "."15

C3H5(OH)3 421.1"" 895 ".471

'ota 435.7"" ".485

(*+/jam)

,ensitas(K+/m3)


78/201


79/201


Tekanan (P) '*!! atm

Temperatur (T) !*!! c

Lama Pesediaan (t) *!! hari


,2.*!! %g/m

Laju Alir massa (F) ++++++*+! kg/jam

Faktor keaman !*!


Laju Alir volumetris +1,*'+ m/jam

Volume bahan baku (Vb) 1-.*1' m

jumlah kolam direncanakan 1*!! kolam

Volume bahan baku (Vb)/kolam ''1*-! m

volume keamanan kolam !" '.*.+ m


Panjang .*11 m

Lebar 1*-! m

Tinggi *.1 m

5ensitas (6)


80/201


81/201


82/201


83/201


84/201


85/201


86/201


87/201


88/201


89/201


90/201


91/201

!

!

!!


92/201


93/201

2


94/201


95/201


96/201


97/201


98/201


99/201


100/201

'.+!

'!!!'!

'212*22-

782

895

213"


101/201

1!"""


102/201


103/201


104/201


105/201


106/201


107/201


108/201


109/201


110/201


111/201


112/201


113/201


114/201


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116/201


117/201


118/201


119/201


120/201


121/201


122/201


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127/201


128/201


129/201


130/201


131/201


132/201


133/201


134/201


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140/201


141/201


142/201


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155/201


156/201


157/201


Tekanan (P)

Temperatur (T)

Lama Pesediaan (t)


Laju Alir massa (F)

Faktor keaman


Laju Alir volumetris

Volume bahan baku (Vb)

jumlah kolam direncanakan

Volume bahan baku (Vb)/kolam

volume keamanan kolam !"


Panjang

Lebar

Tinggi

rangkuman #pesi$kasi kolam bahan baku

kode %&'!'

tipe kolam terbuka berbentuk balok

bahan kontruksi dinding betonvolume !*+,

panjang 1*.2

lebar '-*+

tinggi .*2

jumlah '!

C.3 Dekanter aulia

kondisi operasi



densittas campuran ,2*1!.!22+!-

3aktu tinggal '

4aktor keaman !"


5ensitas (6)


158/201


159/201

gravitasi ,*.

Ph -,+!*-

Pd .*.+

tebal didnidng tangki

F !!!!

!*.1

; !*'1r !*,1!,!2+.

ts !*'.-+'+'1

tebal head

th !*'.-++1,'+

C.5 re! Con"e#or $C%1&1'

=ate umpsn msuk 22*'12

6 ;a >entonit 2!!

Laju Alir !*.,,+2-1-kondsi (re! (on"e#or #ang diren(anakan

5ari Tabel >ro3n',-.

5iameter .

Putaran 21

%oe$sien '*

Panjang 1!

kapsitas '+1*,,+.!,12'

Perhitungan da#a pada s(re! Con"e#or

P !*!+-,--

%ebutuhan daa !*!1,,!+!,'

22*'12 kg *!+2 ib

jam ' kg

2!! kg *!+2 ib

m kg

C.) Tangki Pemanas aulia

kondisi operasi


laju alir massa 22..*++!

densittas campuran ,+*+-2.'-,+',

3aktu tinggal '


160/201

4aktor keaman !"


laju alir volumetrik -*!,2222'12

volume bahan (Vb) -*!,2222'12

volume tangki .*1'1,,1'..



5iameter tangki (5t) '*22,!111,.

Tinggisilinder *.!1''',2

Tinggi head (8h) !*+'-12,

Tinggi total (8t) +*'-12.,,1


tinggi cairan (8li9) *+1-+--+

gravitasi ,*.

Ph ,,-+*-

Pd !*,1tebal didnidng silinder tangki

F !!!!

!*.1

; !*'1

r !*.+1'--,,

ts !*'21+-,1

tebal head

th !*'21+.-,'+,

ran(angan pengaduk

5a/dt !*+3/da !*

c/5t !*

L/5a !*1

?/5t !*!.

dimana

5a !*22-2'!, m

L !*'22,!112 m

; !*11!--.++- m

@ !*'1!++. m

? !*'.1,''1m

Po!er Penagduk

n +

viskositas !*!+-.

rho ,+*+-2.'-,+',

5a !*22-2'!,

gc *

= 1'1'*.,,++

p 1


161/201

P '+*'22''1!.


