neraca massa dan panas laporan
TRANSCRIPT
-
7/26/2019 Neraca Massa Dan Panas Laporan
1/54
-
7/26/2019 Neraca Massa Dan Panas Laporan
2/54
#! #!
Trigliserida 4145.$333 -g
FFA *0.$333 -g
Metanol 394.*404 -g
Air 133.3333 -g
Sod. Methylate 339.095 -g
Metil ster 34$1.334$ -g
liserol 3$$3.*014 -g
Sa2+n *0*.1* -g
TOT+ 50000.0000 kg
#! #!
Trigliserida 41*5.104* -g
FFA 10.416 -gMetanol 3**5.1043 -g
Air 66.666 -g
Sod. Methylate 169.549 -g
Metil ster 349.460$ -g
liserol 1553.*$05 -g
Sa2+n *.0*13 -g
TOT+ 46631.6023 kg
-
7/26/2019 Neraca Massa Dan Panas Laporan
3/54
TR
#! #!
Trigliserida 4104.4$6 -g
FFA 5.*0$3 -gMetanol *41.33$ -g
Air 33.3333 -g
Sod. Methylate $4.39 -g
Metil ster 34.5$6$ -g
liserol 6*1.31** -g
Sa2+n 0.0*0* -g
TOT+ 45068.0522 kg
Feed +ight 44106.7*31 kg 9$.*3*%
1.43% Metanol 1.500% 661.601*
Fresh Metanol 49.500%
Metanol Recovery 49.500%
Air 1.000%
0.*95% Sod. Methylate 0.300% 132.3204
-
7/26/2019 Neraca Massa Dan Panas Laporan
4/54
Sod. Methylate 30.000%
Metanol 65.000%
Air 5.000%
$on'e()i Reak)i *0.000%
3!5"##1$!333 3 !3#!
Trigliserida & Metanol
'M $$4.0000 g()ol 3*.0000
M+la,)+la 4.6199 -)ol 95.9*9
Rea-si 4.159 -)ol 1*.436
Sisa 0.46*0 -)ol $3.4993
*61.961
1!33##! /a#!3
FFA & Sodi+) Methylate'M *$*.0000 g()ol 54.0000
M+la,)+la 0.009* -)ol 1.5*01
Rea-si 0.00$3 -)ol 0.00$3
Sisa 0.0009 -)ol 1.511
M# #! #!
4.6199 Trigliserida 40$3.9563 -g
0.009* FFA *.604* -g
95.9*9 Metanol 301.13*0 -g
1.6610 Air *9.$9$ -g
1.5*01 Sod. Methylate $*.0$31 -g
1*6.601 Metil ster 345.1*9 -g
1.6$$3 liserol 155.3*$1 -g
0.0000 Sa2+n 0.000* -g
TOT+ 44*00.7154 kg
#! #!
Trigliserida 40$.3956 -g
FFA 0.*604 -g
Metanol *6*.*4*1 -g
Air *9.$9$ -g
Sod. Methylate $1.6343 -g
Metil ster 4116.9050 -g
liserol 53.$5*5 -g
Sa2+n *.5*6$ -gTOT+ 44*00.7154 kg
-
7/26/2019 Neraca Massa Dan Panas Laporan
5/54
#! #!
Trigliserida 406.3536 -g
FFA 0.130* -g
Metanol **1.405$ -g
Air 14.9494 -g
Sod. Methylate 40.$11 -g
Metil ster 41165.$46 -g
liserol *15.1410 -g
Sa2+n 0.0*53 -gTOT+ 44114.66*0 kg
Feed +ight 43612.8101 kg
a)h ate( 5.500% 23*8.7046
-
7/26/2019 Neraca Massa Dan Panas Laporan
6/54
Asa) Fosat $*.000%
Air $.000%
Air Recovery 4.000%
#! #!
Trigliserida 404.3*19 -g
FFA 0.0651 -g
Metanol 1930.6949 -g
Air *95.319* -g
Sod. Methylate *0.40$6 -g
Metil ster 41163.$$4 -g
liserol $6.0564 -g
Sa2+n 0.0003 -g
Asa) Fosat 1966.93 -gTOT+ 45867.5*24 kg
,.44
#! #!
Trigliserida 40*.3003 -g
FFA 0.03*6 -g
Metanol 1641.090 -g
Air 14.6596 -g
Sod. Methylate 10.*043 -g
Metil ster 41161.30* -g
liserol *1.5141 -g
Sa2+n 0.0000 -g
Asa) Fosat 9$3.46$9 -g
TOT+ 44368.0005 kg
-
7/26/2019 Neraca Massa Dan Panas Laporan
7/54
Feed +ight 43383.3461 kg
a)h ate( 5.500% 2386.0840
Asa) Fosat $*.000%
Air 4.000%
Air Recovery 4.000%
#! #!
Trigliserida 40*.3003 -g
FFA 0.03*6 -g
Metanol 656.4363 -g
Air 33$.5463 -g
Sod. Methylate *01.0910 -g
Metil ster 41161.30* -g
liserol *1.5141 -g
Sa2+n 0.0000 -gAsa) Fosat *940.05$ -g
TOT+ 45721.7085 kg
#! #!
