Abstract
The study explores how changes in process variables, residence time and pulp consistency in refining influence the pulp properties. The equipment utilized in this study was a conical disc chip refiner (RGP82CD) producing thermomechanical pulp (TMP). The focus was on the ratio between tensile index and specific energy consumption. Pulp properties were measured for composite pulp samples taken from the refiner blow line. Residence times and pulp consistencies were estimated by use of the extended entropy model. This showed that the CD-refiner, with the flat and conical refining zone, has a process performance similar to that of a two-stage refiner set-up, and that the consistency in both refining zones is of high importance. Comparing different periods revealed that even if the values of measured blow line consistency are similar, significant differences in the estimated consistency in the flat zone can prevail. Therefore, only monitoring blow line consistency is not enough. Specifically, it was found that the pulp consistency after the flat zone could be very high, considerably higher than in the blow line, and this could have negative effects on tensile index and fibre length.
Funding statement: This publication is a part of the Energy Efficient Mechanical Pulping (e2mp) program at Mid Sweden University funded by the Knowledge Foundation, Stora Enso, SCA, Holmen, and Valmet. Special thanks to all who gave support to these trials and testing of the pulps.
Conflict of interest: The authors do not have any conflicts of interest to declare.
Appendix
Data from TEST2.
Composite Pulp Sample | 21 | 22 | 23 | 24 | 25 | 26 | 27 | 28 | 29 |
Load, MW | 23.7 | 24.6 | 24.9 | 23.3 | 21.9 | 23.1 | 24.2 | 24.2 | 21.4 |
Gap FZ, mm | 1.35 | 1.20 | 1.05 | 1.21 | 1.37 | 1.35 | 1.36 | 1.35 | 1.36 |
Gap CD, mm | 0.78 | 0.79 | 0.78 | 0.77 | 0.77 | 0.79 | 0.78 | 0.75 | 0.78 |
Dil. water FZ, l/s | 3.42 | 3.43 | 3.43 | 3.43 | 3.43 | 3.36 | 3.26 | 3.17 | 3.43 |
Dil. water CD, l/s | 5.23 | 5.24 | 5.24 | 5.23 | 5.23 | 5.23 | 5.23 | 5.24 | 5.23 |
Prod., admt/h | 15.9 | 15.9 | 15.9 | 15.9 | 15.9 | 15.9 | 15.9 | 15.9 | 15.9 |
SE., kWh/admt | 1493 | 1552 | 1569 | 1473 | 1381 | 1457 | 1525 | 1527 | 1353 |
Calc. conc. FZ, % | 76.7 | 84.3 | 89.8 | 77.9 | 69.3 | 75.9 | 81.0 | 82.0 | 68.2 |
Calc. conc. CD, % | 60.0 | 64.1 | 65.4 | 58.9 | 53.7 | 58.6 | 64.0 | 65.3 | 52.3 |
