Flow Assurance Analysis Training
Flow Assurance AnalysisTraining (Technical Method)
The scope of the training cover detail flow assurance stability in pipelines. This popular course provides participants with a multidisciplinary understanding of flow assurance For more info contact: Tel: 08133476558, 07085740887
Address: Opebi, Ikeja, Lagos State, Nigeria
Email: vogwconcept50 (at) gmail.com
Port Harcourt contact: 08032766980
[IMG]file:///C:\Users\HIZ\AppData\Local\Temp\msohtmlclip1\01\cl ip_image002.png[/IMG]
COURSE OUTLINE
MODULE 1
1.0. Fluid Properties and Phase behaviour modeling
1.1. Component of production system
1.2. Flow assurance concerns that need to be examined:
- Pipeline rupture from corrosion
- Pipeline blockage from hydrates or wax
- Severe slugging can damage separator
- Large pressure drop in pipelines can cause lower flow than should be
MODULE 2
2.1. Flow assurance strategies that need to be adopted:
- Hydraulic Analysis – acceptable pressure drops, pipeline size, erosion & corrosion limits
- Thermal Analysis – temperature distribution, heat loss
- Inhibition Analysis – hydrate inhibitors, wax inhibitors, corrosion inhibitors, scale inhibitors
2.2. Flow assurance strategies Terms
· Beggs and Brill method
· Volume fraction, holdup and water cut
· Superficial velocity
· Mixture velocity and density
· Mass conservation
· Momentum conservation
· Energy conservation
· Mass transfer between phases
· Subsonic vs. transonic, supersonic and hypersonic flows
MODULE 3
3.1. Steady State Design:
- Hydraulics
- Line Sizing
- Pressure Drop
- Max./Min. Velocity
- Flow Regime Prediction
- Slugging (Hydrodynamic and Severe Slugging)
- Pots equation for Severe Slugging (or Terrain Slugging)
- Mean Slug Length and Probabilistic Model for
- Slug Length (Hill & Wood Method)
- Maximum Slug Length = 6 times the mean slug length
- Slug Frequency (Hill & Wood Method)
3.2· Pigging slugs
o A quasi-transient model of Baker – McDonald
- Thermal
- Insulation Requirements:
- Hydrate Formation
- Wax Deposition
- Insulation Types
- Pipe-in-Pipe
- Wet Insulation
- Flexible Pipe
MODULE 4
4.1 Transient Design:
- Shut Down
- Depressurisation
- Blow Down
- Turn Down – Ramp up (For Gas Condensate Systems)
- Start-up
- Cold Start-up
- Warm Start-up
- Interrupted Start-up
- Pigging
- Presentation of Result and Project reporting
- Project work/ Case study
For more info contact: Tel: 08133476558, 07085740887
Address: Opebi, Ikeja, Lagos State, Nigeria
Email: vogwconcept50 (at) gmail.com
Port Harcourt contact: 08032766980
Re: Flow Assurance Analysis Training
Flow Assurance AnalysisTraining (Technical Method)
The scope of the training cover detail flow assurance stability in pipelines. This popular course provides participants with a multidisciplinary understanding of flow assurance For more info contact: Tel: 08133476558, 07085740887
Address: Opebi, Ikeja, Lagos State, Nigeria
Email: vogwconcept50 (at) gmail.com
Port Harcourt contact: 08032766980
[IMG]file:///C:\Users\HIZ\AppData\Local\Temp\msohtmlclip1\01\cl ip_image002.png[/IMG]
COURSE OUTLINE
MODULE 1
1.0. Fluid Properties and Phase behaviour modeling
1.1. Component of production system
1.2. Flow assurance concerns that need to be examined:
- Pipeline rupture from corrosion
- Pipeline blockage from hydrates or wax
- Severe slugging can damage separator
- Large pressure drop in pipelines can cause lower flow than should be
MODULE 2
2.1. Flow assurance strategies that need to be adopted:
- Hydraulic Analysis – acceptable pressure drops, pipeline size, erosion & corrosion limits
- Thermal Analysis – temperature distribution, heat loss
- Inhibition Analysis – hydrate inhibitors, wax inhibitors, corrosion inhibitors, scale inhibitors
2.2. Flow assurance strategies Terms
· Beggs and Brill method
· Volume fraction, holdup and water cut
