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FEL-2 Feasibility Study: GreenGene
SMITH GROUP – Hayoung Lee, Soo Lee, Iyore Olaye, Sang Yoo
School of Chemical and Biomolecular Engineering
Cornell University
Ithaca, NY 14853
May 8, 2016
Table of Contents
I. Project Statement
II. Market Analysis
III. Process Units
IV. Plant Location and Plant Layout
V. Constructability
VI. Economic Analysis
VII. Recommendation for FEL-3
2
SMITH
Group
GreenGene May 9, 2016
Project Statement
q Client: NanoBio Pharmaceuticals
• New product : GreenGene (anti-hypertensive drug)
• Modeled using Penicillin G production process
q Objective
• Capture 20% of the North American market after 5 years
• Produce 120% of the estimated year five demand
• Assumed dosage: 100mg/day
q Determine
• Capital and operating costs for the facility
• Ex-plant price of GreenGene proxy
3
SMITH
Group
GreenGene May 9, 2016
GreenGene Feasibility Study
4
SMITH
Group
GreenGene
Process is financially robust based on Penicillin G study
Proceed to FEL-3 Stage
May 9, 2016
Location?
Fairfax, Iowa
Economic Analysis?
Price per dose at 18% DCFROR: $0.008/dose
Based on Penicillin G production process
Average Competitive price per dose of hypertension API: $0.03/dose
Total Project Cost: $110 MM
Operating Cost: $21 MM
Environmental Concerns?
No significant environmental or safety concerns
5
SMITH
Group
GreenGene May 9, 2016
Market Analysis
Market Analysis
6
SMITH
Group
GreenGene May 9, 2016
0.00
0.50
1.00
1.50
2.00
2.50
3.00
3.50
4.00
4.50
5.00
0 1 2 3 4 5 6 7 8 9 10
AmountofAnti-hypertensiveDrug(Tg)
Years	of	Production	2019
q Target Market :
North Americans with Hypertension
q 100 mg dose per day
q Economic Goals for GreenGene:
• Capture 20 % of total market
• Supply 120% of demand by year 5
Supply estimate served as a basis for equipment sizing and
economic analysis throughout FEL-2 study
Annual demand
Annual supply
High Blood Pressure Facts." Centers for Disease Control and
Prevention. Centers for Disease Control and Prevention, 19 Feb.
2015. Web. 09 May 2016.
7
SMITH
Group
GreenGene May 9, 2016
Process Units
Process Overview
8
SMITH
Group
GreenGene May 9, 2016
Media Preparation
9
SMITH
Group
GreenGene May 9, 2016
See PFD: Process Sheet 1
Objective: Mix raw materials and sterilize the media without
degrading nutrients
Media Preparation
10
SMITH
Group
GreenGene May 9, 2016
Fermentation
11
SMITH
Group
GreenGene May 9, 2016
See PFD: Process Sheet 2
Objective: Purify air to meet pharmaceutical standards / Achieve
desired concentration of titer through controlled reaction kinetics
Fermentation
12
SMITH
Group
GreenGene May 9, 2016
Reaction Basics
13
SMITH
GROUP
GreenGene
Main Reaction :
Cell + Glucose + O2 + PAA + (NH4)2SO4
à More Cells + Penicillin G + CO2 + H2O + Heat
Penicillin G
Penillic Acid
Penicilloic Acid
Degradation of Penicillin G (Side Reactions) :
May 9, 2016
Birol, Gülnur, Cenk Ündey, and Ali Çinar. "A Modular Simulation
Package for Fed-batch Fermentation: Penicillin Production." Computers
& Chemical Engineering 26.11 (2002): 1553-565. Web.
0
50
100
150
200
250
300
350
400
450
500
0 50 100 150 200
Concentration(g/L)
Time (hr)
14
SMITH
GROUP
GreenGene
[Glucose]
[Cell]
[Penicillin	G]
Chemical Reaction Kinetics
• Based on Bajpai & Reuss
kinetic model
• [Cell]max = [Glucose]min
• [Cell]min = [Glucose]max
• Stress fermenter 4
May 9, 2016
After 200 total hours, 50 g/L
of [Penicillin G] is achieved
15
SMITH
GROUP
GreenGene
Chemical Reaction Kinetics-Penicillin G
• 18th Hour [Substrate] = 0
growth is constant at a
maximum
• Batch Mode = 7 hours
• Stress = 50 hours
0
10
20
30
40
50
60
0 20 40 60 80 100 120 140
Concentration(g/L)
Time (hr)
Batch
Stress
May 9, 2016
What about the production goal?