Tot. res. time, s | 1.23 | 1.28 | 1.30 | 1.23 | 1.17 | 1.22 | 1.28 | 1.30 | 1.15 |
Res. time ratio FZ/CD | 1.03 | 0.98 | 0.97 | 1.04 | 1.11 | 1.05 | 1.00 | 0.99 | 1.13 |
Force FZ 3, N | 1.11 | 1.20 | 1.26 | 1.19 | 1.21 | 1.15 | 1.11 | 1.13 | 1.26 |
Pulp conc., % | 57.6 | 61.0 | 62.6 | 57.0 | 53.5 | 58.9 | 62.5 | 64.2 | 53.8 |
Freeness, ml CSF | 198 | 192 | 182 | 197 | 225 | 202 | 192 | 193 | 230 |
Fiber length (ww), mm | 2.11 | 1.96 | 1.92 | 2.15 | 2.29 | 2.20 | 2.03 | 2.01 | 2.31 |
CWT, μm | 7.8 | 8.0 | 7.8 | 7.9 | 7.8 | 8.0 | 7.9 | 7.9 | 8.0 |
Fibrillation, % | 5.43 | 5.64 | 5.62 | 5.39 | 5.56 | 5.82 | 6.06 | 5.67 | 5.62 |
Curl, % | 14.1 | 13.6 | 13.5 | 13.6 | 13.6 | 13.9 | 13.8 | 13.4 | 13.6 |
Somerville, % | 1.61 | 1.15 | 1.04 | 1.46 | 1.78 | 1.44 | 1.32 | 1.34 | 1.79 |
Density, kg/m3 | 329 | 352 | 362 | 343 | 330 | 343 | 348 | 358 | 326 |
Tensile index, Nm/g | 27.7 | 27.2 | 28.0 | 30.1 | 29.7 | 29.6 | 27.3 | 27.1 | 29.1 |
Elongation, % | 1.78 | 1.71 | 1.73 | 1.82 | 1.73 | 1.79 | 1.78 | 1.73 | 1.83 |
Tear index, mNm2/g | 6.37 | 5.72 | 5.86 | 6.72 | 7.21 | 6.88 | 5.95 | 6.11 | 7.27 |
Light scatt. coeff. m2/kg | 45.3 | 47.7 | 48.1 | 45.9 | 43.2 | 45.5 | 47.0 | 47.8 | 43.5 |
Data from TEST3.
Composite Pulp Sample | 31 | 32 | 33 | 34 |
Load, MW | 22.4 | 22.1 | 22.1 | 21.9 |
Gap FZ, mm | 1.23 | 1.24 | 1.22 | 1.23 |
Gap CD, mm | 0.63 | 0.57 | 0.63 | 0.64 |
Dil. water FZ, l/s | 3.78 | 3.79 | 3.78 | 3.79 |
Dil. water CD, l/s | 5.12 | 5.11 | 5.12 | 5.06 |
Prod., admt/h | 15.0 | 15.0 | 15.0 | 15.0 |
SE., kWh/admt | 1496 | 1476 | 1470 | 1463 |
Calc. conc. FZ, % | 60.7 | 58.0 | 59.8 | 59.5 |
Calc. conc. CD, % | 50.6 | 49.6 | 49.4 | 49.5 |
Tot. res. time, s | 1.03 | 1.15 | 1.15 | 1.15 |
Res. time ratio FZ/CD | 1.13 | 0.99 | 0.99 | 0.99 |
Force FZ 3, N | 1.23 | 1.28 | 1.27 | 1.25 |
Pulp conc., % | 51.4 | 51.4 | 50.8 | 50.8 |
Freeness, ml CSF | 214 | 212 | 213 | 220 |
Fiber length (ww), mm | 2.22 | 2.21 | 2.28 | 2.20 |
CWT, μm | 7.9 | 7.9 | 7.8 | 7.9 |
Fibrillation, % | 5.48 | 5.31 | 5.72 | 5.72 |
Curl, % | 14.5 | 13.7 | 14.8 | 14.0 |
Somerville, % | 1.78 | 1.88 | 1.75 | 1.86 |
Density, kg/m3 | 316 | 328 | 337 | 340 |
Tensile index, Nm/g | 26.8 | 26.3 | 27.8 | 27.9 |
Elongation, % | 1.78 | 1.71 | 1.77 | 1.78 |
Tear index, mNm2/g | 6.42 | 6.36 | 6.82 | 6.79 |
Light scatt. coeff. m2/kg | 44.0 | 44.2 | 43.8 | 43.9 |
Data from TEST4.
