oil gas engineering-41-phpapp02
TRANSCRIPT
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HERVE BARON HERVE BARON Oil & Gas Engineering Training
Welcome!
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HERVE BARON HERVE BARON
Dear colleague,
I am glad to share with your this educative material on the Engineering of Oil & Gas facilities.
I developed it for classroom training sessions which I have been conducting since 2009.
This material will give you an overview of the work and deliverables of the different engineering disciplines.
I also thrived to produce workflow visuals to help understand the work sequence of each discipline and how they interface.
I wish you an enjoyable journey within Engineering
Oil & Gas Engineering Training
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HERVE BARON HERVE BARON Oil & Gas Engineering Training
HSE Moment
Project Engineering The Design Basis Discipline presentations
Field engineering
Quality Schedule
Intro, scope & objectives
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HERVE BARON HERVE BARON Oil & Gas Engineering Training
HSE Moment
Project Engineering The Design Basis Discipline presentations
Field engineering
Quality Schedule
Intro, scope & objectives
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HERVE BARON
Training Objectives
Scope
To give a detailed knowledge of what engineering of oil and gas facilities consist of
To describe the activities and show a sample deliverable in the various disciplines
To explain the challenges
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HERVE BARON HERVE BARON
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HERVE BARON HERVE BARON Oil & Gas Engineering Training
HSE Moment
Project Engineering The Design Basis Discipline presentations
Field engineering
Quality Schedule
Intro, scope & objectives
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HERVE BARON HERVE BARON Design Procurement Manufacturing Shipping
Installation Construction & erection Inspection &
tests Hand-over
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Engineering Sub-Contractor (Delhi) Detail Engineering (part)
Shipyard (Korea) Hull Engineering & Fabrication
Shipyards (Singapore & Malaysia) Topsides Fabrication & Integration
Home office (Paris) Project management Detail Engineering (part) Procurement
Satellite office (Pau) Detail Engineering (part)
Fabrication yard (Nigeria): Fabrication (part)
Offshore (Nigeria): Installation, commissioning, start-up
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Project
Engineering Procurement Construction
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Project
Engineering
Instrumentation & Control
Layout & Piping Process Electrical Equipment Civil Safety
Procurement Construction
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HERVE BARON HERVE BARON Engineering document register
Document number
Document title Document revision
A 1 48104 Service building instrument. rooms cables routing B
A 2 48102 Trouble shooting diagrams D
A 3 48134 F&G system architecture drawing E
A 4 50100 Instrument index B
A 7 50003 Spec for instrument installation works and service C
A 8 50960 Instrument Data sheets for temperature switches B
A 9 50110 Requisition for pressure relief valves B
M 1 62059 General plot plan B
M 2 62020 Piping details standard C
M 2 62070 Piping general arrangement Area 1 D
M 4 60100 Special items list D
M 5 62250 Piping isometrics booklet C
M 6 60000 Pipes and fittings thickness calculation A
M 6 62351 Calculation note CN1 - piping stress analysis A
M 7 60001 General piping specification C
M 8 60103 Data sheets for station piping material B
M 9 60200 Requisition for pipes F
Discipline code
A Instrumentation & Control
C Civil engineering
E Electrical
G Project general documents
J Mechanical
K Safety
M Piping & Layout
P Processes
S Steel Structures
V Vessels Heat exchangers
W Materials Welding
Document code
1 Installation drawings
2 Detail drawings
3 Diagrams
4 Lists Bill of Quantities
5 Isometrics
6 Calculation notes
7 Specifications
8 Data sheets
9 Requisitions
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Key plan
Diagram
Drawing
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Drawings common sizes & scales
Scale 1m =
1/1000 1 mm
1/500 2 mm
1/250 4 mm
1/100 1 cm
1/50 2 cm
1/33 3 cm A0 = 840x1188
A1 = 594x840
A2 = 420x594
A4 = 210x297
A3 = 297x420