Penicillin G Degradation Rate
• Penicillin degradation is a first
order reaction
• After 50 hours of stressing,
40g/L remains
• After 90 hours of stressing,
40g/L remains due to higher
degradation rate
A. Kheirolomoom et al., The combined effects of pH and
temperature on penicillin G decomposition and its stability
modeling Process Biochemistry.. 35: 205-211, 1999
16
SMITH
GROUP
GreenGene
Shorter time still yields the same amount of Penicillin G
v
ç pH 6.8
!"
!
!!
= −!"!
!"#!! = [!"#!!]!!!!.!!"#!!
!
May 9, 2016
0
10
20
30
40
50
60
0 2 4 6 8 10 12 14
PenicillinG(g/L)
pH
Sensitivity Analysis on pH
• [Penicillin G]max at pH 7
• Optimal operating range: 6.5-7.5
• pH 7 ± 2 yields only 80% [Penicillin G]max
• VERY SENSITIVE!!!!
17
SMITH
GROUP
GreenGene
Optimal pH during stressing is 6.5 – 7.5
Variation in pH has a significant impact
May 9, 2016
A. Kheirolomoom et al., The combined effects of pH and
temperature on penicillin G decomposition and its stability
modeling Process Biochemistry.. 35: 205-211, 1999
Example of Process Control
18
SMITH
Group
GreenGene
q Process Control Objective
• Provide oxygen to keep cells alive
• Maintain constant pH at 6.5
q Process Control Strategy
• Monitor the concentration of air and
pH level
• Implement a feed forward control loop
based on the kinetic model
May 9, 2016
Fermentation Campaign Diagram
19
SMITH
GROUP
GreenGene
Train 1
Train 2
Train 3
Train 4
1
2
3
4
1
2
3
4
3
4
3
4
q Number of Reactor Trains : 4
• Train 1,2 : fermenter 1, 2, 3, 4
• Train 3,4 : fermenter 3, 4
May 9, 2016
Achieved optimal operation schedule with reduced cost
Extraction
20
SMITH
Group
GreenGene May 9, 2016
See PFD: Process Sheet 3
Objective: Obtain a product with maximum percent yield
Extraction
21
SMITH
Group
GreenGene May 9, 2016
Water-rich MIBK Recovery
22
SMITH
Group
GreenGene May 9, 2016
See PFD: Process Sheet 4
Objective: Maintain economically and environmentally optimal
recovery of extraction solvent
Water-rich MIBK Recovery
23
SMITH
Group
GreenGene May 9, 2016
Optimization: Water-rich MIBK Recovery
24
SMITH
Group
GreenGene
0
200
400
600
800
1000
1200
0 10 20 30 40 50 60 70
moleMIBKtransferred(mole)
Time elapsed (min)
Optimal utilities cost achieved at 82% recovery
May 9, 2016
0
20,000
40,000
60,000
80,000
100,000
120,000
0 20 40 60 80 100 120
Cost($)
Percent Recovery (%)
"MIBK Markets and Analysis." Web. 09 May 2016.
MIBK-rich Solvent Recovery
25
SMITH
Group
GreenGene May 9, 2016
See PFD: Process Sheet 5
Objective: Maintain economically and environmentally optimal
recovery of extraction solvent
MIBK-rich Solvent Recovery
26
SMITH
Group
GreenGene May 9, 2016
IPA Solvent Recovery
27
SMITH
Group
GreenGene May 9, 2016
See PFD: Process Sheet 6
Objective: Maintain economically and environmentally optimal
recovery of extraction solvent
IPA Solvent Recovery
28
SMITH
Group
GreenGene May 9, 2016
Water and Biowaste Treatment
29
SMITH
Group
GreenGene May 9, 2016
See PFD: Utilities Sheet 1,2
Objective: Purify water to meet pharmaceutical standards / Treat
any waste produced by the plant to meet the EPA regulations
Water Treatment
30
SMITH
Group
GreenGene May 9, 2016
Biowaste Treatment
31
SMITH
Group
GreenGene May 9, 2016
Environmental and Health Issues
32
SMITH
Group
GreenGene
q Environmental Design Considerations
q Health Issues
May 9, 2016
Boiler
• Burn off-gas from fermenters and biodigestors
• Prevent toxic gas release to atmosphere
Biodigestors • Treat biowaste properly
EPA regulations
• Clean Air Act
• Waste effluent limitation
Protection of Plant
Personnel
• Personal protective equipment: eyewear, gloves, etc.
