วารสารวิชาการพระจอมเกล้าพระนครเหนือ ปีท่ี 12 ฉบับที่ 2 เม.ย. - มิ.ย. 2545 The Journal of KMITNB., Vol. 12, No. 2, Apr. - Jun. 2002 Correlation between Excess Oxygen Level and Secondary Combustion Chamber Temperature on the Combustion Efficiency from the Incineration of Real Infectious Waste in A Controlled-Air Incinerator Woranuch Jangsawang* and Somrat Kerdsuwan** Abstract results of the experimental investigation shown that The prime objective of this study is to study the secondary air supplies influence on the the correlation between the excess oxygen level and combustion efficiency of gaseous exit from primary secondary combustion chamber temperature. chamber. The combustion with higher secondary air According to the amount of secondary air supply supply achieves lower CO concentration and higher influence on both the temperature distribution in O2 level. Moreover the results shown NO and SO2 secondary chamber and the oxygen level exiting were not evident on the adjusting of secondary air secondary chamber. Proper air supply is key to the supply. The real infectious waste has the achievement of high combustion efficiency and disconsistency with respect to heating values and reduction of pollutant emissions. Experiments, using moisture contents. These effects result on the a prototype 50 kg/hr controlled-air incinerator with variety of combustion behavior and combustion two combustion chamber, were performed to efficiency. So, the optimum way to optimize the investigate the influence of secondary air supply secondary air supply in a controlled-air incinerator rate on the combustion efficiency of real infectious for burning the disconsistency waste should be waste. The effective preheating primary chamber add the oxygen regulator system to get the optimum temperature and feeding waste is 700 °C with 5 kg secondary air supply by using the information from feeding waste. These results are used as the this study. starting point to optimize the operating conditions for the real infectious waste. By adjusting the Keywords : Secondary air supply rate, Infectious secondary air supply rate and studied its effect on waste, Optimization, Disconsistency, the combustion efficiency which is the correlation Incineration between the excess oxygen level and secondary chamber temperature. Specifically, under the constant 1. Rational conditions (e.g., preheating primary and secondary The formation and generation of the gaseous chamber temperature, feeding waste and primary air emissions from incineration are dependent on either supply), the combustion gas temperatures and the availability of certain materials in the waste feed concentration of gaseous emissions were measured or on the efficiency of the combustion process [1]. under various secondary air supplies. The significant There are two strategies that are used to control * The Joint Graduate School of Energy & Environment, King Mongkut’s University of Technology Thonburi. ** The Waste Incineration Research Center (WIRC), Department of Mechanical Engineering, Faculty of Engineering, King Mongkut’s Institute of Technology North Bangok. 21 วารสารวิชาการพระจอมเกล้าพระนครเหนือ ปีท่ี 12 ฉบับที่ 2 เม.ย. - มิ.ย. 2545 The Journal of KMITNB., Vol. 12, No. 2, Apr. - Jun. 2002 gaseous pollutants from incineration [2]. The first al.,[8] .The results shown that the real infectious strategy uses the air pollution control systems to waste has the disconsistency in the components, control the gaseous pollutant at downstream through and to achieve high combustion efficiency, the wet scrubbers, fabric filters or dry scrubbers. The secondary air supply should be introduced by second strategy uses the combustion control to adjusting the secondary air supply along with the control the gaseous pollutant at upstream through waste being burnt. Moreover they recommended the optimum operating condition. The controlling at that the optimum way to optimize the secondary air upstream is a challenge way to minimize the gaseous supply should be controlled by using the automatic pollutants from combustion process. oxygen regulator to sensor the oxygen level in the The present study is the continuing study off-gases. The primary interest of this study is to from the previous study. The previous study studied study the effects of secondary air supply and the influence of primary