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Unit Processes and Optimization Opportunities in the Pulp & Paper Mill
Brad S. Carlberg, P.E. Senior Controls & Instrumentation Engineer Waste Treatment Plant Bechtel National Inc. Richland, WA
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Brad S. Carlberg, P.E. (Control Systems)
My Pulp & Paper career began with my 3rd grade science project in 1965 – who knew? Over twenty years experience in Process Engineering and Process Control specifically with Distributed Control Systems and Programmable Logic Controllers combining extensive experience with both Hardware and Software Design, Programming, Implementation and Startup, including Advanced Continuous and Batch Control Programming. Currently working (less than an hour drive from where he was born) for Bechtel on the Hanford Vitrification Plant in Richland, Washington
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Lessons learned: understand the equipment and the processes in a pulp & paper mill understand the similarities to other industries understand specific areas where control system optimization can decrease costs and/or increase production
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The Typical Pulp & Paper Mill
There are six main “islands” of automation of the mill: raw material receiving & preparation (the woodyard) the pulp mill the powerhouse the paper mill converting and finishing effluent treatment.
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THE WOODYARD (RAW MATERIAL RECEIVING & PREPARATION)
Debarking Drum is rotates and raw logs pass axially through to remove bark Bark doesn’t make good paper AT ALL
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THE WOODYARD Pulpwood logs out of debarking drum to the chippers
Chips are ”classified” (sorted) by size & species
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THE WOODYARD (RAW MATERIAL RECEIVING & PREPARATION)
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THE WOODYARD (RAW MATERIAL RECEIVING & PREPARATION)
Chips pneumatically transported from the Woodyard first to the chip bins and then to fill the Digester
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THE PULP MILL Lime Kiln (the two rotating cylinders) Gas/Oil fired
Dry and Calcine the Lime Mud from the Slaker for reuse in the Causticizer
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THE POWERHOUSE Multiple stories to house the Kraft Recovery Boiler
Like any industrial boiler, EXCEPT burns Black Liquor Produces Green Liquor for Pulping Induced Draft Fan Multiple (~Fifty) Sootblowers Electrostatic Precipitators remove particulate from stack gases Steam feeds Digester, Evaporators, Paper Machine & Turbine-Generator
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LIQUOR BURNERS IN THE KRAFT RECOVERY BOILER
Multiple (~12) burners per boiler Strong black liquor 65% solids Recovers inorganic chemicals as molten smelt that exits the bottom of the boiler into the green liquor dissolving tank to be reused in the digesting (cooking) process
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% CONSISTENCY (of Wood Pulp Fiber) = 100 x Lbsfiber / (Lbsfiber + LbsWater)
microwave Blade Rotating Disk Can be pumped at 3-5% Can be stored at 15%
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BROWN STOCK WASHERS Rotating Cylinders covered with wire mesh pick up a 2” mat of pulp from the vat COUNTERCURRENTLY Wash the pulp mat with water to Remove the weak black liquor Filtrate sucked through the wire mesh by a gravity-formed vacuum into tanks directly below Washed pulp “doctored” off of the rotating cylinders 180o after pickup
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BLEACH PLANT TOWERS Towers provide residence time for Bleaching chemicals to react with and to brighten pulp stock 3-Stage: D1-Eop-D2 D=Chlorine Dioxide Eop = Extraction with oxygen & peroxide
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CHLORINE DIOXIDE GENERATOR
Environmentally friendly alternative to Liquid or Gaseous Chlorine Bleaching Agent Interlocked to guard against a “puff” (explosion) A great case for MPC control to control Cl O2 density ( g/l )
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BLEACH PLANT WASHERS Used to remove residual bleaching chemicals from the pulp
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PULP HIGH-DENSITY STORAGE CHESTS
That’s A LOT of pulp Enough for a couple of shifts in case the pulp mill goes down – the paper machine can still run
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THE PAPER MILL – STOCK PREP
The refiners condition the pulp stock when cooking in the digesters is stopped early
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THE PAPER MILL – STOCK PREP
The two plates cut & brush up the fibers Optimize Power/Ton
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STOCK PREP CLEANERS Centrifugal force separates lights from heavies
Remove contaminants or non-uniform sized fibers
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THE PAPER MILL – WET END Headbox at the far end feeds the Fourdrinier wire Vacuum to remove water
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PAPER MACHINE – DRY END LOOKING TO WET WET END
