Process Design Training (Technical and Industrial Method)
Process Design Training
(Technical and Industrial Method)
This training will provide participants rich multidisciplinary understanding of the design and materials selection in process design.
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
Delivered entirely by capable facilitators withthorough, accurate and up-to-date knowledge of process engineering.
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
THE COURSE CONTENTS:
MODULE 1
1.1 Process Engineering deliverable
1.1.1. Conceptual Design:
1.1.2. FEED
1.1.3 Basic/Detailed Design
1.1.4. Commissioning & Startup
1.2 Component of production system
1.2.1 Overview of Upstream and Downstream
1.2.2. Major products in upstream and downstream sector1.2.3. Diagrams of the various oil and gas production systems
1.3. Types of process diagrams
-Introduction to DIN and ISA basic instrument Symbols
-PFD and P & ID diagram
-Flow Diagram
-Electrical drawing
- Elevation drawing
-Equipment location drawing
-Foundational drawing
-Legends diagram
- Plot plan and equipment arrangements
- Isometric drawing
1.4. Scope of process engineering inputs and outputs
P and IDs Design Process - Preparation of Block Diagram
- Preparation of Process Flow Diagrams (PFDs)
- Preparation of Piping and Instrument Diagrams (P & IDs)
- Utility flow diagram (UFD)
- Preparation of Mass, Heat and Energy Balance
- Pipe Isometric drawing
- EMCS block diagrams (Electronic Measuring Control System)
-Estimating production cost and profitability
1.5. Component of pipe connection
- Methods of pipe connections (Body materials, end connection, operation, pressure class, size, specification)
- Fittings (valve, flanges, pipe and tube, elbow, Tee, Gasket, Fastener, industrial bolt ), Some different, Pipeline, pipe, Conduit, Tubing, Ducting, class, Schedule, NPS, NB & OD of a pipe, National Pipe Thread Taper NPT, code, standard, specification.
- ANSI B16.6 and API 6A pressure rating
Project work
MODULE 2
2.1. Fluid flow design
- Fluid flow types and characteristics
- Flow conditions
- Laminar vs. Turbulent
- Velocity limitation
- Temperature and pressure consideration
- Reynolds’s number (When and how to use it)
- Liquid and Gas viscosity (When and how to use it)
- Relative roughness (When and how to use it)
- Frictional factor - equation and charts (When and how to use it)
- Z – factor correlation (When and how to use it)
- Operating , design and environmental condition and consideration
- Class, Schedule, Code and standard
2.2 Application of Basic equation in process design
- Bernoulli’s equation (When and how to use it)
- Darcy’s s equation (When and how to use it)
- General and empirical Hazen – Williams equation for liquids (When and how to use it)
- Isothermal, General, Weymouth and Panhandle equation General and empirical equation (When and how to use it)
- Approximate equations for small pressure drops (When and how to use it)
- Spitzglass equation for very low pressure line (When and how to use it)
- Fritzsch’s and Babcock equation for steam flow (When and how to use it)
- AGA, API RP 14 E and other empirical equations for 2- phase flow (When and how to use it)
- Effects of elevation on pipeline pressure drop (When and how to use it )
2.3 Head Loss in valves and fitting in process line
- Head loss in valves and fitting
- Resistance and flow coefficients
- Equivalent length determination
Project work
MODULE 3
3.1 Line sizing determination
- Flow rate and surge factor consideration
- Pressure drop consideration
- Erosion velocity
- Single phase Liquid and Gas line sizing
- 2- phase line sizing
- Multiphase line sizing
3.2 Sizing and specification of process equipment and selection
Pressure vessel equipment
Distillation column
Pumps (Vacuum pump, Dynamic pump)
Pipe sizing and pipe sizing for heating system
Separators
Knock out drum
Compressors
Valves
Flanges
Gaskets
Chiller/heater
Boilers
Ducts
Heat exchanger
Stripper
Absorber
Reflux drum
Turbines
Fan
Reactors
Filters
e.t.c
3.3 Control valve sizing – Gas line, Liquid line, oil line
Project work
MODULE 4
4.1. Process control design:
Control parameter - Feed forward, feed back, cascade, ratio, Adaptive, inferential
- Mathematical model, PID Tuning and the design of controllers, Mode of operation of various controller types Characteristic parameters
- The proportional controller
- The integral-action controller
- The PI controller
- The PD controller
- The PID controller
- PI flow diagram
- EMCS block diagrams interpretation of point (Electronic Measuring Control System)
- Process protection measures
4.2. Introduction to:
4.2.1 HAZID and HAZOP study
4.2.2. Preparation of Datasheet for:
-Equipment
-Process instrument
-Corrosion coupon and corrosion probe
4.3.3. Basic process design philosophy
5.0. Presentation of Result and Project reporting
Project work
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: Process Design Training (Technical and Industrial Method)
Process Design Training
(Technical and Industrial Method)
This training will provide participants rich multidisciplinary understanding of the design and materials selection in process design.
