4.16 Cooler III C-03
Tabel 4.16 Neraca Energi pada Cooler III C-03 Neraca Panas Cooler III C-03
Masuk kJ Keluar kJ
∆H26 -2517138068,7799 ∆H27
-2766047361,5088 dQdt
248909292,7289 Total -2517138068,7799
Total -2517138068,7799
4.17 Reaktor Epoksidasi CRV-02
Tabel 4.17 Neraca Energi pada Reaktor Epoksidasi CRV-02 Neraca Panas Reaktor Epoksidasi CRV-02
Masuk kJ Keluar kJ
ΔH27 -2766047361,5088
ΔH28 -2930364193,4680
ΔH
rx
-328633663,9183 dQdt
-164316831,9592 Total
-3094681025,4271 Total -3094681025,4271
4.18 Cooler IV C-04
Tabel 4.18 Neraca Energi pada Cooler IV C-04 Neraca Panas Cooler IV C-04
Masuk kJ Keluar kJ
∆H28 -2930364193,4680 ∆H29
-4825642921,8558 dQdt
1895278728,3878 Total -2930364193,4680 Total
-2930364193,4680
4.19 Flash Drum III FD-03
Tabel 4.19 Neraca Energi pada Flash Drum III FD-03 Neraca Panas Flash Drum III FD-03
Masuk kJ Keluar kJ
∆H29 -4825642921,8558 ∆H30
-4032592489,7994 ∆H31
-793050432,0565 Total -4825642921,8558 Total
-4825642921,8558
Universitas Sumatera Utara
4.20 Kolom Destilasi II MD-02
Tabel 4.20 Neraca Energi pada Koom Destilasi II MD-02 Neraca Panas Kolom Distilasi IIMD-02
Masuk kJ Keluar kJ
∆H31 -793069728,8521
∆H32 -212125593,1190
Qr 128022260,9217
∆H33 -613905848,0765
Q
C
160983973,2651 Total
-665047467,9304 Total
-665047467,9304
4.21 Kolom Destilasi III MD-03
Tabel 4.21 Neraca Energi pada Kolom Destilasi III MD-03 Neraca Panas Kolom Distilasi III MD-03
Masuk kJ Keluar kJ
∆H32 -212125593,1190
∆H35 -107867307,6585
Qr 87981375,7894
∆H34 -102020768,3452
Q
C
85743858,6741 -124144217,3296 Total
-124144217,3296
4.22 Mixer IV M-04
Tabel 4.22 Neraca Energi pada Mixer IV M-04 Neraca Panas Mixer IV M-04
Masuk kJ Keluar kJ
ΔH37 -4032592489,7994
ΔH38 -4140459797,4578
ΔH35 -107867307,6585
Total -4140459797,4578 Total
-4140459797,4578
4.23 Cooler V C-05
Tabel 4.23 Neraca Energi pada Cooler V C-05
Neraca Panas Cooler V C-05 Masuk kJ
Keluar kJ
∆H36 -4140459797,4578
∆H37 -4748608736,5430
Dqdt 608148939,0852
Total -4140459797,4578
Total -4140459797,4578
Universitas Sumatera Utara
V-100
Udara
PC FC
V-138 FC
V-133 TC
PC V-132
TC
LC V-134
TC V-135
V-136 P-
104 3
2 FC
V-128 TC
PC V-127
TC
LC V-129
TC V-130
LC V-131
P- 104
PC FC
V-101 V-106
V-117 TC
V-113 PC
TC V-115
LC V-116
LC FC
V-103 2
P-117
T-01 P-
01
FC 1
V-102 TC
PC V-104
T C
PC FC
V-110
F C
V-118
V-121 FC
V-122 TC
TC V-105
V-124 TC
FC
Steam Air pendingin
LC V-123
PC V-119
V-120 TC
PC
LC V-126
V-125
LC
LC TC
V-137
6
1 7
2 3
2 6
2 8
3
3 3
3 5
Kondensat Air Pendingin
Bekas
C-01 G-01
B-01 H-01
H-02 C-02
FD- 01
E-01 FD-
02
CD-01