-
7/26/2019 Neraca Massa Dan Panas Laporan
8/54
Trigliserida 400.*$$$ -g
FFA 0.0163 -g
Metanol 55.90$ -g
Air 169.*3* -g
Sod. Methylate 100.5455 -g
Metil ster 41159.6*1 -gliserol 5.3$5 -g
Sa2+n 0.0000 -g
Asa) Fosat 140.0*$9 -g
TOT+ 43863.1740 kg
Feed ea'y 1053*.2385 kg
Trigliserida 69.9$39 -g
FFA 1$.433 -g
Metanol *593.194 -gAir 456.0*35 -g
Sod. Methylate 46$.6$43 -g
Metil ster 13.$549 -g
liserol 4*60.34* -g
Sa2+n *04.6543 -g
Asa) Fosat *453.49$ -g
-l 1.000% 105.3*24
!l 3*.000%
Air 6$.000%
1!33##/a !l
Sa2+n & Asa) lorida
'M 304.0000 g()ol 36.5000
M+la,)+la 0.63* -)ol 0.9*40
Rea-si 0.63* -)ol 0.63*
Sisa 0.0000 -)ol 0.*50$
#! #!
Trigliserida 69.9$39 -g
FFA 1$.433 -gMetanol *593.194 -g
-
7/26/2019 Neraca Massa Dan Panas Laporan
9/54
Air 5*.6903 -g
Sod. Methylate 46$.6$43 -g
Metil ster 13.$549 -g
liserol 4*60.34* -g
Sa2+n *04.6543 -g
Asa) Fosat *453.49$ -g!l 33.*56 -g
TOT+ 10644.630* kg
#! #!
Trigliserida 69.9$39 -gFFA *0$.311 -g
Metanol *593.194 -g
Air 5*.6903 -g
Sod. Methylate 46$.6$43 -g
Metil ster 13.$549 -g
liserol 4*60.34* -g
Sa2+n 0.0000 -g
Asa) Fosat *453.49$ -g
!l 9.1536 -g
ara) 39.3$*5 -g
TOT+ 10644.630* kg
#! #!
-
7/26/2019 Neraca Massa Dan Panas Laporan
10/54
-
7/26/2019 Neraca Massa Dan Panas Laporan
11/54
-
7/26/2019 Neraca Massa Dan Panas Laporan
12/54
ton/day 1000.0000 ton/day 1000000.0000 kg/day
kg
*0$.3333 -g
4145$.3333 -g
kg
3506.*500 -g
3506.*500 -g
0.$333 -g
kg
35.0000 -g
$1*.5000 -g
6*.5000 -g
TR!S"ST"R#F#$S# # R"$TOR&
3 1!33##!3 3!5"#!3
Metil ster & liserol
g()ol *96.0000 g()ol 9*.0000 g()ol
-)ol 0.0000 -)ol 0.0000 -)ol-)ol 1*6.6*61 -)ol 4*.*0$ -)ol
-)ol 1*6.6*61 -)ol 4*.*0$ -)ol
1!33##/a !3#!
Sa2+n & Metanol
g()ol 304.0000 g()ol 3*.0000 g()ol
-)ol 0.0000 -)ol 0.0000 -)ol
-)ol 0.6649 -)ol 0.6649 -)ol
-)ol 0.6649 -)ol 0.6649 -)ol
OT OT
Trigliserida 4145.$333 -g 4.6$99
FFA *0.$333 -g 0.039
Metanol 394.*404 -g 11$.500
Air 133.3333 -g
Sod. Methylate 339.095 -g 6.*96
Metil ster 34$1.334$ -g 1*6.6*61
liserol 3$$3.*014 -g 4*.*0$
Sa2+n *0*.1* -g 0.6649
-
7/26/2019 Neraca Massa Dan Panas Laporan
13/54
TOT+ 50000.0000 kg
TR!S"ST"R#F#$S# # $O+OM S",RTOR #&
OT OT OT
+ight ,ha)e
Trigliserida 99.500% 41*5.104* -g
FFA 50.000% 10.416 -g
Metanol $5.000% 3**5.1043 -g
Air 50.000% 66.666 -g
Sod. Methylate 50.000% 169.549 -g
Metil ster 99.995% 349.460$ -g
liserol 40.000% 1553.*$05 -g
Sa2+n 1.000% *.0*13 -gTOT+ +#T 46631.6023 kg
ea'y ,ha)e
Trigliserida 0.500% *0.*9* -g
FFA 50.000% 10.416 -g
Metanol 15.000% 569.1361 -g
Air 50.000% 66.666 -g
Sod. Methylate 50.000% 169.549 -g
Metil ster 0.005% 1.$41 -g
liserol 60.000% *3*9.9*0$ -g
Sa2+n 99.000% *00.1064 -gTOT+ " 3368.3*77 kg
TOT+ 50000.0000 kg
R!S"ST"R#F#$S# # $O+OM S",RTOR ##&
OT OT OT
+ight ,ha)e
Trigliserida 99.500% 4104.4$6 -gFFA 50.000% 5.*0$3 -g
Metanol $5.000% *41.33$ -g
Air 50.000% 33.3333 -g
Sod. Methylate 50.000% $4.39 -g
Metil ster 99.995% 34.5$6$ -g
liserol 40.000% 6*1.31** -g
Sa2+n 1.000% 0.0*0* -g
TOT+ +#T 45068.0522 kg
ea'y ,ha)e
Trigliserida 0.500% *0.6*55 -g
FFA 50.000% 5.*0$3 -g
-
7/26/2019 Neraca Massa Dan Panas Laporan
14/54
Metanol 15.000% 4$3.65 -g
Air 50.000% 33.3333 -g
Sod. Methylate 50.000% $4.39 -g
Metil ster 0.005% 1.$40 -g
liserol 60.000% 931.96$3 -g
Sa2+n 99.000% *.0011 -gTOT+ " 1563.5501 kg
TOT+ 46631.6023 kg
!S"ST"R#F#$S# # S",RTOR -"!TR#F+&
OT OT OT
+ight ,ha)e
Trigliserida 99.500% 40$3.9563 -gFFA 50.000% *.604* -g
Metanol $5.000% *330.139 -g
Air 50.000% 16.666 -g
Sod. Methylate 50.000% 4*.3$0 -g
Metil ster 99.995% 345.1*9 -g
liserol *5.000% 155.3*$1 -g
Sa2+n 1.000% 0.000* -g
TOT+ +#T 44106.7*31 kg
ea'y ,ha)e
Trigliserida 0.500% *0.5**4 -gFFA 50.000% *.604* -g
Metanol 15.000% 411.*00$ -g
Air 50.000% 16.666 -g
Sod. Methylate 50.000% 4*.3$0 -g
Metil ster 0.005% 1.$39 -g
liserol 5.000% 465.9$4* -g
Sa2+n 99.000% 0.0*00 -g
TOT+ " *61.25*1 kg
TOT+ 45068.0522 kg
R!S"ST"R#F#$S# ## $O+OM S",RTOR ###&
Metanol 40.9941
Air 13.*3*0
kg
3*.49*9 -g
3*.49*9 -g
6.6160 -g
kg
-
7/26/2019 Neraca Massa Dan Panas Laporan
15/54
39.6961 -g
$6.00$* -g
6.6160 -g
3 1!33##!3 3!5"#!3
Metil ster & liserol
g()ol *96.0000 g()ol 9*.0000 g()ol
-)ol 0.0000 -)ol 0.0000 -)ol
-)ol 1*.436 -)ol 4.159 -)ol
-)ol 1*.436 -)ol 4.159 -)ol
-g
1!33##/a !3#!