Composite Pulp Sample | 35 | 36 | 37 | 38 | 39 | 40 | 41 | 42 | 43 | 44 | 45 | 46 | 47 | 48 | 49 |
Load, MW | 19.7 | 19.6 | 19.7 | 19.5 | 19.6 | 21.5 | 21.5 | 21.6 | 21.3 | 21.3 | 22.5 | 22.5 | 22.3 | 22.4 | 22.5 |
Gap FZ, mm | 1.48 | 1.48 | 1.48 | 1.49 | 1.48 | 1.48 | 1.47 | 1.47 | 1.48 | 1.48 | 1.49 | 1.48 | 1.48 | 1.48 | 1.48 |
Gap CD, mm | 1.14 | 1.14 | 1.13 | 1.13 | 1.14 | 1.15 | 1.15 | 1.15 | 1.15 | 1.14 | 1.11 | 1.12 | 1.14 | 1.14 | 1.13 |
Dil. water FZ, l/s | 3.39 | 3.39 | 3.39 | 3.39 | 3.40 | 3.41 | 3.40 | 3.40 | 3.39 | 3.39 | 3.38 | 3.41 | 3.40 | 3.43 | 3.38 |
Dil. water CD, l/s | 3.89 | 3.88 | 3.88 | 3.88 | 3.88 | 3.88 | 3.88 | 3.88 | 3.88 | 3.89 | 3.88 | 3.89 | 3.88 | 3.89 | 3.88 |
Prod., admt/h | 12.5 | 12.5 | 12.5 | 12.5 | 12.5 | 14.4 | 14.4 | 14.4 | 14.4 | 14.4 | 15.9 | 15.9 | 15.9 | 15.9 | 15.9 |
SE., kWh/admt | 1580 | 1566 | 1578 | 1564 | 1568 | 1490 | 1494 | 1497 | 1478 | 1482 | 1418 | 1415 | 1403 | 1410 | 1418 |
Calc. conc. FZ, % | 75.5 | 75.0 | 75.0 | 74.1 | 74.2 | 76.0 | 76.4 | 76.5 | 75.2 | 75.6 | 76.6 | 76.2 | 75.8 | 75.6 | 77.6 |
Calc. conc. CD, % | – | 58.6 | 58.6 | 57.6 | 57.7 | 64.5 | 64.9 | 65.2 | 63.9 | 64.2 | 65.9 | 65.4 | 65.0 | 65.3 | 66.1 |
Tot. res. time, s | 1.59 | 1.58 | 1.58 | 1.57 | 1.57 | 1.47 | 1.48 | 1.48 | 1.46 | 1.47 | 1.36 | 1.35 | 1.35 | 1.35 | 1.36 |
Res. time ratio FZ/CD | 0.85 | 0.85 | 0.85 | 0.86 | 0.86 | 0.80 | 0.80 | 0.80 | 0.81 | 0.81 | 0.80 | 0.80 | 0.80 | 0.80 | 0.80 |
Force FZ 3, N | 0.56 | 0.55 | 0.56 | 0.58 | 0.58 | 0.79 | 0.78 | 0.80 | 0.78 | 0.79 | 0.99 | 1.02 | 1.00 | 0.99 | 0.99 |
Pulp conc., % | 56.7 | 63.2 | 60.3 | 58.9 | 58.8 | 67.7 | 68.5 | 70.4 | 64.0 | 65.8 | 70.8 | 73.2 | 70.9 | 69.5 | 75.8 |
Freeness, ml CSF | 183 | 198 | 190 | 191 | 194 | 235 | 235 | 260 | 226 | 253 | 303 | 327 | 295 | 280 | 307 |
Fiber length (ww), mm | 2.34 | 2.33 | 2.32 | 2.33 | 2.32 | 2.31 | 2.31 | 2.28 | 2.30 | 2.31 | 2.33 | 2.34 | 2.34 | 2.36 | 2.28 |
CWT, μm | 7.6 | 7.7 | 7.8 | 7.7 | 7.7 | 7.9 | 7.9 | 8.0 | 7.9 | 7.9 | 8.1 | 8.2 | 8.0 | 8.0 | 8.3 |
Fibrillation, % | 6.7 | 6.47 | 6.42 | 6.38 | 6.6 | 6.13 | 6.24 | 6.18 | 6.09 | 6.19 | 6.15 | 6.12 | 6.28 | 6.15 | 5.97 |
Curl, % | 15.3 | 15.1 | 15.1 | 14.9 | 15.4 | 14.4 | 14.6 | 14.5 | 14.6 | 14.6 | 14.6 | 14.6 | 15.0 | 14.8 | 14.2 |
Somerville, % | 0.88 | 0.92 | 0.85 | 0.78 | 0.95 | 1.26 | 1.27 | 1.22 | 1.32 | 1.28 | 1.40 | 1.54 | 1.43 | 1.39 | 1.34 |
Density, kg/m3 | 362 | 355 | 360 | 360 | 364 | 341 | 352 | 350 | 356 | 346 | 336 | 337 | 339 | 350 | 339 |
Tensile index, Nm/g | 34.4 | 31.6 | 33.1 | 32.9 | 32.9 | 28.1 | 28.6 | 28.0 | 30.5 | 28.4 | 25.5 | 24.5 | 27.2 | 28.1 | 24.9 |
