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  • https://doi.org/10.2172/5569413Copy DOI Icon

Process integration study Kraft and Magnefite pulp and paper mill

  • Dec 1, 1989
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Abstract

The James River Camas mill produces 500,000 tons/year of paper from an integrated operation comprising both Kraft and Magnefite pulping, bleaching, recovery and paper machines. In addition to liquor recovery boilers the mill burns hog fuel and gas to supplement steam requirements. Electrical power demands on the site are met by a combination of on site back pressure turbines and purchased power. The mill was studied by the pinch analysis method and revealed scope to reduce thermal energy requirements by 12% on the Nos. 15, 16 and 20 paper machines and 7% in the cross pinch heat transfer in the existing mill configuration. These savings are equivalent to approximately 73 MBtu/hr in process steam, or 6.2% of total energy use. Pinch techniques reveal additional potential to save between 11--16 MBtu/hr in steam by appropriate process change, principally to black liquor concentrator and evaporator configuration. More significantly, about 36 MBtu/hr steam savings could be achieved by vapor compression heat pumping at the expense of about 1.3 MW electrical power. This amounts to 2.5% of total energy use. To realize these savings appropriate heat recovery networks are required downstream of the modified process equipment. Further scope was identified but not quantified on the remaining paper machines both to make heat savings and to integrate gas turbine power generation. Projects were identified to save up to 38 MBtu/hr of steam by process integration (i.e. 2.7% of total energy use). With appropriate process changes to concentrator configuration this saving can be increased by 9 MBtu/hr. Alternatively, vapor compression heat pumping can achieve 16 MBtu/hr in additional steam savings (1.8% of total energy use). 30 figs., 1 tab.

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