Sa2+n & Metanolg()ol 304.0000 g()ol 3*.0000 g()ol
-)ol 0.0000 -)ol 0.0000 -)ol
-)ol 0.00$3 -)ol 0.00$3 -)ol
-)ol 0.00$3 -)ol 0.00$3 -)ol
0.*660 -g
OT OT M#
Trigliserida 40$.3956 -g 0.46*0
FFA 0.*604 -g 0.0009
Metanol *6*.*4*1 -g $3.506
Air *9.$9$ -g 1.6610
Sod. Methylate $1.6343 -g 1.511
Metil ster 4116.9050 -g 139.0$0$
liserol 53.$5*5 -g 5.$46*
Sa2+n *.5*6$ -g 0.00$3
TOT+ 44*00.7154 kg
R!S"ST"R#F#$S# ## $O+OM S",RTOR ###&
OT OT OT
+ight ,ha)e
Trigliserida 99.500% 406.3536 -g
FFA 50.000% 0.130* -g
Metanol $5.000% **1.405$ -g
Air 50.000% 14.9494 -g
Sod. Methylate 50.000% 40.$11 -g
Metil ster 99.995% 41165.$46 -g
liserol 40.000% *15.1410 -gSa2+n 1.000% 0.0*53 -g
-
7/26/2019 Neraca Massa Dan Panas Laporan
16/54
-
7/26/2019 Neraca Massa Dan Panas Laporan
17/54
1966.93 -g
191.$964 -g
95.94$* -g
OT OT OT
+ight ,ha)e
Trigliserida 99.500% 40*.3003 -g
FFA 50.000% 0.03*6 -g
Metanol $5.000% 1641.090 -g
Air 50.000% 14.6596 -g
Sod. Methylate 50.000% 10.*043 -g
Metil ster 99.995% 41161.30* -g
liserol *5.000% *1.5141 -g
Sa2+n 1.000% 0.0000 -gAsa) Fosat 50.000% 9$3.46$9 -g
TOT+ +#T 44368.0005 kg
ea'y ,ha)e
Trigliserida 0.500% *.0*16 -g
FFA 50.000% 0.03*6 -g
Metanol 15.000% *$9.604* -g
Air 50.000% 14.6596 -g
Sod. Methylate 50.000% 10.*043 -g
Metil ster 0.005% *.05$* -g
liserol 5.000% 64.54*3 -g
Sa2+n 99.000% 0.0003 -g
Asa) Fosat 50.000% 9$3.46$9 -g
TOT+ " 14**.5*1* kg
TOT+ 45867.5*24 kg
S#! R#! M"T!O+ F+S"R&
OT OT OT
+ight ,ha)e
Trigliserida 100.000% 40*.3003 -g
FFA 100.000% 0.03*6 -g
Metanol 40.000% 656.4363 -g
Air 100.000% 14.6596 -g
Sod. Methylate 100.000% 10.*043 -g
Metil ster 100.000% 41161.30* -g
liserol 100.000% *1.5141 -g
Sa2+n 100.000% 0.0000 -g
Asa) Fosat 100.000% 9$3.46$9 -g
TOT+ +#T 43383.3461 kga)
-
7/26/2019 Neraca Massa Dan Panas Laporan
18/54
Metanol 60.000% 9$4.6544 -g
TOT+ S *84.6544 kg
TOT+ 44368.0005 kg
S#! R#! S",RTOR -"!TR#F+&
kg
1956.5$$9 -g
95.4434 -g
95.4434 -g
OT OT OT
+ight ,ha)e
Trigliserida 99.500% 400.*$$$ -g
FFA 50.000% 0.0163 -g
Metanol $5.000% 55.90$ -g
Air 50.000% 169.*3* -g
Sod. Methylate 50.000% 100.5455 -g
Metil ster 99.995% 41159.6*1 -g
liserol *5.000% 5.3$5 -gSa2+n 1.000% 0.0000 -g
Asa) Fosat 50.000% 140.0*$9 -g
TOT+ +#T 43863.1740 kg
ea'y ,ha)e
Trigliserida 0.500% *.0115 -g
FFA 50.000% 0.0163 -g
Metanol 15.000% 9$.4654 -g
Air 50.000% 169.*3* -g
Sod. Methylate 50.000% 100.5455 -g
Metil ster 0.005% *.05$1 -g
liserol 5.000% 16.1356 -g
Sa2+n 99.000% 0.0000 -g
Asa) Fosat 50.000% 140.0*$9 -g
TOT+ " 1858.5344 kg
TOT+ 45721.7085 kg
S#! R#! ,M" R"R&
OT OT OT
-
7/26/2019 Neraca Massa Dan Panas Laporan
19/54
+ight ,ha)e
Trigliserida 100.000% 400.*$$$ -g
FFA 100.000% 0.0163 -g
Metanol 10.000% 55.91 -g
Air 30.000% 50.$*0 -g
Sod. Methylate 100.000% 100.5455 -gMetil ster 100.000% 41159.6*1 -g
liserol 100.000% 5.3$5 -g
Sa2+n 100.000% 0.0000 -g
Asa) Fosat 50.000% 35.0144 -g
TOT+ +#T 42507.4*46 kg
a)
Metanol 90.000% 50*.13 -g
Air 0.000% 11$.491* -g
Asa) Fosat 50.000% 35.0144 -g
TOT+ S 1355.67*4 kgTOT+ 43863.1740 kg
