analisa ekonomi

8
 PERHITUNGAN EKONOMI 1. MENENTUKAN INDEKS HARGA Indeks harga tahun 1987 - 2002 tahun = X indeks harga = Y X Y XY X2 1.0000 1,987.0000 324.0000 643,788.0000 3,948,169.0000 2.0000 1,988.0000 343.0000 681,884.0000 3,952,144.0000 3.0000 1,989.0000 355.0000 706,095.0000 3,956,121.0000 4.0000 1,990.0000 357.6000 711,624.0000 3,960,100.0000 5.0000 1,991.0000 361.3000 719,348.3000 3,964,081.0000 6.0000 1,992.0000 358.2000 713,534.4000 3,968,064.0000 7.0000 1,993.0000 359.2000 715,885.6000 3,972,049.0000 8.0000 1,994.0000 368.1000 733,991.4000 3,976,036.0000 9.0000 1,995.0000 381.1000 760,294.5000 3,980,025.0000 10.0000 1,996.0000 381.7000 761,873.2000 3,984,016.0000 11.0000 1,997.0000 386.5000 771,840.5000 3,988,009.0000 12.0000 1,998.0000 389.5000 778,221.0000 3,992,004.0000 13.0000 1,999.0000 390.6000 780,809.4000 3,996,001.0000 14.0000 2,000.0000 394.1000 788,200.0000 4,000,000.0000 15.0000 2,001.0000 394.3000 788,994.3000 4,004,001.0000 16.0000 2,002.0000 390.4000 781,580.8000 4,008,004.0000 31,912.0000 5,934.6000 11,837,964.4000 63,648,824.0000 SLOPE = n.sigmaXY-sigmaX.sigmaY/n.sigmaX2-(sigmaX)2 A = 4.1315 INTE RCE PT = sigmaY.sigmaX2 -sigmaXY.sigmaX/n.s igmaX2-(sigmaX)2 B = -7,869.3056 Persamaan untuk indeks harga Y = AX + B Y = 4.1315 X -7,869.3056 Jadi indeks harga tahun 2003 - 2020 tahun indeks harga 2003 406.0300 2004 410.1615 2005 414.2929 2006 418.4244 2007 422.5559 2008 426.6874 2009 430.8188 2010 434.9503 2011 439.0818 2012 443.2132 2013 447.3447 2014 451.4762 2015 455.6076 2016 459.7391 2017 463.8706 2018 468.0021 2019 472.1335 2020 476.2650

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analisa ekonomi pabrik MIBK kapasitas 20.000 ton/thn