chamber temperature on present the correlation between excess oxygen level the generation of gaseous emissions [5-6]. The and secondary chamber temperature on the previous study used the strategy to control the combustion efficiency as a basis information to volume of gaseous pollutants exiting primary chamber control the secondary combustion air supply. by obtaining the experiments to determine the 2. Experimental Facilities effective condition in primary chamber such as preheating primary chamber and feeding waste. The The incinerator that be used in this study is present study aims to determine the effective the 50 kg/hr infectious waste controlled-air incinerator condition in secondary chamber to complete the which installed at the Samphran Hospital, combustion gases initiated from primary chamber. Nakhornphatom Province. This incinerator is the The parameters that control the combustion prototype infectious waste incinerator that be conditions in secondary chamber such as secondary designed and constructed to solve the problem of chamber temperature, oxygen level and degree of black smoke and bad odor during the operations of mixing of the combustion gas and air [7]. These the traditional infectious waste incinerators [10]. three parameters were introduced by regulate the The working principle of this prototype infectious secondary air supply. The proper amount of waste incinerator is intermittent controlled-air [11]. secondary air supply is required to sustain the The process diagram of this plant is shown in sufficient secondary chamber temperature, the proper Figure 1. The incinerator composes of two oxygen level and degree of good mixing of the combustion chambers with automatic feeding machine combustion gas and air. and an air pollution control unit. The waste will be With the aim of gaining more fundamental put in the hopper and pushed in the primary knowledge of effects of secondary air supply rate chamber. The combustion environment in primary on the combustion processes, the experiments were chamber is controlled to obtain starved air condition. conducted to provide data for determining the The incomplete combustion products will flow to proper amount of secondary air supply. The secondary chamber and reburn again with the experiments were conducted with the real infectious additional of secondary air supplies. An air blower waste by using the starting conditions that be is installed on the top of secondary combustion obtained from the experiments with simulated chamber for supply air to primary and secondary infectious waste [5]. The real infectious waste chamber. The burners are installed within of combustion has been studied by W. Jangsawang et combustion chambers to ignite the waste and maintain 22 วารสารวิชาการพระจอมเกล้าพระนครเหนือ ปีท่ี 12 ฉบับที่ 2 เม.ย. - มิ.ย. 2545 The Journal of KMITNB., Vol. 12, No. 2, Apr. - Jun. 2002 Stack Secondary Chamber Feeding Machine Air Pollution Control System Primary Chamber Combustion Air Figure 1 Experimental Facilities Table 1 Experimental Program Parameter Unit Condition Condition Condition Preheating Primary Chamber Temperature Degree C 700 700 700 Feeding Waste kg/batch 5 5 5 Preheating Secondary Chamber Temperature Degree C 900 900 900 Primary Air Supply % Open 0 0 0 Secondary Air Supply % Open 10 20 30 the desired temperature. The total two K-type be obtained from the experimental results of simulated thermocouple temperature sensors are installed in infectious waste. The effective condition is at the primary and secondary chamber. They are installed preheating primary chamber temperature 700 °C with near the exit of the combustion chamber to provide 5 kg feeding waste. By doing the experiments under a representative temperature reading away from the these flame zone. Gas samples were taken at secondary secondary air supply rate, the optimum condition combustion chamber exit. For each test, flue gas for the real infectious waste can be obtained. The samples including CO, O2, NO and SO2 were monitored combustion efficiency of this study depends on the and recorded continuously. secondary air supply rate to sustain high sufficient effective conditions and adjusting the secondary chamber temperature and to clean the 3. Test Conditions and Procedures combustion gases exiting primary chamber. The This research aims to study the effect of secondary air supply is set to be varied by open secondary air supply rate on the combustion the secondary air valve at 10, 20 and 30 percents efficiency and determine the optimum secondary air of total secondary air supply (as the experimental supply rate of a 50kg/hr infectious waste controlled- program in Table 1). The results from the previous air incinerator. By using the starting condition that study shown the primary chamber temperature 23 วารสารวิชาการพระจอมเกล้าพระนครเหนือ ปีท่ี 12 ฉบับที่ 2 เม.