T steam masuk !

T steam %eluar 2!

Bassa steam '!'*'1

Volume tutup ba3ah !*2!..12-'

volume cairan 2*+..--+.2ketinggian ;airan dlm shell(8sh) *,2-'1211!.

5iameter luar tangki '*2.'-111,.

diameter dlm jaket '*2.'-111,.

Ash '1*22.+'!112

Ael *!.-.,1.

Luas Permukaan dindidng jaket(Aj) !

Tinggi jaket *.++',+!-

Lebar ?aket '*-.'-111,.

5iameter eki4alen jaket (5ej) !*!1,+2-+

Laju aliran steam *,2+.+'--laju aliran massa steam persatuan luas +'!*++''1-+.


panjang pengaduk L !*'22,!112

lebar pengaduk ? !*'.1,''1

jarak pengaduk dr dsr tngki ; !*11!--.++-

tinggi larutan T *,2-'1211!.

rho ,+*+-2.'-,+',

viskositas +-*.

n +!

k !*!.1

c !*2

=ej 2*2!+,.-2.

?h +'!

asumsi tj !*!1

5j '*-2,!111,.

c*viskos/k -*''22-2

hi +'*,2!.+1

hoi '1!!

C; +!*.'.,1-2121

=d !*!!1

hd !!

Cd *,!!'',.2,'




1+ 1+


162/201

LBT5 '*'.!.2,2.

A 11,*-,-!!--1

1--+ 1-1*!2.1'

C%+ ,-T/0-

Tekanan (P)

Laju Alir >ahan

6 PEB

Laju Alir volumetris ()

Laju Alir Ampas %eluar

6 Ampas

Laju Alir Filtrasi %eluarLaju AlirVolumetrik keluar(out)

L

psilon

6 Ampas

Volume $ltrat (V)

volume

Perhitungan Volume ;airan

@

A

A

@aktu Tinggal (G)

C.1 degumming aulia

kondisi operasi


laju alir massa 2+'*!-!

densittas ,*+,.+.1-,


163/201


164/201

P '++!*'..2,1'.

C.14 Centri7uge

kondisi operasi


laju alir massa -2+*1-!

densittas ,+1*!,,.1,2'

3aktu tinggal '

4aktor keaman !"


laju alir volumetrik .*!..'---!2

volume bahan (Vb) .*!..'---!2

Volume tangki (Vs) ,*-!1.'+-


5iameter tangki (5t) '*.1'12'+'

tinggi silinder (8s) *2-!2'.

tinggi krucut head (8k) !*1!21

volume krucut !*+2'!2',

panjang total (Pt) +*',2,2

menentukan tebal shell dan tebal headtinggi bahan (8b) *!1..1,12.

gravitasi ,*.

Ph ..*,,

Pd !*2,

tebal didnidng tangki

F !!!!

!*.1

; !*'1

r !*,'-21-.!-

ts !*'2.,+-,+1tebal head

th !*'2.,2,.,

perhitungan ke(epatan pengendapan

r' '*.-1 in

r 1*-1 in

kec*put(omega) 2!!!

igma ,.!!!

%ecepatan pengendapan (vt) !*!!'+1-!-


165/201

g( *

C.12 8a(uum dr#er aulia

kondisi operasi


laju alir massa +1.*!,!

densittas campuran ,!-*'.--12++

3aktu tinggal '

4aktor keaman !"


laju alir volumetrik +*.!+'11-'

volume bahan (Vb) +*.!+'11-'

volume tangki 1*-21!1.2.1



V atas 7 V ba3ah !*2'222222-

5iameter tangki (5t) '*!''-

Tinggisilinder *,!22,+'!,

Tinggi head (8h) !*1!1-.+

Tinggi total (8t) +*11+.!,-,


tinggi cairan (8li9) *2'+1!.-'.gravitasi ,*.

Ph '*.+

Pd '*!


F !!!!

