scholarly journals Hydrogen Peroxide Bleaching. GreenOx Bleaching Process.

1998 ◽  
Vol 52 (5) ◽  
pp. 630-638
Author(s):  
A. Parén
Keyword(s):  
Hydrogen Peroxide ◽  
Bleaching Process ◽  
Peroxide Bleaching

Study on Magnesium Hydroxide-Based Hydrogen Peroxide Bleaching Process of Nigra poplar CTMP

2011 ◽  
Vol 233-235 ◽  
pp. 1328-1331 ◽  
Author(s):  
Qiang Zhao ◽  
De Zhi Sun ◽  
Ming Yang Zhang ◽  
Su Min Kang
Keyword(s):  
Hydrogen Peroxide ◽  
Reaction Time ◽  
Magnesium Hydroxide ◽  
High Yield ◽  
Pulp Yield ◽  
Pulp Bleaching ◽  
Bleaching Process ◽  
Peroxide Bleaching ◽  
Bleaching Condition ◽  
Pulp Consistency

The Mg(OH)2-based peroxide bleaching process of Nigra poplar CTMP pulp was confirmed. The optimal bleaching condition were as follows: 4% H2O2,1% Mg(OH)2, 15% pulp consistency, the reaction temperature was 80°C and the suitable reaction time was 2 hours. The Mg(OH)2-based bleaching process shows significant benefits over sodium hydroxide process. In contrast, magnesium hydroxide bleaching generates higher pulp yield and lower effluent COD at the same chemical dosage. The study shows peroxide bleaching of CTMP pulp with magnesium hydroxide as alkali source is to be an option for the high-yield pulp bleaching.

Hydrogen Peroxide Bleaching to Wine Corks with a Novel Catalyst

2013 ◽  
Vol 734-737 ◽  
pp. 2282-2286 ◽  
Author(s):  
Li Liu ◽  
Shu Ling Cui
Keyword(s):  
Hydrogen Peroxide ◽  
Cork Stopper ◽  
Capillary Effect ◽  
Sewage Disposal ◽  
Bleaching Process ◽  
Peroxide Bleaching ◽  
Novel Catalyst

A novel catalyst CF-R for hydrogen peroxide bleaching to wine cork stopper was chosen to substitute the traditional imported item, and the corresponding bleaching process was studied. The influence of catalyst CF-R dosage, H2O2 concentration, bleaching temperature and time on cork whiteness and capillary effect were discussed. The optimized bleaching process for wine corks was obtained as follows: H2O2 concentration 14%, catalyst CF-R dosage 80g/L, bleaching temperature 70°Cand bleaching time 60 min. Comparing with the expensive imported catalyst, the amount of catalyst CF-R is greatly decreased, as is significant for not only cutting down the expenditure of chemicals, but also minimizing the burden on bleaching sewage disposal.

New evidence for the role of the borohydride pretreatment on the hydrogen peroxide bleaching of kraft pulp

RSC Advances ◽  
2015 ◽  
Vol 5 (119) ◽  
pp. 98067-98074 ◽  
Author(s):  
Jing Li ◽  
Huichao Hu ◽  
Yanting Song ◽  
Xin-Sheng Chai
Keyword(s):  
Hydrogen Peroxide ◽  
Kraft Pulp ◽  
Carbonyl Groups ◽  
Bleaching Process ◽  
Peroxide Bleaching ◽  
Chemical Pulps ◽  
New Evidence ◽  
Lignin Structure

New evidences for the role of borohydride pretreatment in hydrogen peroxide bleaching process of eucalyptus chemical pulps were provided, i.e., suppressing the catalysis effect of Fe(iii), decreasing carbonyl groups, and constituent lignin structure.

Low Temperature Bleaching of Cotton with a Novel Cationic Activator

2012 ◽  
Vol 608-609 ◽  
pp. 1391-1394
Author(s):  
Yan Li Li ◽  
Zhen Dong Liu ◽  
Xiao Ning Wang
Keyword(s):  
Hydrogen Peroxide ◽  
Low Temperature ◽  
Experimental Method ◽  
Dwell Time ◽  
Bleaching Process ◽  
Fiber Damage ◽  
Peroxide Bleaching ◽  
Bleach Activator ◽  
Fabric Strength ◽  
Activated Peroxide System

A new cationic bleach activator (CBA) N-[4-pyridmoniomethyl)benzoyl]caprolactam bromide (PBCB) was synthesized and evaluated in a hot peroxide bleaching process. The effects of time, temperature and the concentrations of hydrogen peroxide and activator on the bleaching of cotton fabric were investigated using an orthogonal experimental method. The optimal bleaching process of PBCB-activated peroxide system was 5g/L H2O2, 0.5g/L CBA, 40°Cand 45min dwell time under neutral pH, with which a whiteness equivalent to that of the conventional-bleaching system was achieved, but the PBCB system resulted in almost no fiber damage based on fabric strength.