R"$TOR " ,S"
kg
33.*56 -g
1.666$ -g
1!33##! /al
FFA & ara)
g()ol *$*.0000 g()ol 5$.5000 g()ol
-)ol 0.0000 -)ol 0.0000 -)ol
-)ol 0.63* -)ol 0.63* -)ol
-)ol 0.63* -)ol 0.63* -)ol
OT OT
Trigliserida 69.9$39 -g 0.16$%
FFA *0$.311 -g 0.500%Metanol *593.194 -g 6.**5%
-
7/26/2019 Neraca Massa Dan Panas Laporan
20/54
Air 5*.6903 -g 1.*66%
Sod. Methylate 46$.6$43 -g 1.1*5%
Metil ster 13.$549 -g 0.033%
liserol 4*60.34* -g 10.**5%
Sa2+n 0.0000 -g 0.000%
Asa) Fosat *453.49$ -g 5.$$$%!l 9.1536 -g 0.0**%
ara) 39.3$*5 -g 0.095%
TOT+ 10644.630* kg
S"T+#! S,+#T T!$&
OT OT OT
Fatty Mate(Trigliserida 99.500% 69.6340 -g
FFA 99.500% *0.*55 -g
Metanol $5.000% **04.6615 -g
Air 50.000% *63.$451 -g
Sod. Methylate 50.000% *34.34*1 -g
Metil ster 99.990% 13.$535 -g
liserol 30.000% 1*$.104* -g
Sa2+n 1.000% 0.0000 -g
Asa) Fosat 50.000% 1**6.4$9 -g
!l 1.000% 0.0915 -g
ara) 0.100% 0.0394 -g
TOT+ FTT MT"R 54*8.5*57 kg
ea'y ,ha)e
Trigliserida 0.500% 0.3499 -g
FFA 0.500% 1.0416 -g
Metanol 15.000% 3$9.059 -g
Air 50.000% *63.$451 -g
Sod. Methylate 50.000% *34.34*1 -g
Metil ster 0.010% 0.0014 -g
liserol 0.000% *9$*.*431 -g
Sa2+n 99.000% 0.0000 -g
Asa) Fosat 50.000% 1**6.4$9 -g
!l 99.000% 9.06*1 -g
ara) 99.900% 39.3431 -g
TOT+ " 5146.0352 kg
TOT+ 10644.630* kg
R"-T#F#-T#O! ## #ST#+S#&
-
7/26/2019 Neraca Massa Dan Panas Laporan
21/54
M Feed $ol& F i)tilat $ol&
Metanol 3*.0000 1*.15$1 0.4534 11.550*
Air 1$.0000 14.65$1 0.5466 0.3*9
26.8161 1.0000 12.2831
OT OT OT
Re9l:k
Metanol 95.000% 369.6050 -g
Air 5.000% 13.19*3 -g
TOT+ Re9l:k 382.7*73 kg
ly;ate(
Trigliserida 100.000% 0.3499 -g
FFA 100.000% 1.0416 -g
Metanol 5.000% 19.45*9 -g
Air 95.000% *50.65*9 -g
Sod. Methylate 100.000% *34.34*1 -g
Metil ster 100.000% 0.0014 -g
liserol 100.000% *9$*.*431 -g
Sa2+n 100.000% 0.0000 -g
Asa) Fosat 100.000% 1**6.4$9 -g
!l 100.000% 9.06*1 -g
ara) 100.000% 39.3431 -gTOT+ ly;ate( 4763.237* kg
TOT+ 5146.0352 kg
R"-T#F#-T#O! ## ",ORS#&
OT OT OT
ate(
Metanol 90.000% 1.506 -gAir 0.000% 15.450 -g
TOT+ T"R 1*2.*646 kg
li)e(ol
Trigliserida 100.000% 0.3499 -g
FFA 100.000% 1.0416 -g
Metanol 10.000% 1.9453 -g
Air 30.000% 5.1959 -g
Sod. Methylate 100.000% *34.34*1 -g
Metil ster 100.000% 0.0014 -g
liserol 100.000% *9$*.*431 -g
Sa2+n 100.000% 0.0000 -g
-
7/26/2019 Neraca Massa Dan Panas Laporan
22/54
Asa) Fosat 100.000% 1**6.4$9 -g
!l 100.000% 9.06*1 -g
ara) 100.000% 39.3431 -g
TOT+ +#S"RO+ 4570.2733 kg
TOT+ 4763.237* kg
-
7/26/2019 Neraca Massa Dan Panas Laporan
23/54
-
7/26/2019 Neraca Massa Dan Panas Laporan
24/54
9.900%
0.0*5%
.40%
0.160%
0.40%
$9.951%
3.*$%
0.005%
0.050%
0.0*5%
1.366%
0.160%
0.40%
0.004%
5.59*%
0.4$0%
9.$51%0.013%
6.59%
0.0$0%
0.*03%
$9.946%
1.491%
0.000%
0.050%
0.013%
-
7/26/2019 Neraca Massa Dan Panas Laporan
25/54
1.161%
0.0$0%
0.*03%
0.004%
*.*3%
0.005%
9.$01%0.006%
5.59*%
0.040%
0.10*%
$9.94*%
0.33%
0.000%
0.049%0.006%
0.9$%
0.040%
0.10*%
0.004%
1.11$%
0.000%
-
7/26/2019 Neraca Massa Dan Panas Laporan
26/54
0.95%
0.000%
5.451%
0.036%