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  • PERHITUNGAN EKONOMI

    1. MENENTUKAN INDEKS HARGA

    Indeks harga tahun 1987 - 2002

    tahun = X

    indeks harga = Y

    X Y XY X2

    1.0000 1,987.0000 324.0000 643,788.0000 3,948,169.0000

    2.0000 1,988.0000 343.0000 681,884.0000 3,952,144.0000

    3.0000 1,989.0000 355.0000 706,095.0000 3,956,121.0000

    4.0000 1,990.0000 357.6000 711,624.0000 3,960,100.0000

    5.0000 1,991.0000 361.3000 719,348.3000 3,964,081.0000

    6.0000 1,992.0000 358.2000 713,534.4000 3,968,064.0000

    7.0000 1,993.0000 359.2000 715,885.6000 3,972,049.0000

    8.0000 1,994.0000 368.1000 733,991.4000 3,976,036.0000

    9.0000 1,995.0000 381.1000 760,294.5000 3,980,025.0000

    10.0000 1,996.0000 381.7000 761,873.2000 3,984,016.0000

    11.0000 1,997.0000 386.5000 771,840.5000 3,988,009.0000

    12.0000 1,998.0000 389.5000 778,221.0000 3,992,004.0000

    13.0000 1,999.0000 390.6000 780,809.4000 3,996,001.0000

    14.0000 2,000.0000 394.1000 788,200.0000 4,000,000.0000

    15.0000 2,001.0000 394.3000 788,994.3000 4,004,001.0000

    16.0000 2,002.0000 390.4000 781,580.8000 4,008,004.0000

    31,912.0000 5,934.6000 11,837,964.4000 63,648,824.0000

    SLOPE = n.sigmaXY-sigmaX.sigmaY/n.sigmaX2-(sigmaX)2

    A = 4.1315

    INTERCEPT = sigmaY.sigmaX2-sigmaXY.sigmaX/n.sigmaX2-(sigmaX)2

    B = -7,869.3056

    Persamaan untuk indeks harga Y = AX + B

    Y = 4.1315 X -7,869.3056

    Jadi indeks harga tahun 2003 - 2020

    tahun indeks harga

    2003 406.0300

    2004 410.1615

    2005 414.2929

    2006 418.4244

    2007 422.5559

    2008 426.6874

    2009 430.8188

    2010 434.9503

    2011 439.0818

    2012 443.2132

    2013 447.3447

    2014 451.4762

    2015 455.6076

    2016 459.7391

    2017 463.8706

    2018 468.0021

    2019 472.1335

    2020 476.2650

  • HARGA ALAT TAHUN 2015

    harga satuan

    US $

    ACC-01 = Accumulator-01 3,000.00

    ACC-02 = Accumulator-02 3,000.00

    ACC-03 = Accumulator-03 3,000.00

    CH-01 = Chiller-01

    C-01 = Cooler-01 2,100.00

    C-02 = Cooler-02 3,200.00

    C-03 = Cooler-03 2,800.00

    C-04 = Cooler-04 2,800.00

    C-05 = Cooler-05 2,800.00

    CD-01 = Condenser-01 76,900.00

    CD-02 = Condenser-02 145,100.00

    CD-03 = Condenser-03 134,700.00

    EXP-01 = Expander-01 1,000.00

    F-01 = Furnace-01 686,700.00

    F-02 = Furnace-02 686,700.00

    H-01 = Heater-01 2,100.00

    KD-01 = Kolom Destilasi-01 1,000,000.00

    KD-02 = Kolom Destilasi-02 1,200,000.00

    KD-03 = Kolom Destilasi-03 1,500,000.00

    KOD-01 = Knock Out Drum-01 15,500.00

    P-01 = Pompa-01 25,000.00

    P-02 = Pompa-02 10,500.00

    P-03 = Pompa-03 10,500.00

    P-04 = Pompa-04 10,500.00

    P-05 = Pompa-05 10,500.00

    P-06 = Pompa-06 10,500.00

    P-07 = Pompa-07 10,500.00

    P-08 = Pompa-08 10,500.00

    P-09 = Pompa-09 10,500.00

    R-01 = Reaktor-01 666,800.00

    RB-01 = Reboiler-01 61,600.00

    RB-02 = Reboiler-02 90,100.00

    RB-03 = Reboiler-03 115,600.00

    T-01 = Tangki-01 520,000.00

    T-02 = Tangki-02 428,900.00

    T-03 = Tangki-03 424,900.00

    T-04 = Tangki-04 140,400.00

    T-05 = Tangki-05 140,400.00

    VP-01 = Vaporizer-01 18,000.00

    8,169,100.0000

    1 US $ = Rp. 13,250.0000

    2. MENENTUKAN BIAYA PERALATAN

    HARGA PERALATAN TAHUN 2014

    harga satuan

    US $

    ACC-01 = Accumulator-01 3,000.00 1 3,000.00

    ACC-02 = Accumulator-02 3,000.00 1 3,000.00

    ACC-03 = Accumulator-03 3,000.00 1 3,000.00

    CH-01 = Chiller-01 3,200.00 1 3,200.00

    C-01 = Cooler-01 2,100.00 1 2,100.00

    C-02 = Cooler-02 2,100.00 1 2,100.00

    C-03 = Cooler-03 2,100.00 1 2,100.00

    Jumlah Harga Total (US$)