· Superficial velocity
· Mixture velocity and density
· Mass conservation
· Momentum conservation
· Energy conservation
· Mass transfer between phases
· Subsonic vs. transonic, supersonic and hypersonic flows
MODULE 3
3.1. Steady State Design:
- Hydraulics
- Line Sizing
- Pressure Drop
- Max./Min. Velocity
- Flow Regime Prediction
- Slugging (Hydrodynamic and Severe Slugging)
- Pots equation for Severe Slugging (or Terrain Slugging)
- Mean Slug Length and Probabilistic Model for
- Slug Length (Hill & Wood Method)
- Maximum Slug Length = 6 times the mean slug length
- Slug Frequency (Hill & Wood Method)
3.2· Pigging slugs
o A quasi-transient model of Baker – McDonald
- Thermal
- Insulation Requirements:
- Hydrate Formation
- Wax Deposition
- Insulation Types
- Pipe-in-Pipe
- Wet Insulation
- Flexible Pipe
MODULE 4
4.1 Transient Design:
- Shut Down
- Depressurisation
- Blow Down
- Turn Down – Ramp up (For Gas Condensate Systems)
- Start-up
- Cold Start-up
- Warm Start-up
- Interrupted Start-up
- Pigging
- Presentation of Result and Project reporting
- Project work/ Case study
For more info contact: Tel: 08133476558, 07085740887
Address: Opebi, Ikeja, Lagos State, Nigeria
Email: vogwconcept50 (at) gmail.com
Port Harcourt contact: 08032766980
Re: Flow Assurance Analysis Training
Flow Assurance AnalysisTraining (Technical Method)
The scope of the training cover detail flow assurance stability in pipelines. This popular course provides participants with a multidisciplinary understanding of flow assurance For more info contact: Tel: 08133476558, 07085740887
Address: Opebi, Ikeja, Lagos State, Nigeria
Email: vogwconcept50 (at) gmail.com
Port Harcourt contact: 08032766980
[IMG]file:///C:\Users\HIZ\AppData\Local\Temp\msohtmlclip1\01\cl ip_image002.png[/IMG]
COURSE OUTLINE
MODULE 1
1.0. Fluid Properties and Phase behaviour modeling
1.1. Component of production system
1.2. Flow assurance concerns that need to be examined:
- Pipeline rupture from corrosion
- Pipeline blockage from hydrates or wax
- Severe slugging can damage separator
- Large pressure drop in pipelines can cause lower flow than should be
MODULE 2
2.1. Flow assurance strategies that need to be adopted:
- Hydraulic Analysis – acceptable pressure drops, pipeline size, erosion & corrosion limits
- Thermal Analysis – temperature distribution, heat loss
- Inhibition Analysis – hydrate inhibitors, wax inhibitors, corrosion inhibitors, scale inhibitors
2.2. Flow assurance strategies Terms
· Beggs and Brill method
· Volume fraction, holdup and water cut
· Superficial velocity
· Mixture velocity and density
· Mass conservation
· Momentum conservation
· Energy conservation
· Mass transfer between phases
· Subsonic vs. transonic, supersonic and hypersonic flows
MODULE 3
3.1. Steady State Design:
- Hydraulics
- Line Sizing
- Pressure Drop
- Max./Min. Velocity
- Flow Regime Prediction
- Slugging (Hydrodynamic and Severe Slugging)
- Pots equation for Severe Slugging (or Terrain Slugging)
- Mean Slug Length and Probabilistic Model for
- Slug Length (Hill & Wood Method)
- Maximum Slug Length = 6 times the mean slug length
- Slug Frequency (Hill & Wood Method)
3.2· Pigging slugs
o A quasi-transient model of Baker – McDonald
- Thermal
- Insulation Requirements:
- Hydrate Formation
- Wax Deposition
- Insulation Types
- Pipe-in-Pipe
- Wet Insulation
- Flexible Pipe
MODULE 4
4.1 Transient Design:
- Shut Down
- Depressurisation
- Blow Down
- Turn Down – Ramp up (For Gas Condensate Systems)
- Start-up
- Cold Start-up
- Warm Start-up
- Interrupted Start-up
- Pigging
- Presentation of Result and Project reporting
- Project work/ Case study
For more info contact: Tel: 08133476558, 07085740887
Address: Opebi, Ikeja, Lagos State, Nigeria
Email: vogwconcept50 (at) gmail.com
Port Harcourt contact: 08032766980
