Home Effects of chip pretreatment and feeding segments on specific energy and pulp quality in TMP production
Article
Licensed
Unlicensed Requires Authentication

Effects of chip pretreatment and feeding segments on specific energy and pulp quality in TMP production

  • Christer Sandberg EMAIL logo , Erik Nelsson , Birgitta A. Engberg , Jan-Erik Berg and Per Engstrand
Published/Copyright: August 22, 2018
Become an author with De Gruyter Brill

Abstract

Increased wood softening and refining intensity have earlier been utilized to improve refining efficiency in mechanical pulping. We have evaluated a combination of increased softening by low dose sulphite chip pretreatment and increased intensity by feeding segment design in a TMP line for production of high quality printing papers.

Norway spruce wood chips were preheated, compressed in an Impressafiner and impregnated with water or sodium sulphite solutions (Na2SO3 charges 3.6 and 7.2 kg/t). Chips were refined in two parallel 68” double disc refiners using two different refining conditions: standard bidirectional segments at normal production rate (9 t/h) and feeding segments at increased production rate (11.1–12.1 t/h).

The feeding segments enabled a 30 % increase in production rate. Refining with feeding segments at 12.1 t/h production rate combined with chip pretreatment with 3.6 kg/t sodium sulphite reduced the specific energy 360 kWh/t (19 %) compared to refining with standard segments and no pretreatment. Pulp properties were similar for the two configurations. The combination of feeding segments and chip pretreatment with water reduced the specific energy 180 kWh/t (9 %). Implementation of most of the technology presented has reduced the electrical energy use for the mill by approximately 80 GWh/year.

Funding source: Knowledge Foundation

Award Identifier / Grant number: 20100281

Funding source: Energimyndigheten

Award Identifier / Grant number: 2009-001882

Funding statement: This work was performed within the research program “Energy Efficient Mechanical Pulping” at FSCN, Mid Sweden University and was financed by the Knowledge Foundation (grant No. 20100281), the Swedish Energy Agency (grant No. 2009-001882) and by in-kind from Holmen AB.

Acknowledgments

The authors are most grateful to the staff at the Braviken mill that assisted with planning and performance of the mill trials.

  1. Conflict of interest: The authors declare no conflicts of interest.

References

Ahrel, I., Bäck, I. (1970) Thermomechanical pulp at Rockhammar, EUCEPA. In: Proc. Symp. Mech. Pulp. Oslo. pp. 83–91.Search in Google Scholar

Andersson, S., Sandberg, C., Engstrand, P. (2012) Comparison of mechanical pulps from two stage HC single disc and HC double disc – LC refining. Appita J. 65(1):57–62.Search in Google Scholar

Asplund, A., Bystedt, I. (1973) Development of the thermo-mechanical pulping method. In: Int. Mech. Pulping Conf. Stockholm, p. 15:1.Search in Google Scholar

Atack, D. (1972) On the characterization of pressurized refiner mechanical pulps. Svensk Papperstidning 75(3):89–94.10.1016/0014-4827(72)90523-XSearch in Google Scholar

Atack, D., Heitner, C., Stationwala, M.I. (1978) Ultra high yield pulping of eastern black spruce. Svensk Papperstidning 81(5):164–176.Search in Google Scholar

Axelson, P., Simonson, R. (1982) Thermomechanical pulping with low addition of sulfite Part 1. Effects of mild sulfite treatment of spruce chips prior to defibration. Svensk Papperstidn. 85(15):R132–R139.Search in Google Scholar

Becker, H., Höglund, H., Tistad, G. (1977) Frequency and temperature in chip refining. Pap. Puu 59(3):123–130.Search in Google Scholar

Charters, M.T., Ward, R.O. (1973) Elevated temperature refining for high quality mechanical pulp. In: Int. Mech. Pulping Conf. Stockholm. pp. 16:1–16:20.Search in Google Scholar

Engberg, B., Berg, J.-E. (2011) A comparative study of models describing high consistency refining. In: Int. Mech. Pulping Conf. Beijing. pp. 96–100.Search in Google Scholar

