ppt assig 2 sispro
TRANSCRIPT
![Page 1: PPT Assig 2 Sispro](https://reader036.vdocument.in/reader036/viewer/2022081808/577c7de81a28abe054a011af/html5/thumbnails/1.jpg)
Pabrik Etilen Glikol dari Reaksi Non Katalitik Etilen Oksida dan Air
80000 ton/tahun
Aulia Rahmi Harianti1306370631
![Page 2: PPT Assig 2 Sispro](https://reader036.vdocument.in/reader036/viewer/2022081808/577c7de81a28abe054a011af/html5/thumbnails/2.jpg)
Reaksi yang dipilih
Hidrolisis Etilen Oksida Non-KatalitikC2H4O + H2O C2H6O2
Etilen Oksida + Air Etilen Glikol
H2O
C2H6O2 99%H2O 1%
n C2H6O2 : n H2O = 1:20
C2H4O
![Page 3: PPT Assig 2 Sispro](https://reader036.vdocument.in/reader036/viewer/2022081808/577c7de81a28abe054a011af/html5/thumbnails/3.jpg)
Process Flow Diagram
Komponen Unit 1 2 3 4 5 6 7 8 9 10 11 12Suhu 0C 9,98 10 24,83 25 95,6 65 65 99,63 99,63 186 30 99,63Tekanan kPa 100 120 100 1900 100 90 90 100 100 105 95 100Etilen Oksida
kg/jam
7621 7621 0 0 62,02 0 66137,1 0 0 0 0 58,68Air 0 0 3337 3337 61958 0 3502,89 0 58864,1 100,161 100,161 58621,3Etilen Glikol 0 0 0 0 0 0 0 0 5,887 10669,8 10669,8 0TOTAL 7621 7621 3337 3337 62020 0 69640 0 58870 10770 10770 58680
![Page 4: PPT Assig 2 Sispro](https://reader036.vdocument.in/reader036/viewer/2022081808/577c7de81a28abe054a011af/html5/thumbnails/4.jpg)
Etilen Oksida (C2H4O)
Sifat fisis (McKetta, 1984): • Berat molekul : 44,05 g/mol • Bentuk : Cair • Warna : jernih, tak berwarna • Kemurnian : 99,97% (0,03% air) • Titik didih(1 atm) : 10,4oC • Titik beku (1 atm) : -112,6oC • Viskositas (20oC) : 0,28 cP • Densitas (20oC ) : 0,8697 g/mL • Panas spesifik (20oC) : 0,44 kkal/goC • Panas penguapan (1 atm) : 6,1 kkal/gmol• Panas peleburan ( 1 atm) : 1,236 kkal/gmol
![Page 5: PPT Assig 2 Sispro](https://reader036.vdocument.in/reader036/viewer/2022081808/577c7de81a28abe054a011af/html5/thumbnails/5.jpg)
Air (H2O)
• Sifat Fisis (Perry and Chilton, 1984)
Berat molekul : 18,05 g/molBentuk : cairWarna : jernih, tak berwarnaTitik didih (1 atm) : 100oCTitik beku : 0oCDensitas : 1 g/mLTekanan kritis : 218 atmSuhu kritis : 374,2oCPanas pembentuka : -68,31 kkal/gmolPanas penguapan : 9,71 kkal/gmol
• Sifat KimiaMudah melarutkan zat-zat baik cair, padat maupun gasMerupakan reagent penghidrolisa pada proses hidrolisa
![Page 6: PPT Assig 2 Sispro](https://reader036.vdocument.in/reader036/viewer/2022081808/577c7de81a28abe054a011af/html5/thumbnails/6.jpg)
Monoetilen Glikol (C2H6O2)
Sifat fisis (McKetta, 1984)• Berat molekul : 62,07 g/mol• Bentuk : Cair• Warna : Jernih, tak bewarna• Kemurnian : 99,8%• Titik didih (1 atm) : 197,60oC• Titk beku (1 atm ) : - 13oC• Viskositas (20oC ) : 19,83 cP• Densitas ( 20oC ) : 1,11336 g/mL• Panas spesifik ( 20oC ) : 0,561
kkal/kg
• Panas peleburan (1 atm) : 44,7 kkal /g
• Panas penguapan (1 atm) : 202 kkal/kg
• Panas pembentukan (20oC ) : -108,1 kkal/mol
• Panas pembakaran (20oC) : -283,1 kkal/mol
![Page 7: PPT Assig 2 Sispro](https://reader036.vdocument.in/reader036/viewer/2022081808/577c7de81a28abe054a011af/html5/thumbnails/7.jpg)
Pompa-101
Komponen 1 2Suhu (C) 9,98 10Tekanan (kPa) 100 165Laju Massa Total (kg/jam) 7621 7621
PM-101Mass flow 7621kg/hDensity 885,4kg/m3Flowrate 8,60741m3/h 37,9013gpmP required 0,21kWh ⅓HpHarga US$ 302