Research on the Bleaching Process of the Non-Silicon Oxygen Bleaching Stabilizer

2014 ◽  
Vol 685 ◽  
pp. 64-67
Author(s):  
Hua Ling He ◽  
Sheng Lu ◽  
Ming Su Song ◽  
Zhi Cai Yu ◽  
De Hong Cheng
Keyword(s):  
Hydrogen Peroxide ◽  
Breaking Strength ◽  
Tetraacetic Acid ◽  
Optimal Conditions ◽  
Hydrogen Peroxide Decomposition ◽  
Bleaching Process ◽  
Peroxide Bleaching ◽  
Peroxide Decomposition ◽  
Silicon Oxygen ◽  
Oxygen Bleaching

In this study, a type of non-silicon oxygen bleaching stabilizer was used to cotton fabric in the hydrogen peroxide bleaching process. This type of novel non-silicon oxygen bleaching stabilizer was prepared mainly with ethylene diamine tetraacetic acid (EDTA) and magnesium chloride. The results showed that adding the non-silicon oxygen bleaching stabilizer into the bleaching solution obviously decreased the hydrogen peroxide decomposition rate and improved the fabric whiteness. Optimal conditions was found as follow: non-silicon oxygen bleaching stabilizer 4.5 g/l; bleaching temperature 75-85 °C; pH of bleaching liquid 11; bleaching time 40-45 min. In summary, the results showed that the self-made non-silicon oxygen bleaching stabilizer could make the cotton fabrics obtained great whiteness, capillary ability and breaking strength.

scholarly journals Improving hydrogen peroxide bleaching of aspen CTMP by using aqueous alcohol media

BioResources ◽  
2011 ◽  
Vol 6 (4) ◽  
pp. 4005-4011
Keyword(s):  
Hydrogen Peroxide ◽  
Pulp Yield ◽  
Aqueous Alcohol ◽  
Laboratory Studies ◽  
Bleaching Process ◽  
Peroxide Bleaching ◽  
Bleaching Procedure ◽  
Mechanical Pulps

Preliminary tests of a new hydrogen peroxide bleaching procedure for mechanical pulps were performed in a bleaching medium comprised of water and an alcohol, which is characterized by good miscibility with water, poor solvency for hemicelluloses, and good solvency for lignin. As compared with a conventional bleaching method, this modified process is aimed at reducing the removal of hemicelluloses while moderately increasing the dissolution of lignin. Results showed that an aspen CTMP pulp can be bleached to a target brightness with less bleaching chemicals and/or with a higher pulp yield. The laboratory studies demonstrate that this new bleaching process offers substantially enhanced efficiency and selectivity over the conventional peroxide bleaching. Overall, the brightness increased by about 5 ISO units for a given peroxide consumption and the yield increased by 2 to 3 percent at the same target brightness.

A Survey of Hydrogen Peroxide Bleaching and FAS Bleaching of Liquid Package Recycled Pulp

2014 ◽  
Vol 1081 ◽  
pp. 48-52
Author(s):  
Zong Juan Xu ◽  
Yu Liu ◽  
Zhen Wang
Keyword(s):  
Adverse Effect ◽  
Hydrogen Peroxide ◽  
Process Conditions ◽  
Pulp Fiber ◽  
Bleaching Process ◽  
Peroxide Bleaching ◽  
Bleached Pulp ◽  
Recycled Pulp

This document demonstrates how to affect the brightness of liquid package recycled pulp by hydrogen peroxide bleaching and FAS beaching. The optimum H2O2 bleaching process conditions: 8% H2O2, 4% NaOH, bleaching temperature 80 °C, bleaching time 1.5h. The best FAS bleaching conditions was FAS dosage of 0.5%, NaOH dosage of 0.25%, bleaching temperature at 80 °C, time for 30min. And bleaching had no adverse effect on the performance of bleached pulp fiber.

The Study of Bleaching Silk Sanitary Materials

2011 ◽  
Vol 175-176 ◽  
pp. 765-768
Author(s):  
Wu Wen Wang ◽  
Ji Hong Lao ◽  
Ya Qin Yang
Keyword(s):  
Hydrogen Peroxide ◽  
Sodium Silicate ◽  
Ph Value ◽  
Raw Materials ◽  
Orthogonal Test ◽  
Experimental Program ◽  
Single Factor ◽  
Silicate Concentration ◽  
Bleaching Process ◽  
Peroxide Bleaching

The silk Sanitary Materials in hydrogen peroxide bleaching process, various experimental factors affect on the raw materials’ whiteness and tension. And through the single factor experiments and orthogonal test research and analysis, the significant influencing order of the whiteness of silk fiber is: temperature, concentration of hydrogen peroxide, and bleaching time; the significant influencing order of breaking tension is: bleaching time, temperature, and concentration of hydrogen peroxide. The optimum experimental program is as follows: hydrogen peroxide concentration of 22.5g / L, bleaching temperature of 80 °C, bleaching time, 60min, PH value of 9, sodium silicate concentration of 11.25g / L.

Sign in / Sign up

Export Citation Format

Share Document