ย. - มิ.ย. 2545 The Journal of KMITNB., Vol. 12, No. 2, Apr. - Jun. 2002 940 Secon dary Cham ber Temp eratur e (C) 935 930 925 920 915 910 905 Waste Type 1 900 Waste Type 2 895 Waste Type 3 890 0 10 20 30 40 Secondary Air Supply (%) Figure 2 The effect of secondary air supply rate on the temperature distribution in secondary chamber strongly effect on the combustion efficiency [5-6]. simulated infectious waste. The proportional of wet According to the condition in primary chamber is cotton: syringe: rubber glove in the waste type1 is set to be constant for all trials so the concentration 8:1:1 by weight. The waste type 2 and 3 compose of off-gases from primary chamber effects from the of higher combustible matters than the simulated disconsistency in the components of waste input. infectious waste. The proportional of wet cotton: The disconsistency in the components result on syringe: rubber glove in the waste type 2 is 7:1:2 by the variety in heating values and moisture content weight. The proportional of wet cotton: syringe: in each of red bag. These causes affect on the rubber glove in the waste type 3 is 6:1:3 by weight. combustion behavior and combustion efficiency of The experiments will conduct with the three types the burning waste. In practical way to burn the of waste under the various secondary air supply to infectious waste normally used the charging by study its effect and correlation between oxygen random input. So, to study the effect of secondary level and secondary chamber temperature on the air supply rates on the combustion efficiency, it combustion efficiency and presented respectively. needs to know the components of what is burning in the combustion chamber. The experiments will 4. Results and Discussions conduct with the real infectious waste that be 4.1 Correlation between Oxygen Level and Secondary known the compositions before charging in the Chamber Temperature chamber. According to a charge of waste that The amount of secondary air supply influence composes of high amount of combustible matters on both the temperature distribution in secondary such as rubber gloves produce high rate of gasify chamber and the excess oxygen level in off-gases. in the chamber, resulting on the emission of black The secondary chamber temperature depending upon smoke from incinerator [8]. So, the waste that be the initiated combustion gases from primary chamber used in this study will consider on the basis of the and the amount of secondary air supply. The effect amount of combustible matters in that waste. The of secondary air supply rate on the temperature waste will be categorized in to three types in which distribution in secondary chamber temperature compose of; low, medium and high combustible shown in Figure 2. From the experimental results in matter. The waste type 1 has low combustible burning the three types of infectious waste shown matter that has the compositions similar as the the amount of the secondary air supply influence 24 วารสารวิชาการพระจอมเกล้าพระนครเหนือ ปีท่ี 12 ฉบับที่ 2 เม.ย. - มิ.ย. 2545 The Journal of KMITNB., Vol. 12, No. 2, Apr. - Jun. 2002 12 11 O2 Level (%) 10 9 W a s te Type 1 8 W a s te Type 2 7 W a s te Type 3 6 5 0 10 20 30 40 Secondary Air supply (%) Figure 3 The effect of secondary air supply rate on the oxygen level. on the temperature distribution in secondary chamber. creates significant mixing. The large volumes of off The secondary chamber temperature decreases as gases in a fixed size of secondary chamber require increases the secondary air supply. The possible high secondary air supply for good mixing. reason is as increase secondary air supply requires Consequently, increase secondary air supplies more heat to combust the combustion air. And the decrease O2 level. results shown that for burning the wastes that The secondary air