RB- 01
MD-01
G-03 H-06
H-05 G-02
P-03 T-02
C-03 C-04
FD- 03
MD-02 CD-02
P-04
RB-02 T-03
MD-03 CD-03
P-05
RB-03
T-04 C-05
G-04 MP-01
MP-04 MP-02
Ke Flare
3 5
7
11
16
2 1
8 2
4 2
5
2 9
3 1
3 4
3 6
3 7
3 8
4 V-293
P-02
1 3
2 2
R-1
R-2
CRV- 01
2 7
MP-03 CRV-
02
V-419
2
1 9
T C
H-04
F C
V-114
H-03
1
1 4
1 2
1 5
1 8
TC LC
FC V-107
TC V-109
TC FC
V-423 TC
V-108 TC
9
V-111
chiller
Chiler bekas
A lur 1 Alur 2
Alur 3 Alur 4
A lur 5 Alur 6
Alur 7 Alur 8
Alur 9 Alur 10
A lur 11 Alur 12
Alur 13 Alur 14
Alur 15 Alur 16
Alur 17 Alur 18
Alur 19 Alur 20
Alur 21 Alur 22
Alur 23 Alur 24
Alur 25 Alur 26
Alur 27 Alur 28
Alur 29 A lur 30
Alur 31 Alur 32
Alur 33 Alur 34
Alur 35 Alur 36
Alur 37 Alur 38
Isobutana
185155,5603 185155,5603
347387,2059 347387,2059
237337,5528 5833,4913
237337,5528 163219,3131
74118,2397 54637,8473
25313,8837 54637,8473
54637,8473 163219,3131
56112,8247 107106,4884
54637,8473 161744,3357
161744,3357 161744,3357
25313,8837 25313,8837
2800629,9840 2800629,9840
2800629,9840 2800629,9840
2763522,1278 37107,8555
37107,8555 0,0000
0,0000 37107,8555
2800629,9833 2800629,9833
2800629,9833
Oksigen 258766,1083
258766,1083 259362,0660
259362,0660 216259,0857
71,0510 216259,0857
215814,5191 444,5666
515,6177 515,6177
515,6177 215814,5191
215747,6138 66,9053
515,6177 582,5230
582,5230 582,5230
Nitrogen
852167,2535 852167,2535
853971,6531 853971,6531
853734,9505 236,7028
853734,9505 852379,6091
1355,3414 1592,0442
1592,0442 1592,0442
852379,6091 852220,4625
159,1466 1592,0442
1751,1907 1751,1907
1751,1907 TB HP
310,5088 310,5088
41987,9277 39117,0007
41987,9277 321,0014
41666,9263 80783,9269
321,0014 0,0013
321,0001 321,0001
321,0001 321,0001
80783,9269 80783,9269
81698,5464 81698,5464
1633,9709 1633,9709
954,2565 679,7144
0,0000 679,7144
954,2565 954,2565
954,2565
Tert B utyl Alcoho l 1810,9300
1810,9300 53653,4427
14608,6486 53653,4427
1833,5795 51819,8632
66428,5117 1833,5795
0,0634 1833,5161
1833,5161 1833,5161
1833,5161 66428,5118
66428,5118 753963,3313
753963,3313 819814,2161
819814,2161 686111,5806
133702,6355 3,5680
133699,0675 3,5680
0,0000 686111,5806
686111,5806 686111,5806
Pro pylen 77914,5721
12764805,3678 12764805,3678 12727420,9561 12727420,9561
12666355,5728 61065,3839
61065,3839 0,0000
61065,3839 12727420,9567 12727420,9567
12727420,9567
Pro pylen Oxide
1157792,2676 1157792,2676
1209390,5496 1209390,5496
1158427,7773 50962,7723
50315,5451 647,2272
50000,0000 315,5451
1158743,3224 1158743,3224
1158743,3224
Total 1110933,3618
185155,5603 1110933,3618
185155,5603 1462842,3638
1462842,3638 1402972,9595