0.09$%
9$.9$%
0.516%0.000%
-
7/26/2019 Neraca Massa Dan Panas Laporan
27/54
0.005%
0.000%
0.96*%
0.036%
0.09$%
0.005%
0.5%
0.006%
0.90%
0.000%
4.634%
0.01$%
0.049%
9$.93%
0.*0%0.000%
0.005%
0.000%
0.$1$%
0.01$%
0.049%
0.005%
0.310%0.000%
-
7/26/2019 Neraca Massa Dan Panas Laporan
28/54
0.966%
0.000%
3.939%
0.354%
0.0*4%
9$.$$%
0.05*%
0.000%*.360%
0.005%
0.000%
0.695%
0.354%
0.0*4%
0.005%
0.155%
0.000%
*.360%
0.966%
0.000%
1.55%
0.354%
0.0*4%
9$.$$%
0.05*%
0.000%
*.360%
-
7/26/2019 Neraca Massa Dan Panas Laporan
29/54
*.363%
0.961%
0.000%
1.339%
0.406%
0.*41%
9$.$3%
0.013%0.000%
3.5*$%
0.005%
0.000%
0.*36%
0.406%
0.*41%
0.005%
0.039%
0.000%
3.5*$%
-
7/26/2019 Neraca Massa Dan Panas Laporan
30/54
0.961% 0.94*%
0.000% 0.000%
0.134% 0.131%
0.1**% 0.119%
0.*41% 0.*3%9$.$3% 96.$*9%
0.013% 0.013%
0.000% 0.000%
1.64% 1.*9%
100.000%
1.*05%
0.*$4%
1.64%
-
7/26/2019 Neraca Massa Dan Panas Laporan
31/54
0.16% 1.*66%
0.49% 3.0%
5.*91% 40.095%
0.633% 4.9$%
0.56*% 4.*6*%
0.033% 0.*5*%
3.06% *3.*44%
0.000% 0.000%
*.944% **.310%
0.000% 0.00*%
0.000% 0.001%
100.000%
0.001% 0.00%
0.00*% 0.0*0%
0.934% .560%
0.633% 5.1*%
0.56*% 4.554%
0.000% 0.000%
.15% 5.95*%
0.000% 0.000%
*.944% *3.$39%
0.0**% 0.16%
0.094% 0.65%
100.000%
-
7/26/2019 Neraca Massa Dan Panas Laporan
32/54
otto $ol&
0.9403 0.609 0.041$
0.059 13.9*5* 0.95$*
1.0000 14.5331 1.0000
0.001% 0.00%
0.00*% 0.0**%
0.04% 0.40$%
0.60*% 5.*6*%
0.56*% 4.9*0%
0.000% 0.000%
.15% 6*.610%
0.000% 0.000%
*.944% *5.55%
0.0**% 0.190%
0.094% 0.$*6%100.000%
0.001% 0.00$%
0.00*% 0.0*3%
0.005% 0.043%
0.1$0% 1.645%
0.56*% 5.1*$%
0.000% 0.000%
.15% 65.*53%
0.000% 0.000%
-
7/26/2019 Neraca Massa Dan Panas Laporan
33/54
*.944% *6.$4*%
0.0**% 0.19$%
0.094% 0.$61%
100.000%
-
7/26/2019 Neraca Massa Dan Panas Laporan
34/54
Feed Oil 41
-
7/26/2019 Neraca Massa Dan Panas Laporan
35/54
1
-
7/26/2019 Neraca Massa Dan Panas Laporan
36/54
8elta T alor :
3$.0000 559.564 ;()ol. 17*497*347**0.5000
3$.0000 1700.$656 ;()ol. *736$7417660736.0000
3$.0000 $5.561$ ;()ol. 36676437*1.*400
3$.0000 $5.561$ ;()ol. 36676437*1.*400
3$.0000 4.9411 ;()ol. 17$15744$.145
3$.0000 65.300 ;()ol. 50730*7*15.0000
3$.0000 $5.561$ ;()ol. $47535705$.4000
3$.0000 4.9411 ;()ol. 37*0373*.0*50
-
7/26/2019 Neraca Massa Dan Panas Laporan
37/54
Cp
Komponen Rumus CH2- JUMLAH CH3-
FFA (Asam Oleat) 1!33##! 14.0000 2.20!4 3"4.#!$ 1.0000 41.$114CH2- JUMLAH CH3-
%&'l'se&'a (%&' Ole'n)3!5"##1$!333 44.0000 2.20!4 1*241.03#$ 3.0000 41.$114
CH3- JUMLAH OH-
Metanol !3#! 1.0000 41.$114 41.$114 1.0000 43."!04
H+
Komponen Rumus CH2- JUMLAH CH3-
FFA (Asam Oleat) 1!33##! 14.0000 -20.$400 -2."$00 1.0000 -#$.4!00
CH2- JUMLAH CH3-
%&'l'se&'a (%&' Ole'n)3!5"##1$!333 44.0000 -20.$400 -"0.1$00 3.0000 -#$.4!00
CH2- JUMLAH CH3-Met'l ,ste& 1!33##!3 1$.0000 -20.$400 -330.2400 2.0000 -#$.4!00
-
7/26/2019 Neraca Massa Dan Panas Laporan
38/54
JUMLAH COOH- JUMLAH CH JUMLAH
41.$114 1.0000 #.#300 #.#300 2.0000 22.1#!2 44.3!04 559.5674JUMLAH COO- JUMLAH CH JUMLAH CH-
