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Treatment of thermomechanical (TMP) white water with organically-tailored synthetic zeolites Kurniawan, Christophorus Budi
Abstract
In an effort to reduce fresh water usage and wastewater discharge, white water process streams in pulp and paper mills can be targeted for recycling. However, accumulations of dissolved and colloidal substances (DCS) in a closed white water system are detrimental to mill operations, machine runnability, and product quality. This study determined the technical feasibility of using organically-tailored synthetic zeolites, whose cation exchange capacities (CEC) and external CEC (ECEC) values ranged from approximately 80 to 240 meq/lOOg and 20 to 160 meq/lOOg, respectively, for treatments of synthetic process water (SPW) and thermomechanical (TMP) white water (WW) samples. The SPW contained only dehydroabietic acid (DHA) at a concentration of approximately 30 mg/L. Treatment of SPW with untailored synthetic zeolites at 20 g/L mineral dose resulted in removal of 19-45% of DHA. Complete uptakes of DHA were also achieved when water-soluble organic cations (C15 and C17) were used to tailor the zeolites. Lower DHA uptake capacities (9-71% removal efficiencies) were observed when alcohol- (methanol and ethanol) soluble organic surfactants (C20-C40) were used for tailoring the zeolites. Mineral doses of TDTMA-tailored synthetic zeolite as low as 5 g/L removed 90% of the DHA from SPW, and complete DHA removal was obtained at doses of 10 g/L and higher. Also, the uptake of DHA from SPW by TDTMA-tailored synthetic zeolite occurred within minutes of contact, where the maximum removal efficiency was achieved after 3 minutes of treatment. DHA removals at low pH (4-7.25) values ranged from 40 to 100%, as compared to the 20-27% removals observed at pH 10-12. In addition, the removal of DHA from SPW was not affected by the nature of the buffering system used (unbuffered, acetate, and phosphate). Treatment of white waters (pH 7.25) using TDTMA-tailored zeolites at 1 g/L mineral dose resulted in 51% reduction of resin and fatty acids (RFA), 10% removals of soluble biochemical and chemical oxygen demands, 85% removal of acute toxicity, and 24% uptake of sterols. Higher (20 g/L) mineral doses resulted in more complete removals of the compounds of concern: RFA (100%), soluble biochemical oxygen demand (SBOD) (36%), soluble chemical oxygen demand (SCOD) (38%), acute toxicity (91%), and sterols (100%).
Item Metadata
Title |
Treatment of thermomechanical (TMP) white water with organically-tailored synthetic zeolites
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Creator | |
Publisher |
University of British Columbia
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Date Issued |
2001
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Description |
In an effort to reduce fresh water usage and wastewater discharge, white water
process streams in pulp and paper mills can be targeted for recycling. However,
accumulations of dissolved and colloidal substances (DCS) in a closed white water
system are detrimental to mill operations, machine runnability, and product quality.
This study determined the technical feasibility of using organically-tailored
synthetic zeolites, whose cation exchange capacities (CEC) and external CEC (ECEC)
values ranged from approximately 80 to 240 meq/lOOg and 20 to 160 meq/lOOg,
respectively, for treatments of synthetic process water (SPW) and thermomechanical
(TMP) white water (WW) samples. The SPW contained only dehydroabietic acid (DHA)
at a concentration of approximately 30 mg/L.
Treatment of SPW with untailored synthetic zeolites at 20 g/L mineral dose resulted
in removal of 19-45% of DHA. Complete uptakes of DHA were also achieved when
water-soluble organic cations (C15 and C17) were used to tailor the zeolites. Lower
DHA uptake capacities (9-71% removal efficiencies) were observed when alcohol-
(methanol and ethanol) soluble organic surfactants (C20-C40) were used for tailoring the
zeolites. Mineral doses of TDTMA-tailored synthetic zeolite as low as 5 g/L removed
90% of the DHA from SPW, and complete DHA removal was obtained at doses of 10
g/L and higher. Also, the uptake of DHA from SPW by TDTMA-tailored synthetic
zeolite occurred within minutes of contact, where the maximum removal efficiency was
achieved after 3 minutes of treatment. DHA removals at low pH (4-7.25) values ranged
from 40 to 100%, as compared to the 20-27% removals observed at pH 10-12. In
addition, the removal of DHA from SPW was not affected by the nature of the buffering
system used (unbuffered, acetate, and phosphate).
Treatment of white waters (pH 7.25) using TDTMA-tailored zeolites at 1 g/L
mineral dose resulted in 51% reduction of resin and fatty acids (RFA), 10% removals of
soluble biochemical and chemical oxygen demands, 85% removal of acute toxicity, and
24% uptake of sterols. Higher (20 g/L) mineral doses resulted in more complete
removals of the compounds of concern: RFA (100%), soluble biochemical oxygen
demand (SBOD) (36%), soluble chemical oxygen demand (SCOD) (38%), acute toxicity
(91%), and sterols (100%).
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Extent |
11731730 bytes
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Genre | |
Type | |
File Format |
application/pdf
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Language |
eng
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Date Available |
2009-08-13
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Provider |
Vancouver : University of British Columbia Library
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Rights |
For non-commercial purposes only, such as research, private study and education. Additional conditions apply, see Terms of Use https://open.library.ubc.ca/terms_of_use.
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DOI |
10.14288/1.0058942
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URI | |
Degree | |
Program | |
Affiliation | |
Degree Grantor |
University of British Columbia
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Graduation Date |
2002-05
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Campus | |
Scholarly Level |
Graduate
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Aggregated Source Repository |
DSpace
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Item Media
Item Citations and Data
Rights
For non-commercial purposes only, such as research, private study and education. Additional conditions apply, see Terms of Use https://open.library.ubc.ca/terms_of_use.