Elongation, % | 1.92 | 1.83 | 1.86 | 1.91 | 1.88 | 1.75 | 1.66 | 1.67 | 1.71 | 1.69 | 1.53 | 1.56 | 1.63 | 1.68 | 1.56 |
Tear index, mNm2/g | 7.47 | 7.22 | 7.59 | 7.31 | 7.37 | 7.16 | 6.95 | 6.48 | 6.93 | 6.61 | 6.19 | 6.23 | 6.55 | 6.83 | 6.06 |
Light scatt. coeff. m2/kg | 47.5 | 47.4 | 47.3 | 47.1 | 47.3 | 46.0 | 47.1 | 47.4 | 47.3 | 46.4 | 45.2 | 44.6 | 45.2 | 45.4 | 44.9 |
Data from TEST5.
Composite Pulp Sample | 50 | 51 | 52 | 53 | 54 | 55 | 56 | 57 | 58 | 59 | 60 | 61 | 62 | 63 | 64 |
Load, MW | 21.9 | 22.3 | 22.1 | 22.1 | 22.6 | 18.4 | 18.1 | 18.5 | 18.9 | 18.7 | 20.0 | 19.0 | 18.8 | 17.6 | 17.4 |
Gap FZ, mm | 0.87 | 0.87 | 0.86 | 0.86 | 0.87 | 0.85 | 0.85 | 0.86 | 0.86 | 0.86 | 0.85 | 0.86 | 0.85 | 0.85 | 0.86 |
Gap CD, mm | 0.67 | 0.67 | 0.67 | 0.67 | 0.65 | 0.65 | 0.64 | 0.65 | 0.65 | 0.65 | 0.67 | 0.66 | 0.66 | 0.65 | 0.65 |
Dil. water FZ, l/s | 3.29 | 3.28 | 3.28 | 3.28 | 3.28 | 3.51 | 3.51 | 3.51 | 3.51 | 3.51 | 3.51 | 3.51 | 3.51 | 3.51 | 3.52 |
Dil. water CD, l/s | 4.69 | 4.70 | 4.70 | 4.69 | 4.70 | 4.69 | 4.69 | 4.69 | 4.69 | 4.69 | 4.45 | 4.44 | 4.45 | 4.44 | 4.44 |
Prod., admt/h | 14.2 | 14.2 | 14.2 | 14.2 | 14.2 | 14.3 | 14.3 | 14.3 | 14.3 | 14.3 | 14.2 | 14.2 | 14.2 | 14.2 | 14.2 |
SE., kWh/admt | 1540 | 1568 | 1555 | 1555 | 1588 | 1285 | 1264 | 1297 | 1321 | 1306 | 1407 | 1339 | 1322 | 1243 | 1223 |
Calc. conc. FZ, % | 61.2 | 62.5 | 62.1 | 62.2 | 62.5 | 53.4 | 52.9 | 53.6 | 54.3 | 53.9 | 56.4 | 54.6 | 54.2 | 52.4 | 51.9 |
Calc. conc. CD, % | 57.7 | 59.2 | 58.4 | 58.5 | 60.4 | 45.4 | 44.7 | 45.7 | 46.8 | 46.2 | 51.5 | 48.8 | 48.1 | 45.2 | 44.5 |
Tot. res. time, s | 1.16 | 1.17 | 1.17 | 1.17 | 1.18 | 1.04 | 1.03 | 1.04 | 1.05 | 1.05 | 1.10 | 1.07 | 1.06 | 1.04 | 1.03 |
Res. time ratio FZ/CD | 0.94 | 0.92 | 0.93 | 0.93 | 0.90 | 1.11 | 1.13 | 1.11 | 1.09 | 1.10 | 1.01 | 1.05 | 1.06 | 1.11 | 1.12 |
Force FZ 3, N | 1.56 | 1.64 | 1.62 | 1.63 | 1.68 | 1.28 | 1.27 | 1.30 | 1.32 | 1.31 | 1.42 | 1.29 | 1.30 | 1.25 | 1.26 |
Pulp conc., % | 59.0 | 61.2 | 59.6 | 60.7 | 61.4 | 45.0 | 43.7 | 45.5 | 48.0 | 48.6 | 49.0 | 49.7 | 48.7 | 44.3 | 44.4 |
Freeness, ml CSF | 190 | 194 | 194 | 203 | 205 | 262 | 270 | 259 | 252 | 253 | 214 | 235 | 244 | 286 | 295 |
Fiber length (ww), mm | 2.29 | 2.24 | 2.22 | 2.24 | 2.19 | 2.33 | 2.39 | 2.39 | 2.34 | 2.37 | 2.34 | 2.38 | 2.35 | 2.33 | 2.38 |
CWT, μm | 7.8 | 7.8 | 7.9 | 7.8 | 8.0 | 7.8 | 7.8 | 7.8 | 7.8 | 7.9 | 7.9 | 7.8 | 7.7 | 7.6 | 7.7 |
Fibrillation, % | 6.3 | 6.3 | 6.4 | 6.29 | 6.2 | 5.92 | 6.03 | 6.05 | 6.03 | 6.12 | 6.16 | 6.05 | 6.04 | 5.91 | 6.12 |