124.342 3.0000 !".012$ 1##.03# $.0000 22.1#!2 133.0!12 1.0000
JUMLAH
43."!04 85.5618 J/mol.K
JUMLAH COOH- JUMLAH CH JUMLAH
-#$.4!00 1.0000 -42$.#200 -42$.#200 2.0000 3#."#00 #!."400 -716.1900
JUMLAH COO- JUMLAH CH JUMLAH CH-
-22".3!00 3.0000 -33#."200 -1*013.#$00 $.0000 3#."#00 22#.200 1.0000
JUMLAH COO- JUMLAH-1!2."000 1.0000 -33#."200 -33#."200 -821.0600 kJ/mol.K $.2"00 -752.7700
-
7/26/2019 Neraca Massa Dan Panas Laporan
39/54
J/mol.KJUMLAH
24."04 24."04 1,700.8656 J/mol.K
kJ/mol.K $.2"00 -647.9000
JUMLAH
2"."00 2"."00 -1,893.5600 kJ/mol.K $.2"00 -1,825.2700
-
7/26/2019 Neraca Massa Dan Panas Laporan
40/54
Feed Oil 41666.6667 kg/h 41.6667 ton/day
Feed Oil 41666.6667 kg
FFA 0.0050
Trigliserida 0.9950
Feed Metanol 17.000% 7083.3333 kg
Fresh Metanol 0.4950
Metanol Recovery 0.4950
Air 0.0100
Feed Sod. Methy 3.000% 1250.0000 kg
Sod. Methylate 0.3000
Metanol 0.6500
Air 0.0500
TR!S"ST"
$on'e()i Reak)i *0.000%
3!5"##1$!333 3 !3#!
Trigliserida & Metanol
'M $$4.0000 g()ol 3*.0000 g()ol
Massa M+la,)+la 46.$9$6 -)ol *44.5313 -)ol
Rea-si 4*.*0$ -)ol 1*6.6*61 -)ol
Sisa 4.6$99 -)ol 11.9051 -)ol
1!33##! /a#!3
FFA & Sodi+) Methylate
'M *$*.0000 g()ol 54.0000 g()ol
M+la,)+la 0.3$$ -)ol 6.9444 -)ol
Rea-si 0.6649 -)ol 0.6649 -)ol
Sisa 0.039 -)ol 6.*96 -)ol
#!,T
$o=onen M kg/kol& Mol kol& Ma))a kg&
Trigliserida $$4.00 46.$9$6 4145$.3333
FFA *$*.00 0.3$$ *0$.3333
Metanol 3*.00 *44.5313 $*5.0000
Air 1$.00 .404 133.3333
54.00 6.9444 35.0000
Metil ster *96.00 0.0000 0.0000
liserol 9*.00 0.0000 0.0000Sa2+n 304.00 0.0000 0.0000
Sodi+)Methylate
-
7/26/2019 Neraca Massa Dan Panas Laporan
41/54
TOT+ 306.5204 50000.0000
TR!S"ST"R#F#$
#!,T
$o=onen M kg/kol& Mol kol& Ma))a kg&
Trigliserida $$4.00 4.6$99 4145.$333
FFA *$*.00 0.039 *0.$333
Metanol 3*.00 11$.500 394.*404
Air 1$.00 .404 133.3333
54.00 6.*96 339.095
Metil ster *96.00 1*6.6*61 34$1.334$
liserol 9*.00 4*.*0$ 3$$3.*014Sa2+n 304.00 0.6649 *0*.1*
TOT+ 306.5204 50000.0000
TR!S"ST"R#F#$
#!,T
$o=onen M kg/kol& Mol kol& Ma))a kg&
Trigliserida $$4.00 4.6664 41*5.104*
FFA *$*.00 0.0369 10.416
Metanol 3*.00 100.$45 3**5.1043
Air 1$.00 3.03 66.666
54.00 3.139$ 169.549
Metil ster *96.00 1*6.619$ 349.460$
liserol 9*.00 16.$$35 1553.*$05
Sa2+n 304.00 0.0066 *.0*13
TOT+ 255.8413 46631.6023
Sodi+)Methylate
Sodi+)Methylate
-
7/26/2019 Neraca Massa Dan Panas Laporan
42/54
TR!S"ST"R#F#$S#
#!,T
$o=onen M kg/kol& Mol kol& Ma))a kg&
Trigliserida $$4.00 4.6431 4104.4$6
FFA *$*.00 0.01$5 5.*0$3
Metanol 3*.00 $5.666$ *41.33$
Air 1$.00 1.$519 33.3333
54.00 1.5699 $4.39
Metil ster *96.00 1*6.6135 34.5$6$
liserol 9*.00 6.534 6*1.31**
Sa2+n 304.00 0.0001 0.0*0*
TOT+ 227.1170 45068.0522
TR!S"ST"R#F#$
Feed +ight 44106.7*31 kg
Metanol 1.500% 661.601* kg
Fresh Metanol 49.500%
Sodi+)Methylate
-
7/26/2019 Neraca Massa Dan Panas Laporan
43/54
Metanol Recovery 49.500%
Air 1.000%
Sod. Methylate 0.300% 132.3204 kg
Sod. Methylate 30.000%
Metanol 65.000%Air 5.000%
$on'e()i Reak)i *0.000%
3!5"##1$!333 3 !3#!