supply influence on both compose of high combustible matters, the average the secondary chamber temperature and the oxygen secondary chamber temperature was higher than the level as the results shown in Figure 2 and 3. another trials. That is because the combustion of the Consequently, the oxygen level and secondary waste that compose of higher combustible matter chamber temperature are related. The correlation produce the combustion gas at higher temperature between oxygen level and secondary chamber from the primary chamber exit. temperature was shown in Figure 4. The result The level of excess oxygen in the off-gases shown the oxygen level exiting secondary chamber plays an important role in combustion control and related on secondary chamber temperature. The variations in the gas temperature. The effect of oxygen level increase as temperature decrease. The secondary air supply rate on the oxygen level oxygen level as a function of secondary chamber in exiting secondary chamber will be presented as in equation O2 = -56.58 (lnT2)+394.7 Figure 3. The result shown the secondary air supply rate affects on O2 level. The O2 level exiting the 4.2 Correlation between CO Concentration and O2 secondary chamber for burning the waste that Level composes of low combustible matter is higher than The concentration of CO in the exhaust gas burning the higher one. That is because the rate of stream is an indicator of the combustion efficiency. devolatilization is not high for burning the waste The formation of CO is dictated by a number of that composes of low combustible matters, so it factors such as the oxygen level in secondary requires low excess O2 for complete combustion. chamber, the degree of mixing of the combustion But for burning the waste type 3, the trend of O2 gas and air, the secondary chamber temperature, and level is slowly decrease. The reasonable reason is the volume of combustion gas direct to secondary increasing the amount of secondary air supply chamber. The volume of combustion gas exit from 25 วารสารวิชาการพระจอมเกล้าพระนครเหนือ ปีท่ี 12 ฉบับที่ 2 เม.ย. - มิ.ย. 2545 The Journal of KMITNB., Vol. 12, No. 2, Apr. - Jun. 2002 12 10 Oxygen Level (%) 8 Oxyge n Level (%) 6 y = -56.579Ln(x) + 394.7 4 2 0 89 90 90 91 91 92 92 93 93 Secondary Chamber Temperature (C) Figure 4 Correlation between O2 level and T2 600 500 CO Concentration (ppm) 400 300 Waste Type1 200 Waste Type 2 100 Waste Type 3 0 0 10 20 30 40 Secondary Air Supply (%) Figure 5 The effect of secondary air supply rate on CO concentration primary chamber is primary effect that resulting 3). As increase secondary air supply, decrease CO from the waste input. The generation of volatile concentration. That is because increasing more combustion gases depends on the characteristic of secondary air supply results on the combustion waste input. If the waste has high combustible gases combust more completely. But the results on matter, it will burn rapidly and produce a large the combustion of the waste type1 shown that the volume of flue gas entering the secondary chamber. amount of secondary air supply weakly effect on This rapid rise in off-gases volume in a fixed size the reduction in CO. That is because the waste secondary type1 has low combustible matters, the waste will chamber can lead to incomplete combustion. burn slowly and produce a little volume of off-gases Figure 5 shown the effect of the secondary air exit the primary chamber. So it requires small amount supply on CO concentration. The results shown the of secondary air supply to complete the combustion secondary air supply strongly effect on the CO gases from this waste type. concentration for burning the waste that compose The CO concentration and the oxygen level of high combustible matter (as in waste type 2 and exiting secondary chamber are related. The 26 วารสารวิชาการพระจอมเกล้าพระนครเหนือ ปีท่ี 12 ฉบับที่ 2 เม.ย. - มิ.