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
Delivered entirely by capable facilitators withthorough, accurate and up-to-date knowledge of process engineering.
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
THE COURSE CONTENTS:
MODULE 1
1.1 Process Engineering deliverable
1.1.1. Conceptual Design:
1.1.2. FEED
1.1.3 Basic/Detailed Design
1.1.4. Commissioning & Startup
1.2 Component of production system
1.2.1 Overview of Upstream and Downstream
1.2.2. Major products in upstream and downstream sector1.2.3. Diagrams of the various oil and gas production systems
1.3. Types of process diagrams
-Introduction to DIN and ISA basic instrument Symbols
-PFD and P & ID diagram
-Flow Diagram
-Electrical drawing
- Elevation drawing
-Equipment location drawing
-Foundational drawing
-Legends diagram
- Plot plan and equipment arrangements
- Isometric drawing
1.4. Scope of process engineering inputs and outputs
P and IDs Design Process - Preparation of Block Diagram
- Preparation of Process Flow Diagrams (PFDs)
- Preparation of Piping and Instrument Diagrams (P & IDs)
- Utility flow diagram (UFD)
- Preparation of Mass, Heat and Energy Balance
- Pipe Isometric drawing
- EMCS block diagrams (Electronic Measuring Control System)
-Estimating production cost and profitability
1.5. Component of pipe connection
- Methods of pipe connections (Body materials, end connection, operation, pressure class, size, specification)
- Fittings (valve, flanges, pipe and tube, elbow, Tee, Gasket, Fastener, industrial bolt ), Some different, Pipeline, pipe, Conduit, Tubing, Ducting, class, Schedule, NPS, NB & OD of a pipe, National Pipe Thread Taper NPT, code, standard, specification.
- ANSI B16.6 and API 6A pressure rating
Project work
MODULE 2
2.1. Fluid flow design
- Fluid flow types and characteristics
- Flow conditions
- Laminar vs. Turbulent
- Velocity limitation
- Temperature and pressure consideration
- Reynolds’s number (When and how to use it)
- Liquid and Gas viscosity (When and how to use it)
- Relative roughness (When and how to use it)
- Frictional factor - equation and charts (When and how to use it)
- Z – factor correlation (When and how to use it)
- Operating , design and environmental condition and consideration
- Class, Schedule, Code and standard
2.2 Application of Basic equation in process design
- Bernoulli’s equation (When and how to use it)
- Darcy’s s equation (When and how to use it)
- General and empirical Hazen – Williams equation for liquids (When and how to use it)
- Isothermal, General, Weymouth and Panhandle equation General and empirical equation (When and how to use it)
- Approximate equations for small pressure drops (When and how to use it)
- Spitzglass equation for very low pressure line (When and how to use it)
- Fritzsch’s and Babcock equation for steam flow (When and how to use it)
- AGA, API RP 14 E and other empirical equations for 2- phase flow (When and how to use it)
- Effects of elevation on pipeline pressure drop (When and how to use it )
2.3 Head Loss in valves and fitting in process line
- Head loss in valves and fitting
- Resistance and flow coefficients
- Equivalent length determination
Project work
MODULE 3
3.1 Line sizing determination
- Flow rate and surge factor consideration
- Pressure drop consideration