Engstrand, P., Ferritsius, O., Björkqvist, O., Johansson, L. (2015) Mekmassainitiativet för energieffektivitet, e2mp-i. Report series FSCN 2015:58, Mid Sweden University, Sundsvall, ISBN 978-91-88025-56-2. In Swedish.Search in Google Scholar

Ferritsius, O., Moldenius, S. (1985) The effect of impregnation method on CTMP properties In: 3rd Int. Symp. Wood Pulp. Chem. Vancouver, Canada, 91–100.Search in Google Scholar

Ferritsius, O., Mörseburg, K., Ferritsius, R. (2014) BAT of CTMP and TMP plants with respect to quality development and energy efficiency. In: Int. Mech. Pulping Conf. Helsinki.Search in Google Scholar

Gellerstedt, G. (1976) Reactions of lignin during sulfite pulping. Svensk Papperstidning 79(16):537–543.Search in Google Scholar

Goring, D. (1963) Thermal softening of lignin, hemicellulose and cellulose. Pulp Paper Mag. Can. 64(12):T517–T528.Search in Google Scholar

Heikkurinen, A., Vaarasalo, J., Karnis, A. (1993) Effect of initial defiberization on the properties of refiner mechanical pulp. J. Pulp Pap. Sci. 19(3):119–124.Search in Google Scholar

Høydahl, H.-E., Solbakken, M., Dahlquist, G. (1995) TMP for SC grades – A challenge in fiber modelling. In: Int. Mech. Pulping Conf. Montreal, 233–241.Search in Google Scholar

Irvine, G.M. (1985) The significance of the glass-transition of lignin in thermomechanical pulping. Wood Sci. Technol. 19:139–149.10.1007/BF00353074Search in Google Scholar

Johansson, L., Peng, F., Simonson, R. (1997) Effects of temperature and sulfonation on shear deformation of spruce wood. Wood Sci. Technol. 31:105–117.10.1007/BF00705926Search in Google Scholar

Karlström, A., Eriksson, K. (2014) Fiber energy efficiency part II: Forces acting on the refiner bars. Nord. Pulp Pap. Res. J. 29(2):332–343.10.3183/npprj-2014-29-02-p332-343Search in Google Scholar

Karlström, A., Eriksson, K., Sikter, D., Gustavsson, M. (2008) Refining models for control purposes. Nord. Pulp Pap. Res. J. 23(1):129–138.10.3183/npprj-2008-23-01-p129-138Search in Google Scholar

Karnis, A. (1994) The mechanism of fibre development in mechanical pulping. J. Pulp Pap. Sci. 20(10):J280–J288.Search in Google Scholar

Kerekes, R.J. (2011) Force-based characterization of refining intensity. Nord. Pulp Pap. Res. J. 26(1):14–20.10.3183/npprj-2011-26-01-p014-020Search in Google Scholar

Koran, Z. (1967) Electron microscopy of radial tracheid surface of black spruce separated by tensile failure at various temperatures. Tappi J. 50(2):60–67.Search in Google Scholar

Koran, Z. (1981) Energy consumption in mechanical fibre separation as a function of temperature. Pulp Pap. Can. 82(6):TR40–TR44.Search in Google Scholar

Kure, K.-A., Dahlqvist, G. (1998) Development of structural fibre properties in high intensity refining – Cross-sectional fibre dimensions are significantly changed in refining. Pulp Pap. Can. 99(7):59–63.Search in Google Scholar

Kure, K.-A., Dahlqvist, G., Sabourin, M.J., Helle, T. (1999) Development of spruce fibre properties by a combination of a pressurized compressive pretreatment and high intensity refining. In: Int. Mech. Pulping Conf. Houston. pp. 427–433.Search in Google Scholar

Kure, K.-A., Sabourin, M.J., Dahlqvist, G., Helle, T. (2000) Adjusting refining intensity by changing refiner plate design and rotational speed – Effects on structural fibre properties. J. Pulp Pap. Sci. 26:346–352.Search in Google Scholar

Lai, Y.-Z., Iwamida, T. (1993) Effect of Chemical Treatments on Ultra-High-Yield Pulping. 1. Fibre Separation. Wood Sci. Technol. 27:195–203.10.1007/BF00192816Search in Google Scholar

