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Toluene (in line) 30 1 M-01 P-01 2 V-01 F-01 M-02 3 R-01 UDARA FUEL OIL Flue Gas 5 H2 Make-up 6 C-01 PC PC CD-01 CW HW TC FC 32 S-01 PC 32 8 32 32 9 P-02 FC LC PC CD-02 CW FC HW ACC-01 FC P-05 P-03 RB-01 P-04 FC S C FC LC PC CD-03 CW FC HW ACC-02 FC P-08 P-06 RB-02 P-07 S C D-01 D-02 P-09 FC FC TC HE-01 TC 1.1 92.11 92.11 30 1 289.51 30 30 30 FC 1.1 30 450 186.85 1.5 EX-01 430 30 1.1 10 1.1 1.1 1 13 118.59 11 121.74 1.2 HE-02 T-01 T-02 14 156.72 1.5 CW HW 40 1 40 3 3 12 82.03 PABRIK PARAXYLENE PROSES DISPROPORSIONASI TOLUENE KAPASITAS 3000.000 TON/TAHUN JURUSAN TEKNIK KIMIA POLITEKNIK NEGERI SAMARINDA Digambar Dilihat Diperiksa Disetujui Rifki Fadhilah Firman, ST., M.Eng NIM. 13614050 KETERANGAN : Nomor aliran Temperatur (C) Tekanan (bar) C : Kompresor CD : Kondensor D : Kolom Destilasi EX : Expander F : Furnace HE : Heat Exchanger M : Mixer P : Pompa R : Reaktor S : Separator T : Tangki V : Vaporizer CW HW

Para Xy Lene

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  • Toluene

    (in line)

    30

    1

    M-01P-01

    2

    V-01

    F-01

    M-02

    3

    R-01

    UDARA

    FUEL OIL

    Flue Gas

    5

    H2 Make-up

    6

    C-01

    PCPC

    CD-01

    CW

    HW

    TC

    FC

    32

    S-01

    PC

    32

    8

    32

    32

    9

    P-02

    FC

    LC

    PC

    CD-02

    CW

    FC

    HW

    ACC-01

    FC

    P-05

    P-03

    RB-01

    P-04

    FC

    S

    C

    FC

    LC

    PCCD-03

    CW

    FC

    HW

    ACC-02

    FC

    P-08

    P-06

    RB-02

    P-07

    S

    C

    D-01 D-02

    P-09

    FC

    FC

    TC

    HE-01

    TC

    1.1

    92.11

    92.11

    30

    1

    289.51

    30

    30

    30

    FC

    1.1

    30

    450

    186.85

    1.5EX-01

    430

    30

    1.1

    10

    1.1

    1.1

    1

    13

    118.59

    11

    121.74

    1.2 HE-02

    T-01

    T-02

    14

    156.72

    1.5

    CW

    HW

    40

    1

    40

    3

    3

    12

    82.03

    PABRIK PARAXYLENE PROSES DISPROPORSIONASI

    TOLUENE KAPASITAS 3000.000 TON/TAHUN

    JURUSAN TEKNIK KIMIA

    POLITEKNIK NEGERI SAMARINDA

    Digambar

    Dilihat

    Diperiksa

    Disetujui

    Rifki Fadhilah

    Firman, ST., M.Eng

    NIM. 13614050

    KETERANGAN :

    Nomor aliran

    Temperatur (C)

    Tekanan (bar)

    C : Kompresor

    CD : Kondensor

    D : Kolom Destilasi

    EX : Expander

    F : Furnace

    HE : Heat Exchanger

    M : Mixer

    P : Pompa

    R : Reaktor

    S : Separator

    T : Tangki

    V : Vaporizer

    CW

    HW

  • PARAXYLENE.vsdPage-1Page-2