- Erosion velocity
- Single phase Liquid and Gas line sizing
- 2- phase line sizing
- Multiphase line sizing
3.2 Sizing and specification of process equipment and selection
Pressure vessel equipment
Distillation column
Pumps (Vacuum pump, Dynamic pump)
Pipe sizing and pipe sizing for heating system
Separators
Knock out drum
Compressors
Valves
Flanges
Gaskets
Chiller/heater
Boilers
Ducts
Heat exchanger
Stripper
Absorber
Reflux drum
Turbines
Fan
Reactors
Filters
e.t.c
3.3 Control valve sizing – Gas line, Liquid line, oil line
Project work
MODULE 4
4.1. Process control design:
Control parameter - Feed forward, feed back, cascade, ratio, Adaptive, inferential
- Mathematical model, PID Tuning and the design of controllers, Mode of operation of various controller types Characteristic parameters
- The proportional controller
- The integral-action controller
- The PI controller
- The PD controller
- The PID controller
- PI flow diagram
- EMCS block diagrams interpretation of point (Electronic Measuring Control System)
- Process protection measures
4.2. Introduction to:
4.2.1 HAZID and HAZOP study
4.2.2. Preparation of Datasheet for:
-Equipment
-Process instrument
-Corrosion coupon and corrosion probe
4.3.3. Basic process design philosophy
5.0. Presentation of Result and Project reporting
Project work
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: Process Design Training (Technical and Industrial Method)
Process Design Training
(Technical and Industrial Method)
This training will provide participants rich multidisciplinary understanding of the design and materials selection in process design. 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
Delivered entirely by capable facilitators withthorough, accurate and up-to-date knowledge of process engineering.
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 THE COURSE CONTENTS: MODULE 1
1.1 Process Engineering deliverable
1.1.1. Conceptual Design:
1.1.2. FEED
1.1.3 Basic/Detailed Design
1.1.4. Commissioning & Startup
1.2 Component of production system
1.2.1 Overview of Upstream and Downstream
1.2.2. Major products in upstream and downstream sector1.2.3. Diagrams of the various oil and gas production systems
1.3. Types of process diagrams -Introduction to DIN and ISA basic instrument Symbols
-PFD and P & ID diagram
-Flow Diagram
-Electrical drawing
- Elevation drawing
-Equipment location drawing
-Foundational drawing
-Legends diagram
- Plot plan and equipment arrangements
- Isometric drawing 1.4. Scope of process engineering inputs and outputs
P and IDs Design Process - Preparation of Block Diagram
- Preparation of Process Flow Diagrams (PFDs)
- Preparation of Piping and Instrument Diagrams (P & IDs)
- Utility flow diagram (UFD)
- Preparation of Mass, Heat and Energy Balance
- Pipe Isometric drawing
- EMCS block diagrams (Electronic Measuring Control System)
-Estimating production cost and profitability 1.5. Component of pipe connection - Methods of pipe connections (Body materials, end connection, operation, pressure class, size, specification)
- Fittings (valve, flanges, pipe and tube, elbow, Tee, Gasket, Fastener, industrial bolt ), Some different, Pipeline, pipe, Conduit, Tubing, Ducting, class, Schedule, NPS, NB & OD of a pipe, National Pipe Thread Taper NPT, code, standard, specification.