Trigliserida & Metanol
'M $$4.0000 g()ol 3*.0000 g()ol
Massa M+la,)+la 4.6199 -)ol 95.9*9 -)ol
Rea-si 4.159 -)ol 1*.436 -)olSisa 0.46*0 -)ol $3.4993 -)ol
1!33##! /a#!3
FFA & Sodi+) Methylate
'M *$*.0000 g()ol 54.0000 g()ol
M+la,)+la 0.009* -)ol 1.5*01 -)ol
Rea-si 0.00$3 -)ol 0.00$3 -)ol
Sisa 0.0009 -)ol 1.511 -)ol
#!,T
$o=onen M kg/kol& Mol kol& Ma))a kg&
Trigliserida $$4.00 4.6199 40$3.9563
FFA *$*.00 0.009* *.604*
Metanol 3*.00 95.9*9 301.13*0
Air 1$.00 1.6610 *9.$9$
54.00 1.5*01 $*.0$31
Metil ster *96.00 1*6.601 345.1*9liserol 9*.00 1.6$$3 155.3*$1
Sa2+n 304.00 0.0000 0.000*
TOT+ 232.0786 44*00.7154
#!,T
$o=onen M kg/kol& Mol kol& Ma))a kg&
Trigliserida $$4.00 0.46*0 40$.3956
FFA *$*.00 0.0009 0.*604Metanol 3*.00 $3.506 *6*.*4*1
Sodi+)Methylate
-
7/26/2019 Neraca Massa Dan Panas Laporan
44/54
Air 1$.00 1.6610 *9.$9$
54.00 1.511 $1.6343
Metil ster *96.00 139.0$0$ 4116.9050
liserol 9*.00 5.$46* 53.$5*5
Sa2+n 304.00 0.00$3 *.5*6$
TOT+ 232.0786 44*00.7154
TR!S"ST"R#F#$
#!,T
$o=onen M kg/kol& Mol kol& Ma))a kg&
Trigliserida $$4.00 0.459 406.3536FFA *$*.00 0.0005 0.130*
Metanol 3*.00 0.9$14 **1.405$
Air 1$.00 0.$305 14.9494
54.00 0.559 40.$11
Metil ster *96.00 139.03$ 41165.$46
liserol 9*.00 *.33$5 *15.1410
Sa2+n 304.00 0.0001 0.0*53
TOT+ 214.4403 44114.66*0
Sodi+)Methylate
Sodi+)Methylate
-
7/26/2019 Neraca Massa Dan Panas Laporan
45/54
1000.0000 ton/day 1000000.0000 kg/day
*0$.3333 -g
4145$.3333 -g
3506.*500 -g
3506.*500 -g
0.$333 -g
35.0000 -g
$1*.5000 -g
6*.5000 -g
R#F#$S# # R"$TOR&
3 1!33##!3 3!5"#!3
Metil ster & liserol
*96.0000 g()ol 9*.0000 g()ol
0.0000 -)ol 0.0000 -)ol
1*6.6*61 -)ol 4*.*0$ -)ol
1*6.6*61 -)ol 4*.*0$ -)ol
1!33##/a !3#!
Sa2+n & Metanol
304.0000 g()ol 3*.0000 g()ol
0.0000 -)ol 0.0000 -)ol
0.6649 -)ol 0.6649 -)ol
0.6649 -)ol 0.6649 -)ol
OT,T
$o=onen Mol kol& Ma))a kg&
Trigliserida $$4.00 4.6$99 4145.$333
FFA *$*.00 0.039 *0.$333
Metanol 3*.00 11$.500 394.*404
Air 1$.00 .404 133.3333
Sodi+) Methylate 54.00 6.*96 339.095
Metil ster *96.00 1*6.6*61 34$1.334$
liserol 9*.00 4*.*0$ 3$$3.*014Sa2+n 304.00 0.6649 *0*.1*
Mkg/kol&
-
7/26/2019 Neraca Massa Dan Panas Laporan
46/54
TOT+ 306.5204 50000.0000
S# # $O+OM S",RTOR #&
OT,T
$o=onen "99i)ie)i Mol kol& Ma))a kg&
+ight ,ha)e
Trigliserida $$4.00 99.500% 4.6664 41*5.104*
FFA *$*.00 50.000% 0.0369 10.416
Metanol 3*.00 $5.000% 100.$45 3**5.1043
Air 1$.00 50.000% 3.03 66.666
Sodi+) Methylate 54.00 50.000% 3.139$ 169.549
Metil ster *96.00 99.995% 1*6.619$ 349.460$
liserol 9*.00 40.000% 16.$$35 1553.*$05Sa2+n 304.00 1.000% 0.0066 *.0*13
TOT+ 255.8413 46631.6023
ea'y ,ha)e
Trigliserida $$4.00 0.500% 0.0*34 *0.*9*
FFA *$*.00 50.000% 0.0369 10.416
Metanol 3*.00 15.000% 1.$55 569.1361
Air 1$.00 50.000% 3.03 66.666
Sodi+) Methylate 54.00 50.000% 3.139$ 169.549
Metil ster *96.00 0.005% 0.0063 1.$41
liserol 9*.00 60.000% *5.3*5* *3*9.9*0$Sa2+n 304.00 99.000% 0.65$* *00.1064
TOT+ 50.67*2 3368.3*77
>M+ 306.5204 50000.0000
S# # $O+OM S",RTOR ##&
OT,T
$o=onen "99i)ie)i Mol kol& Ma))a kg&
+ight ,ha)e
Trigliserida $$4.00 99.500% 4.6431 4104.4$6
FFA *$*.00 50.000% 0.01$5 5.*0$3
Metanol 3*.00 $5.000% $5.666$ *41.33$
