63
Lampiran 1 Hasil ANOVA dan Uji Lanjut Duncan untuk pengaruh homogenisasi terhadap stabilitas emulsi
Class Levels Values factor 1
factor 2 3 3
Rpm10000 Rpm8000 Rpm6000 Waktu1 Waktu3 Waktu4
Source DF Sum of Squares Mean Square F Value
Pr>F Model 8 13.59631111 1.69953889 28.60 <.0001 Error 9 0.53485000 0.05942778
Corrected Total 17 14.13116111
R-Square Coeff Var Root MSE Respon Mean 0.962151 0.249996 0.243778 97.51278
Source DF Type I SS Mean Square F Value Pr>F faktor 1 faktor 2 faktor 1*faktor 2 2 2 4 3.90201111 8.86137778 0.83292222 1.95100556 4.43068889 0.20823056 32.83 74.56 3.50 <.0001 <.0001 0.0547 Duncan’s Multiple Range Test for respon
Alpha 0.05
Error Degrees of Freedom 9
Error Mean Square 0.059428
Number of Mean 2 3
Critical Range .3184 .3323
Means with the same letter are not significantly different Duncan Grouping Mean N faktor
A 97.9633 6 Rpm10000
A 97.7033 6 Rpm8000
B 96.8717 6 Rpm6000
Means with the same letter are not significantly different Duncan Grouping Mean N faktor 2
A 98.2250 6 Waktu 4
B 97.7550 6 Waktu 3
Lampiran 2 Hasil ANOVA dan Uji Lanjut Duncan untuk pengaruh homogenisasi terhadap ukuran rata-rata droplet emulsi [d3,2]
Class Levels Values factor 1
factor 2
3 3
Rpm10000 Rpm8000 Rpm6000 Waktu1 Waktu3 Waktu4
Source DF Sum of Squares Mean Square F Value Pr>F Model 8 1.67507778 0.20938472 129.52 <.0001
Error 9 0.01455000 0.00161667
Corrected Total 17 1.68962778
R-Square Coeff Var Root MSE Respon Mean 0.991389 1.679601 0.040208 2.393889 Source DF Type I SS Mean Square F
Value Pr>F faktor 1 faktor 2 faktor 1*faktor 2 2 2 4 0.67814444 0.95231111 0.04462222 0.33907222 0.47615556 0.01115556 209.74 294.53 6.90 <.0001 <.0001 0.0080 Duncan’s Multiple Range Test for respon
Alpha 0.05
Error Degrees of Freedom 9
Error Mean Square 0.001617
Number of Mean 2 3
Critical Range .05251 .05481 Means with the same letter are not significantly different Duncan Grouping Mean N faktor 1
A 2.65500 6 Rpm6000
B 2.33667 6 Rpm8000
C 2.19000 6 Rpm10000
Means with the same letter are not significantly different Duncan Grouping Mean N faktor 2
A 2.71500 6 Waktu 1
B 2.27833 6 Waktu 3
65
Lampiran 3 Hasil ANOVA dan Uji Lanjut Duncan untuk pengaruh suhu dan waktu pasteurisasi terhadap stabilitas emulsi
Class Levels Values faktor 1 faktor 2 2 2 Suhu 70 Suhu 80 Waktu 10 Waktu 15
Source DF Sum of Squares Mean Square F Value Pr>F Model 3 4.63135000 1.54378333 25.37 0.0046 Error 4 0.11045000 0.06085000
Corrected Total 7 0.11045000
R-Square Coeff Var Root MSE Respon Mean 0.950069 0.254130 0.246678 97.06750
Source DF Type I SS Mean Square F Value Pr>F faktor 1 faktor 2 faktor 1*faktor 2 1 1 1 4.41045000 0.11045000 0.11045000 4.41045000 0.11045000 0.11045000 72.48 1.82 1.82 0.0010 0.2492 0.2492 Duncan’s Multiple Range Test for respon
Alpha 0.05
Error Degrees of Freedom 4 Error Mean Square 0.06085
Number of Mean 2
Critical Range .4843
Means with the same letter are not significantly different Duncan Grouping Mean N faktor 1
A 97.8100 4 Suhu 70
B 963250 4 Suhu 80
Means with the same letter are not significantly different Duncan Grouping Mean N faktor 2
A 97.1850 4 Waktu 10
Lampiran 4 Hasil ANOVA dan Uji Lanjut Duncan untuk pengaruh suhu dan waktu pasteurisasi terhadap nilai L (kecerahan) emulsi
Class Levels Values faktor 1 faktor 2 2 2 Suhu 70 Suhu 80 Waktu 10 Waktu 15
Source DF Sum of Squares Mean Square F Value Pr>F Model 3 5.54470000 1.84823333 2.02 0.2541 Error 4 3.66570000 0.91642500
Corrected Total 7 9.21040000
R-Square Coeff Var Root MSE Respon Mean 0.602004 1.174746 0.957301 81.49000 Source DF Type I SS Mean Square F
