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SL. KUZU et al./ ISEM2016 Alanya – Turkey Figure 3. Temperature distribution at different inlet angles According to the plots in Figure 3, any significant visual variation was not achieved. Apart from 0 ο angle, the inlet with 15 ο and 30 ο seems to have a better temperature distribution. However, in the inlet with 30 ο contact with the waste is lesser in the downstream of the kiln. Inlet with 15 ο is somewhat more preferable than inlet with 30 ο . Inlet with 0 ο and 15 ο were compared in Figure 4. Figure 4. Comparison of inlet angles of 0 ο and 15 ο 774
SL. KUZU et al./ ISEM2016 Alanya – Turkey Figure 4 shows the temperature distribution on a planar surface which is vertically placed in the kiln. The temperature difference at the waste contact level is not significant. Thus, considering this insignificancy and ease of engineering application for hole opening, 0 ο angle was selected for the inlet angle. That means auxiliary air pipes are parallel to the surface of the kiln. 4. Discussion In the previous configuration of the kiln, there was no auxiliary air feed channel. This study helped us to find the accurate places for more efficient combustion. It is decided to open holes for auxiliary air pipes at the bottom of the kiln. Thus, the air had opportunity to contact with the waste at any part of the kiln. Secondly, different geometries with varying inlet hole angles were prepared. It was decided that there was not a significant difference between different configurations. So the inlet pipes were placed parallel to the kiln. The plant is now being operated with the proposed configuration suggested in this study. Conclusions Air feed from the middle or the top of the kiln is not appropriate for the operational purpose. Temperature layering occurs between the air and the waste. This prevents the complete combustion in the upstream of the kiln. The best place for air feed was the bottom of the inlet wall, which is perpendicular to the kiln. Furthermore, the variations in the inlet angles didn’t make significant changes. Pipes were placed parallel to the kiln. Acknowledgements The authors would like to acknowledge ISTAC AS for sharing the rotary kiln geometry and operation details in order to make this study. References [1] Marinkovic N, Vitale K, Holcer NJ, Dzakula A, Pavic t. Management of hazardous medical waste in Croatia. Waste Management 2007; 28:1049-56. [2] Eker HH, Bilgili MS, Sekman E, Top S. Evaluation of the regulation changes in medical waste management in Turkey. Waste Management and Research 2010; 28, 1034-8. [3] Birpınar ME, Bilgili MS, Erdoğan T. Medical waste management in Turkey: A case study of Istanbul. Waste Management 2009; 29, 445-8. [4] Güneş G, Saral A, Yıldız Ş, Kuzu SL. Determination of optimum dose of adsorbent for PCDD/F removal in the flue gas of a medical waste incineration plant. Chemical Engineering Research and Design 2015; 104, 695-702. 775
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