Curl, % | 14.7 | 14.5 | 14.5 | 14.9 | 14.4 | 13.7 | 14.0 | 13.6 | 14.0 | 13.9 | 14.2 | 13.9 | 14.1 | 13.8 | 13.9 |
Somerville, % | 0.86 | 0.76 | 0.75 | 0.80 | 0.64 | 1.75 | 2.00 | 1.66 | 1.75 | 1.72 | 1.32 | 1.42 | 1.75 | 2.24 | 2.28 |
Density, kg/m3 | 372 | 375 | 376 | 381 | 373 | 333 | 329 | 340 | 340 | 338 | 348 | 333 | 329 | 331 | 327 |
Tensile index, Nm/g | 34.2 | 33.8 | 33.9 | 33.5 | 32.1 | 27.9 | 26.8 | 28.5 | 29.1 | 28.8 | 31.2 | 29.0 | 27.2 | 26.0 | 25.8 |
Elongation, % | 1.80 | 1.83 | 1.81 | 1.91 | 1.82 | 1.76 | 1.71 | 1.76 | 1.81 | 1.76 | 1.85 | 1.78 | 1.78 | 1.68 | 1.75 |
Tear index, mNm2/g | 7.44 | 7.51 | 7.74 | 7.54 | 7.12 | 7.18 | 6.88 | 7.16 | 7.14 | 7.10 | 7.35 | 7.26 | 6.92 | 6.75 | 6.44 |
Light scatt. coeff. m2/kg | 46.6 | 47.2 | 47.1 | 46.5 | 47.1 | 43.2 | 43.0 | 42.8 | 43.4 | 43.5 | 44.5 | 43.5 | 43.1 | 42.0 | 41.9 |
References
Backlund, H.-O. (2004) Measurement of shear force, temperature profiles and fibre development in mill-scale TMP refiners. Licentiate thesis, Mid Sweden University ISBN 91-87908-81-6.Search in Google Scholar
Bussiere, S., Vuorio, P., Ullmar, M., Hensley, E., Arid, J., Huhtanen, J.-P. (2007) Mill scale development towards high-production, low-energy TMP refining line. In: Int. Mech. Pulping Conf., Minneapolis, USA.Search in Google Scholar
Deer, G., Carello, G., Fox, B., Cloutier, D. (2007) Power cost reduction through advanced quality control and refiner segment change at Tembec Pine Falls. In: Int. Mech. Pulping Conf., Minneapolis, USA.Search in Google Scholar
Engstrand, P., Engberg, B., Eds. (2014) Filling the gap – Final report. Report series FSCN 2014:57, Mid-Sweden University, Sundsvall, Sweden, ISSN 1650-5387.Search in Google Scholar
Eriksen, O. (2003) High-frequency pressure measurements in the refining zone of a high-consistency refiner. Ph.D thesis, Trondheim, Norway. ISBN 82-471-5601-6.Search in Google Scholar
Ferritsius, O., Ferritsius, R., Hill, J., Karlström, A., Ferritsius, J. (2017) Process considerations and its demands on TMP property measurements – A study on tensile index. Nord. Pulp Pap. Res. J. 32(1):45–53.10.3183/npprj-2017-32-01-p045-053Search in Google Scholar
Ferritsius, O., Ferritsius, R., Rundlöf, M. (2018a) Average fiber length as a measure of the amount of long fibers in mechanical pulps. Part I: Ranking of Pulps May Shift. Nord. Pulp Pap. Res. J. submitted.10.1515/npprj-2018-3058Search in Google Scholar