    kode nama alat

    kode nama alat

  • C-04 = Cooler-04 2,100.00 1 2,100.00

    C-05 = Cooler-05 2,100.00 1 2,100.00

    CD-01 = Condenser-01 76,900.00 1 76,900.00

    CD-02 = Condenser-02 134,700.00 1 134,700.00

    CD-03 = Condenser-03 134,700.00 1 134,700.00

    EXP-01 = Expander-01 94,300.00 1 94,300.00

    F-01 = Furnace-01 686,700.00 1 686,700.00

    F-02 = Furnace-02 686,700.00 1 686,700.00

    H-01 = Heater-01 2,200.00 1 2,200.00

    KD-01 = Kolom Destilasi-01 1,000,000.00 1 1,000,000.00

    KD-02 = Kolom Destilasi-02 1,200,000.00 1 1,200,000.00

    KD-03 = Kolom Destilasi-03 1,500,000.00 1 1,500,000.00

    KOD-01 = Knock Out Drum-01 15,500.00 1 15,500.00

    P-01 = Pompa-01 25,000.00 1 25,000.00

    P-02 = Pompa-02 10,500.00 1 10,500.00

    P-03 = Pompa-03 10,500.00 1 10,500.00

    P-04 = Pompa-04 10,500.00 1 10,500.00

    P-05 = Pompa-05 10,500.00 1 10,500.00

    P-06 = Pompa-06 10,500.00 1 10,500.00

    R-01 = Reaktor-01 666,800.00 1 666,800.00

    RB-01 = Reboiler-01 61,600.00 1 61,600.00

    RB-02 = Reboiler-02 90,100.00 1 90,100.00

    RB-03 = Reboiler-03 115,600.00 1 115,600.00

    T-01 = Tangki-01 520,000.00 20 10,400,000.00

    T-02 = Tangki-02 428,900.00 3 1,286,700.00

    T-03 = Tangki-03 424,900.00 1 424,900.00

    T-04 = Tangki-04 140,400.00 5 702,000.00

    T-05 = Tangki-05 140,400.00 2 280,800.00

    VP-01 = Vaporizer-01 18,000.00 1 18,000.00

    Total Purchased Equipment Cost = 19,678,400.00

    3. PERHITUNGAN BIAYA

    perhitungan biaya meliputi :

    BIAYA PERALATAN = 19,678,400.0000

    BIAYA BAHAN BAKU

    Hydrogen

    Harga (US $/ kg) = 0.30

    Kebutuhan /tahun (kg) = 2856469.7228 396.7319

    Biaya / tahun (US$) = 856940.92

    Acetone

    Harga (US $/ kg) = 1.50

    Kebutuhan /tahun (kg) = 41418810.980 5,752.6126

    Biaya / tahun (US$) = 62128216.47

    Katalis nano Pd

    Harga (US $/ kg) = 2,000,000.00

    Kebutuhan /tahun (kg) = 0.250 0.2500

    Biaya / tahun (US$) = 500000.00

    Katalis nano ZnCr42O4

    Harga (US $/ kg) = 12,000.00

    Kebutuhan /tahun (kg) = 24.75 24.7500

    Biaya / tahun (US$) = 297000.00

  • TOTAL BIAYA BAHAN BAKU = 63,782,157.39

    BIAYA BAHAN BAKAR

    Kebutuhan FurnaceHarga (US $/ liter) = 0.4700

    Kebutuhan /tahun (liter) = 938,923.5869 130.4061 liter/jam

    Biaya / tahun (US$) = 441,294.0858

    Kebutuhan Generator dan BoilerHarga (US $/ liter) = 0.2700

    Kebutuhan /tahun (liter) = 5,112,809.5883 710.1124 liter/jam

    Biaya / tahun (US$) = 1,380,458.5888

    PERHITUNGAN HARGA TANAH

    Luas tanah (m2) = 50,000.000

    Harga tanah per m2 (Rp) = 2,500,000.000

    Biaya penyediaan tanah (Rp) = 125,000,000,000.000

    US$ = 9,433,962.2642

    PERHITUNGAN HARGA BANGUNAN

    Luas bangunan (m2) = 15,000.0000

    Harga bangunan per m2 (Rp) = 2,000,000.0000

    Biaya penyediaan bangunan (Rp) = 30,000,000,000.0000

    US$ = 2,264,150.9434

    4.4. PERHITUNGAN BIAYA OPERATING LABOR

    Gaji Karyawan (Operating Labor)

    No. jabatan jumlah gaji/bulan (Rp) Total gaji/bulan (Rp)

    1 Direktur Utama 1 50,000,000 50,000,000

    2 Sekretaris Direktur Utama 1 15,000,000 15,000,000

    3 Process Engineer 8 30,000,000 240,000,000

    4 Project Engineer 3 10,000,000 30,000,000

    5 Kepala Bagian 6 12,000,000 72,000,000

    6 Kepala Seksi 9 9,000,000 81,000,000

    7 Operator 65 3,000,000 195,000,000

    8 Paramedis 5 5,000,000 25,000,000

    9 Analis 3 4,000,000 12,000,000

    10 Satpam 32 2,500,000 80,000,000

    11 Pengemudi 7 2,500,000 17,500,000

    13 Karyawan 39 4,500,000 175,500,000

    14 IT 3 5,000,000 15,000,000

    total 182 1,008,000,000

    Jumlah gaji karyawan per bulan = 1,008,000,000.0000

    Jumlah gaji karyawan per tahun + Tunjangan hari raya = 13,104,000,000.0000

    Gaji karyawan per tahun (US $) = 988,981.1321

    91.0000

    4.5. PERHITUNGAN TOTAL CAPITAL INVESTMENT (TCI)

    TOTAL DIRECT COST (DC)

