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TRANSCRIPT
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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)
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Menentukan dimensi tangki
laju alir volumetrik !*!1+-!!-2,
volume bahan (Vb) .*11-,+1.+2
volume tangki '!*2,11!'1+
Volume silinder (Vs) '*1-
volume krucut '/ phi r
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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 ,!
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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)
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C.1 degumming aulia
kondisi operasi
kondisi penimpanan p0' atm
laju alir massa 2+'*!-!
densittas ,*+,.+.1-,
3aktu tinggal '
4aktor keaman !"
Menentukan dimensi tangki
laju alir volumetrik 2*2.12---!2
volume bahan (Vb) 2*2.12---!2
volume tangki .*!.'+-
Volume silinder (Vs) '*1-
volume krucut '/ phi r
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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
kondisi penimpanan p0' atm
laju alir massa +2!*!,!densittas campuran ,!-*111!.2'-
3aktu tinggal '
4aktor keaman !"
Menentukan dimensi tangki
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.
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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+
Peren(anaan *aket Pemanas
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'-.-
luas permukaan dinding
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!+-'.
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?h +'!
asumsi tj !*!1
5j '*1211,''+
c*viskos/k -*''22-2
hi +-*+'',1.-
hoi '1!!
C; +1*,2!+.',-=d !*!!1
hd !!
Cd -*-!',
hot Duida cold Duida selisish
+. #hu rend4ah .2 '2
+. shu tinggi '+! '!.
1+
LBT5 '*'.!.2,2.
A 1!-*-.1111+.22
C.3 penampungmetanol aulia
kondisi operasi
kondisi penimpanan p0' atm
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,
Volume silinder (Vs) '*1-
volume elipsiodal head (Vh) !*'!.
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-
menentukan tebal shell dan tebal head
tinggi cairan (8li9) 2*+,1-'!
gravitasi ,*.
Ph +++''*
Pd *2
tebal didnidng silinder tangki
F !!!!
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!*.1
; !*'1
r '*2!!-!11'
ts !*'''2'21-
tebal head
th !*''',-!'
C.) ettler aulia
kondisi operasi
kondisi penimpanan p0' atm
laju alir massa +1+*+!
densittas campuran ,2*-2.1'3aktu tinggal
4aktor keaman !"
Menentukan dimensi tangki
laju alir volumetrik +*2,.1'+,..,
volume bahan (Vb) ,*,-!,,---
volume tangki ''*-2+1,-
Volume silinder (Vs) *11
volume elipsiodal head (Vh) !*'!.
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,,-,
menentukan tebal shell dan tebal head
tinggi cairan (8li9) '*12'!+-1-
gravitasi ,*.
Ph ''2*!+
Pd '.*'
tebal didnidng silinder tangki
F !!!!
!*.1
; !*'1
r !*.'22.1+
ts !*'1,'1-.-.
tebal head
th !*'1,'2..!.2
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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 !"
Menentukan dimensi tangki
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
menentukan tebal shell dan tebal head
tinggi cairan (8li9) *',!2!!-
gravitasi ,*.
Ph 222!!*1,Pd 2*.!
tebal didnidng silinder tangki
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
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; !*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
kondisi penimpanan p0' atm
laju alir massa 1+-*-1
densittas campuran ..,*!.2,+-1
3aktu tinggal '
4aktor keaman !"
Menentukan dimensi tangki
laju alir volumetrik 1*,!12,,
volume bahan (Vb) 1*,!12,,
volume tangki -*!.-!-2-..Volume silinder (Vs) '*1-
volume elipsiodal head (Vh) !*'!.
V atas 7 V ba3ah !*2'222222-
5iameter tangki (5t) '*12,1.!!+
Tinggisilinder *','22!+!.
Tinggi head (8h) !*,,1-11'
Tinggi total (8t) *,,1-11'
menentukan tebal shell dan tebal head
tinggi cairan (8li9) *!1',22,.+'
gravitasi ,*.Ph 21,!*!
Pd !*+'
tebal didnidng silinder tangki
F !!!!
!*.1
; !*'1
r !*-.+-,'1'!
ts !*'2!.'!.,1
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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..
Peren(anaan *aket Pemanas
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
luas permukaan dinding
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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.
hot Duida cold Duida selisish
+. #hu rend4ah '+! '!.
+. shu tinggi ',+ 1+
1+
LBT5 --*,!11!.
