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Consultancy.
Project Delivery.
Innovation.
Case Study: Resin Reactor Vent Analysis
Detailed assessment of reacting two-phase relief
Client: Top Tier COMAH Phenolic Resin Manufacturer
Who are we?
Process engineering consultancy
Specialising in advanced modelling techniques, to give answers that
are more accurate, reliable and robust
Decades of process and mechanical engineering experience
Combine cutting edge simulation with real world understanding, to
provide you with solutions that are effective and practical.
Core team of eight engineers, supported by a wide network of
associates.
Page  2
Project Background
Top tier COMAH site
HSE Regulator questions mechanical integrity of reactor emergency vent
system to withstand a full relief event
Original mechanical calculations no longer available
No process flows to support pipe work dynamic assessment, likely to be
two phase reacting flow
Client no longer has access to internal process/mechanical expertise
Flex Process brought in to help address HSE action
Page  3
Our Responsibilities
Page  4
Site Survey of vessels, pipes and catchment tank
Complete two phase relief calculations to generate process flows
Build pipe stress models for each reactor system and assess against
pipe code (ASME) for thermal, sustained and dynamic cases
Complete vessel nozzle strength calculations
Report findings and agree way forward
Site Survey
Page  5
General Arrangement
Drawing
Site Measurements
Research Site Data
Records
Two Phase Flow Modelling
Use own in-house DIERS based software to calculate two
phase flow through vent lines
Use detailed mechanical survey data
Use physical properties for phenol, water, formaldehyde, resin in
calculations
Input actual calorimetry data
Worst case static or dynamic flow outputs
Flows, temperatures and pressures at various points within vent system
to support detailed pipe stress modelling
Page  6
Process Data Output
Page  7
Pipe Stress Engineering
Page  8
CAESAR II Simulations
Main Conclusions
Significant deviations in thermal, sustained and dynamic cases from the
ASME design code. Simple changes not possible.
Original designs had limited pipe stress analysis, some were site run
Insufficient allowance for pipe thermal expansion (e.g. straight runs)
Incorrectly specified pipe bellows
Insufficient pipe supports for dynamic loads, such as disk rupture
Weak nozzles on heat exchangers, reactors and catchment tank
No supporting calculations for catchment tank foundations
Page  9
Proposal for Redesign
Redesign vent pipe runs to allow for thermal expansion, minimise
bellows on wetted duty
Install new pipe bellows designed to withstand movement on reactor
nozzles
Change heat exchanger heads with stronger nozzles
Install special pipe supports to withstand dynamic loads
Change catchment tank instead of making repairs to weak nozzles and
adopt new centrifugal design for more effective separation
Page  10
Redesign Proposal
Page  11
Detailed Proposal Drawings
New Vessel General Arrangement Drawings
Redesign, Estimate and Programme
Redesign proposal developed in drawings incorporating all the required
changes
Fully checked out proposals through additional site survey, pipe stress
analysis and two phase relief calculations to ensure that relief capacity
not compromised
New, more flexible pipe specification developed that minimises the
requirement for bellows
Detailed capital cost estimate for changes
Installation programme developed, which minimises disruption to
operations
Suggestions made to optimise vent size through further scenario
analysis
Page  12
Summary
Client had a complex problem involving the HSE
Through a mix of process and mechanical in-house expertise, the
analysis could be completed effectively
Findings were clearly reported and a way forward discussed
Fully checked out redesign completed, costed and installation
programme devised that minimised disruption
Deliverables produced that could be used to support discussions with
HSE regulator
Page  13
Summary
Page  14
Consultancy.
Project Delivery.
Innovation.
Please get in touch to find out how we can help your
business today.
E: enquiries@flexprocess.co.uk W: flexprocess.co.uk
T: +44 1454 629 689

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Resin Reactor Vent Analysis Case Study

  • 1. Consultancy. Project Delivery. Innovation. Case Study: Resin Reactor Vent Analysis Detailed assessment of reacting two-phase relief Client: Top Tier COMAH Phenolic Resin Manufacturer
  • 2. Who are we? Process engineering consultancy Specialising in advanced modelling techniques, to give answers that are more accurate, reliable and robust Decades of process and mechanical engineering experience Combine cutting edge simulation with real world understanding, to provide you with solutions that are effective and practical. Core team of eight engineers, supported by a wide network of associates. Page  2
  • 3. Project Background Top tier COMAH site HSE Regulator questions mechanical integrity of reactor emergency vent system to withstand a full relief event Original mechanical calculations no longer available No process flows to support pipe work dynamic assessment, likely to be two phase reacting flow Client no longer has access to internal process/mechanical expertise Flex Process brought in to help address HSE action Page  3
  • 4. Our Responsibilities Page  4 Site Survey of vessels, pipes and catchment tank Complete two phase relief calculations to generate process flows Build pipe stress models for each reactor system and assess against pipe code (ASME) for thermal, sustained and dynamic cases Complete vessel nozzle strength calculations Report findings and agree way forward
  • 5. Site Survey Page  5 General Arrangement Drawing Site Measurements Research Site Data Records
  • 6. Two Phase Flow Modelling Use own in-house DIERS based software to calculate two phase flow through vent lines Use detailed mechanical survey data Use physical properties for phenol, water, formaldehyde, resin in calculations Input actual calorimetry data Worst case static or dynamic flow outputs Flows, temperatures and pressures at various points within vent system to support detailed pipe stress modelling Page  6
  • 8. Pipe Stress Engineering Page  8 CAESAR II Simulations
  • 9. Main Conclusions Significant deviations in thermal, sustained and dynamic cases from the ASME design code. Simple changes not possible. Original designs had limited pipe stress analysis, some were site run Insufficient allowance for pipe thermal expansion (e.g. straight runs) Incorrectly specified pipe bellows Insufficient pipe supports for dynamic loads, such as disk rupture Weak nozzles on heat exchangers, reactors and catchment tank No supporting calculations for catchment tank foundations Page  9
  • 10. Proposal for Redesign Redesign vent pipe runs to allow for thermal expansion, minimise bellows on wetted duty Install new pipe bellows designed to withstand movement on reactor nozzles Change heat exchanger heads with stronger nozzles Install special pipe supports to withstand dynamic loads Change catchment tank instead of making repairs to weak nozzles and adopt new centrifugal design for more effective separation Page  10
  • 11. Redesign Proposal Page  11 Detailed Proposal Drawings New Vessel General Arrangement Drawings
  • 12. Redesign, Estimate and Programme Redesign proposal developed in drawings incorporating all the required changes Fully checked out proposals through additional site survey, pipe stress analysis and two phase relief calculations to ensure that relief capacity not compromised New, more flexible pipe specification developed that minimises the requirement for bellows Detailed capital cost estimate for changes Installation programme developed, which minimises disruption to operations Suggestions made to optimise vent size through further scenario analysis Page  12
  • 13. Summary Client had a complex problem involving the HSE Through a mix of process and mechanical in-house expertise, the analysis could be completed effectively Findings were clearly reported and a way forward discussed Fully checked out redesign completed, costed and installation programme devised that minimised disruption Deliverables produced that could be used to support discussions with HSE regulator Page  13
  • 14. Summary Page  14 Consultancy. Project Delivery. Innovation. Please get in touch to find out how we can help your business today. E: enquiries@flexprocess.co.uk W: flexprocess.co.uk T: +44 1454 629 689