Tangki Mixer-Ammonium Nitrat, NH Tangki Mixer-Kalium Klorida, KCl M-102 Tangki Mixer-Magnesium Sulfat, MgSO Tangki Mixer-Ammonium Klorida, NH Fermenter R-101 Filter Press-1 H-101

BAB III NERACA MASSA

Basis perhitungan : 1 jam operasi Kapasitas produksi : 3 tonhari : 125 kgjam Satuan proses : kgjam

3.1 Tangki Mixer-Ammonium Nitrat, NH

4 NO 3 M-101 Tabel 3.1 Neraca Massa Pada Tangki Mixer-Ammonium Nitrat, NH 4 NO 3 M-101 Komponen Massa Masuk Massa Keluar Alur-4 Alur-5 Alur-6 NH 4 NO 3 25,7840 – 25,7840 H 2 O – 6,2888 6,2888 Total 32,0728 32,0728

3.2 Tangki Mixer-Kalium Klorida, KCl M-102

Tabel 3.2 Neraca Massa Pada Tangki Mixer-Kalium Klorida, KCl M-102 Komponen Massa Masuk Massa Keluar Alur-7 Alur-8 Alur-9 KCl 24,0114 – 24,0114 H 2 O – 160,0760 160,0760 Total 184,0874 184,0874

3.3 Tangki Mixer-Magnesium Sulfat, MgSO

4 M-103 Tabel 3.3 Neraca Massa Pada Tangki Mixer-Magnesium Sulfat, MgSO 4 M-103 Komponen Massa Masuk Massa Keluar Alur-10 Alur-11 Alur-12 MgSO 4 38,6760 – 38,6760 H 2 O – 154,7040 154,7040 Total 193,3800 193,3800

3.4 Tangki Mixer-Ammonium Klorida, NH

4 Cl M-104 Tabel 3.4 Neraca Massa Pada Tangki Mixer-Ammonium Klorida, NH 4 Cl M-104 Komponen Massa Masuk Massa Keluar Alur-13 Alur-14 Alur-15 NH 4 Cl 17,2431 – 17,2431 H 2 O – 9,0753 9,0753 Total 26,3184 26,3184 Universitas Sumatera Utara

3.5 Fermenter R-101

Tabel 3.5 Neraca Massa Pada Fermenter R-101 Komponen Massa Masuk Massa Keluar Alur-2 Alur-3 Alur-6 Alur-9 Alur-12 Alur-15 Alur-16 Alur-17 Alur-18 Alur-19 Alur-20 C 6 H 12 O 6 183,2021 – – – – – – – – – 9,1601 Impurities 152,6684 – – – – – – – – – 152,6684 NH 4 NO 3 – – 25,7840 – – – – – – – – KCl – – – 24,0114 – – – – – – – MgSO 4 – – – – 38,6760 – – – – – – NH 4 Cl – – – – – 17,2431 – – – – – CH 3 OH – – – – – – 10,3136 – – – – H 2 O 274,8032 – 6,2888 160,0760 154,7040 9,0753 333,4731 122,1347 – – 1112,7677 Aspergillus niger – 31,2933 – – – – – – – – – O 2 – – – – – – – – 105,1987 17,5331 – N 2 – – – – – – – – 395,7475 395,7475 – CO 2 – – – – – – – – – 56,7248 – C 6 H 8 O 7 – – – – – – – – – – 123,7632 C 2 H 2 O 4 – – – – – – – – – – 29,0070 Sel tersuspensi – – – – – – – – – – 147,3214 Total 610,6737 31,2933 32,0728 184,0874 193,3800 26,3184 343,7867 122,1347 500,9462 470,0054 1574,6878 2044,6932 2044,6932

3.6 Filter Press-1 H-101

Tabel 3.6 Neraca Massa Pada Filter Press-1 H-101 Komponen Massa Masuk Massa Keluar Alur-20 Alur-21 Alur-22 C 6 H 12 O 6 9,1601 9,1601 – Impurities 152,6684 152,6684 – Sel tersuspensi 147,3214 147,3214 – H 2 O 1112,7677 – 1112,7677 C 6 H 8 O 7 123,7632 – 123,7632 C 2 H 2 O 4 29,0070 – 29,0070 Total 1574,6878 309,1499 1265,5379 1574,6878 1574,6878

3.7 Tangki Koagulasi R-201