    Equipment, Installation dan Investment 50 - 60 FCI

    Purchased Equipment-Delivered (PEC) = 19,678,400.0000 15 - 40 FCI

    Installation, insulation and painting (25% PEC) = 4,919,600.0000 25 - 55 PEC

  • Instrumentation and Control (15% PEC) = 2,951,760.0000 6 - 30 PEC

    Piping and installed (40% PEC) = 7,871,360.0000 10 - 80 PEC fluida

    Electrical and installed (10% PEC) = 1,967,840.0000 10 - 15 PEC

    Building = 2,264,150.9434

    Service Facilities & yard improvement (20% PEC) = 3,935,680.0000 yard : 10 - 20 PEC | service fac. 30 - 80 PEC

    Land = 9,433,962.2642 1 - 2 FCI / 4 - 8 PEC

    TOTAL DIRECT COST (DC) = 53,022,753.2075

    INDIRECT COST (ID)

    Engineering and supervision (30 % PEC) = 5,903,520.0000 30 PEC 5 - 30 DC

    Contruction expense (10 % DC) = 5,302,275.3208 10 DC

    Contractors fee (4 % DC) = 2,120,910.1283 2 - 8 DC 1,5- 6 FCI

    Contigency (5 % FCI) = 3,492,076.7714 5 - 15 FCI

    TOTAL INDIRECT COST (IDC) = 16,818,782.2205

    FIXED CAPITAL INVESTMENT

    FCI = DC + IDC

    = 69,841,535.4280 69,841,535.4280

    WORKING CAPITAL

    WC = 15% TCI

    = 12,324,976.8402

    TOTAL CAPITAL INVESTMENT

    TCI = FCI + WC

    = 82,166,512.2682 82,166,512.2682

    4.6. PERHITUNGAN TOTAL PRODUCTION COST (TPC)

    MANUFACTURING COST, MC

    DIRECT PRODUCTION COST, DPC

    Raw material = 63,782,157.3874 10 - 50 TPC

    Operating Labor (OL) = 988,981.1321 15 TPC

    Direct supervisory and clerical labor, DSCL (15% OL) = 148,347.1698 15 OL

    Utilities (10% TPC) = 8,284,276.1276 10 - 20 TPC

    Maintenance & repair,MR (6% FCI) = 4,190,492.1257 6 FCI

    Labortory charge (10% OL) = 148,347.1698 10 - 20 OL

    Patent & royalties (1 % TPC) = 828,427.6128 0 - 6 TPC

  • TOTAL DPC 78,371,028.7252

    FIXED CHARGE, FC

    Depreciation (10% FCI) = 6,984,153.5428 10 FCI

    Local taxes (2% FCI) = 1,396,830.7086 2 - 4 FCI

    Insurance (1% FCI) = 698,415.3543 0,4 - 1 FCI

    Total FC 9,079,399.6056

    PLANT OVERHEAD COST, POC = 50 % (MR + OL + DSCL) 50 - 70 (OL+DSCL+MR)

    = 2,663,910.2138

    TOTAL MANUFACTURING COST, MC = 90,114,338.5446

    GENERAL EXPENSES (GE)