- ANSI B16.6 and API 6A pressure rating
Project work
MODULE 2
2.1. Fluid flow design
- Fluid flow types and characteristics
- Flow conditions
- Laminar vs. Turbulent
- Velocity limitation
- Temperature and pressure consideration
- Reynolds’s number (When and how to use it)
- Liquid and Gas viscosity (When and how to use it)
- Relative roughness (When and how to use it)
- Frictional factor - equation and charts (When and how to use it)
- Z – factor correlation (When and how to use it)
- Operating , design and environmental condition and consideration
- Class, Schedule, Code and standard
2.2 Application of Basic equation in process design - Bernoulli’s equation (When and how to use it)
- Darcy’s s equation (When and how to use it)
- General and empirical Hazen – Williams equation for liquids (When and how to use it)
- Isothermal, General, Weymouth and Panhandle equation General and empirical equation (When and how to use it)
- Approximate equations for small pressure drops (When and how to use it)
- Spitzglass equation for very low pressure line (When and how to use it)
- Fritzsch’s and Babcock equation for steam flow (When and how to use it)
- AGA, API RP 14 E and other empirical equations for 2- phase flow (When and how to use it)
- Effects of elevation on pipeline pressure drop (When and how to use it )
2.3 Head Loss in valves and fitting in process line - Head loss in valves and fitting
- Resistance and flow coefficients
- Equivalent length determination
Project work
MODULE 3
3.1 Line sizing determination - Flow rate and surge factor consideration
- Pressure drop consideration
- Erosion velocity
- Single phase Liquid and Gas line sizing
- 2- phase line sizing
- Multiphase line sizing
3.2 Sizing and specification of process equipment and selection
Pressure vessel equipment
Distillation column
Pumps (Vacuum pump, Dynamic pump)
Pipe sizing and pipe sizing for heating system
Separators
Knock out drum
Compressors
Valves
Flanges
Gaskets
Chiller/heater
Boilers
Ducts
Heat exchanger
Stripper
Absorber
Reflux drum
Turbines
Fan
Reactors
Filters
e.t.c 3.3 Control valve sizing – Gas line, Liquid line, oil line Project work
MODULE 4
4.1. Process control design:
Control parameter - Feed forward, feed back, cascade, ratio, Adaptive, inferential - Mathematical model, PID Tuning and the design of controllers, Mode of operation of various controller types Characteristic parameters
- The proportional controller
- The integral-action controller
- The PI controller
- The PD controller
- The PID controller
- PI flow diagram
- EMCS block diagrams interpretation of point (Electronic Measuring Control System)
- Process protection measures
4.2. Introduction to:
4.2.1 HAZID and HAZOP study 4.2.2. Preparation of Datasheet for:
-Equipment
-Process instrument
-Corrosion coupon and corrosion probe 4.3.3. Basic process design philosophy 5.0. Presentation of Result and Project reporting Project work
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: Process Design Training (Technical and Industrial Method)
Process Design Training
(Technical and Industrial Method)
This training will provide participants rich multidisciplinary understanding of the design and materials selection in process design. 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
Delivered entirely by capable facilitators withthorough, accurate and up-to-date knowledge of process engineering.
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 THE COURSE CONTENTS: MODULE 1
1.1 Process Engineering deliverable
1.1.1. Conceptual Design:
1.1.2. FEED
1.1.3 Basic/Detailed Design
1.1.4. Commissioning & Startup
1.2 Component of production system
1.2.1 Overview of Upstream and Downstream
1.2.2. Major products in upstream and downstream sector1.2.3. Diagrams of the various oil and gas production systems
1.3. Types of process diagrams -Introduction to DIN and ISA basic instrument Symbols
-PFD and P & ID diagram
-Flow Diagram
-Electrical drawing
- Elevation drawing
-Equipment location drawing
-Foundational drawing
-Legends diagram
- Plot plan and equipment arrangements
- Isometric drawing 1.4. Scope of process engineering inputs and outputs
P and IDs Design Process - Preparation of Block Diagram
- Preparation of Process Flow Diagrams (PFDs)
- Preparation of Piping and Instrument Diagrams (P & IDs)
- Utility flow diagram (UFD)
- Preparation of Mass, Heat and Energy Balance
- Pipe Isometric drawing
- EMCS block diagrams (Electronic Measuring Control System)
-Estimating production cost and profitability 1.5. Component of pipe connection - Methods of pipe connections (Body materials, end connection, operation, pressure class, size, specification)
- Fittings (valve, flanges, pipe and tube, elbow, Tee, Gasket, Fastener, industrial bolt ), Some different, Pipeline, pipe, Conduit, Tubing, Ducting, class, Schedule, NPS, NB & OD of a pipe, National Pipe Thread Taper NPT, code, standard, specification.