• Hazard communication trainings
Accident Prevention/
Emergency Response
• Toxicity detectors to indicate exposure
• In case of leakage
- Have the necessary clean up materials ready
- Have trained personnel to clean up the area
"US Environmental Protection Agency." US Environmental
Protection Agency. Web. 09 May 2016.
Safety Issues
33
SMITH
Group
GreenGene
q General Considerations
• Fire prevention
• Fire suppression
• Dust explosion prevention
q Greatest risk: Tornado
• Build underground shelter
• Emergency response plan
May 9, 2016
No significant safety concerns
A. Kheirolomoom et al., The combined effects of pH and
temperature on penicillin G decomposition and its stability
modeling Process Biochemistry.. 35: 205-211, 1999
34
SMITH
Group
GreenGene May 9, 2016
Plant Location
& Plant Layout
35
SMITH
Group
GreenGene May 9, 2016
Plant Location Considerations
• Proximity to major raw materials
– Corn steep liquor
• Ease of transportation for
materials/ equipment/ product
– Railroad, highway
• Weather conditions
– Tornado
Location: Fairfax, Iowa
Plant Layout Philosophy
36
SMITH
Group
GreenGene
q Safety
q Sufficient roadway
• Easy and efficient access to different units
q Strategic placement of unit operations
q Wind Direction
May 9, 2016
Plot Plan
37
SMITH
Group
GreenGene May 9, 2016
OSBL
38
SMITH
Group
GreenGene
Fire House
Warehouse
Control Room
Laboratory
Maintenance/equipment room
Administration Building
Main Process Building
Motor Control Center
Emergency Generator
Uninterrupted Power Supply
Switch Board
Fuel Gas Supply Drum
Instrument Air Compression
Backup Instrument Air Compression
Guard House
May 9, 2016
39
SMITH
Group
GREENGENE May 9, 2016
Constructability
Project Organization
40
SMITH
Group
GreenGene April 27, 2016
Project
Manager
Construction
Manager
Plumbing Civil Electrical
Project
Accountant
Engineering
Manager
Controls
Manager
Utilities
Manager
Process	Section	
Managers	
Fermenters
Managers
Downstream	
Manager
Solvent	
Recovery	
Manager
Commissioning	
Manager	
Safety	Manager
Quality
Inspectors
Constructability
41
SMITH
Group
GreenGene
Total time from planning to startup: 34 months
May 9, 2016
Labor Requirements
42
SMITH
Group
GreenGene
5 8 12
25
40
98
165
180
155
55
Q1 Q2 Q3 Q4 Q5 Q6 Q7 Q8 Q9 Q10
#ofLarborers
Quarter of Project TImeline
May 9, 2016
Maximum number of laborers = 200
Will not impact the surrounding city; labor need can be fulfilled
Startup and Shut Down Procedure
43
SMITH
Group
GreenGene April 27, 2016
Startup
1. Activate electrical system
2. Activate fire and water systems
3. Activate natural gas/
instrument
4. Fill Cooling-water system and
circulate
5. Activate air and steam systems
6. Turn on boiler
7. Start air compressors
8. Start feed to the biodigestor
9. Sterilize media using steam
10. Start up one fermenter train at
a time
Shut Down
1. Remove hazardous process
materials
2. Reroute streams to
designated area
3. Turn heat and coolant off
4. De-pressure the systems
5. Isolate the systems from other
processes
6. If shut down prolongs, protect
the equipmentfrom
deteriorating
No significant deviation from the standard procedure
44
SMITH
Group
GREENGENE May 9, 2016
Economic Analysis
ICARUS Summary Costs
45
SMITH
Group
GreenGene
Item Cost (MM$)
Equipment 9.0
Equipment Setting 0.34
Piping 5.4
Civil
(Building & Construction)
16
Steel 0.54
Instrumentation
(Model Base Controls)
7.0
Electrical 3.8
Insulation 0.44
Paint 0.45
Other 38
G and A Overheads 3.0
Owner’s Costs 6.6
Total Project Cost: $110 MM with 25 % contingency
May 9, 2016
Economic Analysis Breakdown
Item Cost ($MM)
Annual Amount of Product Sold 10,500 (MM of Doses)
Total Sales Revenue
(at .008 cent/dose)
84
Raw Material Cost 4.0
Variable Costs 4.0
Fixed Costs 6.5
Gross Margin 74
46
SMITH
Group
GreenGene
Operating ramp-up:
Initial Start Up: 50 % Capacity
Ramp up linearly to 100 % in year 5
Determining product price:
DCFROR: 18% (NPV: 0) in year 10 at 100% capacity
