materi-3 karakter refinery
DESCRIPTION
refinery engineeringTRANSCRIPT
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KARAKTERISTIK BISNIS PENGOLAHAN
2
Apa Yang dilakukan Refinery ??
Refinery
Crude Oil
Biaya Investasi
Produk Yang Lakudijual (usable)
EnergyFixedCosts
LossFuel Gas& Oil
Refinery (pengolahan) adalah proses pemisahan
bermacam-macam fraksi yang terdapat di dalam minyak bumi
dan mengkonversikannya menjadi poduk yang berguna
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Siklus Pemanfaatan Minyak Bumi
Refinery
Crude Oil Terminal
Transport
Retail
AviationExploration &
Production
Marine
Product Shippin
g
Product Tankag
e
Distribution Terminal
4
Physical Supply Chain
Value Creation:
• Crude Slade / Product Yield
• Technology & Catalyst selection
• Severity of Operation
• Blending Optimization
• Energy &Loss Efficiency
• Cost Efficiency
K i l a n g
Retail DistributionProduct Distribution
Processing
Crude Supply
Crude Source
Inbound Logistic Outbound Logistic
5
Rantai Nilai Minyak Bumi
Fig. 4.3
Cost-Added
Production, Storage & Transport Costs & The Time Costs of Money
Raw
MaterialStock
Production
FinishedProduct
In-Transit
RegionalStock Customer
OrderCycle
Value-Added
Time Place & Form Utility
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7
REFINERYMARGIN
REALISATION/BBL
CR-OIL COST/BBL
COST/BBL
VOLUME
YIELD/BBL
MARKET PRICE/BBL
PROC. COST/BBL
DESIGN CAPACITY
PAF
VOLUME LOSS UTILISATION
AVAILABILITYDAYS DOWN TIME
CALENDAR DAY
PRIMARY PROCESS
SECONDARY PROCESS
OPERATION
SUPPORTGA
UTILITIES
SECONDARY PROCESS
PRIMARY PROCESS
MARKET
VOLUME
CRUDE SLATE
UNIT SEVERITY
CRUDE SLATE
CRUDE ASSAY
VALUE DRIVER TREE BISNIS PENGOLAHAN (REFINERY)
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MISI BISNIS KILANG
(REFINERY)
PROFIT MAKS = REVENUE MAKS – COST OPT
COST OPT = BIAYA BAHAN BAKU + PROCESS.
COST
REVENUE MAKS = VOLUME MAKS x PRICE HIGH
-
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UPAYA-UPAYA MEMAKSIMALKAN REVENUE &
MEMINIMALKAN COST
2. COST OPT = BIAYA BAHAN BAKU + PROCESSING COST
Memilih Berbagai Alternatif Bahan Baku Yang Memiliki Harga Relatif Murah, Impurities Yang Tidak Terlalu Membebani Processing Cost, Serta Yield Sesuai Design Kilang.
1. REVENUE MAKS = VOLUME MAKS x PRICE HIGH
Mengoptimalkan Utilisasi Unit Proses (Kilang), Menekan Loss Produk Dan Mempertahankan Yield Produk (Konversi) Tetap Tinggi Sehingga Volume Produk Menjadi Maksimal
Merencanakan Produk Yang Bernilai Ekonomis Tinggi (Valuable Produk).
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Komponen Biaya Refinery
KILANG
Biaya Tetap
•Gaji
•Depresiasi
•Bunga
•PemeliharaanBiaya Bahan Baku
Bahan Baku
Bahan Pembantu•Katalis•Bahan Kimia
Produk Utama
Produk Samping
Nilai
Biaya Utilitas
•Bahan Bakar•Tenaga Listrik•Air•Udara•Nitrogen
•Crude•BBM•Non-BBM
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Demand Crude Oil - asumsi tingkat pertumbuhan Low Growth Case (mb/d)
Opec Report 2006
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Top 20 Oil Consumers, 2004
- 5,000 10,000 15,000 20,000 25,000
TaiwanThailand
NetherlandsIndonesia
IranSpain
Saudi ArabiaUnited Kingdom
BrazilItaly
MexicoFrance
CanadaSouth Korea
IndiaRussian
GermanyJapanChina
USATotal Asia Pacific*
thousand barrels per day
* Included for Comparison.
No. 17, 1.4% of World's Total
Source: BP Statistics.
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Top 20 Refiners, 2004
- 2,000 4,000 6,000 8,000 10,000 12,000 14,000 16,000 18,000
IndonesiaTaiwan
VenezuelaNetherlands
SingaporeSpain
MexicoIran
United KingdomBrazil
CanadaFrance
Saudi ArabiaItaly
GermanyIndia
South KoreaJapan
Russian FederationChina
USA
Thousand Barrels Daily
No. 21, 1.2% of World's Total
Source: BP Statistics.