!*.1

; !*'1

r !*21!2''12.1

ts !*'1-!-''+

tebal headth !*'1-!.+2


166/201

'*!! atm NO

!*!! c 1

*!! hari - jam 2

3

4

,,.*,, %g/m 5

++++++*+! kg/jam

!*!

+++*,! m/jam

!*+, m

'!*!! kolam

!*1 m

.+*,! m

1*.2 m

'-*+ m

.*2 m

NO

T0! c 1

kg/jam 2

kg/m 3

jam 4

5


167/201

m/jam

m +'.,*.-1+-,

m !*!+-1.'

5t

5t

5t NO

m '2.*!',!2+- in 1

m 2*!.',+ in 2

m +*!!+-22'- in 3

m +!*!+-22'- in 4

5

m

m/s

pa ''*!1 psi

psi

m .+*!!,11 in

in !*-1

in

T0! c

kg/jam

kg/m

jam

Aalpha 1 derjat !*-

m/jam

m

m5t '!*2,11!

m -*2.,2.' in !*,1!,'

m &!*!-!'.',2

m

m '*-''1.,'2,

m

m


168/201

m/s

pa ''*1 psi

psi

m 2*.'++.'+' in

in

in

kg/jam *+ ib/mnit '+1*,,+. ib/jam

kg/m '2*'+.,+ ib/4t

4t/jam

in !* m

rpm

4t '1*+ m

ib/jam *+ ib/mnit

hp

hp ' hp

' jam *++- ib/menit

2!menit

' m '2*'1 ib/4t

1*'+2-4

NO

T02! c 1

kg/jam 2

kg/m 3

jam 4


169/201

5

6

m/jam

m

m 5iamter tingggi

5t '

5t5t

m 21*-!,+2,1 in 1*+-1-., +*+-1-.,

m ''*+'.,,' in '!*,1'1. '+*!1,.

m '2*+-2-. in '*2.,+- *.'!-,2

m '2+*-2-. in '*2.,+- !+*1,!1

.-+*+,2

m

m/s

pa +*1 psi

psi

m *.1+-+-2 in

in !*1 !*!!21 m

in

rps +!

kg/m*s

kg/m

m

4t/s


170/201

j/s '*221'2+hp *!.'1'-

celcius .2 F

celcius '+! F

kg/jam

m

mm ,*-+-22 4t

m 1*1'-+1122. 4t

m 1*1'-+1122. 4t

m '2, 4t

m 4t

4t

m ''*'! 4t

m 1*. 4t

m !*-

4tib/jam*4t

m !*1+-1-.,' 4t

m

m

m

kg/m 1.*.2.! ib/4t

kg/m*s ''1*2-2 ib/4t*hr

rpm

m !*'2+!+'1 4t

m 1*.!.-'- 4t

btu*/hr*4t*F

btu*/hr*4t*F

btu*/hr*4t*F


171/201

* atm

22..*++%g/jam

,+*+-2.'-,+',%g/m

-*!,22222'-m/jam 1!*2'2+Ft/jam

++-*- kg/jam NO

'!..*1'+1!,,! kg/m 1

2+'*!-kg/jam 22*2',.-1+, m/jam 3

' in !*!1+ m 4

!*2-1!.,'2 5

2!! %g/m 6

2*2',.-1+, m/jam

-*!,22222'- m/jam

'-!*',,,.,!+ m 2!'+*-,1 Ft/jam

!*, NO

&!*'!-.'1.-+2 1

!*',+2m 2

+ jam '++! menit 3

4

5

6

NO

T0! c 1

kg/jam 2

kg/m 3


172/201


173/201

j/s '*,!2--1'hp *+'+-

T0! c NO

kg/jam 1

kg/m 2

jam 3

4

Aalpha 1 derjat !*1-

m/jam .1*2'22 4t/jam 1*2'''.

m

m

5t ,*-!1.'+-

m -*12!' in

m &!*!1'12'+

m

m '*2'-211+'

m

m

m/s

pa +*'' psi

psi

m 2*'.'1''2 in

in

in

rpm '!! rps

4t

4t/jam


174/201

4t/s

NO

T02! c 1

kg/jam 2

kg/m 3

jam

m/jam

m

m 5iamter tingggi

5t '