Value Pr>F Factor 1 Faktor 2 Faktor 1*Faktor 2 1 1 1 5.44500000 0.03125000 0.06845000 5.44500000 0.03125000 0.06845000 5.94 0.03 0.07 0.0714 0.8625 0.7982 Duncan’s Multiple Range Test for respon
Alpha 0.05
Error Degrees of Freedom 4
Error Mean Square 0.916425
Number of Mean 2
Critical Range 1.879
Means with the same letter are not significantly different Duncan Grouping Mean N Perlakuan
A 82.3150 4 Suhu 80
A 80.6650 4 Suhu 70
Means with the same letter are not significantly different Duncan Grouping Mean N Perlakuan
A 81.5525 4 Waktu 10
67
Lampiran 5 Hasil ANOVA dan Uji Lanjut Duncan untuk pengaruh suhu dan waktu pasteurisasi terhadap nilai a emulsi
Class Levels Values faktor 1 faktor 2 2 2 Suhu 70 Suhu 80 Waktu 10 Waktu 15
Source DF Sum of Squares Mean Square F Value Pr>F Model 3 11.25343750 3.75114583 6.41 0.0522 Error 4 2.33945000 0.58486250
Corrected Total 7 13.59288750
R-Square Coeff Var Root MSE Respon Mean 0.827892 21.47457 0.764763 3.561250
Source DF Type I SS Mean Square F Value Pr>F faktor 1 faktor 2 faktor 1*faktor 2 1 1 1 11.06851250 0.09031250 0.09461250 11.06851250 0.09031250 0.09461250 18.92 0.15 0.16 0.0122 0.7144 0.7081 Duncan’s Multiple Range Test for respon
Alpha 0.05
Error Degrees of Freedom 4
Error Mean Square 0.584862
Number of Mean 2
Critical Range 1.501
Means with the same letter are not significantly different Duncan Grouping Mean N faktor 1
A 4.7375 4 Suhu 70
B 2.3850 4 Suhu 80
Means with the same letter are not significantly different Duncan Grouping Mean N faktor 2
A 3.6675 4 Waktu 10
B 3.4550 4 Waktu 15
Lampiran 6 Hasil ANOVA dan Uji Lanjut Duncan untuk pengaruh suhu dan waktu pasteurisasi terhadap nilai b emulsi
Class Levels Values faktor 1 faktor 2 2 2 Suhu 70 Suhu 80 Waktu 10 Waktu 15
Source DF Sum of Squares Mean Square F Value Pr>F
Model 3 7.76695000 2.58898333 0.98 0.4862
Error 4 10.57540000 2.64385000 Corrected Total 7 18.34235000
R-Square Coeff Var Root MSE Respon Mean 0.423444 1.972753 1.625992 82.42250
Source DF Type I SS Mean Square F Value Pr>F faktor 1 faktor 2 faktor 1*faktor 2 1 1 1 5.02445000 0.99405000 1.74845000 5.02445000 0.99405000 1.74845000 1.90 0.38 0.66 0.2401 0.5729 0.4617 Duncan’s Multiple Range Test for respon
Alpha 0.05
Error Degrees of Freedom 4 Error Mean Square 2.64385
Number of Mean 2
Critical Range 3.192
Means with the same letter are not significantly different Duncan Grouping Mean N faktor 1
A 83.215 4 Suhu 70
B 81.630 4 Suhu 80
Means with the same letter are not significantly different Duncan Grouping Mean N faktor 2
A 82.775 4 Waktu 10
Lampiran 7 Perincian biaya investasi minuman emulsi minyak sawit merah 1 Lahan 200 m2 350.000 70.000.000 2 Bangunan 180 m2 2.000.000 360.000.000 Sub total 430.000.000 3
Mesin dan Alat
a. Homogenizer Rotor Stator 2 unit 27.175.000 54.350.000
b. Panci email 2 unit 300.000 600.000
c. Timbangan 2 unit 500.000 1.000.000
d. Gelas ukur 4 unit 25.000 100.000
e. Corong plastik 2 unit 15.000 30.000
f. Pasteurizer 1 unit 6.226.920 6.226.920 g. Kereta dorong 1 500.000 500.000 Sub total 62.806.920 4 Perlengkapan a. Perlengkapan K3 1 unit 500.000 500.000
b. Alat-alat kantor 1 paket 10.000.000 10.000.000
Sub total 10.500.000
5
Instalasi penunjang
Instalasi air 1 Paket 633.500 633.500
Instalasi listrik 1 Paket 2.000.000 2.000.000
Instalasi telepon 1 Paket 500.000 500.000
Sub total 3.133.500 6 Perizinan 1 Paket 600.000 600.000 507.040.420 62 Total Investasi Biaya
Lampiran 10 Perhitungan biaya pokok produksi Deskripsi Biaya A. Biaya Variabel 1 Bahan baku 458,430,000 2 Kemasan 262,500,000 3 Listrik 15,000,000 4 Air 1,200,000
5 Gaji tenaga kerja langsung
48,000,000
6
Biaya pemasaran dan distribusi 6,000,000 Sub total 791,130,000 B. Biaya Tetap 1 Penyusutan 40,198,688 2 Pemeliharaan 8,726,208 3
