z-logo
open-access-imgOpen Access
Low consistency refining of mechanical pulp — system design
Author(s) -
Christer Sandberg,
Jan-Erik Berg,
Per Engstrand
Publication year - 2017
Publication title -
tappi journal
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 0.217
H-Index - 45
ISSN - 0734-1415
DOI - 10.32964/tj16.7.419
Subject(s) - refining (metallurgy) , pulp (tooth) , specific energy , ultimate tensile strength , process engineering , pulp and paper industry , materials science , energy consumption , efficient energy use , composite material , engineering , metallurgy , medicine , physics , electrical engineering , pathology , quantum mechanics
Many mechanical pulping mills use low consistency (LC) refining for energy efficient fiber development. In this study, energy efficiency and pulp quality were evaluated for six processes, of which four included LC refining. We studied two different types of chip refiners – single disc (SD) and double disc (DD) – with LC refining in the main and reject lines. All process combinations have been used in the Holmen Paper Braviken mill, Sweden, to make thermomechanical pulp for printing papers. LC refining was more energy efficient than high consistency (HC) refining at certain tensile index increases in all evaluated combinations. LC refining in the main line had somewhat higher energy efficiency than did LC refining in the reject line. The type of chip refiner (DD or SD) did not affect the efficiency or pulp property development in LC refining. The process with a combination of DD chip refining and LC refining had the highest energy efficiency (tensile index at certain specific energy consumption). All processes with LC refining produced pulp with somewhat lower light scattering and fiber length than did the corresponding system with only HC refining. Thus, for printing papers, the best combination was LC refining with DD chip refining. LC refiners seem to have a narrow range in specific energy for maximum energy efficiency and a good balance between tensile index increase and fiber length reduction. Much higher specific energy was applied on reject pulp. However, the reject share was only around 30%. The LC refining specific energy, based on main line production, was around 80 kWh/air-dried metric ton (a.d. metric ton), whereas up to 180 kWh/a.d. metric ton was applied in main line.

The content you want is available to Zendy users.

Already have an account? Click here to sign in.
Having issues? You can contact us here
Accelerating Research

Address

John Eccles House
Robert Robinson Avenue,
Oxford Science Park, Oxford
OX4 4GP, United Kingdom