Berguna untuk mengalirkan Etilen Oksida dari Storage ke
Reaktor R-101
![Page 8: PPT Assig 2 Sispro](https://reader036.vdocument.in/reader036/viewer/2022081808/577c7de81a28abe054a011af/html5/thumbnails/8.jpg)
Pompa-102
PM-102Mass flow 33337kg/hDensity 1007kg/m3Flowrate 33,1053m3/h 145,774gpmP required 2,21kWh 3HpHarga US$ 852
Komponen 3 4Suhu (C) 25 25Tekanan (kPa) 100 1900Laju Massa Total (kg/jam) 3337 3337
Berguna untuk mengalirkan Air dari Storage ke Mixer MIX-101
![Page 9: PPT Assig 2 Sispro](https://reader036.vdocument.in/reader036/viewer/2022081808/577c7de81a28abe054a011af/html5/thumbnails/9.jpg)
Mixer-101
MIX-101Volume flow 60m3/hBahan SSHarga US$ 12.100
Komponen 4 5 12Suhu (C) 25 95,6 99,63Tekanan (kPa) 1900 100 100TOTAL (kg/jam) 3337 62020 58680
![Page 10: PPT Assig 2 Sispro](https://reader036.vdocument.in/reader036/viewer/2022081808/577c7de81a28abe054a011af/html5/thumbnails/10.jpg)
Reaktor-101
Komponen 2 5 6 7Suhu (C) 10 95,6 65 65Tekanan (kPa) 165 100 90 90TOTAL (kg/jam) 7621 62020 0 69640
R-101Volume 100m3/hBahan SSP 90kPaT 65CTinggi 4,395mDiameter 3,96inHarga US$6.342.440
![Page 11: PPT Assig 2 Sispro](https://reader036.vdocument.in/reader036/viewer/2022081808/577c7de81a28abe054a011af/html5/thumbnails/11.jpg)
Kolom Distilasi-101
MX-101Volume flow 60m3/hBahan CSTray Sieve TrayPlate Min 9,67Plate Ideal 21Plate Aktual 35Harga US$ 616.347
Komponen 7 8 9 10Suhu (C) 65 99,63 99,63 186Tekanan (kPa) 90 100 100 105TOTAL (kg/jam) 69640 0 58870 10770
![Page 12: PPT Assig 2 Sispro](https://reader036.vdocument.in/reader036/viewer/2022081808/577c7de81a28abe054a011af/html5/thumbnails/12.jpg)
Pendingin-101
Komponen 10 11Suhu (C) 186 30Tekanan (kPa) 105 95TOTAL (kg/jam) 0 10770
![Page 13: PPT Assig 2 Sispro](https://reader036.vdocument.in/reader036/viewer/2022081808/577c7de81a28abe054a011af/html5/thumbnails/13.jpg)
Tangki-101
LD-101Volume flow 8,640m3/hBahan SSDimensi 1,9 x 7,5Harga US$ 2.970
Berguna untuk menyimpan reaktan Etilen Oksida
![Page 14: PPT Assig 2 Sispro](https://reader036.vdocument.in/reader036/viewer/2022081808/577c7de81a28abe054a011af/html5/thumbnails/14.jpg)
Tangki-102
LD-102Tekanan 100 kPaSuhu 24,83 CVolume flow 3,344m3/hBahan SSDimensi 1,1 x 6,0Harga US$ 2.145
Berguna untuk menyimpan reaktan Air
![Page 15: PPT Assig 2 Sispro](https://reader036.vdocument.in/reader036/viewer/2022081808/577c7de81a28abe054a011af/html5/thumbnails/15.jpg)
Tangki-103
LD-103Tekanan 95 kPaSuhu 30 CVolume flow 9,697m3/hBahan SSDimensi 2,1 x 8,0Harga US$ 3.300
Spesifikasi ProdukEG % 0,9970H2O% 0,0093Massa EG 10.737 kg/hr
80.393 ton/thn
Berguna untuk menyimpan produk Etilen Glikol
![Page 16: PPT Assig 2 Sispro](https://reader036.vdocument.in/reader036/viewer/2022081808/577c7de81a28abe054a011af/html5/thumbnails/16.jpg)
Grade Etilen GlikolSpesifikasi Produk
EG % 0,9970H2O% 0,0093Massa EG 10.737 kg/hr
80.393 ton/thn
![Page 17: PPT Assig 2 Sispro](https://reader036.vdocument.in/reader036/viewer/2022081808/577c7de81a28abe054a011af/html5/thumbnails/17.jpg)
Analisis Ekonomi
Komponen Harga Beli Harga JualRaw Material Rp 885.803.418.427,88 Rp - Produk Rp - Rp 972.000.000.000,00 Onsite Rp 97.726.384.000 RpTotal Rp 983.529.802.427,88 Rp 972.000.000.000,00 Selisih Rp (11.529.802.427,87)