Compact wet end systems for superior papermaking

Compact wet end systems for superior papermaking Compact wet end systems for superior papermaking

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WET ENDFIG. 5. Flexible cascade cleaner arrangement.with higher flow velocities than a conventional white water system.Therefore, bacteria growth and scale build-up are minimized.Flexible cleaner arrangementAs an additional volume reduction opportunity, compact wetend systems can incorporate a cleaner arrangement that reducesequipment sizing and energy cost while further reducing systemvolume. This system is shown in Figure 5.The primary cleaners of the flexible cascade arrangement aresized for minimum headbox flow or optimum cleaning efficiency.Here, secondary accepts are recirculated in a full cascadearrangement. As headbox flow increases, secondary accepts feedforward automatically for an open cascade operation to satisfythe higher flow requirement. When flow requirements exceedthe combined primary and secondary accepts flow, additionalwhite water dilution flow is drawn from the distribution header.Cleaners of the “Flexible Cascade” arrangement operate at optimumflow or cleaning efficiency throughout a broader range of theheadbox flow. Equipment selections are minimized, horsepowerrequirements are reduced and control and piping systems are simplified.Compact seal pitThe flat box or vacuum leg seal pit is often overlooked as an areaof the papermaking process requiring improvements orupgrade. For compact wet end systems, it provides anotheropportunity to reduce system volume and improve papermachine performance.Typical, seal pit operations are dirty, turbulent, large volumechest that can generate vacuum variations at the forming section.In addition, slime buildup can be difficult to manage leading toincreased frequency of required thermal, mechanical and/orchemical cleaning. With the compact wet end system approach,a compact, pre-fabricated seal pit is provided. See Figure 6.This unit allows each vacuum leg to be sealed individuallyand operators can view the performance of each table elementand make adjustments as may be necessary. The individual sealchambers can be easily fitted with a “V-notch weir” to allow directand simple flow measure and sampling from each vacuumdevice. Figure 7, is an operating compact seal pit unit.RESULTSAfter the first compact wet end system startup in 1997, it becamequickly apparent that performance and additional opportunitiesfor improvement would be much greater than anticipated. Benefitsthat have been reported to date include:• 60% reduction in grade change time• 75% reduction in wet end breaks• 50% reduction in wash-up frequency• 25% reduction in energy consumption• 20% improvement in sheet formation• 99.5+% “air-free” white water• 10% operating efficiency improvementFIG. 6. Compact seal pit.FIG. 7. Operating compact seal pit.A discussion of these improvements and opportunities [5]include:Reduced grade change timePaper machines incorporating compact wet end systems havereduced grade change time on average by 60%. Reduced processvolumes allow thick stock and white water systems to purgequickly, minimizing off-quality production and transition time.The improvements in change time apply to simple basisweight changes or complete color and/or wet end chemistrychanges. One installation reported simple basis weight changeswere improved by 65% where a color producer reduced gradeto-gradechange time by greater than 80%. Many specialtymachines find downtime for wash-up between grade changes areno longer required and major production changes are nowmade on the fly.Reduced wet end breaksCompact wet end systems have disproved the age-old assumptionthat large volume processes are required for maintaining astable system. Whether in thick stock or white water systems,large volume systems can generate low frequency variations thatare difficult if not impossible to attenuate. These variations usuallycontribute to significant MD weight swings.With the minimum retention time in a compact stock mixerand the higher flow velocities of the hydraulic white water distributionsystem, low frequency variations are avoided. The elevatedoverflow head tank further enhances the white water systemstability with the optimum in pressure control forminimizing variability.Stable white water systems are the key to a stable wet end. One30 ❘❘❘ 105:4 (2004) T 85 Pulp & Paper Canada