A ,'*1'!,'.,''
C.33 ettler -- aulia
kondisi operasi
kondisi penimpanan p0' atm
laju alir massa 1+-*1
densittas campuran .--*.2!.13aktu tinggal '*1+11-,.-,
4aktor keaman !"
Menentukan dimensi tangki
laju alir volumetrik 1*,--+1++!+
volume bahan (Vb) ,*.2!!+
volume tangki ''*!.2122+1
Volume silinder (Vs) *11
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volume elipsiodal head (Vh) !*'!.
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 '.*!
tebal didnidng silinder tangki
F !!!!
!*.1
; !*'1
r !*.!,!21',ts !*'1.-1''!.
tebal head
th !*'1.-2'.+!
perhitungan 3aktu tinggal
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
kondisi penimpanan p0' atm
laju alir massa 1,!*,
densittas campuran .,*-1+'.+,'
3aktu tinggal '
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4aktor keaman !"
Menentukan dimensi tangki
laju alir volumetrik 1*,.+.,2
volume bahan (Vb) 1*,.+.,2
volume tangki -*''+'2-11,
Volume silinder (Vs) '*1-
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',
menentukan tebal shell dan tebal head
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 *
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= '-2'*'-,+-1
p 1
P .-'*+,,!2!2,',
C.3+ ettler --- aulia
kondisi operasi
kondisi penimpanan p0' atm
laju alir massa ++12*,'!
densittas campuran ,+*,1,2-13aktu tinggal !*12.1!-!1.
4aktor keaman !"
Menentukan dimensi tangki
laju alir volumetrik +*.'.+,'2-
volume bahan (Vb) *-,+2!,
volume tangki *.-1.-
Volume silinder (Vs) *11
volume elipsiodal head (Vh) !*'!.
V atas 7 V ba3ah !*2'222222-
5iameter tangki (5t) '*!-,!--1
panjang silinder *-!.1,.
panjang head (Ph) !*2,-12,.
panjang total (Pt) *--21,-'2+
menentukan tebal shell dan tebal head
tinggi cairan (8li9) !*.,,'.,-,++
gravitasi ,*.
Ph .'1!*.!
Pd '-*+-
tebal didnidng silinder tangki
F !!!!
!*.1
; !*'1
r !*1,1'.-22
ts !*'+2.',,,.
tebal head
th !*'+2.2'2
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perhitungan 3aktu tinggal
t !*12.1!-!1.
C.4 "a(uum dr#er aulia
kondisi operasi
kondisi penimpanan p0' atm
laju alir massa ++12*,!
densittas campuran .1*,,!+2+1!'
3aktu tinggal '
4aktor keaman !"
Menentukan dimensi tangki
laju alir volumetrik 1*'.,+2!+
volume bahan (Vb) 1*'.,+2!+
volume tangki 2*2-1.,
Volume silinder (Vs) *11
volume elipsiodal head (Vh) !*'!.
V atas 7 V ba3ah !*2'222222-
5iameter tangki (5t) '*-2-.1-
Tinggisilinder +*!','11.
Tinggi head (8h) !*++!,+2
Tinggi total (8t) +*2.'-+.+
menentukan tebal shell dan tebal head
tinggi cairan (8li9) *-'122!-!'.gravitasi ,*.
Ph '!,2*-2
Pd '*'
tebal didnidng silinder tangki
F !!!!
!*.1
; !*'1
r !*22..'.,2
ts !*'1--',---
tebal headth !*'1--2'-1+
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C.45 penampung biodiesel aulia
kondisi operasi
kondisi penimpanan p0' atm
laju alir massa +2.*-!!
densittas campuran .1'*!2'+-1,.1
3aktu tinggal '2.
4aktor keaman !"
Menentukan dimensi tangki
laju alir volumetrik 1*'2,.2
volume bahan (Vb) .2*..!+!!-'
volume tangki '!*+.2!12+.!,
Volume silinder (Vs) '*1-
volume elipsiodal head (Vh) !*'!.
V atas 7 V ba3ah !*2'222222-
5iameter tangki (5t) *.-'-22,..
Tinggisilinder -*2-+1,-1 Tinggi head (8h) !*,1,,+'-+-
Tinggi total (8t) ,*1,,+'-+2,
menentukan tebal shell dan tebal head
tinggi cairan (8li9) -*+2''-2,'+
gravitasi ,*.
Ph 2,*
Pd 2*'!
tebal didnidng silinder tangki
F !!!!
!*.1; !*'1
r '*,'.1..+,+
ts !*+!...21.
tebal head
th !*+!,+',,!.