- ANSI B16.6 and API 6A pressure rating
Project work
MODULE 2
2.1. Fluid flow design
- Fluid flow types and characteristics
- Flow conditions
- Laminar vs. Turbulent
- Velocity limitation
- Temperature and pressure consideration
- Reynolds’s number (When and how to use it)
- Liquid and Gas viscosity (When and how to use it)
- Relative roughness (When and how to use it)
- Frictional factor - equation and charts (When and how to use it)
- Z – factor correlation (When and how to use it)
- Operating , design and environmental condition and consideration
- Class, Schedule, Code and standard
2.2 Application of Basic equation in process design - Bernoulli’s equation (When and how to use it)
- Darcy’s s equation (When and how to use it)
- General and empirical Hazen – Williams equation for liquids (When and how to use it)
- Isothermal, General, Weymouth and Panhandle equation General and empirical equation (When and how to use it)
- Approximate equations for small pressure drops (When and how to use it)
- Spitzglass equation for very low pressure line (When and how to use it)
- Fritzsch’s and Babcock equation for steam flow (When and how to use it)
- AGA, API RP 14 E and other empirical equations for 2- phase flow (When and how to use it)
- Effects of elevation on pipeline pressure drop (When and how to use it )
2.3 Head Loss in valves and fitting in process line - Head loss in valves and fitting
- Resistance and flow coefficients
- Equivalent length determination
Project work
MODULE 3
3.1 Line sizing determination - Flow rate and surge factor consideration
- Pressure drop consideration
- Erosion velocity
- Single phase Liquid and Gas line sizing
- 2- phase line sizing
- Multiphase line sizing
3.2 Sizing and specification of process equipment and selection
Pressure vessel equipment
Distillation column
Pumps (Vacuum pump, Dynamic pump)
Pipe sizing and pipe sizing for heating system
Separators
Knock out drum
Compressors
Valves
Flanges
Gaskets
Chiller/heater
Boilers
Ducts
Heat exchanger
Stripper
Absorber
Reflux drum
Turbines
Fan
Reactors
Filters
e.t.c 3.3 Control valve sizing – Gas line, Liquid line, oil line Project work
MODULE 4
4.1. Process control design:
Control parameter - Feed forward, feed back, cascade, ratio, Adaptive, inferential - Mathematical model, PID Tuning and the design of controllers, Mode of operation of various controller types Characteristic parameters
- The proportional controller
- The integral-action controller
- The PI controller
- The PD controller
- The PID controller
- PI flow diagram
- EMCS block diagrams interpretation of point (Electronic Measuring Control System)
- Process protection measures
4.2. Introduction to:
4.2.1 HAZID and HAZOP study 4.2.2. Preparation of Datasheet for:
-Equipment
-Process instrument
-Corrosion coupon and corrosion probe 4.3.3. Basic process design philosophy 5.0. Presentation of Result and Project reporting Project work
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: Process Design Training (Technical and Industrial Method)
Process Design Training
(Technical and Industrial Method)
This training will provide participants rich multidisciplinary understanding of the design and materials selection in process design. 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
Delivered entirely by capable facilitators withthorough, accurate and up-to-date knowledge of process engineering.
