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 Manual Drafting Method
 Piping Design Model Method
 CADD Method
 CADD Model Combined with Physical Scale Model
 Involves determination of detailed piping with the use
of drawings
 Process scheme transposed from flow diagrams onto
Equipment Location Plan
 Designer then produces detailed drawings in form of
Piping Plans and Piping Sections called Piping
Arrangement Drawings
 Drawn to a scale of 3/8” = 1’0” (imperial) or 1:30 (metric)
 Isometrics are then developed from the Arrangement
Drawings
 Plastic Scale Models
 Lay out piping and valves directly on model
 Arrangement and isometric drawings developed from
model
 scale of 3/8” = 1’0” (imperial) or 1:30 (metric)
 Advantages
 Accurate and reliable
 Points out costly interferences & construction problems
 Produces better plant layout
 Improves communication between design disciplines
 Better indication of progress to management
 Reduces construction costs by eliminating “ignorance
contingencies” used by bidders
 Assists in the writing of better operation manuals
 Reduces amount of time spent training plant operators
 Speed up drawing function and enhance design
function
 Allows production of “intelligent” flow diagram
 Reports line & instrumentation list and prelim M.T.O.
 Reports inconsistencies in pipe sizing and specs
 Major strength: data storage and retrieval capability
which allows massive amounts of design information
to be available for checking and reporting
 Designer produces plant design using following steps:
 Set up section of plant as computer model in isometric
 Insert foundations and structures
 Construct vessels and equipment
 Route piping between nozzles
 Add fittings, vales and instruments
 Report interferences
 Report inconsistencies re: size, specs or space
 Produce double line plan or section views
 Automatically produce isos incl. M.T.O.
 Link all sections of plant together
 Combined to produce faster, more efficient and effective
design with cleaner construction
 Early design – plastic model
 Plastic model data fed into CADD database which:
 Allows for interference checks to be made
 Allows Structural load verification to indicate supports and hangars
and interface with stress analysis programs
 Provides easy access to drawings of each area
 Aids with MTOs and spec compatibility checking
 CADD designs related back to physical model
 CADD develops Isos, arrangement drawings, MTOs and
inventory lists for use during construction
 Physical model available during approvals, construction,
operator training and as basis for revision
 Positive Pressure Head must be present at piping outlet
 Produced by pump, gravity, displacement or static head, suction
 Friction loss
 Keep piping runs short as possible with few fittings
 Viscosity (internal friction of fluid)
 Design piping and valving for minimum liquid hold-up during shut-down
 Vents and drains
 Properly placed to allow filling and draining of vessels during testing and purging
 Turbulence is required
 Avoid dead spots in piping and use bends of 5 pipe diameter
 Control valves
 Commonly one pipe size smaller than line size
 Points of sudden pressure drop causing “flashing”
 Provide sufficient N.P.S.H.
 Vapour lock
 Slope the line or vent high point
 Condensable vapours like steam piped to avoid liquid pocketing
 Special pipe materials
 may be needed when transporting hazardous liquids
 Economics
 Minimize length of lines and number of fittings
 Carefully consider design changes due to increasing operation costs
in facilities
 Maintenance
 Adequate space must be provided for assembly, disassembly,
adjustment and lubrication of equipment
 Utility stations should be readily available
 Special lifting or rigging devices may be required
 Breakout flanges may be required to aid equipment removal
 Vibration
 Air chambers may be required for quick valve opening & closing
 Reciprocating equipment requires surge tanks or pulsation bottles
plus sufficient piping support

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Module 13 plant piping design

  • 1.
  • 2.  Manual Drafting Method  Piping Design Model Method  CADD Method  CADD Model Combined with Physical Scale Model
  • 3.  Involves determination of detailed piping with the use of drawings  Process scheme transposed from flow diagrams onto Equipment Location Plan  Designer then produces detailed drawings in form of Piping Plans and Piping Sections called Piping Arrangement Drawings  Drawn to a scale of 3/8” = 1’0” (imperial) or 1:30 (metric)  Isometrics are then developed from the Arrangement Drawings
  • 4.  Plastic Scale Models  Lay out piping and valves directly on model  Arrangement and isometric drawings developed from model  scale of 3/8” = 1’0” (imperial) or 1:30 (metric)  Advantages  Accurate and reliable  Points out costly interferences & construction problems  Produces better plant layout  Improves communication between design disciplines
  • 5.  Better indication of progress to management  Reduces construction costs by eliminating “ignorance contingencies” used by bidders  Assists in the writing of better operation manuals  Reduces amount of time spent training plant operators
  • 6.  Speed up drawing function and enhance design function  Allows production of “intelligent” flow diagram  Reports line & instrumentation list and prelim M.T.O.  Reports inconsistencies in pipe sizing and specs  Major strength: data storage and retrieval capability which allows massive amounts of design information to be available for checking and reporting
  • 7.  Designer produces plant design using following steps:  Set up section of plant as computer model in isometric  Insert foundations and structures  Construct vessels and equipment  Route piping between nozzles  Add fittings, vales and instruments  Report interferences  Report inconsistencies re: size, specs or space  Produce double line plan or section views  Automatically produce isos incl. M.T.O.  Link all sections of plant together
  • 8.  Combined to produce faster, more efficient and effective design with cleaner construction  Early design – plastic model  Plastic model data fed into CADD database which:  Allows for interference checks to be made  Allows Structural load verification to indicate supports and hangars and interface with stress analysis programs  Provides easy access to drawings of each area  Aids with MTOs and spec compatibility checking  CADD designs related back to physical model  CADD develops Isos, arrangement drawings, MTOs and inventory lists for use during construction  Physical model available during approvals, construction, operator training and as basis for revision
  • 9.  Positive Pressure Head must be present at piping outlet  Produced by pump, gravity, displacement or static head, suction  Friction loss  Keep piping runs short as possible with few fittings  Viscosity (internal friction of fluid)  Design piping and valving for minimum liquid hold-up during shut-down  Vents and drains  Properly placed to allow filling and draining of vessels during testing and purging  Turbulence is required  Avoid dead spots in piping and use bends of 5 pipe diameter  Control valves  Commonly one pipe size smaller than line size  Points of sudden pressure drop causing “flashing”  Provide sufficient N.P.S.H.  Vapour lock  Slope the line or vent high point  Condensable vapours like steam piped to avoid liquid pocketing  Special pipe materials  may be needed when transporting hazardous liquids
  • 10.  Economics  Minimize length of lines and number of fittings  Carefully consider design changes due to increasing operation costs in facilities  Maintenance  Adequate space must be provided for assembly, disassembly, adjustment and lubrication of equipment  Utility stations should be readily available  Special lifting or rigging devices may be required  Breakout flanges may be required to aid equipment removal  Vibration  Air chambers may be required for quick valve opening & closing  Reciprocating equipment requires surge tanks or pulsation bottles plus sufficient piping support