ย. 2545 The Journal of KMITNB., Vol. 12, No. 2, Apr. - Jun. 2002 12 Oxygen O x y g e n Level L e v e l (%) (% 10 8 y = -0.5585Ln(x) + 11.509 6 4 2 0 0 100 200 300 CO 400 500 600 C o n c e n t ra t i o n (ppm) Figure 6 Correlation between O2 level and CO concentration 112 110 C o n c e n t r ation (ppm) (ppm) NoN OConcentration 108 106 104 102 Waste Type 1 100 Waste Type 2 98 Waste Type 3 96 94 0 10 20 30 40 Secondary Air Supply (%) Figure 7 The effect of secondary air supply rate on NO emission correlation between O2 level and CO concentration NO)[12]. The relative importance of these three was shown in Figure 6. The oxygen level increase as sources of nitrogen oxide depends on the operating CO concentration decrease. The correlation between conditions and the type of the fuel. Thermal NO is O2 & CO as in equation O2 = -0.558ln (CO)+11.51 very temperature-dependent whereas the conversion of fuel nitrogen to NO is not strongly temperature- 4.3 Correlation between O2 Level and NO dependent [13]. Therefore, the NOx derived from Concentration nitrogen in the air can be minimized by lowering the Nitrogen oxides are one of the major air flame temperature and decreasing the oxygen content pollutants emitted by stationary combustion sources. in combustion systems. The factors which affect the Nitrogen oxides produced during incineration are emissions of nitrogen oxides during combustion may oxidation of molecular nitrogen in the post flame be divided into combustion conditions and nitrogen zone (thermal NO), formation of NO in the flame content in the waste. The combustion condition zone (prompt NO), and oxidation of nitrogen- that be studied in this research is secondary air containing compounds in the fuel (fuel-bound supply rate. 27 วารสารวิชาการพระจอมเกล้าพระนครเหนือ ปีท่ี 12 ฉบับที่ 2 เม.ย. - มิ.ย. 2545 The Journal of KMITNB., Vol. 12, No. 2, Apr. - Jun. 2002 1 2 O xyg e n L e ve l (% Oxygen Level (%) 1 0 8 y = 3.6127Ln(x) - 7.8371 6 4 2 0 9 6 9 8 100 102 104 106 108 110 112 N O C oncentration (ppm) Figure 8 Correlation between O2 level and NO concentration 80 70 SO2 Concentratio SO2 Concentrationtration 60 50 40 W as te Type1 30 Waste Type 2 20 Waste Type 3 10 0 0 10 20 30 40 S e c o n d a r y Air Supply (%) Figure 9 The effect of secondary air supply on SO2 emissions The effect of secondary air supply rate on NO 4.4 Correlation between O2 Level and SO2 production was shown in Figure 7. The results shown Concentration the influence of the amount of secondary air supply Sulfur, which is chemically bound within the on NO production is not evident. For burning all the materials making up hospital waste, is oxidizes three waste types studied shown that increasing during the combustion process to form SO2 [7]. the amount of secondary air results on increasing Sulfur dioxide produce from the combustion process NO production slowly. The NO production from comes from the sulfur content in the fuel. The burning the same waste type is almost equal. combustion condition has little or no effect on The correlation between O2 level and NO emission of SO2 [7,11]. concentration shown in Figure 8. The result shown The effect of secondary air supply rate on SO2 the oxygen level and NO concentration exiting production was shown in Figure 9. The results very secondary chamber is not significant change. The clearly shown that the SO2 production from burning correlation as in equation O2 = 3.163ln (NO)-7.84 the same waste type are almost the same. This 28 วารสารวิชาการพระจอมเกล้าพระนครเหนือ ปีท่ี 12 ฉบับที่ 2 เม.ย. - มิ.ย. 2545 The Journal of KMITNB., Vol. 12, No. 2, Apr. - Jun. 2002 12 Oxygen Level (% 10 8 y = -1.0384Ln(x) + 12.002 6 4 2 0 0 10 20 30 40 50 60 70 80 SO2 Concentration (ppm) Figure 10 Correlation between O2 level and SO2 concentration result implies that the SO2 production depending is not evident on the secondary air supply rate. upon the sulfur contents in the waste being burnt. From the results shown in the burning the The increasing in secondary air supply is not waste that has the disconsistency in the composition evident on SO2 production for all trials. And the as the real infectious waste, the secondary air wastes that compose of higher amount of rubber supply should be varied to optimize the combustion gloves produce more SO2 than the lower one. processes. In case of burning the waste that The correlation between O2 level and SO2 compose of high amounts of combustible matters, concentration was shown in Figure 10. The the high burning rate will occur and produce high production of SO2 is not significant relate on the volume of combustion gases, more secondary air oxygen level exiting secondary chamber. supply is required. For the waste that compose a little of combustible matters, increase more combustible matters resulting