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