    Administrative cost (20% OL) = 197,796.2264 20 - 30 OL

    Distribution & selling price (3% TPC) = 2,485,282.8383 2 - 20 TPC

    Research & Development cost (1% TPC) = 828,427.6128 16,898,146.7422 5 TPC

    Financing (2% TCI) = 1,643,330.2454 0 - 10 TCI

    TOTAL GENERAL EXPENSES (GE) = 5,154,836.9228

    TOTAL PRODUCTION COST (TPC) = MC + GE

    = 95,269,175.4674 82,842,761.2760

    PERHITUNGAN ANNUAL CASH FLOW

    produk Utama

    Produksi MIBK / Tahun 20,000,000.0000 Kg

    Harga Jual (US$) 6.5 harga referensi molbase = US$ 76 / kg

    Penjualan pertahun 130,000,000.0000

    Total Penjualan / Tahun 130,000,000.0000

    TPC 95,269,175.4674

    NPBT 34,730,824.5326 Umur pabrik didapat dari Peter hal 2716,984,153.5428

    Income Tax (35%x NPBT) 12,155,788.5864 Umur pabrik = 10 tahun

    NPAT 22,575,035.9462

    Depresiasi (10% FCI) 6,984,153.5428 d = =

    Annual Cash Flow 29,559,189.4890 %

    %ACF 35.9747

    % d = 10.0000

    JANGKA WAKTU PENGEMBALIAN HUTANG

    Umur Pabrik 10.0000 tahun

    Lama Pengangsuran Hutang

    TCI 82,166,512.2682

    ACF 29,559,189.4890

    Bunga 0.2400

    Pinjaman (P) (75%TCI) 61,624,884.2012

    Lama Angsuran 4.0000 tahun

    A =

    lifeService

    TSV-FCI

    1i 1

    1n

    nii

    P

  • = 25,631,361.3233

    Tahun ke- Pinjaman Bunga Total Hutang Angsuran Sisa Hutang

    0 61,624,884.20 0.00 61,624,884.20 0.00 61,624,884.20

    1 61,624,884.20 14,789,972.21 76,414,856.41 25,631,361.32 50,783,495.09

    2 50,783,495.09 12,188,038.82 62,971,533.91 25,631,361.32 37,340,172.58

    3 37,340,172.58 8,961,641.42 46,301,814.00 25,631,361.32 20,670,452.68

    4 20,670,452.68 4,960,908.64 25,631,361.32 25,631,361.32 0.00

    40,900,561.09 272,944,449.84 102,525,445.29 170,419,004.55

    Pay Out Time

    4.9668

    3.7465 4.0000 tahun setengah dari service life

    KARENA POT KRG DARI 1/2 UMUR PABRIK MAKA PABRIK LAYAK DIDIRIKAN (kurang dari 5 tahun)

    Total Modal Akhir

    a. Net Profit Over Total life of Project (NPOTLP)

    NPOTLP = CCP + CR

    = 235,184,321.7259 CCP = n . ACF - TCI

    = 213,425,382.6215

    TCI + bunga = 123,067,073.3604 CR = WC + Vs + Land

    = 21,758,939.1044

    KARENA NPOTLP LEBIH BESAR DARI TCI + TOTAL BUNGA MAKA PABRIK LAYAK UNTUK DIDIRIKAN

    Total Capital Sink

    TCI = 82,166,512.2682

    TCS = n. ACF Angsuran

    = 193,066,449.5963

    KARENA TCS LEBIH BESAR DARI TCI SEHINGGA PABRIK LAYAK UNTUK DIDIRIKAN

    Laju Pengembalian Modal

    Rate of Return on Investment (ROR)

    = 27.4747 di bawah 100 %

    (harus lebih besar dari bunga bank)

    KARENA % ROR LEBIH BESAR DARI % BUNGA BANK MAKA PABRIK INI LAYAK UNTUK DIDIRIKAN

    Discounted Cash Flow Rate of Return

    ACF

    TCIBungaFCIPOT

    %100Pr

    xTCI

    TaxAfterofitNetROR

    nsn iVWC

    iiiACFTCI

    )1(

    1)(

    )1(

    1....

    )1(

    1

    )1(

    121

  • BUNGA BANK TRIAL TRIAL

    0.3483 2.7641 82,166,512.2952

    TCI 82,166,512.2682

    % = 0.3483

    BEP 34,579,427.89

    BEP =

    = 32.7300 % 20-40 %

    16,898,146.7422

    0.3761

    Fixed Cost = 16,898,146.7422 dollar 16.8981 Selling Price

    Variable Cost = 78,371,028.7252 dollar 78.3710 Kapasitas Harga

    Selling Price = 130,000,000.0000 130.0000 0.0000 0.0000

    TPC = 95,269,175.4674 95.2692 100.0000 130.0000

    BEP = 32.7300

    Fixed Cost

    Kapasitas Harga

    0.0000 16.8981

    100.0000 16.8981

    Total Production Cost

    Kapasitas Harga

    0.0000 16.8981

    100.0000 95.2692

    Variable cost

    Kapasitas Harga

    0.0000 0.0000

    100.0000 78.3710

    0.0000

    50.0000

    100.0000

    150.0000

    0 10 20 30 40 50 60 70 80 90 100 110

    HA

    RG

    A (

    JUTA

    US

    $)

    KAPASITAS PRODUKSI (%)

    SP

    FC

    TPC

    % 100Cost VariablePrice Selling

    Cost Fixed