May 9, 2016
Economic Analysis Results
47
SMITH
Group
GreenGene
-120
-80
-40
0
40
80
120
-4 -2 0 2 4 6 8 10
CashFlow(MM$)
Year of Production
Pay Back Period: 3.7 Years
Cash Flow
Discounted Cash Flow
May 9, 2016
Assumptions:
Depreciation = 10%
Tax Rate = 38%
DCFROR = 18%
Cost/dose = $0.008/dose
Sensitivity Analysis - Controllable
48
SMITH
Group
GreenGene
0 0.002 0.004 0.006 0.008 0.01 0.012 0.014 0.016
Years until Full Capacity
Total Invested Capital
No. of Batches
Labor Cost
Cost per Dose ($)
Attention should be given to the number of failed batches
to ensure product price consistency
2 years
7 years
± 30%
- 5%
± 30%
May 9, 2016
VariableFactors
Sensitivity Analysis - Uncontrollable
49
SMITH
Group
GreenGene
0.0064 0.0069 0.0074 0.0079 0.0084 0.0089 0.0094
± 30%
± 10%
Attention should be given to the amount sold to ensure
product price consistency.
Cost per Dose ($)
Amount Sold
Fixed Cost
Raw Material Cost
± 30%
May 9, 2016
VariableFactors
Economic Analysis
50
SMITH
Group
GreenGene May 9, 2016
Total Project Cost: $110 MM
• Working Capital: $21.0 MMCost Summary
Price/dose at 18% DCFROR: $0.008
• Based on Penicillin G production
process
Pricing Strategy
No significant deviation
Insensitive overall, thus financially
robust
Sensitivity Analysis
Recommendations for FEL-3
51
SMITH
Group
GreenGene May 9, 2016
Recommendation for FEL-3
52
SMITH
Group
GreenGene
• Kinetic modeling based on GreenGene
• Revisit optimization and control strategy for solvent
recovery systems
• Products and in-process quality control sampling
May 9, 2016
Revalidate and modify the process based on GreenGene
Thank you
53
SMITH
Group
GreenGene May 9, 2016
Questions?
54
SMITH
Group
GreenGene May 9, 2016

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FEL-2 Feasibility Study: GreenGene Process is financially robust based on Penicillin G study

  • 1. FEL-2 Feasibility Study: GreenGene SMITH GROUP – Hayoung Lee, Soo Lee, Iyore Olaye, Sang Yoo School of Chemical and Biomolecular Engineering Cornell University Ithaca, NY 14853 May 8, 2016
  • 2. Table of Contents I. Project Statement II. Market Analysis III. Process Units IV. Plant Location and Plant Layout V. Constructability VI. Economic Analysis VII. Recommendation for FEL-3 2 SMITH Group GreenGene May 9, 2016
  • 3. Project Statement q Client: NanoBio Pharmaceuticals • New product : GreenGene (anti-hypertensive drug) • Modeled using Penicillin G production process q Objective • Capture 20% of the North American market after 5 years • Produce 120% of the estimated year five demand • Assumed dosage: 100mg/day q Determine • Capital and operating costs for the facility • Ex-plant price of GreenGene proxy 3 SMITH Group GreenGene May 9, 2016
  • 4. GreenGene Feasibility Study 4 SMITH Group GreenGene Process is financially robust based on Penicillin G study Proceed to FEL-3 Stage May 9, 2016 Location? Fairfax, Iowa Economic Analysis? Price per dose at 18% DCFROR: $0.008/dose Based on Penicillin G production process Average Competitive price per dose of hypertension API: $0.03/dose Total Project Cost: $110 MM Operating Cost: $21 MM Environmental Concerns? No significant environmental or safety concerns
  • 5. 5 SMITH Group GreenGene May 9, 2016 Market Analysis
  • 6. Market Analysis 6 SMITH Group GreenGene May 9, 2016 0.00 0.50 1.00 1.50 2.00 2.50 3.00 3.50 4.00 4.50 5.00 0 1 2 3 4 5 6 7 8 9 10 AmountofAnti-hypertensiveDrug(Tg) Years of Production 2019 q Target Market : North Americans with Hypertension q 100 mg dose per day q Economic Goals for GreenGene: • Capture 20 % of total market • Supply 120% of demand by year 5 Supply estimate served as a basis for equipment sizing and economic analysis throughout FEL-2 study Annual demand Annual supply High Blood Pressure Facts." Centers for Disease Control and Prevention. Centers for Disease Control and Prevention, 19 Feb. 2015. Web. 09 May 2016.