C.4) hold Tank aulia
kondisi operasi
kondisi penimpanan p0' atm
laju alir massa .+,*2+!
densittas campuran .2+*+2'!!,!-,
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3aktu tinggal '
4aktor keaman !"
Menentukan dimensi tangki
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,
menentukan tebal shell dan tebal head
tinggi cairan (8li9) '*2-,!-12.-
gravitasi ,*.
Ph '++*22Pd '.*++
tebal didnidng silinder tangki
F !!!!
!*.1
; !*'1
r !*+'-2'.+
ts !*'++,-2+
tebal head
th !*'++1-1..
C.4) ,lash drum aulia
kondisi operasi
kondisi penimpanan p0' atm
laju alir massa .+,*2+!
densittas campuran .2+*+2'!!,!-,3aktu tinggal '
4aktor keaman !"
Menentukan dimensi tangki
laju alir volumetrik !*,..1+.-!2
volume bahan (Vb) !*,..1+.-!2
volume tangki '*'-,+1.++-
Volume silinder (Vs) *11
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volume elipsiodal head (Vh) !*'!.
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
tebal didnidng silinder tangki
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 !"
Menentukan dimensi tangki
laju alir volumetrik !*1!2'+
volume bahan (Vb) !*1!2'+
volume tangki !*2!++212!.
Volume silinder (Vs) *11
volume elipsiodal head (Vh) !*'!.V atas 7 V ba3ah !*2'222222-
5iameter tangki (5t) !*2'1+++'1
Tinggisilinder '*.+!2-++
Tinggi head (8h) !*'1.2!2!+
Tinggi total (8t) *'+-+!+.+1'
menentukan tebal shell dan tebal head
tinggi cairan (8li9) '*-!+.,11,2
gravitasi ,*.
-
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Ph '1-+.*.+
Pd '.*2.
tebal didnidng silinder tangki
F !!!!
!*.1
; !*'1
r !*!2--'!-ts !*'.2-'2--
tebal head
th !*'.-'1+'+
C.5) ,lash drum lll aulia
kondisi operasi
kondisi penimpanan p0' atm
laju alir massa +1*-!!
densittas campuran .,.*'2!'1+,2+
3aktu tinggal '
4aktor keaman !"
Menentukan dimensi tangki
laju alir volumetrik !*+.1'!-,
volume bahan (Vb) !*+.1'!-,
volume tangki !*1.'1Volume silinder (Vs) *11
volume elipsiodal head (Vh) !*'!.
V atas 7 V ba3ah !*2'222222-
5iameter tangki (5t) !*2!1,,21,
Tinggisilinder '*.'--..,1.-
Tinggi head (8h) !*'1'+.+'
Tinggi total (8t) *'!-1-.1
menentukan tebal shell dan tebal head
tinggi cairan (8li9) '*2.'-,+-
gravitasi ,*.Ph '+.'+*,
Pd '.*1
tebal didnidng silinder tangki
F !!!!
!*.1
; !*'1
r !*!,2+.21
ts !*'-,,.!2'-
-
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tebal head
th !*'.!!'1
C.5 Tanki gliserol aulia
kondisi operasi
kondisi penimpanan p0' atm
laju alir massa +'*'!!
densittas campuran .,1
3aktu tinggal -
4aktor keaman !"
Menentukan dimensi tangki
laju alir volumetrik !*+-!1!-,
volume bahan (Vb) *.-2!'''-volume tangki +!*21'++'+!.
Volume silinder (Vs) '*1-
volume elipsiodal head (Vh) !*'!.
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!.'
menentukan tebal shell dan tebal head
tinggi cairan (8li9) 1*+2+11!--gravitasi ,*.
Ph +-,-*.+
Pd *.
tebal didnidng silinder tangki
F !!!!
