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PRIMARY 
CONTINUOUS 
PROCESS 
UPGRADE
Shamai Cylich, Arcadis, Sr. Project Manager
Scott Cheeseman, GSK, Sr. Process Engineer
Steve Walter Hargrove Life Sciences, Process 
Technology Leader 
PRESENTATION OUTLINE
• Scott
Process Design Development
• Steve
Facility Design Development
• Shamai
Project Management
Closing
PROJECT BACKGROUND
• Process development trends – exploring flow chemistry 
by first intent
• Benefits of continuous processing
• Bridge to commercial facilities
• Existing/limited facilities footprint – for batch equipment
• Single known user requirement:  Agile flexibility!
• Designing to a vision
Project Drivers in Pilot Plant Environment
Known Challenges
PROCESS DESIGN DEVELOPMENT
• Smaller facilities footprint for equal capacity
• Lower energy requirements for heat transfer
• Lower solvent requirements
• Improved control of energetic reactions
• EHS improvements – smaller quantities at any given time
All understood – just no Pilot Plant capability
Expected Benefits – The Basics
PROCESS DESIGN DEVELOPMENT
BATCH CONTINUOUS
PROCESS DESIGN DEVELOPMENT
Safety
Flammables
Containment 
Personal 
Protection
Process Safety
Flexibility
Unit 
Operations
Equipment 
Train 
Breakdown/ 
Turn‐around
Access to 
Utilities
CONSIDERATIONS
PROCESS DESIGN DEVELOPMENT
• Flow chemistry equipment is available
• Examples of lab set‐ups are common
• Examples of large commercial set‐ups are common
• Pilot Plant Space not well defined….at least for this project
• Agile Flexibility
Early Lessons Learned
PROCESS DESIGN DEVELOPMENT
• Delivery of raw materials, collection of product and 
waste solutions
• Utility needs
• Typical safety needs
• Typical footprint of equipment – is a typical space 
acceptable for all equipment (modular?)
• Flexible automation 
• Technical transfer requirements
Understand the (Every) Process
PROCESS DESIGN DEVELOPMENT
Models
PROCESS DESIGN DEVELOPMENT
Models
PROCESS DESIGN DEVELOPMENT
Models
UTILITY 
REQUIREMENTS
PHYSICAL 
LIMITATIONS
BLAST 
CONSTRAINTS
FLEXIBLE 
DESIGN
PACKAGED 
SYSTEMS
FACILITY DESIGN DEVELOPMENT
• EXISTING
• Breathing Air
• Process Water
• Nitrogen 10#
• Nitrogen 85#
• Plant Steam 
• Condensate
• HTF S/R
• Process Vent
• Hydraulic Fluid
• WFO 
UTILITY REQUIREMENTS
Adjacent 
Processes – In 
Use
Shut downs &
Planning across 
multiple projects 
simultaneous
Survey 
Confirmation
Min Qualified 
Systems
PID           Field 
ELIMINATED 
FACILITY DESIGN DEVELOPMENT
UTILITY REQUIREMENTS
BATCH  CONTINUOUS 
Plant Steam & 
Condensate 
Hydraulic Sys 
(Agitators)
Existing HTF 
Sys: Syltherm
‐25C to 160C
Required 
Multiple 
Simultaneous 
Differing 
Temps
Limited 
Temp Range
Single 
Source
FACILITY DESIGN DEVELOPMENT
UTILITY REQUIREMENTS
BATCH  CONTINUOUS 
• Limited HE Area
• Scale Up‐ Space
• Larger Volume 
Rinse / Chase
• Process Water
• Surface Area to 
Volume Ratio 
Increase
• Scale Up In Place
• Min Volume 
Rinse / Chase
FACILITY DESIGN DEVELOPMENT
PHYSICAL CONSTRAINTS
32 Process 
Conn
HT Kit (3x)
Duct, Data, 
Drain, 
Sprinkler
FACILITY DESIGN DEVELOPMENT
PHYSICAL CONSTRAINTS
127.5” To 
Underside
104.5” 
Process 
Plant 
23” of 
Clearance
‐ Exhaust Duct
‐ Sprinkler
‐ Wire Duct
‐ HTF S/R
‐ Cooling Water
‐ N10, N85, 
&N500
‐ Vent
‐ CA
FACILITY DESIGN DEVELOPMENT
PHYSICAL CONSTRAINTS
Valve & 
Instr Access
Electrical 
Clearances
Mechanical 
Access
FACILITY DESIGN DEVELOPMENT
• BEFORE
PHYSICAL CONSTRAINTS
~16’ X 16’ Area:
• 2 – 50 & 2 – 200 
Gallon GL Rx
• 2 – Hydraulic Ag
• Jkt Circulation 
Pumps
• Jkt HX
• Condenser 
4 Reactor 
Bays – Thru 
Floor
Delta V 
MCP
FACILITY DESIGN DEVELOPMENT
• AFTER
PHYSICAL CONSTRAINTS
~16’ X 16’ Area:
• 8 Vessels – upto
1600L (350 G)
• Supply Materials 
Product and Waste 
Collection
• 4 – Utility Panels
• 4 – Filter Stations 
and Automated 
Valve Panels w/ 4 
future spaces avail
• LEVs
FACILITY DESIGN DEVELOPMENT
• Analysis Provided:
• Wall 
• Floors 
• Relief Panels 
BLAST ANALYSIS
Blast Hazard Analysis and 
Preliminary Dynamic 
Structural Analysis
Quantify Any Structural or 
Near Yield Hazards
Adequate for 
Intended 
Operations
Doors
