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Energieffektivisering av aerbo reningsprocess

Tillsats av biprodukter i skogsindustriellt avloppsvatten


In the production of pulp, paper and cardboard, a large amount of water is used daily. The water has to be purified in the internal purifying plant before it reaches the receiving body of water. In the biological purifying stage at the Stora Enso Skoghall mill, an aerated basin is used where the microorganisms, using oxygen, oxidize the organic material to carbon dioxide. The air is pumped from the bottom of the basin and the oxygen can then be transported from the air bubbles to the water through diffusion. The problem with aeration of waste water from the forest industry is that wood residues, such as fatty acids, are making the transport of oxygen in water more difficult. Previous studies show that adding salt improves aeration and the use of energy during the aeration process decreases.In many of the Swedish forest industries the electric power required for the aeration process is responsible for more than 50% of the total use of energy. The aim of this report is to study the aeration of waste water from a forest industry in order to make the aeration in the biological purification stage more energy efficient.The experimental part includes aeration experiments and measurement of surface tension when adding salt in clean and untreated process water. All experiments have been carried out in lab-scale at Karlstad University. The salts used during the study were sodium chloride, lime sludge and also precipitator dust, of which the two latter are by-products of pulping. The project has reached its goal, to compare and measure the speed of aeration when adding different salts to waste water from the forest industry in order to make the purification process more efficient. This study shows that adding by-products may increase the speed of the aeration of waste water from the forest industry and decrease the use of energy during the aerobic treatment process. Adding precipitator dust to the fabrication water increases the speed of the aeration by 60%. The standard oxygen transfer rate (SOTR) decreased from 314tonnes O2/d to 118tonnes O2/d. The energy demand during the aeration process decreased by 100 MWh per day. 

Författare

Isabell Niklasson

Lärosäte och institution

Karlstads universitet/Fakulteten för hälsa, natur- och teknikvetenskap (from 2013)

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