Air 1$.00 50.000% 1.$519 33.3333
Sodi+) Methylate 54.00 50.000% 1.5699 $4.39
Metil ster *96.00 99.995% 1*6.6135 34.5$6$
liserol 9*.00 40.000% 6.534 6*1.31**
Sa2+n 304.00 1.000% 0.0001 0.0*0*
TOT+ 227.1170 45068.0522
ea'y ,ha)e
Mkg/kol&
M
kg/kol&
-
7/26/2019 Neraca Massa Dan Panas Laporan
47/54
Trigliserida $$4.00 0.500% 0.0*33 *0.6*55
FFA *$*.00 50.000% 0.01$5 5.*0$3
Metanol 3*.00 15.000% 15.11 4$3.65
Air 1$.00 50.000% 1.$519 33.3333
Sodi+) Methylate 54.00 50.000% 1.5699 $4.39
Metil ster *96.00 0.005% 0.0063 1.$40liserol 9*.00 60.000% 10.1301 931.96$3
Sa2+n 304.00 99.000% 0.0066 *.0011
TOT+ 28.7242 1563.5501
>M+ 255.8413 46631.6023
# S",RTOR -"!TR#F+&
OT,T$o=onen "99i)ie)i Mol kol& Ma))a kg&
+ight ,ha)e
Trigliserida $$4.00 99.500% 4.6199 40$3.9563
FFA *$*.00 50.000% 0.009* *.604*
Metanol 3*.00 $5.000% *.$16$ *330.139
Air 1$.00 50.000% 0.9*59 16.666
Sodi+) Methylate 54.00 50.000% 0.$49 4*.3$0
Metil ster *96.00 99.995% 1*6.601 345.1*9
liserol 9*.00 *5.000% 1.6$$3 155.3*$1
Sa2+n 304.00 1.000% 0.0000 0.000*
TOT+ 207.4523 44106.7*31
ea'y ,ha)e
Trigliserida $$4.00 0.500% 0.0*3* *0.5**4
FFA *$*.00 50.000% 0.009* *.604*
Metanol 3*.00 15.000% 1*.$500 411.*00$
Air 1$.00 50.000% 0.9*59 16.666
Sodi+) Methylate 54.00 50.000% 0.$49 4*.3$0
Metil ster *96.00 0.005% 0.0063 1.$39
liserol 9*.00 5.000% 5.0650 465.9$4*
Sa2+n 304.00 99.000% 0.0001 0.0*00
TOT+ 1*.6648 *61.25*1
>M+ 227.1170 45068.0522
S# ## $O+OM S",RTOR ###&
3*.49*9 -g
Mkg/kol&
-
7/26/2019 Neraca Massa Dan Panas Laporan
48/54
-
7/26/2019 Neraca Massa Dan Panas Laporan
49/54
Air 1$.00 50.000% 0.$305 14.9494
Sodi+) Methylate 54.00 50.000% 0.559 40.$11
Metil ster *96.00 99.995% 139.03$ 41165.$46
liserol 9*.00 40.000% *.33$5 *15.1410
Sa2+n 304.00 1.000% 0.0001 0.0*53
TOT+ 214.4403 44114.66*0
ea'y ,ha)e
Trigliserida $$4.00 0.500% 0.00*3 *.04*0
FFA *$*.00 50.000% 0.0005 0.130*
Metanol 3*.00 15.000% 1*.5*61 400.$363
Air 1$.00 50.000% 0.$305 14.9494
Sodi+) Methylate 54.00 50.000% 0.559 40.$11
Metil ster *96.00 0.005% 0.000 *.05$4
liserol 9*.00 60.000% 3.50 3**.115
Sa2+n 304.00 99.000% 0.00$* *.5015
TOT+ 17.6382 786.0464>M+ 232.0786 44*00.7154
S# ## $O+OM S",RTOR #&
OT,T
$o=onen "99i)ie)i Mol kol& Ma))a kg&
+ight ,ha)e
Trigliserida $$4.00 99.500% 0.454 404.3*19FFA *$*.00 50.000% 0.000* 0.0651
Metanol 3*.00 $5.000% 60.334* 1930.6949
Air 1$.00 50.000% 0.4153 .44
Sodi+) Methylate 54.00 50.000% 0.39 *0.40$6
Metil ster *96.00 99.995% 139.0669 41163.$$4
liserol 9*.00 40.000% 0.9354 $6.0564
Sa2+n 304.00 1.000% 0.0000 0.0003
TOT+ 201.5873 43612.8101
ea'y ,ha)e
Trigliserida $$4.00 0.500% 0.00*3 *.031$
FFA *$*.00 50.000% 0.000* 0.0651
Metanol 3*.00 15.000% 10.64* 340.109
Air 1$.00 50.000% 0.4153 .44
Sodi+) Methylate 54.00 50.000% 0.39 *0.40$6
Metil ster *96.00 0.005% 0.000 *.05$3
liserol 9*.00 60.000% 1.4031 1*9.0$46
Sa2+n 304.00 99.000% 0.0001 0.0*50
TOT+ 12.8531 501.858*
>M+ 214.4403 44114.66*0
Mkg/kol&
-
7/26/2019 Neraca Massa Dan Panas Laporan
50/54
-
7/26/2019 Neraca Massa Dan Panas Laporan
51/54
-
7/26/2019 Neraca Massa Dan Panas Laporan
52/54
-
7/26/2019 Neraca Massa Dan Panas Laporan
53/54
-
7/26/2019 Neraca Massa Dan Panas Laporan
54/54