5t

5t

m 1'*,'!.1 in +*2,!, *2,!,

m '1*2.-!.2 in '*.!-. '!*2+,1

m '*.!--1-' in '*!2-- *!1,,

m '-,*!'.2 in '+*,+'. .!*'!,1

,1*1,

mm/s

pa +*22 psi

psi

m 1*2'+11'+ in

in !*1 !*!!21 m

in


175/201

densitas 998.9857677323

Komponen V (m3/jam)

C3H5(OOC)3 4!339.555 9"7.34" 4.783

#O4 8.889 1!82" ".""5

$mp%&ities 29.333 932 "."31

COOH 66.667 87".415 "."77

H2O 439!999.956 1!""" 44"

'ota 444!444.4"" 5!529.755 444.896

densitas 936.5"8"664"37

Komponen V (m3/jam)

C3H5(OOC)3 4!317.56" 9"7.34" 4.758

#O4 8.84" 1!82" ".""5

$mp%&ities 29.19" 932 "."31

COOH 66.33" 87".415 "."76

H2O 2!2"".""" 1!""" 2

'ota 6!621.92" 5!529.755 7."71

(*+/jam)

,ensitas(K+/m3)

(*+/jam)

,ensitas(K+/m3)


176/201

2!

densitas 999.9948424212

Komponen V (m3/jam)

C3H5(OOC)3 21.7"" 9"7.34" "."2392

#O4 "."4" 1!82" ".""""2

$mp%&ities ".15" 932 "."""16

COOH ".33" 87".415 "."""38

H2O 437!799.96" 1!""" 438

'ota 437!822.18" 5!529.755 437.824

(*+/jam)

,ensitas

(K+/m3)


177/201

densitas 942.4768179419

Komponen V (m3/jam)

C3H5(OOC)3 4!317.86" 9"7.34" 4.759

#O4 8.84" 1!82" ".""5

$mp%&ities 29.19" 932 "."31

COOH 66.33" 87".415 "."76

(*+/jam)

,ensitas(K+/m3)


178/201

H2O 2!2"".""" 1!""" 2

Ca-entonite 66.22" 2!6"" "."25

'ota 6!688.44" 8!129.755 7."97


179/201


180/201


181/201


182/201

densitas 945."299285961

Komponen V (m3/jam)

C3H5(OOC)3 4!296.27" 9"7.34" 4.735

#O4 8.8"" 1!82" ".""5

COOH 66.""" 87".415 "."76

H2O 3!272.5"" 1!""" 3

'ota 7!643.57" 8."88

(*+/jam)

,ensitas(K+/m3)


183/201


184/201

C.3 Dekanter aulia

kondisi operasi



densittas campuran Atas ,2*1!.!22+!+

,2.*1'1 densitas campuran ba3ah ,,,*,,

Viskositas campuran !*.!'

t tinggal '*2+...22

4aktor keaman !"


185/201

-1*-+,Menentukan dimensi tangki

laju alir volumetrik +1,*!'-1.!1.

volume bahan (Vb) ''1*.-...2!!

volume tangki ',*!1+22!



5iameter tangki (5t) *-1,21,.,

panjang silinder ''*-.,!1.,22

panjang head (Ph) !*,,,!..+-

panjang total (Pt) '*'1.-1+2'


tinggi cairan (8li9) *'!,+'1-

gravitasi ,*.

Ph .-1+*1

Pd !*-2tebal didnidng silinder tangki

F !!!!

!*.1

; !*'1

r '*.-,.'-2+,+

ts !*'1'

tebal head

th !*'111'+,


186/201


187/201


188/201


189/201


190/201


191/201


192/201


193/201

T0! c

kg/jam

kg/m

kg/m

kg/m*s

jam


194/201

m/jam

m +!,*+2','++-

m !*!+'-1-,+'

5t

5t5t

m '+.*!'22,'' in

m +++*!1!!-,,- in

m -*!!+'-.. in

m 1'.*!1.+',21, in

m

m/s

pa +*'- psi

psi

m -+*!!.+12212 in

in !*-1

in


195/201


196/201


197/201


198/201


199/201


200/201


201/201

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