Method for improved pulping using an environmentally friendly pulping aid
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example 1
[0025]A multi-day trial was used to determine the impact of the pulping aid of this invention on mill pulp production. Hardwood chips comprising a majority of maple wood chips were contacted with between 0.2 lbs and 4.0 lbs of pulping aid per ton of dry pulp, the pulping aid being a mixture of 60% terpenes and 40% of a dispersant blend. As summarized in Table 1, at a constant addition level of 2.5 lbs per dry ton of pulp, the H-factor was unchanged. However, rejects were reduced by 45% and the pulp extractives content was reduced by 57.3%. The incremental fiber production realized from the lower rejects level was about 14.4 dry tons per day. Furthermore, the use of a surfactant-based pitch control chemical was eliminated and the use of defoamers was reduced by about 20%.
example 2
[0026]A multi-day trial was used to determine the impact of the pulping aid of this invention on mill pulp production. Hardwood chips comprising a majority of aspen wood chips were contacted with between 0.2 lbs and 4.0 lbs of pulping aid per ton of dry pulp, the pulping aid being a mixture of 60% terpenes and 40% of a dispersant blend. As summarized in Table 1, at a constant addition level of 2.5 lbs per dry ton of pulp, the H-factor was reduced by 8.0%; rejects were reduced by 53% and the pulp extractives content was reduced by 27.3%. In addition, the pulp production rate of the mill was increased by 4.4% from the base rate. The incremental fiber production realized from the lower rejects level was 7.5 dry tons per day. Furthermore, the use of a surfactant-based pitch control chemical was eliminated and the use of defoamers was reduced by about 20%.
example 3
[0027]A relatively long (multi-week) trial was used to determine the robustness of the method of this invention on mill pulp production. Hardwood chips comprising a blend of aspen and maple wood chips were contacted with 0.2 lbs and 4.0 lbs of pulping aid per ton of dry pulp, the pulping aid being a mixture of 60% terpenes and 40% of a dispersant blend. As summarized in Table 1, at a constant addition level of 0.5 lbs per dry ton of pulp the H-factor was reduced by 6.7%; alkalinity was reduced by 4.3% from 23.0 g / L; rejects were reduced by 47% and the pulp extractives content was reduced by 36.1%. Further, the pulp production rate of mill was increased by 4.8% from the base rate. The incremental pulp fiber production realized from the lower rejects level was 5.5 dry tons per day. Furthermore, the use of a surfactant-based pitch control chemical was eliminated and the use of defoamers was reduced by about 20%.
TABLE 1H-FactorExtractives (g / L)RejectsPercentPercentIncremental TonsExampl...
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