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REBOILERS IN PROCESS INDUSTRIES
Presented By:
Jay Jawalge (11920039)
Rupali Kadam (11920081)
Karthik Iyer (11810069)
Payal Khandagale (11920014)
Arjun Phad (11920021)
Group 7 1
Content
• Reboiler
• Types of reboiler
• Choice of type
• Selection factors of reboiler type
• Variables influence boiler design
• Advantages & disadvantages
• Case study
• Conclusion
• References
Group 7 2
REBOILER: Heat Exchanger
• Used with distillation columns to vaporise a
fraction of the bottom product
• Provide vapor flow up a column and acts as an
additional theoretical stage below the
trays/packing
Group 7 3
Fig. 2, Industrial reboiler, Ref. [2]
Fig. 1, Schematic of industrial reboiler, Ref. [1]
Group 7 4
Continued…
Types of reboilers
• Forced circulation
• Natural circulation (Thermosyphon)
• Kettle Type
Group 7 5
Fig. 3, Classification of reboiler
Forced Circulation Reboiler
• Designed to operate liquid
full
• Flashing occur as the liquid
crosses the control valve
• Valve should be located
close to the column shell
• Offer greater flexibility than
thermosyphons
• Elevation is less critical due
to pump and control valve Group 7 6
Fig. 4, Vertical Forced circulation reboiler
Continued…
Group 7 7
Fig. 5, Horizontal forced circulation reboiler
Thermosyphon reboilers
• Return piping to the
column must be sized for
two-phase flow
• Operates on
thermodynamic
principles, rather than
gravity
• Design detail is important
• Operation is simple, but
difficult to design for a
wide operating range
• Proper elevation is critical
Group 7 8
Fig. 6, Vertical thermosyphon reboiler
Continued…
Group 7 9
Fig. 7, Horizontal thermosyphon reboiler
Fig. 8, Horizontal industrial thermosyphon reboiler
Kettle Type reboilers
• Vapor-Liquid disengagement
occurs in the vapor space,
therefore return piping is
sized for all-vapor flow.
• Proper elevation is critical
to kettle reboiler operation.
• Kettles have a large
footprint, but require less
elevation than a
thermosyphon.
• Works by gravity, rather
than thermodynamics.
Group 7 10
Fig. 9, Kettle reboilerc
Internal reboiler
• Boiling takes place in the
pool of liquid at the bottom
of the tower
• Boiler in conventional
distillation column
• Distillation column size gives
the limitations
• Part of every distillation
column
Group 7 11Fig. 10, Internal reboilercc
Choice of type
Group 7 12
Fig. 11, Choice of type of reboilers, [3]
Selection factors of Reboiler Type
• Cleanability (Fouling)
• Corrosion
• Pressure
• Temperatures
• Heating medium
• Boiling fluid characteristics
Group 7 13
Variables that influence the reboiler
design
• Pressure drop (pressure gradient)
• Mass velocity
• Flow pattern (parallel, cross, counter types)
• Tubes orientation (vertical or horizontal)
• Critical heat flux condition
• Thermal hydraulics
• Reboiler duty
Group 7 14
Advantages & Disadvantages
Group 7 15
Case Study: Evaluation of reboiler temperature
retention time on MEG degradation products at
varying MEG concentrations
Paper specification
 Year of publication: 31
July 2020
 Journal: Journal of
Petroleum Science and
Engineering
Key words
 MEG: Mono Ethylene
Glycol
 Thermodynamic hydrate
inhibitor
Group 7 16
Problem statement
• MEG thermal degradation process can occur due to
dissociation to organic acids including glycolic, acetic
and formic acids.
Group 7 17
Fig. 12, Ref[6] Proposed dissociation products of ethylene glycol within oxygen
contamination under high temperature conditions
Methodology
1. Stock solution preparation
2. Distillation system
3. MEG concentration measurement (Refractometer)
4. Distillation calculations (9 internal configuration)
Group 7 18
Group 7 19
Fig. 12, Distillation setup
Result and discussion
1. Effect of the reboiler temperature retention time on MEG
degradation products
Group 7 20
MEG degradation product increase percentage for different MEG concentrations
Continued…
2. Effect of the reboiler temperature on the total organic
acids accumulation
Group 7 21
Conclusion
• Operating the reboiler at higher temperatures to
achieve better separation by removing surplus water
and produce high purity lean MEG for offshore
recycling and reinjection at the wellhead
• However, this process results in an increase of
degraded MEG and will require further new
quantities of MEG to compensate the degraded MEG
Group 7 22
Reference
[1] Parisher, R. A., & Rhea, R. A. (2012). Mechanical
Equipment. Pipe Drafting and Design, 112–133.
doi:10.1016/b978-0-12-384700-3.00006-2
[2]https://www.arab-oil-naturalgas.com/what-are-reboiler-
types/
[3] wp.auburn.edu
[4] doi: 10.1615/AtoZ.r.reboilers
[5] doi:https://doi.org/10.1016/j.petrol.2020.107735
Group 7 23
[6] ROSSITER JR, W. J., BROWN, P. W. & GODETTE, M.
1983. The determination of acidic degradationproducts
in aqueous ethylene glycol and propylene glycol
solutions using ion chromatography. Solar Energy
Materials, 9, 267-279.