  • 7. 7 SMITH Group GreenGene May 9, 2016 Process Units
  • 9. Media Preparation 9 SMITH Group GreenGene May 9, 2016 See PFD: Process Sheet 1 Objective: Mix raw materials and sterilize the media without degrading nutrients
  • 11. Fermentation 11 SMITH Group GreenGene May 9, 2016 See PFD: Process Sheet 2 Objective: Purify air to meet pharmaceutical standards / Achieve desired concentration of titer through controlled reaction kinetics
  • 13. Reaction Basics 13 SMITH GROUP GreenGene Main Reaction : Cell + Glucose + O2 + PAA + (NH4)2SO4 à More Cells + Penicillin G + CO2 + H2O + Heat Penicillin G Penillic Acid Penicilloic Acid Degradation of Penicillin G (Side Reactions) : May 9, 2016 Birol, Gülnur, Cenk Ündey, and Ali Çinar. "A Modular Simulation Package for Fed-batch Fermentation: Penicillin Production." Computers & Chemical Engineering 26.11 (2002): 1553-565. Web.
  • 14. 0 50 100 150 200 250 300 350 400 450 500 0 50 100 150 200 Concentration(g/L) Time (hr) 14 SMITH GROUP GreenGene [Glucose] [Cell] [Penicillin G] Chemical Reaction Kinetics • Based on Bajpai & Reuss kinetic model • [Cell]max = [Glucose]min • [Cell]min = [Glucose]max • Stress fermenter 4 May 9, 2016 After 200 total hours, 50 g/L of [Penicillin G] is achieved
  • 15. 15 SMITH GROUP GreenGene Chemical Reaction Kinetics-Penicillin G • 18th Hour [Substrate] = 0 growth is constant at a maximum • Batch Mode = 7 hours • Stress = 50 hours 0 10 20 30 40 50 60 0 20 40 60 80 100 120 140 Concentration(g/L) Time (hr) Batch Stress May 9, 2016 What about the production goal?
  • 16. Penicillin G Degradation Rate • Penicillin degradation is a first order reaction • After 50 hours of stressing, 40g/L remains • After 90 hours of stressing, 40g/L remains due to higher degradation rate A. Kheirolomoom et al., The combined effects of pH and temperature on penicillin G decomposition and its stability modeling Process Biochemistry.. 35: 205-211, 1999 16 SMITH GROUP GreenGene Shorter time still yields the same amount of Penicillin G v ç pH 6.8 !" ! !! = −!"! !"#!! = [!"#!!]!!!!.!!"#!! ! May 9, 2016
  • 17. 0 10 20 30 40 50 60 0 2 4 6 8 10 12 14 PenicillinG(g/L) pH Sensitivity Analysis on pH • [Penicillin G]max at pH 7 • Optimal operating range: 6.5-7.5 • pH 7 ± 2 yields only 80% [Penicillin G]max • VERY SENSITIVE!!!! 17 SMITH GROUP GreenGene Optimal pH during stressing is 6.5 – 7.5 Variation in pH has a significant impact May 9, 2016 A. Kheirolomoom et al., The combined effects of pH and temperature on penicillin G decomposition and its stability modeling Process Biochemistry.. 35: 205-211, 1999
  • 18. Example of Process Control 18 SMITH Group GreenGene q Process Control Objective • Provide oxygen to keep cells alive • Maintain constant pH at 6.5 q Process Control Strategy • Monitor the concentration of air and pH level • Implement a feed forward control loop based on the kinetic model May 9, 2016
  • 19. Fermentation Campaign Diagram 19 SMITH GROUP GreenGene Train 1 Train 2 Train 3 Train 4 1 2 3 4 1 2 3 4 3 4 3 4 q Number of Reactor Trains : 4 • Train 1,2 : fermenter 1, 2, 3, 4 • Train 3,4 : fermenter 3, 4 May 9, 2016 Achieved optimal operation schedule with reduced cost
  • 20. Extraction 20 SMITH Group GreenGene May 9, 2016 See PFD: Process Sheet 3 Objective: Obtain a product with maximum percent yield
  • 22. Water-rich MIBK Recovery 22 SMITH Group GreenGene May 9, 2016 See PFD: Process Sheet 4 Objective: Maintain economically and environmentally optimal recovery of extraction solvent