!*.1
; !*'1
r '*+!1'','2
ts !*!+1-+,+,
tebal headth !*!+,!!+1
-
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'*!! 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
-
8/18/2019 alat ulang abhs
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
-
8/18/2019 alat ulang abhs
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
-
8/18/2019 alat ulang abhs
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
-
8/18/2019 alat ulang abhs
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
-
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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
-
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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
-
8/18/2019 alat ulang abhs
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
-
8/18/2019 alat ulang abhs
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
-
8/18/2019 alat ulang abhs
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
-
8/18/2019 alat ulang abhs
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
-
8/18/2019 alat ulang abhs
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
-
8/18/2019 alat ulang abhs
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
-
8/18/2019 alat ulang abhs
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
-
8/18/2019 alat ulang abhs
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
-
8/18/2019 alat ulang abhs
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
-
8/18/2019 alat ulang abhs
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 '
-
8/18/2019 alat ulang abhs
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
-
8/18/2019 alat ulang abhs
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
-
8/18/2019 alat ulang abhs
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
-
8/18/2019 alat ulang abhs
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
-
8/18/2019 alat ulang abhs
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
-
8/18/2019 alat ulang abhs
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 '
-
8/18/2019 alat ulang abhs
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
-
8/18/2019 alat ulang abhs
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
-
8/18/2019 alat ulang abhs
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
-
8/18/2019 alat ulang abhs
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)
-
8/18/2019 alat ulang abhs
54/201
-
8/18/2019 alat ulang abhs
55/201
-
8/18/2019 alat ulang abhs
56/201
-
8/18/2019 alat ulang abhs
57/201
-
8/18/2019 alat ulang abhs
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)
-
8/18/2019 alat ulang abhs
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)
-
8/18/2019 alat ulang abhs
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)
-
8/18/2019 alat ulang abhs
61/201
densitas 18"9.67614392"1
Komponen V (m3/jam)
2so4 ".644 1!84".""" "."""2o "."13 1!""".""" "."""
'ota ".657 "."""
(*+/jam)
,ensitas(K+/m3)
-
8/18/2019 alat ulang abhs
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)
-
8/18/2019 alat ulang abhs
63/201
-
8/18/2019 alat ulang abhs
64/201
densitas 18"9.67614392"1
Komponen V (m3/jam)
2so4 ".644 1!84".""" "."""
2o "."13 1!""".""" "."""
'ota ".657 "."""
(*+/jam)
,ensitas(K+/m3)
-
8/18/2019 alat ulang abhs
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)
-
8/18/2019 alat ulang abhs
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)
-
8/18/2019 alat ulang abhs
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)
-
8/18/2019 alat ulang abhs
68/201
-
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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)
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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)
-
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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
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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)
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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)
-
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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)
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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)
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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)
-
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C.1 Kolam Penampung bahan baku POME
Tekanan (P) '*!! atm
Temperatur (T) !*!! c
Lama Pesediaan (t) *!! hari
Asumsi :Pengaruh Temperatur terhadap densitas diabaikan
,2.*!! %g/m
Laju Alir massa (F) ++++++*+! kg/jam
Faktor keaman !*!
Menghitung kapasitas gudang bahan baku
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
menghitung dimensi kolam
Panjang .*11 m
Lebar 1*-! m
Tinggi *.1 m
5ensitas (6)
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81/201
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82/201
-
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83/201
-
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84/201
-
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85/201
-
8/18/2019 alat ulang abhs
86/201
-
8/18/2019 alat ulang abhs
87/201
-
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88/201
-
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89/201
-
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90/201
-
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!
!
!!
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-
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2
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-
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95/201
-
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-
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-
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-
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-
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'.+!
'!!!'!
'212*22-
782
895
213"
-
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1!"""
-
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-
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-
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-
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-
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-
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107/201
-
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-
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-
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-
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111/201
-
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112/201
-
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113/201
-
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114/201
-
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115/201
-
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116/201
-
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124/201
-
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125/201
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126/201
-
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127/201
-
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128/201
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129/201
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130/201
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131/201
-
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132/201
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133/201
-
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134/201
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135/201
-
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136/201
-
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138/201
-
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139/201
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142/201
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148/201
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150/201
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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 betonvolume !*+,
panjang 1*.2
lebar '-*+
tinggi .*2
jumlah '!
C.3 Dekanter aulia
kondisi operasi
kondisi penimpanan p0' atm
laju alir massa ++++++*++
densittas campuran ,2*1!.!22+!-
3aktu tinggal '
4aktor keaman !"
Menentukan dimensi tangki
5ensitas (6)
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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
kondisi penimpanan p0' atm
laju alir massa 22..*++!
densittas campuran ,+*+-2.'-,+',
3aktu tinggal '
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4aktor keaman !"
Menentukan dimensi tangki
laju alir volumetrik -*!,2222'12
volume bahan (Vb) -*!,2222'12
volume tangki .*1'1,,1'..
Volume silinder (Vs) '*1-
volume elipsiodal head (Vh) !*'!.V atas 7 V ba3ah !*2'222222-
5iameter tangki (5t) '*22,!111,.
