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Facilities Engineering *1 st draft By: Saha. Development options ProposalDevelopment OptionEstimated Cost (Mil) A FPSO converted to Tanker Hull 300 kbo.

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Presentation on theme: "Facilities Engineering *1 st draft By: Saha. Development options ProposalDevelopment OptionEstimated Cost (Mil) A FPSO converted to Tanker Hull 300 kbo."— Presentation transcript:

1 Facilities Engineering *1 st draft By: Saha

2 Development options ProposalDevelopment OptionEstimated Cost (Mil) A FPSO converted to Tanker Hull 300 kbo 223.75 + ( 213.52 Lease rate) B FPSO with pipeline to Berlian Field 261.45 CFPSO with pipeline to PCOT282.45 DCPP with pipeline to Berlian240.95 ECPP with pipeline to PCOT261.95 F Wellhead Platform with pipeline to Berlian Field 220.75 GWellhead platform with pipeline to PCOT 241.75

3 Berlian East Satellite Platform 20 km 8” Crude Pipeline Berlian CPP PCOT 20 km 12” Crude Pipeline Development option: Proposal F

4 Facilities are required for : supporting production offtake gathering produced fluids processing and treatment evacuation or disposal storage and distribution

5 Surface facilities design is based on : fluid flowrates fluid pressure and temperature fluid properties product quality required

6 Production Design Rate Maximum Oil Rate 40 Mbpd Maximum Gas Rate 55 MMscfd Maximum Water Rate 55 Mbpd

7 Platform facilities modules

8 Process System: Process Flow Schematics

9 Oil And Gas Processing System

10 Separation System Scrubbers - 2 phase separation, to recover liquid carried over from production separator or due to condensation Liquid loading smaller. Application: upstream of mechanical equipment like compressors. Normally vertical Filter separators - designed to remove solid and liquid mists particles less than 10 micron

11 Vortex breaker – To stop funneling action, to prevent gas from escaping. Foaming - causes less efficient separation. To add anti foam agent. Critical velocity - cannot be exceeded, otherwise droplets of liquid in gas do not have the time to drop out. Residence time not enough - vapor bubble has no time to rise from the liquid-vapor interface

12 For large volume of production, normally two or more parallel trains of separation. Avoid full shutdown for repair or maintenance Test separators - periodic measurement for a single well, discharged back to common streams.

13 Gas Handling The gas which is naturally produced or separated from the oil may not be transported by pipeline for sales. Other applications of natural gas: 1.Injected back into the reservoir to help maintain pressure. 2.Assist wells to flow known as gas lift. 3.Fuel gas.

14 Utilities System Firewater Systems Instrument Air System Starting Air Systems Seawater & Potable Water System

15 Back up

16

17 This method is using the engineering formula to reconfirm the method 1. Given Q= 38.5 kbd and V= 6 ft/s. Using formula below: d = (0.012Q/V) 1/2 d = (0.012 x 38 500 / 6) 1/2 d = 8.77 inch Percentage error For 10 inch pipeline size Percentage error (%) = (10 – 8.77)/8.77 x 100 = 14.02 % For 8 inch pipeline size Percentage error (%) = (8.77 – 8)/8.77 x 100 = 8.77 %


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