Notes
Slide Show
Outline
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CSChE 2002, Thermal Pinch Analysis

  • Energy Reduction
  • Cost-effectiveness of Process Simulation and Pinch analysis


  • Chris Connaghan, P.Eng., Duncan Industrial
  • Gaétan Noël, M.Sc. Eng., Pragmathic
  • Larry Wasik, P. Eng., Aurel Systems
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Why should I use Process
Simulation and Pinch analysis ?
  • Often heard reasons for lack of interest:
    • Too expensive: it generates no savings by itself and has no payback !
    • We do not need that, we already know what to do ...
    • Energy efficiency is often not profitable, paybacks are always much longer than the studies indicate !
    • Our processes change continuously, any study results will only be valid over a few months period
      • As a consequence, payback of installed projects takes longer


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The Context
  • Mills are complex with many interrelated systems
  • Energy savings in one department may simply cause additional energy usage in another department
  • Improving energy efficiency in a major way needs a dedicated approach
  • This approach is Computer Simulation and Pinch analysis
    • Many case studies can now show the benefits of this expertise
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Process Simulation
of an Entire Pulp and Paper Mill
  • It is now possible to simulate a complex integrated mill with a single computer simulation
  • The energy saving of a given project can be determined rigorously
    • all interactions between the different components of the process are taken into account by the simulation
    • high level of confidence for the predicted energy savings
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Cadsim+ Simulation of a TMP  Mill 
Entire Mill Requires 4 AO Drawings
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Process Simulation and Pinch Analysis deliver fast Paybacks
  • Precise information provided by the process simulation
    • It gives information on the energy efficiencies of your processes, equipments and unit operations
    • It allows the identification of problems that can often be easily and cheaply solved
  • The approach and thinking process governing the streams selection for the Pinch analysis study generates many profitable findings


    • Some examples to come
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Process Simulation and Pinch Analysis deliver fast Paybacks
  • In consequence, the study itself has its own payback
    • Short payback of a few months
  • Based on the authors’ experience, there has been no exception to this rule so far for any mill
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Example 1 - TMP mill in BC Quesnel River Pulp, 2001
  • The process simulation has shown:
    • Severe fouling of the heat exchanger used for effluent cooling by energy recovery
      • Exchanger cleaned
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Example 2 - TMP mill in BC (Quesnel River Pulp), 2001
  • The process simulation has shown:
    • Severe fouling of the TMP reboiler
      • Reboiler retubing has been done
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Example 3 - TMP mill in BC Quesnel River Pulp, 2001
  • From the Pinch Analysis streams data extraction phase:
    • Fresh water can be displaced by ww for the chips impregnation on TMP lines 1 and 2





  • •savings around 200k$/yr
  • • very cheap project
  • • refunds the study
  • within a few months
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Example 4 - TMP mill in BC (Quesnel River Pulp), 2001
  • From the Pinch analysis streams data extraction phase:
    • Excess pressurized contaminated TMP steam from any of the 3 lines can be sent into
    • the chip bins of any other
    • line when fresh steam is
    • consumed
    • Savings around 650 k$/yr
    • with a very small payback
    • Precise contaminated
    • steam balance helps greatly
    • to catch these opportunities
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Example 5 - Another TMP Mill
in BC, 2001
  • From the Pinch Analysis streams data extraction phase:
    • Possible to recycle a
    • reclaim screen effluent
    • to the chip washer
  • Confirmed with the process simulation
  • Very cheap modification
  • with savings around
  • 150 k$/yr


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Precise Methodology          
=Precise Payback
  • Example 6: TMP clear ww cooling by energy recovery: air preheating of the pulp flash dryers
    • The following project had been submitted to management
    • Savings given were around 780 k$/yr
    • Anticipated payback of 13 months
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Precise Methodology
= Precise Payback
  • Process simulation shows that only 25% of estimated savings would happen
    • Cooler ww means less steam generated by the refiners
    • Cooler ww reduces the existing amount of energy already recovered from the TMP


  • Now the corrected payback requires 52 months instead of 13 months !!
  • This is an example where a waste of capital can be avoided
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Precise Methodology
= Precise Payback
  • Question: what is the minimum ww temperature that can be set with no penalty to the energy recovery potential ?
  • Pinch Analysis can answer such a difficult question using composite curves
  • Capital cost can even be
  • assessed ahead of
  • any design!!
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Precise Methodology
= Precise Payback
  • Pinch Analysis can then be used to correctly identify the profitable options to cool ww
  • With the correct evaluation of the savings using the computer simulation
  • The computer simulation output is used to modify the streams’ data set used for the Pinch analysis
    • next slide: example
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Precise Methodology
= Precise Payback
  • Computer Simulation is used to modify the streams’ data set for the Pinch Analysis
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Do you really know what are your best options ?
  • Example 7: TMP Pulp Mill in BC
    • Steam boiler feedwater preheating often on the wish list of all mills
    • What about if you can shut the boiler off 1 or reduce its load drastically within a 1 yr payback ?
    • Pinch analysis and computer simulation can avoid a waste of capital expenditure




    • Note 1 : Obviously, not all mills can afford to shut all the boilers off because of process constraints
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Do you really know what are your best options ?
  • Example 7: TMP Pulp Mill in BC
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Do you really know what are your best options ?
  • Example 8: Kraft Mill in Qc
    • Large flowrate of cold ClO2 solution used for the bleaching
    • Mill’s suggestion: heat the solution with some hot condensate
    • Composite curves show this is a non-optimal choice
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Do you really know what are your best options ?
  • Example 9: TMP Mill in Qc
    • Target: cool the effluent to 37 deg. C
    • Composite curves show this is impossible with the current operating conditions
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Do you really know what are your best options ?
  • Option: consider judicious process modifications
    • To achieve that correctly,
    • Process Simulation is mandatory
    • Solution: increase temperature
    • set point of the TMP ww network
    • to 76°C
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Wrap up... so far
  • You may think that some of the previous examples are very simple, obvious and easy to identify projects, but remember that...


  • A well done job using rigorous approaches often delivers crystal clear solutions that follow the KISS rule: Keep It Simple Stupid


  • This is a usual consequence of Pinch Analysis and Computer Simulation
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A mill is a living process that changes continuously...
  • Major changes frequently occur and can impact  the selected projects of an energy efficiency program
  • A possible approach: include some flexibility in your plan of action
  • A few alternate solutions from Pinch Analysis design rules can be found for a given selected value of dTmin
  • This gives options to the mill and add some flexibility to the solutions presented
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A mill is a living process that changes continuously...
  • Ex. 10 (QRP): ww heating for the bleaching: 2 options
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A mill is a living process that changes continuously...
  • ... leading to a flexible road map of (as much as possible) independent projects
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Conclusions
  • Computer Simulation and Pinch Analysis have come of age
  • Now it is possible to simulate complex integrated mills in a single simulation


  • Energy saving projects identified the conventional way cannot bring the mill to its maximum energy efficiency potential and can lead to some waste of capital


  • With the existing trend resulting from the Greenhouse gases concerns and the Kyoto protocol, this approach is a powerful tool available to minimize a mill’s  CO2 emissions in a profitable economic context