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 THE COURSE CONTENTS: MODULE 1
1.1 Process Engineering deliverable
1.1.1. Conceptual Design:
1.1.2. FEED
1.1.3 Basic/Detailed Design
1.1.4. Commissioning & Startup
1.2 Component of production system
1.2.1 Overview of Upstream and Downstream
1.2.2. Major products in upstream and downstream sector1.2.3. Diagrams of the various oil and gas production systems
1.3. Types of process diagrams -Introduction to DIN and ISA basic instrument Symbols
-PFD and P & ID diagram
-Flow Diagram
-Electrical drawing
- Elevation drawing
-Equipment location drawing
-Foundational drawing
-Legends diagram
- Plot plan and equipment arrangements
- Isometric drawing 1.4. Scope of process engineering inputs and outputs
P and IDs Design Process - Preparation of Block Diagram
- Preparation of Process Flow Diagrams (PFDs)
- Preparation of Piping and Instrument Diagrams (P & IDs)
- Utility flow diagram (UFD)
- Preparation of Mass, Heat and Energy Balance
- Pipe Isometric drawing
- EMCS block diagrams (Electronic Measuring Control System)
-Estimating production cost and profitability 1.5. Component of pipe connection - Methods of pipe connections (Body materials, end connection, operation, pressure class, size, specification)
- Fittings (valve, flanges, pipe and tube, elbow, Tee, Gasket, Fastener, industrial bolt ), Some different, Pipeline, pipe, Conduit, Tubing, Ducting, class, Schedule, NPS, NB & OD of a pipe, National Pipe Thread Taper NPT, code, standard, specification.
- ANSI B16.6 and API 6A pressure rating
Project work
MODULE 2
2.1. Fluid flow design
- Fluid flow types and characteristics
- Flow conditions
- Laminar vs. Turbulent
- Velocity limitation
- Temperature and pressure consideration
- Reynolds’s number (When and how to use it)
- Liquid and Gas viscosity (When and how to use it)
- Relative roughness (When and how to use it)
- Frictional factor - equation and charts (When and how to use it)
- Z – factor correlation (When and how to use it)
- Operating , design and environmental condition and consideration
- Class, Schedule, Code and standard
2.2 Application of Basic equation in process design - Bernoulli’s equation (When and how to use it)
- Darcy’s s equation (When and how to use it)
- General and empirical Hazen – Williams equation for liquids (When and how to use it)
- Isothermal, General, Weymouth and Panhandle equation General and empirical equation (When and how to use it)
- Approximate equations for small pressure drops (When and how to use it)
- Spitzglass equation for very low pressure line (When and how to use it)
- Fritzsch’s and Babcock equation for steam flow (When and how to use it)
- AGA, API RP 14 E and other empirical equations for 2- phase flow (When and how to use it)
- Effects of elevation on pipeline pressure drop (When and how to use it )
2.3 Head Loss in valves and fitting in process line - Head loss in valves and fitting
- Resistance and flow coefficients
- Equivalent length determination
Project work
MODULE 3
3.1 Line sizing determination - Flow rate and surge factor consideration
- Pressure drop consideration
- Erosion velocity
- Single phase Liquid and Gas line sizing
- 2- phase line sizing
- Multiphase line sizing
3.2 Sizing and specification of process equipment and selection
Pressure vessel equipment
Distillation column
Pumps (Vacuum pump, Dynamic pump)
Pipe sizing and pipe sizing for heating system
Separators
Knock out drum
Compressors
Valves
Flanges
Gaskets
Chiller/heater
Boilers
Ducts
Heat exchanger
Stripper
Absorber
Reflux drum
Turbines
Fan
Reactors
Filters
e.t.c 3.3 Control valve sizing – Gas line, Liquid line, oil line Project work
MODULE 4
4.1. Process control design:
Control parameter - Feed forward, feed back, cascade, ratio, Adaptive, inferential - Mathematical model, PID Tuning and the design of controllers, Mode of operation of various controller types Characteristic parameters
- The proportional controller
- The integral-action controller
- The PI controller
- The PD controller
- The PID controller
- PI flow diagram
- EMCS block diagrams interpretation of point (Electronic Measuring Control System)
- Process protection measures
4.2. Introduction to:
4.2.1 HAZID and HAZOP study 4.2.2. Preparation of Datasheet for:
-Equipment
-Process instrument
-Corrosion coupon and corrosion probe 4.3.3. Basic process design philosophy 5.0. Presentation of Result and Project reporting Project work
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
