PABRIK NITROGLISERIN DARI GLISERIN DAN CAMPURAN ASAM KAPASITAS 20.000 TON/TAHUN
Nitroglycerin plant from Glycerol and mixed acid with capacity of 20.000 ton/years is designed to operate continuously for 24 hours/day during 330 days/year. The reaction occurs in the isotherm process in flow stirred tank reactor that operates at a pressure of 1 atm and temperature of 20 o C. The r...
| Main Authors: | , |
|---|---|
| Format: | Thesis |
| Published: |
[Yogyakarta] : Universitas Gadjah Mada
2014
|
| Subjects: |
| _version_ | 1797034698157850624 |
|---|---|
| author | , YUANA PURNAMA SARI , Dr. Ir. Sarto., M.Sc |
| author_facet | , YUANA PURNAMA SARI , Dr. Ir. Sarto., M.Sc |
| author_sort | , YUANA PURNAMA SARI |
| collection | UGM |
| description | Nitroglycerin plant from Glycerol and mixed acid with capacity of 20.000
ton/years is designed to operate continuously for 24 hours/day during 330
days/year. The reaction occurs in the isotherm process in flow stirred tank reactor
that operates at a pressure of 1 atm and temperature of 20
o
C. The reaction�s type
is exothermic. Regarding to the fact, the process need brine cooling liquid (CaCl2
25%) which flow through coil. Planned factory will be established in Bekasi, West
Java in the land area of 20.000 m
2
and employs 178 people.
Nitroglycerin plant with capacity of 20,000 tons/year requires 8.255,44 tons/year
of glycerol 98,5%, 27.374 tons/year of nitric acid 68%, 133,6 tons/year of
sulfuric acid 98%, 3.179,43 tons/year of Na2CO3 and 4.1667 tons/year of
ethanol. Utility components are 126.118,7 liters/year of water, 4.773,45
liters/year of fuel, 65.795 m
3
/year of CaCl2 brine, 270,8 kVA/year of electricity,
and 792.000 m
3
(STP condition) per year.
From economic evaluation, we obtained the results: fixed capital of
Rp65.651.381.878,61 + US$3.678.794,05, working capital of Rp15.335.561.172,25 +
US$1.496.297,81. Return of Investment before Tax = 28,33% , Return of
Investment after Tax = 14,16% , Pay Out Time before Tax =2,61 years, Pay Out
Time after Tax = 4,14 years, Break Even Point = 40,57% , Shut Down Point =
13,3%, and Discounted Cash Flow Rate of Return = DCFRR = 18,67 %.
Based on the results of economic evaluation, we may conclude that the
nitroglycerin plant with capacity of 20.000 tons/ year is quite interesting for
further study. |
| first_indexed | 2024-03-13T23:15:49Z |
| format | Thesis |
| id | oai:generic.eprints.org:127035 |
| institution | Universiti Gadjah Mada |
| last_indexed | 2024-03-13T23:15:49Z |
| publishDate | 2014 |
| publisher | [Yogyakarta] : Universitas Gadjah Mada |
| record_format | dspace |
| spelling | oai:generic.eprints.org:1270352016-03-04T08:18:27Z https://repository.ugm.ac.id/127035/ PABRIK NITROGLISERIN DARI GLISERIN DAN CAMPURAN ASAM KAPASITAS 20.000 TON/TAHUN , YUANA PURNAMA SARI , Dr. Ir. Sarto., M.Sc ETD Nitroglycerin plant from Glycerol and mixed acid with capacity of 20.000 ton/years is designed to operate continuously for 24 hours/day during 330 days/year. The reaction occurs in the isotherm process in flow stirred tank reactor that operates at a pressure of 1 atm and temperature of 20 o C. The reaction�s type is exothermic. Regarding to the fact, the process need brine cooling liquid (CaCl2 25%) which flow through coil. Planned factory will be established in Bekasi, West Java in the land area of 20.000 m 2 and employs 178 people. Nitroglycerin plant with capacity of 20,000 tons/year requires 8.255,44 tons/year of glycerol 98,5%, 27.374 tons/year of nitric acid 68%, 133,6 tons/year of sulfuric acid 98%, 3.179,43 tons/year of Na2CO3 and 4.1667 tons/year of ethanol. Utility components are 126.118,7 liters/year of water, 4.773,45 liters/year of fuel, 65.795 m 3 /year of CaCl2 brine, 270,8 kVA/year of electricity, and 792.000 m 3 (STP condition) per year. From economic evaluation, we obtained the results: fixed capital of Rp65.651.381.878,61 + US$3.678.794,05, working capital of Rp15.335.561.172,25 + US$1.496.297,81. Return of Investment before Tax = 28,33% , Return of Investment after Tax = 14,16% , Pay Out Time before Tax =2,61 years, Pay Out Time after Tax = 4,14 years, Break Even Point = 40,57% , Shut Down Point = 13,3%, and Discounted Cash Flow Rate of Return = DCFRR = 18,67 %. Based on the results of economic evaluation, we may conclude that the nitroglycerin plant with capacity of 20.000 tons/ year is quite interesting for further study. [Yogyakarta] : Universitas Gadjah Mada 2014 Thesis NonPeerReviewed , YUANA PURNAMA SARI and , Dr. Ir. Sarto., M.Sc (2014) PABRIK NITROGLISERIN DARI GLISERIN DAN CAMPURAN ASAM KAPASITAS 20.000 TON/TAHUN. UNSPECIFIED thesis, UNSPECIFIED. http://etd.ugm.ac.id/index.php?mod=penelitian_detail&sub=PenelitianDetail&act=view&typ=html&buku_id=67277 |
| spellingShingle | ETD , YUANA PURNAMA SARI , Dr. Ir. Sarto., M.Sc PABRIK NITROGLISERIN DARI GLISERIN DAN CAMPURAN ASAM KAPASITAS 20.000 TON/TAHUN |
| title | PABRIK NITROGLISERIN DARI GLISERIN DAN
CAMPURAN ASAM
KAPASITAS 20.000 TON/TAHUN |
| title_full | PABRIK NITROGLISERIN DARI GLISERIN DAN
CAMPURAN ASAM
KAPASITAS 20.000 TON/TAHUN |
| title_fullStr | PABRIK NITROGLISERIN DARI GLISERIN DAN
CAMPURAN ASAM
KAPASITAS 20.000 TON/TAHUN |
| title_full_unstemmed | PABRIK NITROGLISERIN DARI GLISERIN DAN
CAMPURAN ASAM
KAPASITAS 20.000 TON/TAHUN |
| title_short | PABRIK NITROGLISERIN DARI GLISERIN DAN
CAMPURAN ASAM
KAPASITAS 20.000 TON/TAHUN |
| title_sort | pabrik nitrogliserin dari gliserin dan campuran asam kapasitas 20 000 ton tahun |
| topic | ETD |
| work_keys_str_mv | AT yuanapurnamasari pabriknitrogliserindarigliserindancampuranasamkapasitas20000tontahun AT drirsartomsc pabriknitrogliserindarigliserindancampuranasamkapasitas20000tontahun |