Tinggisilinder *.!1''',2
Tinggi head (8h) !*+'-12,
Tinggi total (8t) +*'-12.,,1
menentukan tebal shell dan tebal head
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
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P '+*'22''1!.
Peren(anaan *aket Pemanas
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-+.
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 +!
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,'
hot Duida cold Duida selisish
+. #hu rend4ah .2 '2
+. shu tinggi '+! '!.
1+ 1+
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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
kondisi penimpanan p0' atm
laju alir massa 2+'*!-!
densittas ,*+,.+.1-,
-
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P '++!*'..2,1'.
C.14 Centri7uge
kondisi operasi
kondisi penimpanan p0' atm
laju alir massa -2+*1-!
densittas ,+1*!,,.1,2'
3aktu tinggal '
4aktor keaman !"
Menentukan dimensi tangki
laju alir volumetrik .*!..'---!2
volume bahan (Vb) .*!..'---!2
Volume tangki (Vs) ,*-!1.'+-
Volume silinder (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-!-
-
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g( *
C.12 8a(uum dr#er aulia
kondisi operasi
kondisi penimpanan p0' atm
laju alir massa +1.*!,!
densittas campuran ,!-*'.--12++
3aktu tinggal '
4aktor keaman !"
Menentukan dimensi tangki
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 '*.+
Pd '*!
tebal didnidng silinder tangki
F !!!!
!*.1
; !*'1
r !*21!2''12.1
ts !*'1-!-''+
tebal headth !*'1-!.+2
-
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'*!! 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
-
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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
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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
-
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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
-
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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
-
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* 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
-
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172/201
-
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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
-
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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
-
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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)
-
8/18/2019 alat ulang abhs
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)
-
8/18/2019 alat ulang abhs
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)
-
8/18/2019 alat ulang abhs
178/201
H2O 2!2"".""" 1!""" 2
Ca-entonite 66.22" 2!6"" "."25
'ota 6!688.44" 8!129.755 7."97
-
8/18/2019 alat ulang abhs
179/201
-
8/18/2019 alat ulang abhs
180/201
-
8/18/2019 alat ulang abhs
181/201
-
8/18/2019 alat ulang abhs
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)
-
8/18/2019 alat ulang abhs
183/201
-
8/18/2019 alat ulang abhs
184/201
C.3 Dekanter aulia
kondisi operasi
kondisi penimpanan p0' atm
laju alir massa ++++++*++
densittas campuran Atas ,2*1!.!22+!+
,2.*1'1 densitas campuran ba3ah ,,,*,,
Viskositas campuran !*.!'
t tinggal '*2+...22
4aktor keaman !"
-
8/18/2019 alat ulang abhs
185/201
-1*-+,Menentukan dimensi tangki
laju alir volumetrik +1,*!'-1.!1.
volume bahan (Vb) ''1*.-...2!!
volume tangki ',*!1+22!
Volume silinder (Vs) *11
volume elipsiodal head (Vh) !*'!.V atas 7 V ba3ah !*2'222222-
5iameter tangki (5t) *-1,21,.,
panjang silinder ''*-.,!1.,22
panjang head (Ph) !*,,,!..+-
panjang total (Pt) '*'1.-1+2'
menentukan tebal shell dan tebal head
tinggi cairan (8li9) *'!,+'1-
gravitasi ,*.
Ph .-1+*1
Pd !*-2tebal didnidng silinder tangki
F !!!!
!*.1
; !*'1
r '*.-,.'-2+,+
ts !*'1'
tebal head
th !*'111'+,
-
8/18/2019 alat ulang abhs
186/201
-
8/18/2019 alat ulang abhs
187/201
-
8/18/2019 alat ulang abhs
188/201
-
8/18/2019 alat ulang abhs
189/201
-
8/18/2019 alat ulang abhs
190/201
-
8/18/2019 alat ulang abhs
191/201
-
8/18/2019 alat ulang abhs
192/201
-
8/18/2019 alat ulang abhs
193/201
T0! c
kg/jam
kg/m
kg/m
kg/m*s
jam
-
8/18/2019 alat ulang abhs
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
-
8/18/2019 alat ulang abhs
195/201
-
8/18/2019 alat ulang abhs
196/201
-
8/18/2019 alat ulang abhs
197/201
-
8/18/2019 alat ulang abhs
198/201
-
8/18/2019 alat ulang abhs
199/201
-
8/18/2019 alat ulang abhs
200/201
-
8/18/2019 alat ulang abhs
201/201