Page 34 - 2020 Annual Report
P. 34
Kilas Kinerja Laporan Profil Analisis dan Pembahasan Tinjauan Pendukung
Performance Manajemen Perusahaan Manajemen Bisnis
Higlights management Report Company Profile Management Discussion and Business Support
Analysis
inVeSTaSi caPeX uSd6,51 miLiar
CApEx INvEsTMENT Of Usd6.51 bILLION
TahaP 1 TahaP 2
PHASE 1 PHASE 2
aSeT miLiK PerTamina aSeT miLiK KPB Pembangunan New Unit Kilang Tahap II
Pertamina’s Assets KPB’s Assets RDMP Balikpapan:
• Residue Desulphurization (RDS)
Pembangunan Early Works, EPC Lawe- Pembangunan New Unit Tahap I RDMP • Hydrogen Manufacturing Unit
Lawe, dan revamping kilang eksisting: Balikpapan: (HMU) Tahap II
• Pembangunan Early Works • Residual Fluid Catalytic Cracking • Sulphur Recovery Unit (SRU) Tahap II
atau fasilitas pendukung untuk (RFCC) Phase II of RDMP Balikpapan New Unit
kebutuhan pengembangan kilang • Gasoline Hydrotreater (GSH) Construction:
RDMP RU V • Diesel Hydrotreater (DHT) • Residue Desulphurization (RDS)
• Pembangunan Tangki Timbun, • Naphtha Hydrotreater (NHT) • Hydrogen Manufacturing Unit
SPM, Pipeline dan fasilitas • Alkylation & Wet Gas Sulfuric Acid (HMU) Phase II
pendukungnya di Terminal Lawe- • Sulphur Recovery Unit (SRU) Tahap I • Sulphur Recovery Unit (SRU) Phase
Lawe • Hydrogen Manufacturing Unit II
• Revamping unit eksisting Kilang (HMU) Tahap I
RU V Balikpapan antara lain: • Sistem Utilitas
Crude Distillation Unit IV (CDU IV), Phase I of RDMP Balikpapan New Unit
Vacuum Distillation Unit II (VDU II), Construction:
LPG Recovery Unit, Hydro Cracking • Residual Fluid Catalytic Cracking
Unit (HCU), dan jetty. (RFCC)
Early Works and EPC Lawe-Lawe • Gasoline Hydrotreater (GSH)
construction and revamping the • Diesel Hydrotreater (DHT)
existing refinery: • Naphtha Hydrotreater (NHT)
• Early Works construction or the • Alkylation & Wet Gas Sulfuric Acid
supporting facilities to develop the • Sulphur Recovery Unit (SRU) Phase I
RDMP RU V refinery • Hydrogen Manufacturing Unit
• Constructing the Storage Tank, SPM, (HMU) Phase I
Pipeline and supporting facilities • Utility System
in Lawe-Lawe Terminal
• Revamping the existing unit of RU
V Balikpapan Refinery including:
Crude Distillation Unit IV (CDU IV),
Vacuum Distillation Unit II (VDU II),
LPG Recovery Unit, Hydro Cracking
Unit (HCU), and jetty
TahaPan inVeSTaSi KiLang PerTamina inVeSTmenT PhaSe for KiLang
BaLiKPaPan PerTamina BaLiKPaPan
1. Pertimbangan Penggunaan Dana Eksternal Sebagai 1. Consideration of Using External Funds as a Source of
Salah Satu Sumber Pendanaan Financing
Nilai capex investasi RDMP RU V Balikpapan, sesuai According to the Final Investment Decision, the
Final Investment Decision, membutuhkan dana development of RDMP RU V Balikpapan requires
sebesar USD6,51 miliar yang akan diimplementasikan USD6.51 billion. The investment will be made in two
dalam dua tahap pembangunan kilang. Pendanaan phases of refinery construction. It has already been
eksternal dipertimbangkan sebagai salah satu sumber considered to use funding from an external source
pendanaan mengingat kebutuhan investasi yang given the significant amount of investment and
besar dan keterbatasan pendanaan internal. limited internal resources.
Laporan Tahunan 2020 | Annual Report 2020 34 PT Kilang Pertamina Balikpapan