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Engineering schedule
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Piping 31%
Structural 23%
Instrumentation/ICSS/Telecom
10%
Commissioning 9%
Electrical 9%
Mechanical Equipment
6%
Naval 4%
Process 2%
Others 6%
Engineering resources
~1,000,000 man-hours
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Engineering Documents for Purchase:
bill of quantity & specification
Documents for Construction:
Construction drawings & specifications
Documents submitted to client
Client
Approval/
Comments
Design basis:
- Functional requirements
- Client specifications
- Design codes
Vendors
Documents submission Comments
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HERVE BARON HERVE BARON Oil & Gas Engineering Training
HSE Moment
Project Engineering The Design Basis Discipline presentations
Field engineering
Quality Schedule
Intro, scope & objectives
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HERVE BARON HERVE BARON
Process facilities:
Feedstock and products flow
Feedstock composition
Battery limit conditions
Equipment Spare
Performance:
Products specifications
Energy efficiency, emissions
Utilities:
Electric power supply
Other utilities
Systems:
Process control
Fire/gas alarm
Public address, LAN, PABX
Infrastructure:
Administrative and technical buildings
Control room
Access road
Site fencing, gates, check point
Design criteria:
% of over design
Environment data:
Min/max temperature
Rain/snow fall
Wind
Geological conditions
Applicable codes and standards:
International standards
Local rules
0 5
10 15 20 25 30 35 40 45 50
-85 -80 -75 -70 -65 -60 -55
Pre
ssu
re (
ba
r)
Design Basis
Pressure (bar)
Hydrates Curve
Phase Envelope
Temperature (C)
25
20
15
10
5
0
-5
-10
-15
-20
-25
-30
-35
-40
-45
-50
-55
-60
-65
-70
-75
-80
-85
80
75
70
65
60
55
50
45
40
35
30
25
20
15
10
5
0
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HERVE BARON HERVE BARON Oil & Gas Engineering Training
HSE Moment
Project Engineering The Design Basis Discipline presentations
Field engineering
Quality Schedule
Intro, scope & objectives
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HERVE BARON HERVE BARON Engineering disciplines
Process Equipment HSE Civil
Layout
Instrumentation Piping
Electrical
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Functional requirements example of a gas compression station
Gas composition Performance
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Process Scheme Optimization
HP Separator 500 psig
5500 psig
Emul. Treater 50 psig 150 F
3000 psig
200 psig
Degasser 5 psig
5 psig
50 psig
1200 psig Gas Injection
Oil Production
From Wells 165 - 205 F
500 psig
HP Compression & TEG
LP Compression
TEG
Cooler
IP Compression
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Process simulations
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Process Flow Diagram (PFD)
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Heat & Material balance
Thermodynamic calculations
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Equipment sizing
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Process data sheet
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Fluid list
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HERVE BARON HERVE BARON Piping & Instrumentation Diagram (P&ID)
Line List
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HERVE BARON HERVE BARON Piping & Instrumentation Diagram (P&ID)
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HERVE BARON P&IDs legend & symbols
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HERVE BARON HERVE BARON Line sizing
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Process automations: Cause & effect chart
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ESD logic diagram
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ESD simplified diagram
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Flare Report
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HERVE BARON HERVE BARON Operating manual
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Quiz: Is this a P&ID? a PFD?
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Process Equipment HSE Civil
Layout
Instrumentation Piping
Electrical
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Process design
PFDs
H&M balance
Rotating Pressure vessels Fired equipment Heat exchangers Packages etc.
