Polyaluminium chloride and flocculation aids for colour removal from biologically treated textile mill effluent

2018 ◽  
Vol 9 (2) ◽  
pp. 150
Author(s):  
Gemima Santos Arcanjo ◽  
Pedro Henrique Guerra Alves ◽  
Rafael Kopschitz Xavier Bastos ◽  
Leonardo Oliveira Cordeiro
Keyword(s):  
Textile Mill ◽  
Colour Removal ◽  
Polyaluminium Chloride

Polyaluminium chloride and flocculation aids for colour removal from biologically treated textile mill effluent

2018 ◽  
Vol 9 (2) ◽  
pp. 150
Author(s):  
Leonardo Oliveira Cordeiro ◽  
Rafael Kopschitz Xavier Bastos ◽  
Gemima Santos Arcanjo ◽  
Pedro Henrique Guerra Alves
Keyword(s):  
Textile Mill ◽  
Colour Removal ◽  
Polyaluminium Chloride

Fungal mediated decolorization of media containing procion dyes

2001 ◽  
Vol 43 (2) ◽  
pp. 285-290 ◽  
Author(s):  
S. Sumathi ◽  
B. S. Manju
Keyword(s):  
Fungal Biomass ◽  
Large Scale ◽  
Reactive Dyes ◽  
Exponential Growth Phase ◽  
Dye Uptake ◽  
Significant Extent ◽  
Textile Mill ◽  
Colour Removal ◽  
Aspergillus Foetidus ◽  
Uptake Process

An isolated fungus, Aspergillus foetidus was found to effectively decolorize media containing azo reactive dyes, namely Procion dyes, under aerobic conditions. The extent of colour removal was 90% within 48 h of growth of the fungus. The entire colour was found to be strongly bioadsorbed to the rapidly settling spherical fungal biomass pellets. Our investigations reveal that the process of decolorization is concomitant with the exponential growth phase of the fungus and has an obligate requirement for a biodegradable substrate such as glucose. Kinetic analyses of fungal decolorization indicate that the rates of colour uptake decrease to a significant extent with increasing initial concentrations of dye. The fungus was able to grow and decolorize media in the presence of 5 ppm of chromium and 1% sodium chloride. An alternate and cheaper carbon source such as starch supported the growth and decolorization process. These results suggest that the dye uptake process mediated by Aspergillus foetidus has a potential for large-scale treatment of textile mill discharges.

Comparison of the efficacy of oxidative processes and flocculation for the removal of colour from Eop effluent

2007 ◽  
Vol 55 (6) ◽  
pp. 57-64 ◽  
Author(s):  
E.N. Joss ◽  
K.G. McGrouther ◽  
A.H. Slade
Keyword(s):  
Hydrogen Peroxide ◽  
Kraft Pulp ◽  
Operating Costs ◽  
Treated Wastewater ◽  
Colour Removal ◽  
Oxidative Treatment ◽  
Bleached Kraft Pulp ◽  
Physico Chemical ◽  
Oxidative Processes ◽  
Polyaluminium Chloride

Up to 30% of the released colour arising from bleached kraft pulp and paper production comes from the alkaline extraction stage. This waste stream can therefore be readily targeted to remove colour at source in mills where improved colour management is required. The efficacy of five advanced oxidative treatment and physico-chemical technologies in removing colour from a typical Eop stage effluent was compared. The most effective oxidative treatment was peroxymonosulphate (79% colour removal in 15 minutes). Ozone and TAML® treatments removed 74% and 58% of colour respectively within 30 minutes. In comparison, hydrogen peroxide alone was only able to remove 35% of the colour over 4 hours. Coagulation with polyaluminium chloride achieved 89% colour removal within 5 minutes. However, this treatment produced an undesirable sludge, and may cause toxicity in the treated wastewater. Overall, colour removal ability of the five technologies ranked from highest to lowest was polyaluminium chloride > peroxymonosulfate > ozone > TAML® > hydrogen peroxide. Other factors, such as operating costs, feedstock modification and capital infrastructure, also need to be taken into account when selecting the most suitable colour management option.

