Re: Flow Assurance Training
Flow Assurance Training
(Technical and Industrial 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. Delivered entirely by capable facilitators with thorough, accurate and up-to-date knowledge of Flow assurance engineering.
Address: Suite 28, No 4 Irewole street,
Awosika B/S, Opebi Ikeja, Lagos State, Nigeria
Tel: 08133476558, 07085740887
Email:
[email protected],
[email protected]
website:
www.Vogwconcept.Com
At the end of the training the participants will be able to handle life projects.
• Each participant will receive a copy of :
1. ASME/ANSI B31.3, B31.4 and B31.8; APIRP 14E, API RP 14C, API RP 14J, NACE MR-01-75, API 520 Part 1 & 2, API 521, API 526, API 2000 and API 1104
2. A comprehensive manual for reference
3. Case study exercises using dummy and real life projects as applicable in the industries. Duration: Weekdays/weekends schedule (Call for time frame duration)
Venue: VOGW Concept, out station training is also available for client anywhere in the world
Cost: Confirm from the Management
Mode of Training: 99% practical
Prerequisite: Fundamental of engineering terms with ability to reason logically 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
- Shut Down
- Planned
- Unplanned
- Extended
- 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
WHO SHOULD ATTEND? • New engineers, design and construction engineers, team leaders/coordinators, operations engineers, construction coordinators, maintenance team leaders/engineers, operations team leaders, senior operations and maintenance personnel and other personnel who are or will be responsible for designing, selecting, sizing, specifying, installing, testing, operating and maintaining plant piping and oil and gas pipelines • Experienced professionals who want to review or broaden their understanding in process design
• Other professionals who want a better understanding of the subject
For more information:
Address: Suite 28, No 4 Irewole street,
Awosika B/S, Opebi Ikeja, Lagos State, Nigeria
Tel: 08133476558, 07085740887
Email:
[email protected],
[email protected]
website:
www.Vogwconcept.Com
Re: Flow Assurance Training
Flow Assurance Training
(Technical and Industrial 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. Delivered entirely by capable facilitators with thorough, accurate and up-to-date knowledge of Flow assurance engineering.
Address: Suite 28, No 4 Irewole street,
Awosika B/S, Opebi Ikeja, Lagos State, Nigeria
Tel: 08133476558, 07085740887
Email:
[email protected],
[email protected]
website:
www.Vogwconcept.Com
At the end of the training the participants will be able to handle life projects.
• Each participant will receive a copy of :
1. ASME/ANSI B31.3, B31.4 and B31.8; APIRP 14E, API RP 14C, API RP 14J, NACE MR-01-75, API 520 Part 1 & 2, API 521, API 526, API 2000 and API 1104
2. A comprehensive manual for reference
3. Case study exercises using dummy and real life projects as applicable in the industries. Duration: Weekdays/weekends schedule (Call for time frame duration)
Venue: VOGW Concept, out station training is also available for client anywhere in the world
Cost: Confirm from the Management
Mode of Training: 99% practical
Prerequisite: Fundamental of engineering terms with ability to reason logically 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
- Shut Down
- Planned
- Unplanned
- Extended
- 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
WHO SHOULD ATTEND? • New engineers, design and construction engineers, team leaders/coordinators, operations engineers, construction coordinators, maintenance team leaders/engineers, operations team leaders, senior operations and maintenance personnel and other personnel who are or will be responsible for designing, selecting, sizing, specifying, installing, testing, operating and maintaining plant piping and oil and gas pipelines • Experienced professionals who want to review or broaden their understanding in process design
• Other professionals who want a better understanding of the subject
For more information:
Address: Suite 28, No 4 Irewole street,
Awosika B/S, Opebi Ikeja, Lagos State, Nigeria
Tel: 08133476558, 07085740887
Email:
[email protected],
[email protected]
website:
www.Vogwconcept.Com
