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Naji, M. |
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Motta, Antonella |
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Aletan, Dirar |
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Mohamed, Tarek |
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Ertürk, Emre |
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Taccardi, Nicola |
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Kononenko, Denys |
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Petrov, R. H. | Madrid |
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Alshaaer, Mazen | Brussels |
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Bih, L. |
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Casati, R. |
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Muller, Hermance |
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Kočí, Jan | Prague |
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Šuljagić, Marija |
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Kalteremidou, Kalliopi-Artemi | Brussels |
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Azam, Siraj |
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Ospanova, Alyiya |
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Blanpain, Bart |
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Ali, M. A. |
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Popa, V. |
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Rančić, M. |
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Ollier, Nadège |
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Azevedo, Nuno Monteiro |
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Landes, Michael |
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Rignanese, Gian-Marco |
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Kiiskinen, Harri
VTT Technical Research Centre of Finland
in Cooperation with on an Cooperation-Score of 37%
Topics
Publications (10/10 displayed)
- 2023Formable cellulose-based webs enabled by foam forming technology
- 2023High consistency foam in pilot scale
- 2016Porous structure of fibre networks formed by a foaming process: a comparative study of different characterization techniquescitations
- 2012Nano-fibrillated cellulose vs bacterial cellulose
- 2012High performance cellulose nanocompositescitations
- 2012High performance cellulose nanocomposites:Comparing the reinforcing ability of bacterial cellulose and nanofibrillated cellulosecitations
- 2012Nano-fibrillated cellulose vs bacterial cellulose:Reinforcing ability of nanocellulose obtained topdown or bottom-up
- 2009Some insight on paper structure and properties with different drying conditions
- 2003On the mobility of flowing papermaking suspensions and its relationship to formation
- 2002On the mobility of flowing papermaking suspensions and its relationship to formation
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document
High consistency foam in pilot scale
Abstract
Resource-efficientprocessingisoneofthepathwaystomanufacturingsustainablefoam-formed products. Replacingthecurrentfoaming methodswithHigh-ConsistencyFoam(HCF)canreduce resourceconsumptionintermsof water, andequipmentfootprint. Therefore,wecarriedoutpilot-scale HCF trials to address requirements on the process equipment and parameters to generate low-densityporousstructures.ThepilotscaleHCFunitcomprisedof unitoperationsinthefollowing order: (a) 200 L mixing tankwith pitched blade turbines, (b) centrifugal pump with an air-removal system, (c) Headbox with 5 mm and 8 mm rectangular openings and (d) pilot machine with 300 mmand 700 mmweb, impingementand through-airdriers.A mixture of softwood(SW)and hardwood(HW),from 8% to 14%consistencies,were used. 4 to 6 g/L of non-ionic Simulsol 10 was used as a surfactant.Wefoundthat a dualimpellersystem cangeneratehomogeneousHCFwith14%consistency(50%SW+50%HW)resultingin the lowestwetfoamdensityof160g/L. Besides,higher mixing power wasrequiredfor pure SW foam compared toHW foam. The headbox with an 8 mmopening and640mmwidthworkedbetter,whereasthe 5mmopeningencountered frequent blockageprobably due to the too-low flow rates. A minimum flow rate of 0.2 L/sec was required to avoid backpressureand to distribute the foam inside the headbox evenly. Highly porous low-densitysamplesin the density of 20-80 kg/m3were examined using x-ray tomography to detect the structures’flowchannels/weakpoints. HWwaseasierto foamwithoutflocks,butthestructurewasbrittle whereas themixture of HW andSW enhanced the structure. In summary, an improved understanding ofthe operating parameters of different unit operations (mixer, pump, head box,and pilot machine) to form low-density webs with HCF was achieved.