59866,8943 1402972,9595 1233568,0223
169404,9372 56745,5091
172526,3224 56745,5091
56745,5091 1233568,0223
1124080,9657 109487,0565
56745,5091 166232,5656
166232,5656 166232,5656
257826,8709 172526,3224
77914,5721 17558889,4971 17558889,4971 17558889,6767
17558889,6767 17275371,3151
283518,3616 148492,3525
135026,0091 50003,5680
98488,7845 17373860,0996 17373860,0996
17373860,0996 T
o
C 596,8
30,1 95
95 79,38
95 95
95 25
25 19,7
-147,9 62,92
-50,21 10
-78,21 -78,21
-78,21 65
-14,45 40
162,2 150
217,2 30
136,8 130
130 80
80 80
-22,78 101
46,45 -41,26
59,55 40
137,1
P bar
25,33 25,33
25,33 25,33
25,33 25,33
25,33 25,33
25,33 25,33
2,026 2,026
2,026 1,013
1,013 1,013
1,013 1,013
1,013 1,013
1,013 25,33
2,026 14,19
15,2 14,19
14,19 14,19
14,19 14,19
14,19 1,52
2,026 1,52
1,013 1,013
2,026 14,19
Ko mpo nen
ALUR Kg Jam
B-01 : Blower Udara
MP -04 Mix point 4
G-01 : Kompresor - 01
P -03 : P ompa-03
G-02 : Kompresor - 02
P -04 : P ompa-04
G-03 : Kompresor - 03
P -05 : P ompa-05
G-04 : Kompresor - 04
CRV-01 : Conversion Reaction Vessel -01
G-05 : Kompresor - 05
CRV-02 : Conversion Reaction Vessel -02
G-06 : Kompresor - 06
MD-01 : Menara Destilasi -01
G-07 : Kompresor - 07
MD-02 : Menara Destilasi -02
H-01 : Heater - 01
MD-03 : Menara Destilasi -03
H-02 : Heater - 02
FD-01 : Flash Drum -01
H-03 : Heater - 03
FD-02 : Flash Drum -02
H-04 : Heater - 04
FD-03 : Flash Drum -03
H-05 : Heater - 05
T-01 : Tangki Isobutana
H-06 : Heater - 06
T-02 : Tangki P ropilen
C-01 : Cooler -01
T-03 : Tangki Tert Butanol
C-02 : Cooler -02
T-04 : Tangki P ropilen Oksida
C-03 : Cooler -03
CD-01 : Condenser Destilate -01
C-04 : Cooler -04
CD-02 : Condenser Destilate -02
C-05 : Cooler -05
CD-03 : Condenser Destilate -03
P -01 : P ompa-01
RB-01 : Reboiler Bottom -01
P -02 : P ompa-02
RB-02 : Reboiler Bottom -02
MP -01 : Mixer Point -01
RB-03 : Reboiler Bottom -03
MP -02 : Mixer Point -02
MP -03 : Mixer Point -03
KET ERANGAN GAMBAR
DEPARTEMEN TEKNIK KIMIA FAKULTAS TEKNIK
UNIVERSITAS SUMATERA UTARA MEDAN
PRA RANCANGAN PABRIK PEMBUATAN PROPILEN OKSIDA DAN HASIL SAMPING TERT
BUTANOL DENGAN PROSES HIDROPEROKSIDA
Skala : Tanpa Skala Tanggal
Tanda Tangan
Digambar Diperiksa
Disetujui
KAPASITAS PRODUKSI 396. 000 TON TAHUN
Nama :
NIM : 1 . Nama
: NIP
: 2 .
Nama : Ir . Bambang Trisakti , MT
NIP
:
19660925 199103 1 003 Dr . Eng . Ir . Iirvan , M.Si
1968 0820 199501 1 001 Tri Afrianty
090425001
Universitas Sumatera Utara
Universitas Sumatera Utara
BAB V SPESIFIKASI PERALATAN
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