Removal of heavy metal from industrial wastewater
Researchers at Universiti of Tenaga Nasional, Malaysia, embarked on a study to interpret the biosorption process and then develop a cost-effective technology to treat heavy metals-containing industrial wastewater. A new composite biosorbent was prepared by coating chitosan on to acid-treated oil palm shell charcoal (AOPSC). Chitosan loading on the AOPSC support is about 21 per cent by weight. The shape of the adsorbent is nearly spherical, with particle diameter in the range of 100~150 µm.


Results have shown that the use of chitosan-coated AOPSC for removal of chromium ions is environment- friendly, technically viable and quite efficient. Moreover, being composed entirely of agricultural and fishing industry waste, it helps in reducing waste generation. The adsorbent can be regenerated using sodium hydroxide and as such can be reused. This adsorbent can be a good candidate for adsorption of not only chromium ions but also other heavy metal ions in wastewater stream.


Contact: Saifuddin M. Nomanbhay, Chemistry Unit, Dept. of Engineering Sciences, College of Engineering, the Universiti of Tenaga Nasional, 43900 Kajang Selangor, Malaysia. Tel: +60 (3) 8928 7285; Fax: + 60 (3) 8921 2116


E-mail: saifuddin@uniten.edu.my


Website: www.ejbiotechnology.info
Oxidation of reactive blue dye wastewater
Pre-ozonation has been found to be effective in decolourizing and raising the biodegradability of textile dye wastewater while lowering pollution load. However, the cost of ozonation is high due to poor gas-liquid mass transfer and self-decomposition reactions. Ozonation efficiency can be increased by in situ generation of ozone and reacting it immediately with the wastewater contaminants.


In the United States, researchers at Kansas State University have developed a novel porous electrode system for the generation and reaction of ozone with contaminants in aqueous phase. The in situ ozone generator is based on a novel type of corona discharge tube design, wherein the discharge gap is kept juxtaposed to the tubular pathway through which the treatment fluid is passed. Ozone is generated around the periphery of the porous electrode tube and diffuses immediately into the contaminated fluid flowing inside the tube. The inner porous ceramic tube is grounded and the outer glass electrode positively charged to enable corona discharge.


Contact: Mr. Alexander P. M./Mr. Kishora K. Panda, Civil Engineering, Kansas State University, Fiedler Hall, KS 66506, Manhattan, United States of America.


Website: www.aiche.confex.com
Biological process for nitrogen removal
Several nitrification/denitrification methods are available for ammonia and nitrate removal from municipal and industrial wastewater. There are, however, few such methods for the removal of these ions from metal-processing and finishing wastewater. Researchers at Rhodes University, South Africa, examined a biological process for this purpose. The system comprises an aerobic continuously stirred tank reactor (CSTR) followed by an anaerobic packed column. It was tested using wastewater effluent of a metal-processing operation. The proprietary system was inoculated using humus sludge from a municipal trickling filter, and a period of approximately four weeks was required for a denitrifying biofilm to develop.


Results have shown that ammonia removal occurs readily in the CSTR while nitrite oxidation was slower to develop. The CSTR was found to be suitable for ammonia oxidation: up to 89 per cent ammonia removal was achieved. The gravel-packed column reactor was not found to be suitable for nitrate removal in the configuration used (maximum 15 per cent removal efficiency). Critical parameters for denitrification include nitrate concentration, temperature, mean cell retention time and influent flow rate.


Contact: Ms. Joanna E. Burgess, Dept. of Biochemistry, Microbiology and Biotechnology, Rhodes University, Grahamstown 6140, South Africa.


Website: www.wrc.org.za
Advanced treatment for textile wastewater
In China, researchers have studied a method that integrates electrochemical oxidation and membrane filtration to treat wastewater from the textile industry. The team employed a modified transfer-flow membrane (TFM) module, with fibres welded in an arc shape to raise mechanical properties of the fibres as well as enhance the TFM module’s specific membrane surface. The research focused on evaluating performance of the arc-shaped TFM module to demonstrate these sequences of electrochemical oxidation coupled with membrane filtration processes and to develop a potential dye-house wastewater treatment system.


