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Introduction to Process Design

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History of a Typical Plant Design Project And How the Course Relates to This Steps ... modeling Don Robinson ... design of heat exchanger Energy minimization ... – PowerPoint PPT presentation

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Title: Introduction to Process Design


1
Introduction to Process Design
  • Don Robinson
  • September 2003

2
History of a Typical Plant Design Project
  • And How the Course Relates to This

3
Steps (Don Robinson, Dave Mody, not covered)
  • Need Identification
  • Data Gathering
  • Conceptual Design
  • Prelim Equip Design Cost Estimate
  • Profitability Analysis
  • Approval of Development Funds
  • Detailed Equipment Design
  • Accurate Cost Estimate
  • Approval of Construction Funds
  • Construction
  • Startup
  • Post Mortem

4
Identification of a Need
Opportunity
Problem
  • Sales increasing
  • New process technology
  • New product
  • Environmental regulations
  • Costs not competitive
  • Product Deficiencies
  • Obsolete equipment

5
Data Gathering
  • Info from existing process
  • Literature data
  • Data from simulation program
  • Plant tests
  • Lab experiments

6
Conceptual Design
  • Map out structure of process
  • Heat and mass balances
  • Evaluate alternatives
  • Primary tool is process simulation program

7
Preliminary Cost estimate
  • Not all that accurate (20-30)
  • Based on shortcut methods
  • Some additional design work needed
  • Required for the do we proceed decision

8
Profitability Analysis
  • Will the expected return justify the expenditure?
  • A process to direct resources to what is valued
    most by society

9
Approval of Development Funds
  • Get sufficient to do a proper design
  • Perhaps order long delivery time equipment

10
Detailed Equipment Design
  • Sufficient detail to pin down costs
  • Much of the work done by suppliers

11
Accurate Cost Estimate
  • Improved accuracy
  • Required for control of construction

12
Approval of Construction Funds
  • Confirm that the profitability picture is still
    good
  • A chance to bail out if conditions have changed

13
Implementation
  • Construction
  • Startup
  • Postmortem (learnings for future projects)

14
Sections of the Course
  • Concepts tools Barrie Jackson Geoff
    Whitfield
  • Process analysis modeling Don Robinson
  • Equipment design and costing Dave Mody

15
Concepts and Tools
  • Project management
  • Capital cost estimation
  • Engineering economics
  • Profitability analysis
  • Health safety issues
  • Thermodynamics
  • Distillation

16
Process Analysis Modeling
  • HYSYS tutorial and practice session
  • Process Analysis
  • Digest the information
  • Partial mass balance
  • Catalyst research

17
Process Analysis (cont.)
  • Initial HYSYS model
  • Refined Model
  • Optimized distillation column
  • Detailed design of heat exchanger
  • Energy minimization
  • Profitability analysis

18
Equipment Design Costing
  • PIDs
  • Sizing costing of specific equipment
  • Hazard analysis
  • Materials of construction
  • Cost of overall project

19
Computer Facilities
  • Accounts
  • CD
  • Software
  • Web Site
  • Information on Server

20
Computer Software
  • HYSYS process simulation to build models
  • CapCost (comes with the text)
  • crude estimates of equipment costs
  • compiling overall capital costs
  • profitability analysis
  • Excel for various calculations
  • Word for writing reports
  • Internet Explorer for viewing material

21
Computer Accounts
  • Security pass
  • Password
  • CD containing course documentation
  • Cost is 20
  • See Ann Tobin in room 201
  • Must be done by Wednesday afternoon

22
Web Site
  • info.chee.queensu.ca/CHEE470
  • Course description schedule
  • Info about staff and facilities
  • Group lists
  • Message log
  • Documents added after start of course

23
Information on Server
Available in Computer Cluster only
  • home folder (Z) for your private storage
  • group folder (R) used by all group members
  • course folder (P\CHEE470\start.wsf) course
    material (a copy of the CD)

24
Work Groups
  • Groups of 4
  • At least two chemical engineers
  • At least one engineering chemist
  • At least one not attending CSChE conf.
  • Designated A1,A2 . . . B1,B2 . . .
  • For some work the class will be split while the
    A groups do modeling, the B groups will do
    workshops
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