Group 7 24
Continued…
THANK YOU
Group 7 25

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reboiler in process industry.

  • 1. REBOILERS IN PROCESS INDUSTRIES Presented By: Jay Jawalge (11920039) Rupali Kadam (11920081) Karthik Iyer (11810069) Payal Khandagale (11920014) Arjun Phad (11920021) Group 7 1
  • 2. Content • Reboiler • Types of reboiler • Choice of type • Selection factors of reboiler type • Variables influence boiler design • Advantages & disadvantages • Case study • Conclusion • References Group 7 2
  • 3. REBOILER: Heat Exchanger • Used with distillation columns to vaporise a fraction of the bottom product • Provide vapor flow up a column and acts as an additional theoretical stage below the trays/packing Group 7 3
  • 4. Fig. 2, Industrial reboiler, Ref. [2] Fig. 1, Schematic of industrial reboiler, Ref. [1] Group 7 4 Continued…
  • 5. Types of reboilers • Forced circulation • Natural circulation (Thermosyphon) • Kettle Type Group 7 5 Fig. 3, Classification of reboiler
  • 6. Forced Circulation Reboiler • Designed to operate liquid full • Flashing occur as the liquid crosses the control valve • Valve should be located close to the column shell • Offer greater flexibility than thermosyphons • Elevation is less critical due to pump and control valve Group 7 6 Fig. 4, Vertical Forced circulation reboiler
  • 7. Continued… Group 7 7 Fig. 5, Horizontal forced circulation reboiler
  • 8. Thermosyphon reboilers • Return piping to the column must be sized for two-phase flow • Operates on thermodynamic principles, rather than gravity • Design detail is important • Operation is simple, but difficult to design for a wide operating range • Proper elevation is critical Group 7 8 Fig. 6, Vertical thermosyphon reboiler
  • 9. Continued… Group 7 9 Fig. 7, Horizontal thermosyphon reboiler Fig. 8, Horizontal industrial thermosyphon reboiler
  • 10. Kettle Type reboilers • Vapor-Liquid disengagement occurs in the vapor space, therefore return piping is sized for all-vapor flow. • Proper elevation is critical to kettle reboiler operation. • Kettles have a large footprint, but require less elevation than a thermosyphon. • Works by gravity, rather than thermodynamics. Group 7 10 Fig. 9, Kettle reboilerc
  • 11. Internal reboiler • Boiling takes place in the pool of liquid at the bottom of the tower • Boiler in conventional distillation column • Distillation column size gives the limitations • Part of every distillation column Group 7 11Fig. 10, Internal reboilercc
  • 12. Choice of type Group 7 12 Fig. 11, Choice of type of reboilers, [3]
  • 13. Selection factors of Reboiler Type • Cleanability (Fouling) • Corrosion • Pressure • Temperatures • Heating medium • Boiling fluid characteristics Group 7 13
  • 14. Variables that influence the reboiler design • Pressure drop (pressure gradient) • Mass velocity • Flow pattern (parallel, cross, counter types) • Tubes orientation (vertical or horizontal) • Critical heat flux condition • Thermal hydraulics • Reboiler duty Group 7 14
  • 16. Case Study: Evaluation of reboiler temperature retention time on MEG degradation products at varying MEG concentrations Paper specification  Year of publication: 31 July 2020  Journal: Journal of Petroleum Science and Engineering Key words  MEG: Mono Ethylene Glycol  Thermodynamic hydrate inhibitor Group 7 16
  • 17. Problem statement • MEG thermal degradation process can occur due to dissociation to organic acids including glycolic, acetic and formic acids. Group 7 17 Fig. 12, Ref[6] Proposed dissociation products of ethylene glycol within oxygen contamination under high temperature conditions
  • 18. Methodology 1. Stock solution preparation 2. Distillation system 3. MEG concentration measurement (Refractometer) 4. Distillation calculations (9 internal configuration) Group 7 18
  • 19. Group 7 19 Fig. 12, Distillation setup
  • 20. Result and discussion 1. Effect of the reboiler temperature retention time on MEG degradation products Group 7 20 MEG degradation product increase percentage for different MEG concentrations
  • 21. Continued… 2. Effect of the reboiler temperature on the total organic acids accumulation Group 7 21
  • 22. Conclusion • Operating the reboiler at higher temperatures to achieve better separation by removing surplus water and produce high purity lean MEG for offshore recycling and reinjection at the wellhead • However, this process results in an increase of degraded MEG and will require further new quantities of MEG to compensate the degraded MEG Group 7 22
  • 23. Reference [1] Parisher, R. A., & Rhea, R. A. (2012). Mechanical Equipment. Pipe Drafting and Design, 112–133. doi:10.1016/b978-0-12-384700-3.00006-2 [2]https://www.arab-oil-naturalgas.com/what-are-reboiler- types/ [3] wp.auburn.edu [4] doi: 10.1615/AtoZ.r.reboilers [5] doi:https://doi.org/10.1016/j.petrol.2020.107735 Group 7 23
  • 24. [6] ROSSITER JR, W. J., BROWN, P. W. & GODETTE, M. 1983. The determination of acidic degradationproducts in aqueous ethylene glycol and propylene glycol solutions using ion chromatography. Solar Energy Materials, 9, 267-279. Group 7 24 Continued…