  • 24. Optimization: Water-rich MIBK Recovery 24 SMITH Group GreenGene 0 200 400 600 800 1000 1200 0 10 20 30 40 50 60 70 moleMIBKtransferred(mole) Time elapsed (min) Optimal utilities cost achieved at 82% recovery May 9, 2016 0 20,000 40,000 60,000 80,000 100,000 120,000 0 20 40 60 80 100 120 Cost($) Percent Recovery (%) "MIBK Markets and Analysis." Web. 09 May 2016.
  • 25. MIBK-rich Solvent Recovery 25 SMITH Group GreenGene May 9, 2016 See PFD: Process Sheet 5 Objective: Maintain economically and environmentally optimal recovery of extraction solvent
  • 27. IPA Solvent Recovery 27 SMITH Group GreenGene May 9, 2016 See PFD: Process Sheet 6 Objective: Maintain economically and environmentally optimal recovery of extraction solvent
  • 29. Water and Biowaste Treatment 29 SMITH Group GreenGene May 9, 2016 See PFD: Utilities Sheet 1,2 Objective: Purify water to meet pharmaceutical standards / Treat any waste produced by the plant to meet the EPA regulations
  • 32. Environmental and Health Issues 32 SMITH Group GreenGene q Environmental Design Considerations q Health Issues May 9, 2016 Boiler • Burn off-gas from fermenters and biodigestors • Prevent toxic gas release to atmosphere Biodigestors • Treat biowaste properly EPA regulations • Clean Air Act • Waste effluent limitation Protection of Plant Personnel • Personal protective equipment: eyewear, gloves, etc. • Hazard communication trainings Accident Prevention/ Emergency Response • Toxicity detectors to indicate exposure • In case of leakage - Have the necessary clean up materials ready - Have trained personnel to clean up the area "US Environmental Protection Agency." US Environmental Protection Agency. Web. 09 May 2016.
  • 33. Safety Issues 33 SMITH Group GreenGene q General Considerations • Fire prevention • Fire suppression • Dust explosion prevention q Greatest risk: Tornado • Build underground shelter • Emergency response plan May 9, 2016 No significant safety concerns A. Kheirolomoom et al., The combined effects of pH and temperature on penicillin G decomposition and its stability modeling Process Biochemistry.. 35: 205-211, 1999
  • 34. 34 SMITH Group GreenGene May 9, 2016 Plant Location & Plant Layout
  • 35. 35 SMITH Group GreenGene May 9, 2016 Plant Location Considerations • Proximity to major raw materials – Corn steep liquor • Ease of transportation for materials/ equipment/ product – Railroad, highway • Weather conditions – Tornado Location: Fairfax, Iowa
  • 36. Plant Layout Philosophy 36 SMITH Group GreenGene q Safety q Sufficient roadway • Easy and efficient access to different units q Strategic placement of unit operations q Wind Direction May 9, 2016
  • 38. OSBL 38 SMITH Group GreenGene Fire House Warehouse Control Room Laboratory Maintenance/equipment room Administration Building Main Process Building Motor Control Center Emergency Generator Uninterrupted Power Supply Switch Board Fuel Gas Supply Drum Instrument Air Compression Backup Instrument Air Compression Guard House May 9, 2016
  • 39. 39 SMITH Group GREENGENE May 9, 2016 Constructability
  • 40. Project Organization 40 SMITH Group GreenGene April 27, 2016 Project Manager Construction Manager Plumbing Civil Electrical Project Accountant Engineering Manager Controls Manager Utilities Manager Process Section Managers Fermenters Managers Downstream Manager Solvent Recovery Manager Commissioning Manager Safety Manager Quality Inspectors
