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Fischer-Tropsch Liquids refining Plant

Fischer-Tropsch Liquids refining Plant . Team Foxtrot Presentation #4 – April 9, 2013 Mentor: Dan Rusinak, PE Team: Mudassir Ali Stephen Drake Kevin Meaux Brandon Sieve. CHE 397 University of Illinois at Chicago Chemical Engineering Department. Today, Team Foxtrot will Address:

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Fischer-Tropsch Liquids refining Plant

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  1. University of Illinois at Chicago Fischer-TropschLiquids refining Plant Team Foxtrot Presentation #4 – April 9, 2013 Mentor: Dan Rusinak, PE Team: Mudassir Ali Stephen Drake Kevin Meaux Brandon Sieve CHE 397 University of Illinois at Chicago Chemical Engineering Department

  2. University of Illinois at Chicago Today, Team Foxtrot will Address: • Questions/Topics from Presentation #3 • Complete PFD • Process Control Scheme • Plant Layout • Refined Economics

  3. University of Illinois at Chicago Design Project Outline • Executive Summary • Discussion • Recommendations Appendices • Design Basis  • Block Flow Diagram  • Process Flow Diagram showing major equipment  • Material and Energy Balance  (w/ Integration Review) • Calculations  • Annotated Equipment List  • Economic Evaluation factored from Equipment Costs  • Utilities  • Conceptual Control Scheme  • General Arrangement – Major Equipment Layout  • Distribution and End-use Issues Review • Constraints Review • Applicable Standards • Project Communications File • Information Sources and References

  4. University of Illinois at Chicago Topics from Last Presentation - Oligomerization - Hydrocracker

  5. University of Illinois at Chicago Detailed PFD with Level Controls • The next slides will consist of: • PFD Level controls around • Air Membrane Separators • Exchangers • Compressors • 2 Phase Separators • 3 Phase Separators • Vessels • Fired Heater • Reactors

  6. University of Illinois at Chicago Overall FT Loop Foxtrot, University of Illinois at Chicago 6

  7. FT Loop Area 1 PFD 7 University of Illinois at Chicago Area 1- FT Loop PFD 4 2 3 Equipment List 6 1 5

  8. University of Illinois at Chicago FT loop Area 2 PFD 7 9 11 14 8 13 Equipment List 12 10

  9. Oligimerization Loop overall PFD University of Illinois at Chicago

  10. Oligomerization PFD Area 1 University of Illinois at Chicago 3 2 1 5 4

  11. Oligomerization PFD Area 2 University of Illinois at Chicago

  12. Oligomerization PFD Area 3 University of Illinois at Chicago

  13. Hydrocracker Overall PFD IC TIC LIC FIC TIC TIC IC IC FIC

  14. University of Illinois at Chicago Close up Hydrocracker Reactor PFD

  15. Hydrocracker Overall PFD 15 TIC LIC FIC TIC TIC FIC

  16. University of Illinois at Chicago Reactor Specifications

  17. Flare Labs Road Loading Fired Heater Highway Tank Farm Process Road Road Parking Lot Offices Utility Road Road University of Illinois at Chicago Conceptual Plant Layout Perimeter Fence Wind

  18. University of Illinois at Chicago Detailed Process Area Layout R-100 R-101 R-102 M-100 150’ R-100 15’ Side Pipe Rack C-103 C-100 T-104 15’ K-103 K-100 AC-101 T-101 30’ 30’ C-104 C-101 T-105 K-101 K-104 T-102 V-100 Main Pipe Rack 30’ C-105 C-102 T-106 K-105 K-102 V-101 T-103 T-107 C-106 K-106 10’ 10’ V-102 T-108 C-107 K-107 50’ VGO dike D=43ft V= 5310ft^3 Resid dike D=43ft V= 5310ft^3 Cold dike D=59ft V= 11070ft^3 Hot dike D=47ft V= 7062ft^3

  19. University of Illinois at Chicago Storage • Require 10 floating roof storage tanks (for naphtha, jet, diesel, VGO, and residuum) and 2 pressurized storage tanks (for LPG and cold condensate) • 4 storage tanks in process area, 8 in tank farm • Pipeline access every 2 days, will transfer 75% of tank contents • Dike areas must contain the maximum amount of liquid in a tank • $2,600/m3 of storage

  20. University of Illinois at Chicago Tank Farm Bund LPG tank, pressurized D=26.2’,H=9.8’ S-100 S-104 Gasoline tank, floating roof D=26.2’,H=30’ S-101 S-105 Jet Fuel tank, floating roof D=26.2’,H=30’ Bund Pipe Rack S-102 S-106 Diesel tank, floating roof D=32.8’,H=32.8’ 50’ 50’ S-103 S-107 Bund (Concrete): 6’ High 25’ 25’ Bund

  21. University of Illinois at Chicago Economics • 20 year plant life • 30 workers,5 managers • Total Cost: $7.3 MM/year • Utility, catalyst, and maintenance costs: $28.5 MM/year • Cooling water, Steam: $8.1 MM/year • Electricity: $3.79 MM/year • Catalyst: $4.4 MM/year • Maintenance: $12.2 MM/year

  22. University of Illinois at Chicago FTL Plant Production • Feed from Syngas Plant: • Total: 243,558 lb/hr To CHP plant: 103,504 lb/hr • 68 mol% H2 -36 mol% CH4 • 28 mol% CO -34 mole % H2 • 2 mol% N2 -16 mol% CO • 2 mol% CH4 -9 mol % N2 -4 mol % Ethane • Total Product Volume: 5,100 bbl/dayTo Water treatment plant: • 500 bbl/day LPG (10%) -121,159 lb/hr • 1,100 bbl/day Gasoline (21%) -96 mol % Water • 1,000 bbl/day Jet Fuel (20%) -3.8 mol % Alcohol • 2,500 bbl/day Diesel (49%) -0.2 mol % Carboxylic

  23. University of Illinois at Chicago Investment Economics • Capital Cost: $406 MM • NPV: $455 MM • IRR: 21.96% • Interest: 8.00% • Simple Payback: 4.68 years

  24. University of Illinois at Chicago Calculations • *2

  25. University of Illinois at Chicago Bibliography [1] Bartholomew, Calvin, and Robert Fauratto. Fundamentals of Industrial Catalytic Processes. 2nd ed. N.p.: John Wiley & Sons, 2006. Print. [2] Private communication with UOP LLC. [3] De Klerk, Arno. Fischer-Tropsch Refining. Germany: Weinheim, 2011. Print.

  26. University of Illinois at Chicago Thanks For Your Time! Questions?

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