Особенности стандартизации химических реагентов для подготовки питьевой воды (на примере коагулянта полиоксихлорида алюминия)

2020 ◽  
Author(s):  
G. Samburskii ◽  
O. Ustinova ◽  
Svetlana, Leont’eva
Keyword(s):  
Organic Contaminants ◽  
Disperse Medium ◽  
Metal Salts ◽  
National Standard ◽  
Process Technology ◽  
Technical Regulation ◽  
Uniform Assessment ◽  
Dissolved Form ◽  
Polyaluminium Chloride

Распространенным технологическим приемом удаления из воды грубодисперсных примесей, находящихся во взвешенном состоянии, а также коллоидных органических загрязнений, присутствующих в растворенном виде, является процесс коагуляции. Эффективными коагулянтами для систем с водной дисперсионной средой являются соли поливалентных металлов. Цель работы заключалась в создании нового государственного стандарта, предназначенного для обеспечения единообразной оценки качества коагулянтов. Рассмотрена область применения коагулянтов в процессе водоподготовки и проведен их сравнительный анализ. Показана необходимость унификации в области процессов контроля качества коагулянтов. Сформулированы общие требования к контролю качества полиоксихлорида алюминия. Представлен разработанный и утвержденный новый национальный стандарт ГОСТ Р 58580-2019 Полиоксихлорид алюминия. Технические условия , который учитывает требования санитарного законодательства, технического регулирования, безопасности процессов производства и транспортировки полиоксихлорида алюминия.Coagulation process has been a widespread process technology for removing coarse suspended impurities from water, as well as colloidal organic contaminants present in dissolved form. Polyvalent metal salts are effective coagulants for the systems with aqueous disperse medium. The purpose of the work was developing a new state standard to provide for a uniform assessment of the quality of coagulants. The scope of coagulants in the process of water treatment is considered and their comparative analysis is carried out. The general requirements to the control of polyaluminium chloride quality are formulated. The developed and approved new national standard GOST R 58580-2019 Polyaluminium chloride. Technical conditions is presented that takes into account the requirements of sanitary legislation, technical regulation, safety of the processes of production and transportation of polyaluminium chloride.

Extra colour removal in a refinery

2011 ◽  
pp. 718-725 ◽  
Author(s):  
Laura Diego ◽  
Fernando Martín ◽  
Marta G de Quevedo ◽  
Jaime Sagristá
Keyword(s):  
Refining Process ◽  
Ion Exchange Resins ◽  
Colour Removal ◽  
Precipitated Calcium Carbonate ◽  
Sodium Bisulphite ◽  
Powdered Carbon ◽  
Raw Sugar ◽  
Sugar Refinery ◽  
Exchange Resins ◽  
Main Factor

The main factor affecting the raw sugar refining process is certainly “colour”. The higher colour removal, the higher is the obtained sugar yield. Therefore, colour removal is the main goal throughout the process. In a conventional sugar refinery colour is removed in the purification and decolorisation steps – the second one is normally done using ion-exchange resins – but there are some other ways of colour removal such as adding some colour removing agents (powdered carbon, sodium bisulphite, PCC [precipitated calcium carbonate]). In this article the pilot plant results of experiments of increasing colour removal in the refining process are described, such as PCC addition, 3rd carbonatation (re-purification), hydrogen peroxide addition, powdered carbon addition, sodium bisulphite addition and crystallization improvements. The good results achieved in some of these trials led to perform some industrial trials, the results of wich are summarized in this article as well.