Process data sheet
Equipment specification
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Rotating machinery
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HERVE BARON HERVE BARON Pressure vessels
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Heat exchangers
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Process data sheet
Mechanical data sheet
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Vessel guide drawing
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HERVE BARON HERVE BARON Material Requisition
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HERVE BARON HERVE BARON Bid technical evaluation
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Vendor design
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HERVE BARON HERVE BARON Equipment summary
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Process Equipment HSE Civil
Layout
Instrumentation Piping
Electrical
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SEVERITY
FREQENCY
HAZOP Review
RISK MATRIX
RISK LEVEL
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HAZOP Action sheet
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HERVE BARON HERVE BARON Fire Fighting
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HERVE BARON HERVE BARON Fire Water demand
calculation note
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Fire Water P&IDs
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Deluge system
arrangement drawings
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Fire fighting equipment location drawing
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HERVE BARON Passive fire protection drawing
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HERVE BARON Passive fire protection
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HERVE BARON HERVE BARON Fire & Gas detection layout
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Hazardous area classification drawing
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Case stuy: Gas leak from random piping component rupture
Cause: installation error, corrosion, material defect
Possible consequence: Dispersion without ignition / jet fire / flash fire / explosion
Section considered: Compressor building
Quantitative Risk Analysis (QRA)
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Step 1:
Identification and characterisation of initiating events
Gas leak inside compressor buidling due to component rupture
Hole size (% of component section)
5% 20% Full
Frequency (event/year) 1,11E-01 5,06E-04 6,83E-05
Outflow rate (kg/s) 5,7 90,8 2270,0
risk components *failure rate (from statistics)
Quantitative Risk Analysis (QRA)
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Release Frequency Immediate ignition
ESD & Fire Fighting
Delayed Ignition
Explosion/ Flash-fire
Consequence Event Frequency (ev/y)
0,998 Jet fire ESD & FF 7,779E-030,070
0,002 Jet fire no ESD & FF 1,520E-05
1,11E-01Release/yr
0,949 Dispersion 9,827E-020,930
0,120 Explosion 1,774E-050,028
0,051 0,880 Flash fire 1,301E-04
0,972 Dispersion 5,133E-03
Yes Frequency (event/year)Jet fire ESD & FF 7,779E-03Jet fire no ESD & FF 1,520E-05Explosion 1,774E-05
No Flash Fire 1,301E-04Dispersion 1,034E-01
B04a/b/c/d 5%
Step 2: Event tree analysis
Probability of immediate ignition for 1-50 kg/s release rate is 7% (from statistical data)
Probability of delayed ignition takes into account equipment explosion protection (Ex)
Gas detectors are provided inside the building, that activate isolation and depressurization. It is assumed that they operate 95% of the time.
Quantitative Risk Analysis (QRA)
Probability of explosion vs flash fire depends on mass of gas and degree of confinement
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Step 3:
Consequence evalutation
Overpresssure (bar) 0.2 0.1 0.01
Distance (m) 96 167 1270
CONSEQUENCE CLASS QUANTITATIVE CRITERIA EFFECTS
MINOR 0.1 bar locally (within 10m) No effect, no damage
SIGNIFICANT 0.1 bar locally (within 50m) Limited damage to plant and operators
SEVERE > 0.1 bar within plant Damage to plant and operators
MAJOR > 0.1 bar on populated areas Damage to plant, operators & public
Quantitative Risk Analysis (QRA)
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As Low As Reasonably Practicable Plant Management measures
Acceptable risk area
1.0E-02
1.0E-03
1.0E-04 Unlikely
1.0E-05 Rare
1.0E-06 Minor Significant Severe Major
Release Frequency Immediate ignition
ESD & Fire Fighting
Delayed Ignition
Explosion/ Flash-fire
Consequence Event Frequency (ev/y)
0,998 Jet fire ESD & FF 7,779E-030,070
0,002 Jet fire no ESD & FF 1,520E-05
1,11E-01Release/yr
0,949 Dispersion 9,827E-020,930
0,120 Explosion 1,774E-050,028
0,051 0,880 Flash fire 1,301E-04
0,972 Dispersion 5,133E-03
Yes Frequency (event/year)Jet fire ESD & FF 7,779E-03Jet fire no ESD & FF 1,520E-05Explosion 1,774E-05
No Flash Fire 1,301E-04Dispersion 1,034E-01
B04a/b/c/d 5%
Release Frequency Immediate ignition
ESD & Fire Fighting
Delayed Ignition
Explosion/ Flash-fire
Consequence Event Frequency (ev/y)
0,998 Jet fire ESD & FF 7,779E-030,070
0,002 Jet fire no ESD & FF 1,520E-05
1,11E-01Release/yr
0,949 Dispersion 9,827E-020,930
0,120 Explosion 1,774E-050,028