Lindholm, C.A., Kurdin, J.A. (1999) Chemimechanical pulping. In: Sundholm, J, Papermaking Science and Technology, Mechanical Pulping. Fapet Oy, Helsinki. pp. 223–249.Search in Google Scholar

Lunan, W.E., Harris, G., Franzen, R. (1983) High Pressure Refining and Brightening in Thermomechanical Pulping. In: Tappi Pulping Conf. pp. 239–253.Search in Google Scholar

McCrum, N.G., Read, B.E., Williams, G. (1967) Anelastic and Dielectric Effects. In: Polymeric Solids. Wiley, New York. pp. 1–25.Search in Google Scholar

Miles, K.B. (1990) Refining intensity and pulp quality in high consistency chip refining. Pap. Puu 72(5):508–514.Search in Google Scholar

Miles, K.B., May, W.D., Karnis, A. (1991) Refining intensity, energy consumption and pulp quality in two-stage chip refining. Tappi J. 74(3):221–230.Search in Google Scholar

Muhić, D., Huhtanen, J. P., Sundström, L., Sandberg, C., Ullmar, M., Vuorio, P, Engstrand, P. (2011) Energy efficiency in double disc refining – Influence of intensity by segment design. Nord. Pulp Pap. Res. J. 26(3):224–231.10.3183/npprj-2011-26-03-p224-231Search in Google Scholar

Murton, K., Duffy, G. (2005) The influence of pulp residence time on refining intensity and pulp quality. Appita J. 58(1):64–71.Search in Google Scholar

Nelsson, E., Sandberg, C., Hildén, L., Daniel, G. (2012) Pressurised compressive chip pre-treatment of Norway spruce with a mill scale Impressafiner. Nord. Pulp Pap. Res. J. 27(1):56–62.10.3183/npprj-2012-27-01-p056-062Search in Google Scholar

Nelsson, E., Sandberg, C., Svensson-Rundlöf, E., Engstrand, P., Fernando, D., Daniel, G. (2015) Low dosage sulphite pretreatment in a modern TMP-line. Nord. Pulp Pap. Res. J. 30(4):591–598.10.3183/npprj-2015-30-04-p591-598Search in Google Scholar

Nurminen, I. (1999) Influence of refining temperature and intensity (disc rotating speed) on TMP energy consumption and pulp and fibre fraction properties. In: Int. Mech. Pulping Conf.. Houston. pp. 333–345.Search in Google Scholar

Nygaard, J. (1997) Energy aspects on mechanical pulp, chemical pulp and recycled fibres. In: Int. Mech. Pulping Conf. Stockholm. pp. 17–27.Search in Google Scholar

Omholt, I., Miles, K.B. (2008a) Preheating and Refining of Mechanical Pulp at High Temperature. Part I: Fibre Separation and Initial Development. J. Pulp Pap. Sci. 34(1):39–45.Search in Google Scholar

Omholt, I., Miles, K.B. (2008b) Preheating and Refining of Mechanical Pulp at High Temperature. Part II: Final pulp properties. J. Pulp Pap. Sci. 34(1):46–50.Search in Google Scholar

Sabourin, M.J. (2000) Evaluation of a compressive pretreatment process on TMP properties and energy requirements – It extends the quality and energy benefits of low-energy TMP processes. Pulp Pap. Can. 101(2):50–56.Search in Google Scholar

Sabourin, M., Xu, E., Cort, B., Boileau, I., Waller, A. (1997) Optimizing residence time, temperature and speed to improve TMP pulp properties and reduce energy. Pulp Pap. Can. 98(4):38–45.Search in Google Scholar

Salmén, L., Fellers, C. (1982) Fundamentals of energy consumption during viscoelastic and plastic deformation of wood. Trans. Tech. Sect. CPPA 8(4):TR93–TR99.Search in Google Scholar

Schniewind, A.P., Barrett, J.D. (1972) Wood as a linear orthotropic viscoelastic material. Wood Sci. Technol. 6(1):43–57.10.1007/BF00351807Search in Google Scholar

Stationwala, M.I. (1994) Production of high-quality and low-energy chemithermomechanical pulp. Tappi J. 77(2):113–119.Search in Google Scholar

