Mixer MX Reaktor Hidrolisa RH Cooler CO Filter Press-01 FP-01 Tabel Perhitungan Neraca Panas pada Filter press-01 FP-01 Reaktor Netralisasi RN Tabel Perhitungan Neraca Panas pada Reaktor Netralisasi RN

IV-1

BAB IV NERACA ENERGI

Hasil perhitungan neraca energi pada tiap unit peralatan diperoleh dari lampiran B sebagai berikut :

4.1 Mixer MX

Tabel 4.1 Perhitungan Neraca Panas pada Mixer MX Komponen Masuk kkaljam Keluar kkaljam alur 1 alur 2 alur 3 Pati Air Lemak Protein Impuritis Serat Glukosa 1.939,3125 154,0245 68,7862 308,4255 126,1965 1.318,143 497,9565 608,592 1.939,3125 762,6130 68,7862 308,4255 126,1965 1.318,143 497,9565 Total 4.412,9447 608,592 5.021,4367 5.021,4367 5.021,4367

4.2 Reaktor Hidrolisa RH

Tabel 4.2 Perhitungan Neraca Panas pada Reaktor Hidrolisa RH Komponen Masuk kkaljam Keluar kkaljam alur 3 alur 4 alur 5 alur 6 Pati Air Lemak Protein Impuritis Serat Glukosa HCl Panas reaksi Steam 1.939,3125 762,613 68,7862 308,4255 126,1965 1.318,143 497,9565 1,638 84,9705 5,0943 28.538,6865 5.407.728,26 4.266,4888 5.376.658,464 1.524,9382 6.785,3715 2.776,3185 28.999,158 10.955,058 9.346,7889 Total 5.021,4367 86,6085 5.436.272,04 5.441.380,086 5.441.380,086 5.441.380,086 IV-2

4.3 Cooler CO

Tabel 4.3 Perhitungan Neraca Panas pada Cooler CO Komponen Masuk kkaljam Keluar kkaljam Alur 6 alur 7 Pati Air Lemak Protein Impuritis Serat Glukosa HCl Air pendingin 4.266,4888 5.376.658,464 1.524,9382 6.785,3715 2.776,3185 28.999,158 10.955,058 9.346,7889 - 5.402.415,447 969,6565 12.812,6205 346,5768 1.542,1299 630,981 6.590,718 13.947,6865 2.124,27 Total 38.964,6393 38.964,6393 4.4 Filter Press-01 FP-01 Tabel 4.4 Perhitungan Neraca Panas pada Filter press-01 FP-01 Komponen Masuk kkaljam Keluar kkaljam alur 7 alur 8 alur 9 Pati Air Lemak Protein Impuritis Serat Glukosa HCl 969,6565 12.812,6205 346,5768 1.542,1299 630,981 6.590,718 13.947,6865 2.124,27 969,6565 12,813 346,5768 1.542,1299 630,981 6.590,718 13,947 2,1235 12.799,8075 13.947,285 2.122,146 Total 38.964,6393 10.108,9455 28.855,692 38.964,6393 38.964,6393 4.5 Reaktor Netralisasi RN Tabel 4.5 Perhitungan Neraca Panas pada Reaktor Netralisasi RN Komponen Masuk kkaljam Keluar kkaljam alur 9 alur 10 alur 11 Air Glukosa HCl NaOH NaCl Panas reaksi Steam 12.799,8075 13.933,7385 2.122,146 -10.572,5326 20.067,1915 1,7955 621,030 14.798,937 19.487,734 4.686,5055 Total 38.350,3515 622,8255 38.973,177 38.973,177 38.973,177 IV-3 4.6 Tangki Dekanter DK Tabel 4.6 Perhitungan Neraca Panas pada Tangki Dekanter DK