0,051 0,880 Flash fire 1,301E-04
0,972 Dispersion 5,133E-03
Yes Frequency (event/year)Jet fire ESD & FF 7,779E-03Jet fire no ESD & FF 1,520E-05Explosion 1,774E-05
No Flash Fire 1,301E-04Dispersion 1,034E-01
B04a/b/c/d 5%
Damage to plant, operators & public> 0.1 bar on populated areasMAJOR
Damage to plant and operators> 0.1 bar within plantSEVERE
Limited damage to plant and operators0.1 bar locally (within 50m)SIGNIFICANT
No effect, no damage0.1 bar locally (within 10m)MINOR
EFFECTSQUANTITATIVE CRITERIACONSEQUENCE CLASS
Damage to plant, operators & public> 0.1 bar on populated areasMAJOR
Damage to plant and operators> 0.1 bar within plantSEVERE
Limited damage to plant and operators0.1 bar locally (within 50m)SIGNIFICANT
No effect, no damage0.1 bar locally (within 10m)MINOR
EFFECTSQUANTITATIVE CRITERIACONSEQUENCE CLASS
Final step: classification of risk
Quantitative Risk Analysis (QRA)
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Environmental Impact Assessment (Air quality dispersion analysis)
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Noise Map
dB(A)
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Process Equipment HSE Civil
Layout
Instrumentation Piping
Electrical
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Process design
PFDs
H&M balance
Rotating Pressure vessels Fired equipment Heat exchangers Packages etc.
P&IDs
Piping
Instrumentation
Layout
Civil
Electrical
Process data sheet
Equipment specification Vendor
drawings
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Grading plan
Native soil elevation
Required finish level
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Vendor information
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Foundation Calculation
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Foundation drawing/
re-inforcement
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Foundation drawing/
Formwork
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specification
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Loading data
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Structural design
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HERVE BARON HERVE BARON Calculation note
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Structural drawings
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Architectural drawings
Equipment layout drawing
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Heating, Ventilation &Air Conditioning (HVAC)
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Civil Works Installation Drawings
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Standard drawings
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Process Equipment HSE Civil
Layout
Instrumentation Piping
Electrical
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Process design
PFDs
H&M balance
Rotating Pressure vessels Fired equipment Heat exchangers Packages etc.
P&IDs
Piping
Instrumentation
Layout
Civil
Electrical
Process data sheet
Equipment specification Vendor
drawings
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Layout/
principles
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HERVE BARON HERVE BARON Layout/vendor drawings
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Layout/consideration for all networks
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HERVE BARON HERVE BARON General Plot Plan
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Unit Plot Plan
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3D modelling
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3D model clash check
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HERVE BARON HERVE BARON 3D model review
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Equipment handling
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Process Equipment HSE Civil
Layout
Instrumentation Piping
Electrical
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Process design
PFDs
H&M balance
Rotating Pressure vessels Fired equipment Heat exchangers Packages etc.
P&IDs
Piping
Instrumentation
Layout
Civil
Electrical
Process data sheet
Equipment specification Vendor
drawings
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Line Diagram
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Piping Layout drawing
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HERVE BARON HERVE BARON Isometric drawing
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HERVE BARON HERVE BARON Piping Pre-fabrication
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HERVE BARON HERVE BARON Post Weld Heat
Treatment
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HERVE BARON HERVE BARON Piping Inspection and testing
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Piping General Arrangement drawing
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Calculations
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HERVE BARON HERVE BARON Standard Pipe Support
drawings
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Piping line diagram
Plot Plan
Piping studies & layout
Piping 3D modelling
Piping stress analysis
Piping isometric drawing
Stress OK?
Piping isometric drawing IFC
Process OK?