Strand, B.C., Falk, B., Moqvist, A., Jacksom, M. (1993) The effect of production rate on specific energy consumption in high consistency chip refining. In: Int. Mech. Pulping Conf. Oslo. pp. 143–151.Search in Google Scholar

Sundholm, J., Heikkurinen, A., Mannström, B. (1988) The role of rate of rotation and frequency in refiner mechanical pulping. Pap. Puu 5:446–451.Search in Google Scholar

Uhmeier, A., Salmén, L. (1996) Repeated large radial compression of heated spruce. Nord. Pulp Pap. Res. J. 11(3):171–177.10.3183/npprj-1996-11-03-p171-176Search in Google Scholar

Wiberg, R., Forslund, M. (2011) Energiförbrukning i massa- och pappersindustrin (Energy use in the pulp- and paper industry 2011). In: Skogsindustrierna. Stockholm, Sweden. [in Swedish].Search in Google Scholar

Widehammar, S. (2004) Stress-strain relationships for spruce wood: Influence of strain rate, moisture content and loading direction. Exp. Mech. 44(1):44–48.10.1007/BF02427975Search in Google Scholar

Received: 2018-03-22
Accepted: 2018-06-05
Published Online: 2018-08-22
Published in Print: 2018-09-25

© 2018 Walter de Gruyter GmbH, Berlin/Boston

Articles in the same Issue

  1. Frontmatter
  2. Editorials
  3. Farewell and good luck to Nordic Pulp & Paper Research Journal
  4. Change of Editor-in-Chief
  5. Biorefinery
  6. Kinetic study on the decomposition of cellulose into 5-hydroxymethylfurfural in an ionic liquid/organic biphasic system
  7. Antibacterial evaluation of CNF/PVAm multilayer modified cellulose fiber and cellulose model surface
  8. Chemical pulping
  9. Dewatering properties of low grammage handsheets of softwood kraft pulps modified to minimize the need for refining
  10. NSSC pulping of fast growing trees
  11. Addition of corn fiber xylan to eucalyptus and pinus pulp and its effect on pulp bleachability and strength
  12. Recovery
  13. Removal of hazardous trace elements from green liquor dregs by mechanical separation methods
  14. Bleaching
  15. Additives to decrease cellulose chain scission during ozone bleaching of wheat straw pulp
  16. Mechanical pulping
  17. Comparative properties of nanofibers produced using unbleached and bleached wheat straw pulps
  18. Effects of chip pretreatment and feeding segments on specific energy and pulp quality in TMP production
  19. An experimental study of the chipping process with focus on energy consumption and chipping angles
  20. Average fibre length as a measure of the amount of long fibres in mechanical pulps – ranking of pulps may shift
  21. Paper technology
  22. The effect of in-line foam generation on foam quality and sheet formation in foam forming
  23. The wet strength of water- and foam-laid cellulose sheets prepared with polyamideamine-epichlorohydrin (PAE) resin
  24. Manufacture of high bulk paper using alkali swollen kraft pulp
  25. Paper physics
  26. The impact of zeolite filler on ageing and mechanical failure of paper
  27. The relationship between shrinkage and elongation of bleached softwood kraft pulp sheets
  28. Paper chemistry
  29. Engineered porous calcium silicate as paper filler: effect of filler morphology on paper properties
  30. Printing
  31. Edge spread function for the paper-ink system
  32. Packaging
  33. Lignin-containing coatings for packaging materials
  34. Environmental impact
  35. Application of Fenton’s reagent degrades dissolved and colloidal substances in old corrugated container white water
  36. Quick estimation for pollution load contributions of aromatic organics in wastewater from pulp and paper industry
  37. Recycling
  38. Circular action treatment (CAT): a new strategy for mechanical treatment of old corrugated containers II – comparison of CAT with low-consistency beating
  39. Corrigendum
  40. Corrigendum to: The influence of bar width on bar forces and fibre shortening in low consistency pulp refining
Downloaded on 3.11.2025 from https://www.degruyterbrill.com/document/doi/10.1515/npprj-2018-3052/html
Scroll to top button