Javascript must be enabled to continue!
Pre-bleaching of kraft acacia pulp
View through CrossRef
AbstractKraft pulps from acacia hybrid,Acacia mangiumof 8 years old andAcacia auriculiformisof 6, 8 and 10 years old were pre-treated with oxygen, peroxyformic acid and acid treatment prior to bleaching. The kappa number reduction was 52–63 % by oxygen delignification, 31–35 % by peroxyformic acid (PFA) pre-treatment and 11–13 % by acid pre-treatment. Oxygen delignified pulp required less chlorine dioxide charge to reach target brightness. At the consumption of 30 kg ClO2/ton of pulp, the pulp brightness reached to 65–71 % for the untreated pulp, 81–85 % for the oxygen delignified pulp, 81–82 % for the PFA treatment and 79–80 % for acid pre-treated pulp. COD load in bleached effluent was much lower in oxygen delignified pulp. Cold alkali extraction of unbleached and oxygen delignified pulps was also carried out with varying alkali charge to remove hexenuronic acid (HexA) from the pulp. Xylan removal from the pulp was insignificant and resulted in no removal of HexA. Acid pretreatment removed 55.7 % to 17.8 % HexA from acacia hybrid, 57.5 % to 16.3 % fromA. auriculiformisof 10 years and 58.6 % to 20.1 % fromA. auriculiformisof 6 years old, resulting in improved final pulp brightness.
Title: Pre-bleaching of kraft acacia pulp
Description:
AbstractKraft pulps from acacia hybrid,Acacia mangiumof 8 years old andAcacia auriculiformisof 6, 8 and 10 years old were pre-treated with oxygen, peroxyformic acid and acid treatment prior to bleaching.
The kappa number reduction was 52–63 % by oxygen delignification, 31–35 % by peroxyformic acid (PFA) pre-treatment and 11–13 % by acid pre-treatment.
Oxygen delignified pulp required less chlorine dioxide charge to reach target brightness.
At the consumption of 30 kg ClO2/ton of pulp, the pulp brightness reached to 65–71 % for the untreated pulp, 81–85 % for the oxygen delignified pulp, 81–82 % for the PFA treatment and 79–80 % for acid pre-treated pulp.
COD load in bleached effluent was much lower in oxygen delignified pulp.
Cold alkali extraction of unbleached and oxygen delignified pulps was also carried out with varying alkali charge to remove hexenuronic acid (HexA) from the pulp.
Xylan removal from the pulp was insignificant and resulted in no removal of HexA.
Acid pretreatment removed 55.
7 % to 17.
8 % HexA from acacia hybrid, 57.
5 % to 16.
3 % fromA.
auriculiformisof 10 years and 58.
6 % to 20.
1 % fromA.
auriculiformisof 6 years old, resulting in improved final pulp brightness.
Related Results
DISSOLVING PULP FROM KENAF BY BIO-BLEACHING PROCESS
DISSOLVING PULP FROM KENAF BY BIO-BLEACHING PROCESS
The kenaf taken from Malang-East Java was four to five months old and used as the raw material of dissolving pulp. Morphology and chemicals content of kenaf was analyzed based on I...
A preliminary study of skin bleaching and factors associated with skin bleaching among women living in Zimbabwe
A preliminary study of skin bleaching and factors associated with skin bleaching among women living in Zimbabwe
Background: Skin bleaching was reported to be commonly practiced among women and Africa was reported to be one of the most affected yet the subject is not given much attention in p...
Process for the production of dissolving pulp from Trema orientalis (nalita) by prehydrolysis kraft and soda-ethylenediamine (EDA) process
Process for the production of dissolving pulp from Trema orientalis (nalita) by prehydrolysis kraft and soda-ethylenediamine (EDA) process
This paper presents a preliminary study for the production of dissolving pulp from Trema orientalis (Nalita). Water prehydrolysis kraft and soda-ethylenediamine (EDA) pulping for t...
Effects of D0-stage temperature, pH, and kappa factor on chlorine dioxide decomposition and D0-(EP)-D1 bleaching performance for eucalypt pulps
Effects of D0-stage temperature, pH, and kappa factor on chlorine dioxide decomposition and D0-(EP)-D1 bleaching performance for eucalypt pulps
Mills have largely used chlorine dioxide (ClO2) for eucalyptus kraft pulp bleaching. Different mills have observed significant variation in ClO2 demand to reach full brightness (≥9...
Cassava pulp can be nutritionally improved by yeast and various crude protein levels fed to cattle
Cassava pulp can be nutritionally improved by yeast and various crude protein levels fed to cattle
Context Dietary supplementation especially feed residues improve by yeast affected rumen fermentation. Aims The aim of the present experiment was to determine the nutritive...
Improving dissolving wood pulp quality using Brown-stock fractionation
Improving dissolving wood pulp quality using Brown-stock fractionation
Dissolving wood pulp (DWP) contains high levels of cellulose and has various applications. Production of dissolving wood pulp is accompanied by various challenges such as equipment...
Phenol and Tannin Contents of Fresh Phyllodes and Leaf Litter Materials from Three Acacia Species in Brunei Darussalam
Phenol and Tannin Contents of Fresh Phyllodes and Leaf Litter Materials from Three Acacia Species in Brunei Darussalam
Invasive Acacia species are increasingly spreading into degraded forests in Brunei Darussalam since their initial planting in the 1990s. Information on the secondary metabolites of...
MEA/water/AQ-pulping of wheat straw
MEA/water/AQ-pulping of wheat straw
Abstract
Annual plant pulping is faced with serious challenges. Traditional pulping processes with bleaching in chlorine based sequences and without appropriate chem...