  • 41. Constructability 41 SMITH Group GreenGene Total time from planning to startup: 34 months May 9, 2016
  • 42. Labor Requirements 42 SMITH Group GreenGene 5 8 12 25 40 98 165 180 155 55 Q1 Q2 Q3 Q4 Q5 Q6 Q7 Q8 Q9 Q10 #ofLarborers Quarter of Project TImeline May 9, 2016 Maximum number of laborers = 200 Will not impact the surrounding city; labor need can be fulfilled
  • 43. Startup and Shut Down Procedure 43 SMITH Group GreenGene April 27, 2016 Startup 1. Activate electrical system 2. Activate fire and water systems 3. Activate natural gas/ instrument 4. Fill Cooling-water system and circulate 5. Activate air and steam systems 6. Turn on boiler 7. Start air compressors 8. Start feed to the biodigestor 9. Sterilize media using steam 10. Start up one fermenter train at a time Shut Down 1. Remove hazardous process materials 2. Reroute streams to designated area 3. Turn heat and coolant off 4. De-pressure the systems 5. Isolate the systems from other processes 6. If shut down prolongs, protect the equipmentfrom deteriorating No significant deviation from the standard procedure
  • 44. 44 SMITH Group GREENGENE May 9, 2016 Economic Analysis
  • 45. ICARUS Summary Costs 45 SMITH Group GreenGene Item Cost (MM$) Equipment 9.0 Equipment Setting 0.34 Piping 5.4 Civil (Building & Construction) 16 Steel 0.54 Instrumentation (Model Base Controls) 7.0 Electrical 3.8 Insulation 0.44 Paint 0.45 Other 38 G and A Overheads 3.0 Owner’s Costs 6.6 Total Project Cost: $110 MM with 25 % contingency May 9, 2016
  • 46. Economic Analysis Breakdown Item Cost ($MM) Annual Amount of Product Sold 10,500 (MM of Doses) Total Sales Revenue (at .008 cent/dose) 84 Raw Material Cost 4.0 Variable Costs 4.0 Fixed Costs 6.5 Gross Margin 74 46 SMITH Group GreenGene Operating ramp-up: Initial Start Up: 50 % Capacity Ramp up linearly to 100 % in year 5 Determining product price: DCFROR: 18% (NPV: 0) in year 10 at 100% capacity May 9, 2016
  • 47. Economic Analysis Results 47 SMITH Group GreenGene -120 -80 -40 0 40 80 120 -4 -2 0 2 4 6 8 10 CashFlow(MM$) Year of Production Pay Back Period: 3.7 Years Cash Flow Discounted Cash Flow May 9, 2016 Assumptions: Depreciation = 10% Tax Rate = 38% DCFROR = 18% Cost/dose = $0.008/dose
  • 48. Sensitivity Analysis - Controllable 48 SMITH Group GreenGene 0 0.002 0.004 0.006 0.008 0.01 0.012 0.014 0.016 Years until Full Capacity Total Invested Capital No. of Batches Labor Cost Cost per Dose ($) Attention should be given to the number of failed batches to ensure product price consistency 2 years 7 years ± 30% - 5% ± 30% May 9, 2016 VariableFactors
  • 49. Sensitivity Analysis - Uncontrollable 49 SMITH Group GreenGene 0.0064 0.0069 0.0074 0.0079 0.0084 0.0089 0.0094 ± 30% ± 10% Attention should be given to the amount sold to ensure product price consistency. Cost per Dose ($) Amount Sold Fixed Cost Raw Material Cost ± 30% May 9, 2016 VariableFactors
  • 50. Economic Analysis 50 SMITH Group GreenGene May 9, 2016 Total Project Cost: $110 MM • Working Capital: $21.0 MMCost Summary Price/dose at 18% DCFROR: $0.008 • Based on Penicillin G production process Pricing Strategy No significant deviation Insensitive overall, thus financially robust Sensitivity Analysis
  • 52. Recommendation for FEL-3 52 SMITH Group GreenGene • Kinetic modeling based on GreenGene • Revisit optimization and control strategy for solvent recovery systems • Products and in-process quality control sampling May 9, 2016 Revalidate and modify the process based on GreenGene