Gaji tenaga kerja tidak langsung 100,800,000 4 Pajak 10,750,000
5 Administrasi dan kantor
6,000,000 Sub total 166,474,896 Total 957,604,896
- Produk yang dihasilkan pertahun 30.000 liter - Produk yang dihasilkan perhari 100 liter
- HPP/200 ml 6,384 rupiah
- Keuntungan (50%) 3,192 rupiah - Harga + keuntungan 9,576 rupiah
- PPn (10%) 957 rupiah
Lampiran 11 Rencana pengembalian pinjaman (10 tahun)
Tahun Periode Angsuran Pokok Angsuran Bunga Total Angsuran Saldo Akhir Bulan
Tahun 0 1.025.251.721 Tahun 1 Tahun 1 102.525.172 153.787.758 256.312.930 922.726.549 Tahun 2 102.525.172 153.787.758 256.312.930 820.201.377 Tahun 3 102.525.172 153.787.758 256.312.930 717.676.205 Tahun 4 102.525.172 153.787.758 256.312.930 615.151.033 Tahun 5 102.525.172 153.787.758 256.312.930 512.625.861 Tahun 6 102.525.172 153.787.758 256.312.930 410.100.688 Tahun 7 102.525.172 153.787.758 256.312.930 307.575.516 Tahun 8 102.525.172 153.787.758 256.312.930 205.050.344 Tahun 9 102.525.172 153.787.758 256.312.930 102.525.172 Tahun 10 102.525.172 153.787.758 256.312.930 -1.025.251.721 1.537.877.582 2.563.129.303 Total
1 Minuman Emulsi 1.320.000.000 1.485.000.000 1.650.000.000 1.650.000.000 1.650.000.000 1.650.000.000 1.650.000.000 1.650.000.000 1.650.000.000 1.650.000.000 1.320.000.000 1.485.000.000 1.650.000.000 1.650.000.000 1.650.000.000 1.650.000.000 1.650.000.000 1.650.000.000 1.650.000.000 1.650.000.000 1 Tanah 70.000.000 70.000.000 2 Bangunan 360.000.000 360.000.000 3
Mesin dan Alat 62.806.920 62.806.920 4 Perlengkapan 10.500.000 10.500.000 5 Instalasi Penunjang 3.133.500 3.133.500 6 Biaya perizinan 600.000 600.000 507.040.420 507.040.420 799.378.896 878.491.896 957.604.896 957.604.896 957.604.896 957.604.896 957.604.896 957.604.896 957.604.896 957.604.896 1 Biaya tetap 166.474.896 166.474.896 166.474.896 166.474.896 166.474.896 166.474.896 166.474.896 166.474.896 166.474.896 166.474.896 2 Biaya variabel 632.904.000 712.017.000 791.130.000 791.130.000 791.130.000 791.130.000 791.130.000 791.130.000 791.130.000 791.130.000 (507.040.420) 520.621.104 606.508.104 692.395.104 692.395.104 692.395.104 692.395.104 692.395.104 692.395.104 692.395.104 692.395.104 Total Penjualan Investasi Total Investasi Biaya Operasional Surplus (Defisit)
Lampiran 15 Proyeksi arus kas minuman emulsi minyak sawit merah pada penurunan harga jual produk 8%
No. Parameter Tahun 0 Tahun 1 Tahun 2 Tahun 3 Tahun 4 Tahun 5 Tahun 6 Tahun 7 Tahun 8 Tahun 9 Tahun 10
120.000 135.000 150.000 150.000 150.000 150.000 150.000 150.000 150.000 150.000 1 Minuman Emulsi 1.200.000.000 1.350.000.000 1.500.000.000 1.500.000.000 1.500.000.000 1.500.000.000 1.500.000.000 1.500.000.000 1.500.000.000 1.500.000.000 1.200.000.000 1.350.000.000 1.500.000.000 1.500.000.000 1.500.000.000 1.500.000.000 1.500.000.000 1.500.000.000 1.500.000.000 1.500.000.000 1 Tanah 70.000.000 70.000.000 2 Bangunan 360.000.000 360.000.000 3
Mesin dan Alat 62.806.920 62.806.920 4 Perlengkapan 10.500.000 10.500.000 5 Instalasi Penunjang 3.133.500 3.133.500 6 Biaya perizinan 600.000 600.000 507.040.420 507.040.420 799.378.896 878.491.896 957.604.896 957.604.896 957.604.896 957.604.896 957.604.896 957.604.896 957.604.896 957.604.896 1 Biaya tetap 166.474.896 166.474.896 166.474.896 166.474.896 166.474.896 166.474.896 166.474.896 166.474.896 166.474.896 166.474.896 2 Biaya variabel 632.904.000 712.017.000 791.130.000 791.130.000 791.130.000 791.130.000 791.130.000 791.130.000 791.130.000 791.130.000 (507.040.420) 400.621.104 471.508.104 542.395.104 542.395.104 542.395.104 542.395.104 542.395.104 542.395.104 542.395.104 542.395.104 Surplus (Defisit) Penjualan (Botol) Total Penjualan Investasi Total Investasi Biaya Operasional