Ferritsius, R., Ferritsius, O., Hill, J., Karlström, A., Eriksson, K. (2018b) TMP Properties and process conditions in a CD82 chip refiner at different operation points. Part II: Comparison of the five tests. Nord. Pulp Pap. Res. J. accepted.10.1515/npprj-2018-3003Search in Google Scholar
Ferritsius, R., Hill, J., Ferritsius, O., Karlström, A. (2014) On energy efficiency in chip refining. In: Int. Mech. Pulping Conf., Helsinki, Finland.Search in Google Scholar
Fostokjian, R., Arid, J., Vuorio, P., Huhtanen, J.-P. (2005) Development results in reducing of refining energy consumption at Tempec paper group – Spruce Falls operations. In: Proceedings, Int. Mech. Pulping Conf., Oslo, Norway. pp. 229–232.Search in Google Scholar
Fredrikson, A., Salminen, L., Sirviö, J. (2012) Fiber pad phenomena of high-consistency TMP refining. In: Proceedings, Int. Mech. Pulping Conf., Helsinki, Finland, pp. 5.1–5.4.Search in Google Scholar
Härkönen, E., Huusari, E., Ravila, P. (1999) Residence time of fiber in a single disc refiner. In: Int. Mech. Pulping Conf., Huston, USA.Search in Google Scholar
Härkönen, E., Tienvieri, T. (1995) The influence of production rate on refining in a specific refiner. In: Int. Mech. Pulping Conf., Ottawa, Canada.Search in Google Scholar
Härkönen, E., Tienvieri, T. (2001) Energy savings in TMP pulping. In: Int. Mech. Pulping Conf., Helsinki, Finland. pp. 547–556.Search in Google Scholar
Hill, J. (1993) Process understanding profits from sensor and control developments. In: Int. Mech. Pulping Conf., Oslo, Norway.Search in Google Scholar
Hill, J., Saarinen, K., Stenros, R. (1993) On the control of chip refining systems. Pulp Pap. Can. 94(6):43–47.Search in Google Scholar
Johansson, O., Hogan, D., Blankenship, D., Snow, E., More, W., Qualls, R., Pugh, K., Wonderer, M. (2001) Improved process optimization through adjustable refiner plates. In: Int. Mech. Pulping Conf., Helsinki, Finland.Search in Google Scholar
Johansson, B.-L., Karlsson, H., Jung, E. (1980) Experiences with computer control, based on optical sensors for pulp quality, of a two-stage TMP-plant. In: Process Control Conf., Halifax, Nova Scotia, Canada.Search in Google Scholar
Johansson, O., Richardson, J. (2005) The effect of refining zone temperature on refining efficiency and pulp quality. In: Int. Mech. Pulping Conf., Oslo, Norway. pp. 50–58.Search in Google Scholar
Karlström, A., Eriksson, K. (2014) Fiber energy efficiency Part I–IV. Nord. Pulp Pap. Res. J. 29(2):322–331, 332–343, and 29(3):401–408, 409–417.10.3183/npprj-2014-29-02-p322-331Search in Google Scholar
