Veni, . and Kurniawan, Hendra (2004) Prarencana Pabrik Asam Oksalat kapasitas 1650 ton/tahun. Undergraduate thesis, Widya Mandala Catholic University Surabaya.
Preview |
Text (ABSTRAK)
ABSTRAK.pdf Download (281kB) | Preview |
Preview |
Text (BAB 1)
BAB 1.pdf Download (186kB) | Preview |
![[thumbnail of BAB 2]](http://repository.ukwms.ac.id/style/images/fileicons/text.png) |
Text (BAB 2)
BAB 2.pdf Restricted to Registered users only Download (192kB) |
|
Text (BAB 3)
BAB 3.pdf Restricted to Registered users only Download (120kB) |
|
Text (BAB 4)
BAB 4.pdf Restricted to Registered users only Download (101kB) |
|
Text (BAB 5)
BAB 5.pdf Restricted to Registered users only Download (372kB) |
|
Text (BAB 6)
BAB 6.pdf Restricted to Registered users only Download (885kB) |
|
Text (BAB 7)
BAB 7.pdf Restricted to Registered users only Download (240kB) |
|
Text (BAB 8)
BAB 8.pdf Restricted to Registered users only Download (305kB) |
Preview |
Text (BAB 9)
BAB 9.pdf Download (85kB) | Preview |
|
Text (LAMPIRAN)
LAMPIRAN.pdf Restricted to Registered users only Download (2MB) |
Abstract
Asam oksalat adalah senyawa kimia yang memiliki banyak kegunaan. Asam oksalat digunakan dalam pengolahan logam, pelapisan, industri tekstil, pembersihan logam, dan pewarnaan. Asam oksalat dapat dibuat dengan metode oksidasi glukosa menggunakan asam nitrat, bahan dasarnya berupa glukosa dalam ampas tepung tapioka. Asam oksalat yang dihasilkan memiliki kemurnian 99,5%. Asam oksalat diproduksi dengan tahap-tahap: persiapan bahan baku, reaksi hidrolisa dan oksidasi, filtrasi, kristalisasi,pemisahan, dan pengeringan. Rancangan operasi: Kapasilas Produksi : 11,2 ton/hari Bahan baku . : Ampas Tepung Tapioka dan HNO3 Kebutuhan Utilitas • Air : 143,78 m3/hari • Listrik : 66,8722 KVA • 'Bahan Bakar: -Solar: 15 lb/jam -Batu bara: 35869,0977 lb/hari Kebutuhan Pegawai : 100 orang Lokasi Pabrik : Sleman, Yogyakarta Luas Pabrik : 6575 m2 Analisa Ekonomi: Fixed capital investment (FCI): Rp. 9.093.602.347,5 Working capital (WC): Rp. 1.604.753.355,44 Total production'cost: Rp. 104.915.542.107,96 Sales per year: Rp. 182.833:200.000 1. Metode Garis Linier Rate of Return sebelum pajak: 728,31 % Rate Of Return setelah pajak: 473,77% Pay Out Time sebelum pajak: 1 bulan Pay Out Time sesudah pajak: 2 bulan Break Even Point (BEP): 5,30% 2. MetodeDiscounted Cash Flow Rate of Return sebelum pengembalian pinjaman: 385,66 % Rate of Return sesudah pengembalian pinjaman: 382,93% Rate of Equity sebelum pengembalian pinjaman: 572,75% Rate of Equity sesudah pengembalian pinjaman: 568,59% Pay Out Time sebelum pengembalian pinjaman: 5 bulan Pay Out Time sesudah pengembalian pinjaman: 5 bulan Break Even Point (BEP): 5,58%
| Item Type: | Thesis (Undergraduate) |
|---|---|
| Department: | ["eprint_fieldopt_department_Faculty of engineering" not defined] |
| Subjects: | Engineering Engineering > Chemical Engineering |
| Divisions: | Faculty of Engineering > Chemical Engineering Study Program |
| Depositing User: | Users 32 not found. |
| Date Deposited: | 01 Feb 2016 02:12 |
| Last Modified: | 01 Feb 2016 02:12 |
| URI: | http://repository.ukwms.ac.id/id/eprint/3412 |
Actions (login required)
 |
View Item |