- Company : PC GlobeCore
- Region : Kyyiv , Ukraine
- Category : Manufacturing & Processing Machinery > Other Manufacturing & Processing Machinery
- Price : depend from the productivity
- Contact Person : Oksana Bichurina|||sales manager
- Telephone :
- Fax :
- Mobile phone :
- Website : www.fuelcleaning.globecore.com
- Email : [email protected]
- Instant Messenger : skype: bichurina_globecore
- Update : May/19/2014
Product Details
Full information is on our website www.fuelcleaning.globecore.com Qualitative treatment of wastewater from phenol and other organic contaminants has a great practical importance within different branches of industry. In many cases, contemporary ways of usage by enterprises do not provide high qualitative treatment (degree of phenol decline is 75-90%). These ways have defects such as long process duration from 3 to 5 hours, long processing time, high reagent consumption (pyrolusite, kali bichromate or sodium bichromate), and process temperature is 95–100 ??, bulk equipment, necessity of large working area. We have designed new uninterrupted way of wastewater treatment from phenol and other organic contaminants by means of vortex layer. We tested artificial wastewater by Intensifier of Technological Process. These wastewaters contain similar concentration of phenol, acid and contaminants as real manufacturer’s wastewaters. Content of wastewater is indicated in the table 1. Research suggests that Intensifier of Technological Process provides qualitative treatment of wastewater from phenol at lower cost to compare with other known methods. Conditions of the wastewater treatment by AVS unit from phenol concentration 0.5-10 g/dm3 and acidity of the medium 5 g/dm3 are as follows: -oxidizing agents: potassium bichromate (concentration 0.2-5 g/dm3); manganese dioxide (concentration 1.2-10 g/dm3); potassium permanganate (concentration 0.1-1.0 g/dm3); -wastewater’s temperature - 20–45 ??; -oxidization time – 0.1-2 seconds. AVS unit industrial process flowsheet is much simpler in technological execution than contemporary industrial process flowsheets. According to this process flowsheet phenol wastewater enters to equalizing reservoir which is made to blending and equalization of phenol concentration. Wastewater and potassium bichromate (oxidizing agent with conce
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