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HERVE BARON HERVE BARON Material Selection
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HERVE BARON HERVE BARON Material Selection Diagram
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HERVE BARON HERVE BARON Process Fluids list Piping material classes
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HERVE BARON HERVE BARON Piping material
classes Piping material class specification
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Piping material classes specification
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Piping material classes specification
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Piping material classes specification
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HERVE BARON HERVE BARON Piping material requisition
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Process Equipment HSE Civil
Layout
Instrumentation Piping
Electrical
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Piping & Instrumentation Diagram (P&ID)
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Instrument list
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Instrument data sheet
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Process Control System
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System Architecture drawing
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Process automations
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Control narrative
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Mechanical Equipment Control
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PT JB
Process line
Marshalling
cabinet
Controller
cabinet
Instrument room Control room
VDU
CPU
LAN Secondary cable
Multi cable
The instrument hardware
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Junction Box drawing
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Instrument location drawing
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Building detail drawing/
Telecom and PAGA layout
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Instrument standard installation drawings
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Junction box wiring
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HERVE BARON HERVE BARON Cable routing drawings
Cable list
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HERVE BARON Instrument bulk Material Take-Off
ITEM QUANTITY DESIGNATION
1 195 Gauge adapter x
2 37 Block manifold 2 valves (Gas)
3 23 Block manifold 5 valves (Gas)
4 0 Ball valve 12mm
5 300m Tubing 12mm OD x 1mm
6 200 Reducer 12mm x
7 50 Union tee 12 x 12 x 12mm
8 50 Female connector 12mm x
9 350 Male connector 12mm x
10 9 Plug NPTF
11 8 Plug NPTM
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Cable routing inside technical room
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Instrumentation & control rooms layout
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Screen displays
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Instrument loop diagram
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Process Equipment HSE Civil
Layout
Instrumentation Piping
Electrical
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Electrical consumer list
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Electrical Load Summary
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General One Line Diagram
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Generators
Switchgear
Transformer
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HERVE BARON HERVE BARON Switchboard
Single Line Diagram
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HERVE BARON HERVE BARON Switchgear Typical Diagram
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8800
8900
9000
9100
9200
9300
9400
9500
9600
9700
9800
9900
10000
0.0 2.5 5.0 7.5 10.0 12.5 15.0 17.5 20.0
VOLTAGE OF MS-001 (STUDY1)Bus
Voltage (V
olts)
Time (Seconds)
47.0
47.5
48.0
48.5
49.0
49.5
50.0
0.0 2.5 5.0 7.5 10.0 12.5 15.0 17.5 20.0
FREQUENCY OF MS-001 (STUDY1)
Bus Freq
uency (Hz
)
Time (Seconds)
Calculations
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Cable schedule
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Typical installation drawings
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Block Diagram
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Trouble shooting diagrams
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Lighting layout
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Lighting illumination level
Iso lux curves
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Electrical Control System
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Electrical Control System
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From emergency (diesel)
generators
From main power
generators
To normal consummers e.g. pumps in process
and utility units
To essential consummers e.g. fire
water pump
Electrical load shedding
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HERVE BARON HERVE BARON Oil & Gas Engineering Training
HSE Moment
Project Engineering The Design Basis Discipline presentations
Field engineering
Quality Schedule
Intro, scope & objectives
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HERVE BARON HERVE BARON Field Engineering
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HERVE BARON HERVE BARON Site Query