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Hal-hal Yang Mendasari Kenaikan harga Minyak Bumi
Supply - Demand China and global demand factor Supply constraint and the (changing) role of OPEC Refining capacity factor
Non - Fundamental Speculation factor Fear factor
Others
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Supply & Trading
Supply &
Trading
Crude Purchases 5 mbpd
Crude Sales 4.5 mbpd
2.5 mbpd
Product Purchases 3 mbpd
3rd Party Product Sales 2.3 mbpd
Fuel & Loss: 0.2 mbpd
Refining2.5 mbpd
2.3 mbpd
Marketing Sales 3 mbpd
2 mbpd
Production
Supply &
Trading
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Skema Kegiatan Ekspor / Impor
Crude Oil & Produk Refinery
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Optimasi Refinery :
Dari sisi Internal :Operational AvailabilityHydrocarbon LossQuality Giveaway Innovation
Smarter Way of Doing ThingsCosts
Dari sisi eksternal :Selecting the Right CrudeProduct Optimization
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Optimisasi Refinery (dari sisi eksternal)
1. Crude Selection Crude that maximises usage of the refinery
asset
Acid crude, High pour crude, Condensates, Lube/non-lube
Crude approval process
2. Product Management Better pricing of products, New product grades
Increased integration / supply
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Price Differentials Against Dubai, Monthly Averages
-10.0
-5.0
0.0
5.0
10.0
15.0
20.0
25.0
30.0Ju
l-0
2
Se
p-0
2
No
v-0
2
Jan
-03
Ma
r-0
3
Ma
y-0
3
Jul-0
3
Se
p-0
3
No
v-0
3
Jan
-04
Ma
r-0
4
Ma
y-0
4
Jul-0
4
Se
p-0
4
No
v-0
4
Jan
-05
Ma
r-0
5
Ma
y-0
5
Jul-0
5
Se
p-0
5
No
v-0
5
Jan
-06
Ma
r-0
6
Month
US
$/b
bl
Kero/JetGasoilGasolineNaphtha
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Gross Refining Margins* : A Historical Perspective
(2)
2
6
10
81 82 83 84 85 86 87 88 89 90 91 92 93 94 95 96 97 98 99 00 01 02 03 04 05
$/b
Cracking
Hydroskimming
* Dubai Crude (Singapore CIF); Product prices based on Singapore FOB spot prices.
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-2.0
-1.0
0.0
1.0
2.0
3.0
4.0
5.0
6.0
7.0
8.0
1995 1997 1999 2001 2003 2005 2007 2009 2011 2013 2015 2017 2019
Hydroskimming Cracking
* Actual up to 2005 (nominal prices), 2005$ thereafter; Cracking yield is based on RCC.
Past and Projected Gross Refining Margins for Dubai, Singapore Market (US$/b)*
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UP 2001 2002 2003 2004 2005 2006
UP -I 2.19 2.24 2.43 3.79 6.32 3.01
UP - II 2.51 1.50 2.99 6.62 6.07 3.12
UP - III 1.53 1.69 2.13 6.18 4.95 0.56
UP - IV 1.10 2.15 2.78 6.09 5.00 1.71
UP - V 0.68 1.40 2.37 5.44 5.68 0.53
UP - VI 3.98 4.04 5.50 13.48 18.14 13.02
UP - VII 1.04 (0.02) 0.90 3.32 2.60 3.00
Total Gross Margin 1.60 2.00 2.90 6.85 6.97 3.81
( US $/BBL Crude )
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PRODUK & DEMAND BBM
Produksi BBM
Premium : 200.6 MBCD = 11.64 Jt KL
Kerosine : 166.5 MBCD = 9.66 Jt KL
Solar (ADO) : 266.2 MBCD = 15.45 Jt KL
Disel (IDO) : 9.3 MBCD = 0.54 Jt KL
Minyak Bakar (IFO) : 68.0 MBCD = 3.95 Jt KL
T O T A L : 710.6 MBCD = 41.24 Jt KL.
BBM Subsidi
Premium : 17.08 Jt KL
Kerosine : 10.00 Jt KL
Solar : 14.50 Jt KL
TOTAL : 41.58 Jt KL
Import BBM
19.64 Juta KL
BBM Non Subsidi
(Industri)
Premium : 0.037 Jt KL
Kerosine : 0.090 Jt KL
Solar : 13.919 Jt KL
Disel : 0.535 Jt KL
M. Bakar : 4.715 Jt KL
TOTAL : 19.30 Jt KL
DEMANDPRODUK DARI KILANG
Satuan : Jt KL
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Refinery Pictures – Process Units
Crude Distillation
Vacuum Distillation
Catalytic Cracking
Hydrocracking
Catalytic Reforming