~100 yards long Forming section Press section Dryer section Finishing section
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CONVERTING AND FINISHING
Cut the big rolls of paper into transportation-size rolls Rewind the big rolls of paper into transportation-size rolls
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EFFLUENT TREATMENT Just like a municipal waste treatment plant
Aeration Basin Clarifiers Settling ponds
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OPTIMIZATION OPPORTUNITIES IN THE PULP & PAPER MILL
RECOVERY BOILER SOOTBLOWING BLACK LIQUOR EVAPORATORS CAUSTICIZING BATCH AND CONTINUOUS DIGESTERS SCREENING AND REFINING WASHING BLEACHING LIME KILN PULP STOCK PREPARATION, CLEANING, REFINING, AND BLENDING PAPER PAPERMAKING, PRESSING AND DRYING SECTIONS OF THE PAPER MILL
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PULP & PAPER PROCESS OVERVIEW
Woodyard Digester Washer Bleach Plant Weak Black Liq Pulp Mill Hot Buttons Wood Supply Causticizing operation Digester/Washer Production Air Pollution Water Pollution Pulp Quality Chemical and Energy use Maintenance White Liquor Evaporator Paper Mill Strong Black Liq Causticizing Green Liquor Dissolving Tank Recovery Boiler Shipping Lime Kiln
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RECOVERY BOILER DCS GRAPHIC
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RECOVERY BOILER ROTARY SOOTBLOWER
Uses high-pressure steam to blow soot off of boiler tubes to improve heat transfer between furnace gases and boiler water Sequence the individual sootblower operation for optimal steam usage Low Temp & High Diff Press signal which sections to blow
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LIME KILN PROCESS Big energy savings possible here!
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LIME KILN DCS GRAPHIC Long Deadtime means Good case for Multivariable Predictive Controller CV – Temps MV – ID Fan ASD DV – Production Rate
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RECAUSTICIZING – traditional control
Big chemical savings possible here! Long Deadtime means Good case for Multivariable Predictive Controller CV – Conductivity MV – Green Liquor & Lime feeder ASDs DV – White Liquor Production Rate
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RECAUSTICIZING – new sensors
Big chemical savings possible here!
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RECAUSTICIZING DCS GRAPHIC
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BLACK LIQUOR EVAPORATOR
Fouling reduces efficiency Automate boilout when fouling decreases heat transfer from steam to liquor
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EVAPORATOR DCS GRAPHIC
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BROWN STOCK WASHERS DCS GRAPHIC
An Optimum Dilution Factor of 1.0 means that the Lbs wash water equals the lbs pulp stock Less wash water reduces the load on the evaporators i.e. steam usage
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CONTINUOUS DIGESTER DCS GRAPHIC
Kappa Number is the amount of delignification of the pulp fiber For example, brown board will have a higher Kappa Number than bleached pulp White Liquor Analyzer to sense residual chemical Kappa Analyzer to sense fiber delignification
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BATCH DIGESTERS DCS GRAPHIC
Batch Scheduling - Steam Leveling smoothes boiler operation Chip Qualities – uniform moisture Batch digesters- liquor analyzer Better Kappa control Reduce white liquor usage Batch digesters- Kappa analyzer
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PAPER MACHINE SCANNER Multiple sensors across width machine width measure: Moisture Basis Weight Caliper (Thickness)
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PAPER MACHINE SCANNER
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PAPER MACHINE DRYERS Paper sheet rolls over the steam-heated dryer cylinders to evaporate moisture Optimize Steam Usage to save energy costs
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IN CONCLUSION After reading this paper and seeing this presentation you now have a better understanding of the equipment and the processes in a pulp & paper mill, you can see the similarities to other industries You have an idea of several specific areas where control system optimization can decrease costs and/or increase production
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ACKNOWLEDGEMENTS First and foremost, I would not be here today (literally and figuratively) had my Father not spent his entire career with the same pulp & paper manufacturer and, in fact, gave me the raw materials and the technical background for my 3rd science project I likely would not be in instrumentation & controls had (ISA PUPID Life Fellow) John Lavigne written the book “An Introduction To Paper Industry Instrumentation” which I read immediately following graduation I must thank the pulp & paper mill workers in mills scattered throughout North America from whom I gained the immeasurable experience to write this paper
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QUESTIONS If you think of questions later:
Feel free to call or me at either (509) or (251) or me at either: or
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