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Site MASTER set of documents
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HERVE BARON HERVE BARON Oil & Gas Engineering Training
HSE Moment
Project Engineering The Design Basis Discipline presentations
Field engineering
Quality Schedule
Intro, scope & objectives
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7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36PLANT START-UPPIPING PRE-FABRICATION & INSTALLATION X X X X X X X X X XPIPING MATERIAL & DRAWINGS AT SITEPIPING MATERIAL MANUFACTURING & SHIPPING X X X X X XPURCHASE OF PIPING MATERIALTECHNICAL & COMMERCIAL CLARIFICATIONS X XCALL FOR TENDER FOR PIPING MATERIALPREPARE PIPING MATERIAL TAKE-OFF XPIPING ROUTING STUDIES X X XPIPING & INSTRUMENTATION DIAGRAMS (PIDs)
PROJECT SCHEDULEMONTH
1
1
2 3
3
4 5
2
4 5
5
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Process simulations
Equipment selection
& purchase
Foundation drawings
Process data sheet
Vendor data
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Safety valves duty & data
sheet (Process) Safety valves inquiry and purchase
(procurement) Safety valves
sizing & drawings (vendor)
Safety valves location & piping
routing (piping/layout) Piping calcs &
supports (piping/stress)
Steel structure design and
drawings (civil)
Purchase steel (manufacturer) Fabrication
(manufacturer) Shipping
Structure at Site
Size & weight estimates
Supports & loads estimates
Estimates must be done to meet the schedule
Engineering schedule
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What Engineering designed
What the Vendor supplied
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HSE Moment
Project Engineering The Design Basis Discipline presentations
Field engineering
Quality Schedule
Intro, scope & objectives
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Engineering Quality Assurance:
Engineering document register
Document number
Document title Document revision
A 1 48104 Service building instrument. rooms cables routing B
A 2 48102 Trouble shooting diagrams D
A 3 48134 F&G system architecture drawing E
A 4 50100 Instrument index B
A 7 50003 Spec for instrument installation works and service C
A 8 50960 Instrument Data sheets for temperature switches B
A 9 50110 Requisition for pressure relief valves B
M 1 62059 General plot plan B
M 2 62020 Piping details standard C
M 2 62070 Piping general arrangement Area 1 D
M 4 60100 Special items list D
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Engineering Quality Assurance:
Document checking and distribution
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Engineering Quality Assurance:
Document revision
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Engineering Integrity: Site Query from Construction
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Interface Agreement
Section/Step 1
Section/Step 2
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Interface definition
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2015 Herv Baron
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The Oil & Gas Engineering Guide 2nd edition
Do you want to know more... Much more?
-
2015 Herv Baron
HERVE BARON
The Oil & Gas Engineering Guide - 2nd edition
Table of Contents
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2015 Herv Baron
HERVE BARON
The Oil & Gas Engineering Guide - 2nd edition
Table of Contents
Discipline presentation: activities and deliverables
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HERVE BARON
The work of each
Engineering discipline is described
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HERVE BARON
Design activities are explained, e.g., Plant
Equipment layout
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HERVE BARON
Complex activities, such as
QRA, are explained through a practical
example.
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HERVE BARON
A sample of all common Engineering documents is
included
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Difference between
Engineering and Shop drawings
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HERVE BARON
Understand the main
technical aspects, e.g., DCS vs ESD
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HERVE BARON
The Oil & Gas Engineering Guide - 2nd edition
Table of Contents
The overall process
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2015 Herv Baron
HERVE BARON
The Oil & Gas Engineering Guide - 2nd edition
Table of Contents
-
2015 Herv Baron
HERVE BARON
The Oil & Gas Engineering Guide - 2nd edition
Table of Contents
-
2015 Herv Baron
HERVE BARON
The Oil & Gas Engineering Guide - 2nd edition
Table of Contents
-
2015 Herv Baron
HERVE BARON
The Oil & Gas Engineering Guide 2nd edition
Order direct from the publisher:
http://www.editionstechnip.com/en/catalogue-detail/1111/oil-gas-engineering-guide-the.html
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2nd editionThe Oil & Gas Engineering Guide - 2nd editionDiapositive numro 226Diapositive numro 227Diapositive numro 228Diapositive numro 229Diapositive numro 230Diapositive numro 231The Oil & Gas Engineering Guide - 2nd editionThe Oil & Gas Engineering Guide - 2nd editionThe Oil & Gas Engineering Guide - 2nd editionThe Oil & Gas Engineering Guide - 2nd editionThe Oil & Gas Engineering Guide2nd edition