sampling system design - nfogm · sampling system overview take off nozzle ... api mpms ch. 8.2...
TRANSCRIPT
SAMPLING SYSTEM DESIGN
By Steve Watson Gabriel
23rd March 2017
Determine the quality
Density
Water in oil
Composition
Vapour pressure
H2S content
Why Sampling
Sampling Automatic – Flow proportional
Provision for manual sampling
Online Density
Online Water in Oil (water cut)
Others - vapour pressureanalysers
Sampling System Overview
Take off Nozzle
Return Nozzle
Sampling Cabinet
Grab Sampler
Fastloop Pump
Sample Receiver
Densitometer
NPD regulations / NORSOK I-106
• Daily and monthly sampling
• Min. 10 000 samples per day/month/batch
• 1 mL grab min. 10 litres
ISO 3171 Automatic Pipeline Sampling
• Focus on homogenious mix of oil and water
API MPMS Ch. 8.2 Automatic Sampling of Liquid Petroleum
• Installation requirements
Sampling Standards
C1 /C2 ratio > 0.9 indicates good mixing
C1 water concentration at the top
C2 water concentration at the bottom
Mixing Requirements
Mixing Requirements
Turbulence can provide adequate mixing. The minimum turbulence for adequate mixing depends on flow rate, pipe diameter, viscosity, density and interfacial tension.
Samples taken from the pipeline should have the same composition as the average composition of the pipeline cross section
Representative sampling should persist throughout the period of transfer
Sample should maintained in the same condition as at the point ofextraction
That subdivision of the sample and correct analysis is required
Principles of Representative Sampling
Handbook of water fraction metering (2004)
• Simplified ISO 3171 calculations.
• Determine the critical velocity (Vc) required when the fluid properties and the pipe diameter are known.
• Horizontal Vs Vertical pipe
NFOGM Handbook
How we ensure mixing is maintained in fast loop
Keep the fast loop velocity at critical velocity or higher to create adequate turbulence.
Critical velocity can be
determined from the
expression
Worst-case
conditions expected
to be considered
• Lowest density,
• Lowest viscosity
• Highest interfacial
tension
Critical Velocity Vs Density
2,442,35
2,262,18
2,081,99
1,891,78
1,66
0
0,5
1
1,5
2
2,5
3
700 725 750 775 800 825 850 875 900
Cri
tica
l V
elo
city (
m/s
)
Density (Kg/m3)Parameters used for calculationTubing OD: 25mm, ID: 21mmViscosity: 5cPInterfacial tension b/w HC and Water: 0.025 N/m
Critical Velocity Vs Viscosity4,17
3,09
2,6
2,292,08
1,931,8 1,7 1,62 1,55
0
0,5
1
1,5
2
2,5
3
3,5
4
4,5
1 2 3 4 5 6 7 8 9 10
Cri
tica
l V
elo
city (
m/s
)
Viscosity (cP)Parameters used for calculationTubing OD: 25mm, ID: 21mmDensity: 800Kg/m3Interfacial tension b/w HC and Water: 0.025 N/m
- Take off point & sampling cabinet.
• Inlet piping, Probes, Valves, Other piping components
- Within the sampling cabinet.
• Inline Instrument, Bends, Valves, Tee
- Sampling cabinet & return point.
• Return Piping, Valves, Other piping components
Total pressure drop influence the sizing of the pump,eventually the cost.
Pressure Drop On Fast Loop System
Pressure Drop Fast Loop System
- NPSHa > NPSHr, Typical NPSHr is 2m
- Shortest length
- Min Bends, Elbows
Shortest length
Min Bends, Elbows
Pressure Drop within the sampling Cabinet
Pressure Drop Calculation
Inlet Piping: 1”, 5m long
Outlet Piping: 1”, 5m long
25mm tubing in the sampling
cabinet
Density: 840Kg/m3,
Viscosity: 4cP
Flow Rate: 2,65m3/h
PipeFlo Report
Inlet
Piping
Sampling
Cabinet
Outlet
Piping
Pressure
drop (bar)
0,3 3,7 0,15
Pressure Drop Calculation
Inlet Piping: 1”, 6m long
Outlet Piping: 1”, 5 m long
25mm tubing in the sampling
cabinet
Density: 840Kg/m3,
Viscosity: 4cP
Flow Rate: 2,65m3/h
PipeFlo Report
Inlet
Piping
Sampling
Cabinet
Outlet
Piping
Pressure
drop (bar)
0,15 3,7 0,15
Maintain critical velocity / flow in fast loop.
Provide enough head to ensure positive flow
Provide additional mixing
Role of Fast Loop Pumps Pump Curve
Convert to
Pressure
Head Curve
NPSHr Curve
- Size Envelope & Weight
- Material Selection
- Wax Temperature Vs ATEX compliance
Other Challenges
Questions / Comments