Karlström, A., Hill, J., Ferritsius, R., Ferritsius, O. (2015) Pulp property development Part I: Interlacing undersampled pulp properties and TMP process data using piece-wise linear functions. Nord. Pulp Pap. Res. J. 30(4):599–608.10.3183/npprj-2015-30-04-p599-608Search in Google Scholar
Karlström, A., Hill, J., Ferritsius, R., Ferritsius, O. (2016a) Pulp property development Part II: Process nonlinearities and its influence on pulp property development. Nord. Pulp Pap. Res. J. 31(2):287–299.10.3183/npprj-2016-31-02-p287-299Search in Google Scholar
Karlström, A., Hill, J., Ferritsius, R., Ferritsius, O. (2016b) Pulp property development Part III: Fiber residence time and consistency profile impact on specific energy and pulp properties. Nord. Pulp Pap. Res. J. 31(2):300–307.10.3183/npprj-2016-31-02-p300-307Search in Google Scholar
Karlström, A., Isaksson, A. (2009) Multi-rate optimal control of TMP refining processes. In: Int. Mech. Pulping Conf., Sundsvall, Sweden.Search in Google Scholar
Liukkonen, S., Nurminen, I., Fredrikson, A., Salminen, L., Sirviö, J. (2014) Development of pulp properties within refiner plate gap in energy efficient and cutting processes. In: Int. Mech. Pulping Conf., Helsinki, Finland.Search in Google Scholar
May, W.D., Miles, K.B., McRae, M.R., Lunan, W.E. (1988) An approach to the measurement of residence time in a chip refiner. J. Pulp Pap. Sci. 14(3):J47–J53.Search in Google Scholar
Miles, K.B., May, W.D. (1989) The flow of pulp in chip refiners. In: Int. Mech. Pulping Conf., Helsinki, Finland.Search in Google Scholar
Senger, J., Siadat, A., Ouellet, D., Wild, P. (2004) Measurement of normal and shear forces during refining using a piezoelectric force sensor. J. Pulp Pap. Sci. 30(9): 247–251.Search in Google Scholar
Strand, B.C., Grace, B. (2014) Implementation of advanced supervisory control within a TMP refiner quality control system. Int. Mech. Pulping Conf., Helsinki, Finland.Search in Google Scholar
Strand, B.C., Mokvist, A., Falk, B., Jackson, M. (1993) The effect of production rate on specific energy consumption in high consistency chip refining. In: Int. Mech. Pulping Conf., Oslo, Norway.Search in Google Scholar
Tistad, G., Asklund, S., Görfelt, P. (1981) TMP for newsprint produced by single stage refining with and without conical periphery segments. Operating experience from Hallsta Paper mill. In: Int. Mech. Pulping Conf., Oslo, Norway.Search in Google Scholar
Vikman, K., Vuorio, P., Huhtanen, J.-P., Huhtokari, J. (2005) Residence time measurements for a mill scale high consistency CD refiner line. In: Proceedings, Int. Mech. Pulping Conf., Oslo, Norway.Search in Google Scholar
© 2018 Walter de Gruyter GmbH, Berlin/Boston