WET ENDFIG. 5. Flexible cascade cleaner arrangement.with higher flow velocities than a conventional white water system.There<strong>for</strong>e, bacteria growth and scale build-up are minimized.Flexible cleaner arrangementAs an additional volume reduction opportunity, compact <strong>wet</strong><strong>end</strong> <strong>systems</strong> can incorporate a cleaner arrangement that reducesequipment sizing and energy cost while further reducing systemvolume. This system is shown in Figure 5.The primary cleaners of the flexible cascade arrangement aresized <strong>for</strong> minimum headbox flow or optimum cleaning efficiency.Here, secondary accepts are recirculated in a full cascadearrangement. As headbox flow increases, secondary accepts feed<strong>for</strong>ward automatically <strong>for</strong> an open cascade operation to satisfythe higher flow requirement. When flow requirements exceedthe combined primary and secondary accepts flow, additionalwhite water dilution flow is drawn from the distribution header.Cleaners of the “Flexible Cascade” arrangement operate at optimumflow or cleaning efficiency throughout a broader range of theheadbox flow. Equipment selections are minimized, horsepowerrequirements are reduced and control and piping <strong>systems</strong> are simplified.<strong>Compact</strong> seal pitThe flat box or vacuum leg seal pit is often overlooked as an areaof the <strong>papermaking</strong> process requiring improvements orupgrade. For compact <strong>wet</strong> <strong>end</strong> <strong>systems</strong>, it provides anotheropportunity to reduce system volume and improve papermachine per<strong>for</strong>mance.Typical, seal pit operations are dirty, turbulent, large volumechest that can generate vacuum variations at the <strong>for</strong>ming section.In addition, slime buildup can be difficult to manage leading toincreased frequency of required thermal, mechanical and/orchemical cleaning. With the compact <strong>wet</strong> <strong>end</strong> system approach,a compact, pre-fabricated seal pit is provided. See Figure 6.This unit allows each vacuum leg to be sealed individuallyand operators can view the per<strong>for</strong>mance of each table elementand make adjustments as may be necessary. The individual sealchambers can be easily fitted with a “V-notch weir” to allow directand simple flow measure and sampling from each vacuumdevice. Figure 7, is an operating compact seal pit unit.RESULTSAfter the first compact <strong>wet</strong> <strong>end</strong> system startup in 1997, it becamequickly apparent that per<strong>for</strong>mance and additional opportunities<strong>for</strong> improvement would be much greater than anticipated. Benefitsthat have been reported to date include:• 60% reduction in grade change time• 75% reduction in <strong>wet</strong> <strong>end</strong> breaks• 50% reduction in wash-up frequency• 25% reduction in energy consumption• 20% improvement in sheet <strong>for</strong>mation• 99.5+% “air-free” white water• 10% operating efficiency improvementFIG. 6. <strong>Compact</strong> seal pit.FIG. 7. Operating compact seal pit.A discussion of these improvements and opportunities [5]include:Reduced grade change timePaper machines incorporating compact <strong>wet</strong> <strong>end</strong> <strong>systems</strong> havereduced grade change time on average by 60%. Reduced processvolumes allow thick stock and white water <strong>systems</strong> to purgequickly, minimizing off-quality production and transition time.The improvements in change time apply to simple basisweight changes or complete color and/or <strong>wet</strong> <strong>end</strong> chemistrychanges. One installation reported simple basis weight changeswere improved by 65% where a color producer reduced gradeto-gradechange time by greater than 80%. Many specialtymachines find downtime <strong>for</strong> wash-up between grade changes areno longer required and major production changes are nowmade on the fly.Reduced <strong>wet</strong> <strong>end</strong> breaks<strong>Compact</strong> <strong>wet</strong> <strong>end</strong> <strong>systems</strong> have disproved the age-old assumptionthat large volume processes are required <strong>for</strong> maintaining astable system. Whether in thick stock or white water <strong>systems</strong>,large volume <strong>systems</strong> can generate low frequency variations thatare difficult if not impossible to attenuate. These variations usuallycontribute to significant MD weight swings.With the minimum retention time in a compact stock mixerand the higher flow velocities of the hydraulic white water distributionsystem, low frequency variations are avoided. The elevatedoverflow head tank further enhances the white water <strong>systems</strong>tability with the optimum in pressure control <strong>for</strong>minimizing variability.Stable white water <strong>systems</strong> are the key to a stable <strong>wet</strong> <strong>end</strong>. One30 ❘❘❘ 105:4 (2004) T 85 Pulp & Paper Canada

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