on temperature drop and more fuel 5. Conclusions The test results indicate that secondary air consumption. So to optimize the operating condition supply rate is related to the temperature distribution by adjusting the secondary air supply should be done and the concentration of gaseous emissions. As by using the automatically oxygen regulator to increase the secondary air supply, decrease the sensor the amount of oxygen in the secondary primary and secondary chamber temperature. The chamber by using information from this study. CO concentration and excess oxygen level are 6. Acknowledgement strongly effect on secondary air supply rate. The The CO concentrations decrease as increase secondary authors would like to express their air supply. The excess oxygen level directly related grateful to the Joint Graduate School of Energy and on secondary air supply rate. As increase secondary Environment for air supply rate, increase excess oxygen level in the Waste Incineration Research Center, Department of off-gases exiting the secondary chamber. Moreover, Mechanical Engineering, Faculty of Engineering, King the experiments found the good mixing in combustion Mongkut’s Institute of Technology North Bangkok gas and air achieved high combustion efficiency. for facilities support so that this task can be And also the result shown, NO and SO2 production successfully completed. 29 his funding support and the วารสารวิชาการพระจอมเกล้าพระนครเหนือ ปีท่ี 12 ฉบับที่ 2 เม.ย. - มิ.ย. 2545 The Journal of KMITNB., Vol. 12, No. 2, Apr. - Jun. 2002 8. References 1. 2. Hospital Waste Combustion Study, EPA-450/3- Incineration for Hospitals and other Medical 88-017,U.S. EPA, Washington, D.C., 1988. Facilities. New York : Van Nostrand Reinhold, Handbook : Operation and Maintenance of 1990. 9. Hospital Medical Waste Incinerators, EPA/ 3. 5. 6. 7. Jangsawang, W., et al. Effect of Secondary Air 625/6-89/024, Office of Air Quality Planning and Supply Rate on the Combustion Efficiency of Standards, Research Triangle Park NC 27711, Infectious Waste in A controlled-Air Incinerator, U.S.EPA, Washington, D.C., 1990. Proceeding of 6th Asean Science & Technology EPA Guide for Infectious Waste Management, Week, Darussalam, Brunei., 2001. EPA/530-SW-86-014 (NTIS PB 86-199130), U.S. 4. Theodore, L. Air Pollution Control and Waste 10. Kuo, J. T., et al. “Effect of Air Distribution on EPA, Washington, D.C., 1986. Solid Bed Combustion.” Transaction of the Doucet, L.C., Controlled Air Incineration: ASME. 119 (1997) : 120-128. Design, Procurement and Operational 11. Kerdsuwan, S. Design of 50kg/hr Controlled- Considerations: Prepared for the American Air Hospital Waste Incinerator. Proceeding Society of Hospital Engineering, Technical of 93 rd Annual Conference of Air & Waste Document No.55872. 1986. Manage-ment Association, Salt lake City, USA., Guide for Infectious Waste Management, EPA/ 2000. 530-SW-86-014, U.S. EPA, Washington, D.C., 1986. 12. Kerdsuwan, S. On the Performance Testing of the Jangsawang, W and Kerdsuwan, S. Optimization 50 kg/hr Prototyp Controlledair Infectious of The Operating Conditions of Infectious Waste Incineration System, Proceeding of Waste Controlled-Air 16th Inter-national Conference on Solid Waste Incinerator: Effects of Primary Chamber Technology and Management, Philadelphia, PA, Temperature on the Combustion Efficiency, USA., 2000. Incineration in a Proceeding of 94th Annual Conference of Air 13. Jabouille, F., et al. NOx Emission From Reactor & Waste Management Association, Orlando, From Combustion of Municipal Solid Waste: Florida, USA., 2001. Experimentation with Counter Flow Fixed Lertsalaluck, P and Kerdsuwan, S. Combustion Bed Reactor and Rotary Kiln Incinerator. Study of The Incineration of Major Components European-Asean Conference on Combustion of of Controlled-air Solids and Treatment of Product.,Thailand.,1995. Incinerator: The Influence of Bed Temperature 14. Mark, Thomas K. “The Release of Nitrogen and Infectious Waste in a Feeding Rate on the Evolution of oxides During Char Combustion.” Fuel. 76, 6 temperature and Gaseous Emission, Proceeding (1997) : 1997. of 2001 International Conference on Incineration 15. Hospital Waste Combustion Study. EPA-450/3- and Thermal Treatment Technology, Philadelphia, 88-017, U.S. EPA. , Washington., D.C., 1988. PA, 14-18 May 2001. 30
© Copyright 2026 Paperzz