Characterization of hard scale formed in the kraft mill green liquor processing equipment

Scaling, the formation of hard deposits, in green liquor handling systems is a persistent problem in many kraft pulp mills. Scaling is commonly believed to be a result of pirssonite (Na 2 CO 3 ·CaCO 3 ·2H 2 O) formation when the green liquor total titrateable alkali (TTA) is high. In this study, we...

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Published in:TAPPI Journal
Main Authors: Zakir, Tasnuva, Tran, Honghi, Papangelakis, Vladimiros G.
Format: Article in Journal/Newspaper
Language:English
Published: TAPPI Press 2013
Subjects:
Online Access:http://hdl.handle.net/1807/98244
https://doi.org/10.32964/tj12.1.53
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spelling ftunivtoronto:oai:localhost:1807/98244 2023-05-15T17:54:51+02:00 Characterization of hard scale formed in the kraft mill green liquor processing equipment Zakir, Tasnuva Tran, Honghi Papangelakis, Vladimiros G. 2013-01 http://hdl.handle.net/1807/98244 https://doi.org/10.32964/tj12.1.53 en_ca eng TAPPI Press Zakir, T., Tran, H., & Papangelakis, V.G. TAPPI J. 12(1): (2013). 0734-1415 http://hdl.handle.net/1807/98244 doi:10.32964/tj12.1.53 Article 2013 ftunivtoronto https://doi.org/10.32964/tj12.1.53 2020-06-17T12:28:36Z Scaling, the formation of hard deposits, in green liquor handling systems is a persistent problem in many kraft pulp mills. Scaling is commonly believed to be a result of pirssonite (Na 2 CO 3 ·CaCO 3 ·2H 2 O) formation when the green liquor total titrateable alkali (TTA) is high. In this study, we characterized 12 scale samples obtained from 10 kraft pulp mills using various analytical methods, including TGA/DSC (thermogravimetric analysis/ differential scanning calorimetry), XRF (X-ray fluorescence spectrometry), XRD (X-ray diffraction spectrometry), SEM (scanning electron microscopy), and EMPA (electron microprobe analyzer). The analysis identified only four of these samples as pirssonite; the remaining consisted mostly of calcite (CaCO 3 ). The reason for the predominant presence of calcite in the majority of the scale samples is not known. It may be a result of selective dissolution of sodium carbonate (Na 2 CO 3 ) from the pirssonite scale during the time when the green liquor total TTA was low, leaving the insoluble CaCO 3 behind. This work was conducted as part of the research program on Increasing Energy and Chemical Recovery Efficiency in the Kraft Process. The program is jointly supported by the Natural Sciences and Engineering Research Council of Canada (NSERC) and a consortium of the following companies: An - dritz, Babcock & Wilcox, Boise, Carter Holt Harvey, Celulose Nipo-Brasileira, Clyde-Bergemann, DMI Peace River Pulp, Fab - ria, International Paper, Irving Pulp & Paper, Metso Power, MeadWestvaco, StoraEnso Research, and Tembec. Article in Journal/Newspaper Peace River University of Toronto: Research Repository T-Space Canada Wilcox ENVELOPE(-66.933,-66.933,-67.949,-67.949) TAPPI Journal 12 1 53 59
institution Open Polar
collection University of Toronto: Research Repository T-Space
op_collection_id ftunivtoronto
language English
description Scaling, the formation of hard deposits, in green liquor handling systems is a persistent problem in many kraft pulp mills. Scaling is commonly believed to be a result of pirssonite (Na 2 CO 3 ·CaCO 3 ·2H 2 O) formation when the green liquor total titrateable alkali (TTA) is high. In this study, we characterized 12 scale samples obtained from 10 kraft pulp mills using various analytical methods, including TGA/DSC (thermogravimetric analysis/ differential scanning calorimetry), XRF (X-ray fluorescence spectrometry), XRD (X-ray diffraction spectrometry), SEM (scanning electron microscopy), and EMPA (electron microprobe analyzer). The analysis identified only four of these samples as pirssonite; the remaining consisted mostly of calcite (CaCO 3 ). The reason for the predominant presence of calcite in the majority of the scale samples is not known. It may be a result of selective dissolution of sodium carbonate (Na 2 CO 3 ) from the pirssonite scale during the time when the green liquor total TTA was low, leaving the insoluble CaCO 3 behind. This work was conducted as part of the research program on Increasing Energy and Chemical Recovery Efficiency in the Kraft Process. The program is jointly supported by the Natural Sciences and Engineering Research Council of Canada (NSERC) and a consortium of the following companies: An - dritz, Babcock & Wilcox, Boise, Carter Holt Harvey, Celulose Nipo-Brasileira, Clyde-Bergemann, DMI Peace River Pulp, Fab - ria, International Paper, Irving Pulp & Paper, Metso Power, MeadWestvaco, StoraEnso Research, and Tembec.
format Article in Journal/Newspaper
author Zakir, Tasnuva
Tran, Honghi
Papangelakis, Vladimiros G.
spellingShingle Zakir, Tasnuva
Tran, Honghi
Papangelakis, Vladimiros G.
Characterization of hard scale formed in the kraft mill green liquor processing equipment
author_facet Zakir, Tasnuva
Tran, Honghi
Papangelakis, Vladimiros G.
author_sort Zakir, Tasnuva
title Characterization of hard scale formed in the kraft mill green liquor processing equipment
title_short Characterization of hard scale formed in the kraft mill green liquor processing equipment
title_full Characterization of hard scale formed in the kraft mill green liquor processing equipment
title_fullStr Characterization of hard scale formed in the kraft mill green liquor processing equipment
title_full_unstemmed Characterization of hard scale formed in the kraft mill green liquor processing equipment
title_sort characterization of hard scale formed in the kraft mill green liquor processing equipment
publisher TAPPI Press
publishDate 2013
url http://hdl.handle.net/1807/98244
https://doi.org/10.32964/tj12.1.53
long_lat ENVELOPE(-66.933,-66.933,-67.949,-67.949)
geographic Canada
Wilcox
geographic_facet Canada
Wilcox
genre Peace River
genre_facet Peace River
op_relation Zakir, T., Tran, H., & Papangelakis, V.G. TAPPI J. 12(1): (2013).
0734-1415
http://hdl.handle.net/1807/98244
doi:10.32964/tj12.1.53
op_doi https://doi.org/10.32964/tj12.1.53
container_title TAPPI Journal
container_volume 12
container_issue 1
container_start_page 53
op_container_end_page 59
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