Two testing sequences of electrochemical oxidation and membrane filtration were studied in a sequential batch order. Results have shown that fibres welded in an arc shape enhance the mechanical properties of the fibres effectively. Also, electrochemical oxidation and membrane filtration are feasible as sequential methods. Electrochemical oxidation has high removal efficiency (89.8 per cent) of the wastewater’s chemical oxygen demand (COD), while the membrane filter can almost totally – nearly 100 per cent reduction – remove the total suspended solids (TSS) and turbidity (98.3 per cent elimination) in it.


Contact: Mr. Yaobo Fan, Research Centre for the Eco-environmental Sciences, Chinese Academy of
Sciences, Shuangqing Road 18, Beijing 10085, China; Or Mr. Xuejun Chen, Shanghai Jiaotong University, Dongchuan Road 800, Shanghai, 200240, China.


Website: www.wrc.org.za
Wastewater treatment plant for electronics industry
The chemicals used by each printed circuit board (PCB) shop differ. As such, each generate different liquid waste with metals and other contaminants. Kurion Technologies Ltd., the United Kingdom, offers a range of standard stand-alone technologies that can be combined to treat different types of wastewater from the manufacturing facilities.


The simplest treatment is a metal precipitation process designed to meet discharge limits. This “end-of-pipe” concept, the lowest capital cost option, utilizes proprietary two-step reaction system in combination with cyclone settlement technology. Limits of 1.0 ppm copper and 0.4 ppm lead are achievable. Additionally, up to 0.1 ppm copper and 0.1 ppm lead is feasible with IX polishing technology. Much more lower limits can be realized by special chemistry and waste segregation techniques.


Kurion’s batch treatment system or TREAT-RESIST treats other wastes such as permanganate of dry film stripper and developer dumps. Metal recovery and sludge minimization combined with guaranteed effluent compliance is feasible. Treatment of copper solution is accomplished by recirculating the fluid through an electrowinning cell, thus depositing copper on to the cathodes. Kurion has developed a plate-out cell suitable for treating a variety of spent solutions. Typically, over 90 per cent of the metal is recovered from each individual bath. Other systems from Kurion include:
 
  • IX/ER system for copper recovery from rinses and low copper ores;
     
  • The lead-resin system, a cost-effective option to treat lead bearing rinses; and
     
  • Electroless Nickel IX wastewater treatment plant for the treatment of electroless nickel. The ion exchange process employs a proprietary resin to capture nickel to comply with discharge limits below 0.5 ppm.
     

Contact: Kurion Technologies Ltd., 43, Brunel Close, Drayton Fields Industrial Estate, Daventry, Northants NN11 8RB, United Kingdom. Tel/Fax: + 44 (1327) 876 600/705 131


E-mail: info@kurion.co.uk


Website: www.kurion.co.uk

Cryomagnets for wastewater treatment
A purification system developed by Prof. Shigehiro Nishijima and others at Osaka University, Japan, utilizes cryomagnets to treat wastewater from recycled paper plants. In this process, magnetite or iron oxide particles added to the wastewater react with impurities in the waste-forming magnetic compounds. The compounds are then attracted to a stainless filter under the intense magnetic force of a niobium titanium cryomagnet when the wastewater passes through the filter. Both the size and cost of the new system are less than half that of existing units, typically based on activated sludge method.


Website: www.uknow.or.jp
Extracting metal fluoride from waste
R&F Co. Ltd., Republic of Korea, offers technology to recycle fluorine-containing wastewater produced by the semiconductor industry. In this procedure, a metal fluoride reactor tank is constructed as part of the existing wastewater treatment process, which produces metal fluoride through precipitation and filtration. Additional metal fluoride is obtained by eliminating fluoride ions left from the filtered water, utilizing calcium hydroxide sludge. Fluorine ion concentrations less than 3 ppm can be achieved. High-purity metal fluoride thus reclaimed could be used as a solvent for fluoride glass, a solvent for metal fluoride welding rods and as an electrode material for lithium batteries.


Contact: R&F Co. Ltd., 1-139, College of 220 Kung-dong, Yusong-gu, Daejeon city, Republic of Korea. Tel: +82 (42) 8216 692; Fax: +82 (42) 8221 331


E-mail: bjs123@empal.com


Website: www.rnf21.co.kr

Website: www.eng.me.go.kr

Treating industrial/municipal wastewater
Waterleau, Belgium, is offering a so-called hybrid system that combines the benefits of conventional wastewater treatment and SBR methods. Lucas®, a cyclic activated sludge system, in its basic configuration comprises three reactors, all with a similar design and equipment. The reactors are interconnected through openings in common walls. Influent can be sent to each reactor, just as the effluent can be discharged from them individually. In each basin, the desired process environment can be created – aerobic, anoxic, anaerobic or sedimentation state. Individual inlets and outlets can be automatically closed/opened. Influent is fed directly to the reactors. Each basin includes a combined feeding-and- aeration phase, an aeration phase and a sedimentation phase. Thus, each reactor is subsequently:
 
  • Fed and aerated;
     
  • Aerated; and
     
  • Not aerated in order to facilitate sedimentation.
     