Decolorisation of natural organic matter by Phanerochaete chrysosporium: the effect of environmental conditions

2004 ◽  
Vol 4 (4) ◽  
pp. 175-182 ◽  
Author(s):  
K. Rojek ◽  
F.A. Roddick ◽  
A. Parkinson
Keyword(s):  
Organic Matter ◽  
Ionic Strength ◽  
Natural Organic Matter ◽  
Phanerochaete Chrysosporium ◽  
Fungal Growth ◽  
Low Ph ◽  
Colour Removal ◽  
Humic Material ◽  
Carbon And Nitrogen ◽  
Carbon And Nitrogen Content

Phanerochaete chrysosporium was shown to rapidly decolorise a solution of natural organic matter (NOM). The effect of various parameters such as carbon and nitrogen content, pH, ionic strength, NOM concentration and addition of Mn2+ on the colour removal process was investigated. The rapid decolorisation was related to fungal growth and biosorption rather than biodegradation as neither carbon nor nitrogen limitation, nor Mn2+ addition, triggered the decolorisation process. Low pH (pH 3) and increased ionic strength (up to 50 g L‒1 added NaCl) led to greater specific removal (NOM/unit biomass), probably due to increased electrostatic bonding between the humic material and the biomass. Adsorption of NOM with viable and inactivated (autoclaved or by sodium azide) fungal pellets occurred within 24 hours and the colour removal depended on the viability, method of inactivation and pH. Colour removal by viable pellets was higher under the same conditions, and this, combined with desorption data, confirmed that fungal metabolic activity was important in the decolorisation process. Overall, removals of up to 40–50% NOM from solution were obtained. Of this, removal by adsorption was estimated as 60–70%, half of which was physicochemical, the other half metabolically-dependent biosorption and bioaccumulation. The remainder was considered to be removed by biodegradation, although some of this may be ascribed to bioaccumulation and metabolically-dependent biosorption.

Evaluation of treatability for two textile mill effluents

1999 ◽  
Vol 40 (1) ◽  
pp. 145-152 ◽  
Author(s):  
F. Germirli Babuna ◽  
B. Soyhan ◽  
G. Eremektar ◽  
D. Orhon
Keyword(s):  
Experimental Investigation ◽  
Biological Treatment ◽  
Chemical Oxidation ◽  
Domestic Sewage ◽  
Hydrolysis Rate ◽  
Textile Mill ◽  
Acrylic Fiber ◽  
Partial Chemical

The study emphasizes wastewater characteristics of two different textile plants as they apply to biological treatment. Although conventional characterization reveals no major differences, the effluents from the acrylic fiber and yarn dyeing plant exhibit all the properties of a non-biodegradable wastewater. Appropriate pretreatment consisting of partial chemical oxidation with H2O2 reduces its COD content to 700 mg l−1, almost entirely biodegradable whereas COD fractionation indicates that the effluents of the cotton knit dyeing plant contain 9% residual fractions. Experimental investigation shows that most kinetic and stoichiometric properties of both wastewaters are compatible with that of domestic sewage with the exception of a much slower hydrolysis rate.

Use of a sequencing batch biofilter for degradation of azo dyes (acids and bases)

2000 ◽  
Vol 42 (5-6) ◽  
pp. 329-336 ◽  
Author(s):  
M. Quezada ◽  
I. Linares ◽  
G. Buitrón
Keyword(s):  
Azo Dyes ◽  
Azo Dye ◽  
Degradation Rate ◽  
Removal Rate ◽  
Textile Effluent ◽  
Colour Removal ◽  
Substrate Degradation ◽  
Acids And Bases ◽  
Removal Efficiencies ◽  
Basic Red 46

The degradation of azo dyes in an aerobic biofilter operated in an SBR system was studied. The azo dyes studied were Acid Red 151 and a textile effluent containing basic dyes (Basic Blue 41, Basic Red 46 and 16 and Basic Yellow 28 and 19). In the case of Acid Red 151 a maximal substrate degradation rate of 288 mg AR 151/lliquid·d was obtained and degradation efficiencies were between 60 and 99%. Mineralization studies showed that 73% (as carbon) of the initial azo dye was transformed to CO2 by the consortia. The textile effluent was efficiently biodegraded by the reactor. A maximal removal rate of 2.3 kg COD/lliquid·d was obtained with removal efficiencies (as COD) varying from 76 to 97%. In all the cycles the system presented 80% of colour removal.

Sign in / Sign up

Export Citation Format

Share Document