EXCEPT:
Unable to 
Confirm 
Existing Door 
Design 
FACILITY DESIGN DEVELOPMENT
• Enclosure Components not 
Electrically Classified
• Raw Material / Product 
Staged in Adjacent Area
ADDITIONAL SAFETY /HAZARD
Hazard Area 
Classification
HAC
Vessel Design
• Tipping Calcs
• Not Plausible
Mechanical Design
• LEL Detection
• Secondary 
Containment
• Max Door Opening
FACILITY DESIGN DEVELOPMENT
• FLEXIBILITY
• Utility Panels
• Transfer Panels
• Hose 
Connections/Management 
• 360 Access for entire plant
• CONSIDERATIONS
• Consistent Design
• Utilize similar 
components
• Organization
FLEXIBLE DESIGN
Adapt to Future Needs 
of Continuous 
Processing
FACILITY DESIGN DEVELOPMENT
FLEXIBLE DESIGN
FACILITY DESIGN DEVELOPMENT
• Panel Design
• Compact 
• Single Source
• Experience 
• Benefits
• Consistency
• Standardized Approach
• Design portion 
completed for future 
install
PACKAGED SYSTEMS
FACILITY DESIGN DEVELOPMENT
• Transfer Hoses & Panels
• Compact 
• Minimum Floor Space
PACKAGED SYSTEMS
FACILITY DESIGN DEVELOPMENT
• Hose 
• Location 
• Visual 
• Separated
HOSE MANAGEMENT
PROJECT MANAGEMENT
• PM 101 – Deliver project on time, in budget, and 
meeting all functional requirements
• 1st of its kind – didn't really know what we had or 
how best to utilize
• No precedent for pilot plant design…many design 
evolutions
• Schedule – very aggressive…. at first 6‐9 months
• As the team grasped the larger potential we 
realized it was better to get it right than to 
rush…more budget and 2 years to implement.
SCHEDULE
PROJECT MANAGEMENT
• Performing renovations in an operating plant –
windows for shutdowns, dust control, etc.
• Took out the batch reactors, pulled up acid brick floor, 
closed floor openings laid new ESD epoxy flooring.
• Change paradigm of space utilization – (re)connect 
accessibility and increased visibility for the operators.
RETROFIT CONCERNS
PROJECT MANAGEMENT
Mockups
Mock‐up for VIP Tour
Rough Scale Mock‐up
Final True‐Scale Mock‐up
PROJECT MANAGEMENT
Risk Management 
HAZOP
Concept Design, Design 
Complete and Construction
Limited to CP, 
Utility and 
Infrastructure
PRA’s specific 
to chemistry 
EHS, Auto, 
Proc Eng, 
Ops, PM
226 Action 
Items
• Established VWP early
• Developed Project Master Validation Plan early start 
but took a while to complete.
• Challenges:
• URS was purposely not defined at beginning of 
project….rather it evolved as the team grasped the 
capabilities of the technology and how to apply it.
• Automation – Delta V was a GMP qualified system, 
project was able to segregate the work‐in‐progress 
from the existing qualified system.
PROJECT MANAGEMENT
CQV 
PROJECT MANAGEMENT
CQV 
VALIDATION PLAN
DELTA V ‐ CC (QA)
SFAT 
PROCONE
HFAT ACI
Utilities & Infrastructure Demolition / 
Construction (GEP & GMP)
Facility & Utility Commissioning (GEP)
FCPP FAT 
Zeton
Shipping
Install Process Plant        
GSK UP
Loop Checks     
QA
Calibrattion
QA
Process Commissioning    
(Pre‐GMP)
SubstantialCompletion for NON‐GMP 
Operation 15‐Aug‐2016
IQ/OQ ‐ Software & 
Hardware Finalize & 
Execute (QA)
Shipping
• Key component of the Commissioning effort
• HFAT – new control panels ‐ locally
• SFAT – software configuration and graphics ‐ locally 
• Process FAT – shipped control panel and Delta V server 
with the program files to Mfr facility.
• We learned a lot during the 2 week FAT about what we 
had purchased!!
FATs
PROJECT MANAGEMENT
FAT ‐ Process
PROJECT MANAGEMENT
Continuous Plant Electrical/Control Panels Smoke testing
Installation 
PROJECT MANAGEMENT
Skid Arrived!!
Just fit through the roll door
• Site Commissioning  – essentially a repeat of the 
FAT…learn by repetition!
• The team was getting very proficient at using their 
new toy!
• Current Status – Cx complete – ready for 
development work.
• Qualification will be executed once a specific GMP 
campaign is scheduled.
Installation 
PROJECT MANAGEMENT
Installation  ‐ Before
PROJECT MANAGEMENT
2nd Floor 1st Floor
Installation  ‐ After
PROJECT MANAGEMENT
2nd Floor – North Wall 1st Floor
Primary Continuous Processing Retrofit

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