Effluent and excess sludge are withdrawn from the reactor that is in sedimentation. The length of the phases can be adapted according to hydraulic and organic loading.


Contact: Waterleau, Radioweg 18, B 3020 Herent (Leuven), Belgium. Tel/Fax: +32 (16) 650 657/663


E-mail: info@waterleau.com


Website: www.water-leau.com

Desalination of organic wastewater
Research has been carried out in China to assess the efficacy of an evaporation crystallizer for desalinating alkaline organic wastewater. Researchers devised a wastewater evaporation-desalination pretreatment method to remove potassium (K) and sodium (Na) in wastewater that contains volatile organic compounds (VOCs) before it is passed on to the incinerator. VOCs in the wastewater volatilize in the evaporation unit and the ensuing vapours get combusted in the incinerator. In a simulation, phenol wastewater with sodium chloride (NaCl) was evaporated and concentrated, and NaCl crystallized. Results have demonstrated that the higher initial density of NaCl increases the ratio of volatilization of VOCs. This is due to the effect of “salting out” – a fall in the solubility of the non-electrolyte in solution, or more rigorously, an increase in its activity coefficient – caused by the salt addition.


When the evaporation speed was increased from 1.67 ml/min to 2.73 ml/min, total removal coefficient of NaCl was 99.88-99.99 per cent. This pretreatment eliminates slag phenomenon caused by Na and K salts during incineration of wastewater.


Contact: Mr. M.A. Jing-ying, City Construction Department, Zhejiang College of Construction, Hangzhou 311231, China.


E-mail: majy75@163.com


Website: www.zju.edu.cn
Purification of tannery effluent
At the University of Waikato, New Zealand, a new electrolytic effluent processor that enables purification of tannery effluents has been designed by a research team. The specialized proprietary prototype effluent processor, which is based on a novel anode design, was tested extensively and satisfactory results obtained during continuous inline operation, despite wide variation in the composition of the inflow. Over 90 per cent removal of chromium from solution, with similar reductions in turbidity, were achieved at lower operating cost, residual aluminium and total aluminium addition than by dosing with usual commercial aluminium-based flocculants such as poly-aluminium chloride.


While the system performed well under conditions of a real tannery, the mechanism of operation was difficult to discern in the field. This was due to the numerous types of compounds in the effluent and the rapidly varying absolute and relative levels of the component impurities. Particularly, the excellent results with low residual aluminium at pH in excess of 9.5 was unexpected, given the high solubility of aluminium at that pH. Also, the effect of pulsed voltage waveforms was trialed at the tannery, but any effects were swamped by the rapid variations in the effluent content.


Contact: Mr. Alan Langdon, Chemistry Dept., University of Waikato, Private Bag 3105, Hamilton, New Zealand.


Website: www.ecsmeet2.peerx-press.org
Membrane modules to treat wastewater
Koch Membrane Systems Inc., the United States, is offering PURON® submerged membrane modules for membrane bioreactor (MBR) treatment of municipal and industrial wastewater. These technologically advanced membrane modules raise water quality while needing less space than conventional alternatives.


PURON’s patented module design provides reliable removal of filtered material. Hollow fibre membranes, 2 mm in diameter with a pore size less than 0.1 µm, are bundled in a single header at their lower end. Each hollow fibre membrane filter is sealed at the upper end and left to float freely. The filter membrane is coated on a braid, increasing the mechanical strength of each fibre to ensure that they do not break or delaminate. Water flows from the outside to the inside of the filters. Solids and particulates, including bacteria, are blocked and remain on the outside, while the permeate is withdrawn from inside the fibres.


Contact: Koch Membrane Systems Inc., 850-T Main St., Wilmington, MA 01887, the United States. Fax: +1 (978) 6575 208


E-mail: info@kochmembrane.com


Website: www.kochmembrane.com


Website: www.news.thomasnet.com