Prarancangan Pabrik Asam Nitrat Dari Asam Sulfat dan Natrium Nitrat Kapasitas 65.000 Ton Per Tahun

Pratiwi, Luluk and , M. Mujiburohman, Ph.D. and , Hamid Abdillah, S.T., M.T. (2016) Prarancangan Pabrik Asam Nitrat Dari Asam Sulfat dan Natrium Nitrat Kapasitas 65.000 Ton Per Tahun. Diploma thesis, Universitas Muhammadiyah Surakarta.

[img] PDF (Naskah Publikasi)
Naskah Publikasi.pdf

Download (1MB)
[img] PDF (Halaman Depan)
Halaman Depan.pdf

Download (1MB)
[img] PDF (BAB I)
BAB I.pdf

Download (243kB)
[img] PDF (BAB II)
BAB II.pdf
Restricted to Repository staff only

Download (1MB) | Request a copy
[img] PDF (BAB III)
BAB III.pdf
Restricted to Repository staff only

Download (224kB) | Request a copy
[img] PDF (BAB IV)
BAB IV.pdf
Restricted to Repository staff only

Download (380kB) | Request a copy
[img] PDF (BAB V)
BAB V.pdf
Restricted to Repository staff only

Download (275kB) | Request a copy
[img] PDF (BAB VI)
BAB VI.pdf
Restricted to Repository staff only

Download (732kB) | Request a copy
[img] PDF (Daftar Pustaka)
Daftar Pustaka.pdf

Download (244kB)
[img] PDF (Lampiran)
Lampiran.pdf
Restricted to Repository staff only

Download (746kB) | Request a copy
[img] PDF (Pernyataan Publikasi Ilmiah)
Surat Pernyataan Publikasi Karya Ilmiah.pdf
Restricted to Repository staff only

Download (690kB) | Request a copy

Abstract

Nitric acid plant with raw materials of sulphuric acid and sodium nitrate with a capacity 65.000 tons/year is planned to be established in 2020 in Karawang, West Java. The sodium nitrate is imported from Chile and the sulphuric acid is from PT Indonesian Acid Industry. The nitric acid production uses continuous stirred tank reactor (CSTR). The reaction is exothermic, non adiabatic, and irreversible, carried out at temperature of 150°C and pressure of 1 atm. The plant is categorized as low risk process due to the friendly operating conditions. The process of nitric acid production is initiated with reacting sulphuric acid and sodium nitrate in the reactor. The vapor product of reactor is condensed by a partial condenser and is purified in distillation tower to produce nitric acid with purity of 98%, while the liquid product, called niter cake, is stored as side product. Based on the capacity, the production of nitric acid is 8,207.0707 kgs/hour. To support the process, utilities are required including 264,779.5449 kgs/hour of cooling water, 19,772.5449 kgs/hour of steam. Which is obtained from boiler consuming fuel oil as much as 1,473.8109 L/hour, and electricity supplied from PLN and generator set. The water source is taken from Kalimalang river,. The economic analysis gives the profit before tax is Rp113,168,435,407/year, and Rp84,876,326,556/year after tax. The percent Return on Investment (ROI) before tax is 34.52% and 25.89% after tax. The Pay Out Time (POT) before tax is 2.25 years and 2.79 years after tax. The Break Event Point (BEP), the Shut Down Point (SDP), and the Internal Rate of Return (IRR) are 47.80, 25.11%, and 40.27%, respectively. The above economic analysis concludes that the plant is feasible to set.

Item Type: Karya ilmiah (Diploma)
Uncontrolled Keywords: CSTR, niter cake, nitric acid, sulphuric acid
Subjects: Q Science > QD Chemistry
Divisions: Fakultas Teknik > Teknik Kimia
Depositing User: LULUK PRATIWI
Date Deposited: 21 Nov 2016 04:04
Last Modified: 21 Nov 2016 04:04
URI: http://eprints.ums.ac.id/id/eprint/48052

Actions (login required)

View Item View Item