This study tried to seek the plan to recycle chicken residues (bones of seasoned spicy chicken and fried chicken) which are sent out thermally after chickens are delivered to homes and people eat them by grasping their basic characteristics. The analytical results of the weight reduction rate through the change before and after the weight is reduced have found that the average weight reduction rate of 38.0% is shown in the seasoned spicy chickens and fried chickens. The analytical results of low-heating value of chicken residues to grasp the thermochemical characteristics have found that the seasons spice chickens and fried chickens satisfy the SRF quality basis, 3,500 kcal/kg as 5,020.9 kcal/kg and 5,295.2 kcal/kg respectively. On the other hand, the analytical result of TG has found that the thermal weight reduction rate is relatively clear in the fried chickens. It is inferred that creation of the fried chickens is more uniform than that of the seasoned spicy chickens and the effect of bound water is lower than other biodegradable substances. And it is judged that the potential that they can be utilized as sold fuel without any separate preprocessing through the drying process only is shown.

According to the elementary analysis on organic wastes, the C/N ratio, a major condition for anaerobic digestion, is 5.40 to 9.23, except for food waste leachate (FWL). Defined by Tchobanoglous’ mathematical biogas prediction model, methane gas and biogas productions increased, depending on the mixing rate of FWL. Furthermore, anaerobic digestion both wastewater sludge and food waste leachate based on the right mixing ratio, increases methane gas productions compared to digesting wastewater sludge alone. In other words, co-anaerobic digestion is more likely to realize biogasification than single anaerobic digestion. We mix food waste leachate and wastewater sludge from the dairy and beer manufacturing industry by the proportion of 1 : 9, 3 : 7 and 5 : 5. It turns out that they produced 118, 175 and 223 CH4 mL/g VS in the dairy manufacturing and 176, 233 and 263 CH4 mL/g VS in beer manufacturing of methane gas. The result suggests that as the mixing rate of food waste leachate rises, the methane gas productions increases as well. And more methane gas is made when co-digesting wastewater sludge and food waste leachate based on the mixing ratio, rather than digesting only wastewater sludge alone. Modified Gompertz and Exponential Model describe the BMP test results that show how methane gas are produced from organic waste. According to the test, higher the mixing rate of food waste leachate is, higher the methane gas productions is. The mixing ratio of food waste leachate that produces the largest volume of methane gas is 1 : 9 for the dairy industries and 3 : 7 for brewery. Modified Gompertz model and Exponential model describe the test results very well. The correlation values (R2) that show how the results of model prediction and experiment are close is 0.920 to 0.996.

This study was to select five places among apartment houses (apartment), detached houses (including houses, villas), downtown area (markets, shops, restaurants) being operated in Korea and use the analysis of physical and chemical characteristics for treatment residues of weight reduction equipment as basic data. Also, we were to evaluate the recyclability by determining whether discharged treatment residues are available in the thermochemical process such as cement sintering facilities and power plants in which energy can be recovered based on the quality standards of Bio- SRF and SRF. Three components for food waste were analyzed and as a result, moisture average, combustibles average and ash average were found to be 11.9% (2.0 ~ 24.8%), 78.9% (63.3 ~ 93.0%) and 9.2% (5.0 ~ 11.9%) respectively and all of them were found to satisfy less than 25%, the moisture content standard of Solid Refuse Fuel (SRF) products. The results of the elemental analysis were analyzed to be carbon average 49.71% (48.41 ~ 52.14%), hydrogen average 6.62% (31.32 ~ 40.63%), oxygen average 37.92% (31.32 ~ 40.63%), nitrogen average 3.82% (2.79 ~ 5.81%), sulfur average 0.26% (0.19 ~ 0.46%), chlorine average 1.67% (1.10 ~ 3.16%). In addition, the low-heating value measurement result is average 4,016.6 kcal/kg (3,255.9 ~ 4,657.9 kcal/kg) and turned out to satisfy most general Solid Refuse Fuel (SRF) product standards but that of Facility E is 3,255.9 kcal/kg and was analyzed not to meet the quality standard 3,500 kcal/kg. However, if maintaining the moisture content of treatment residues to 20% or less, it is determined to satisfy the caloric value standards of general Solid Refuse Fuel products.

In this study those currently operating pyrolysis oil plant were selected for the investigation. The yield of the oil andfuel was assessed for its use as fuel and the char component analysis, and the reaction time to collect contaminantscollected and analyzed. As the result, about 40% of the oil was yielded and oil could be used as an alternative fuel. Char’sleaching test analysis result was satisfied with the landfill standard. And emission of Dioxin and pollutants was analyzed.The highest concentration of dioxin was 0.7347ng I-TEQ/Sm3. The result satisfied the requirement however the emissionconcentration was changed depending on the input Fuel. Therefore the appropriate pollution control facility should berequired.

In this study those currently operating SRF (Solid Refuse Fuel) combustion plant were selected for the investigation. The SRF component analysis, and the reaction time to collect contaminants collected and analyzed. As the result, the average caloric value of the SRF was about 8,114 kcal/kg and the result of the analysis was satisfied with the Fuel standard. The SRF could be used as an alternative Coal fuel. However CO, NOx and Dust analysis result was exceeded the emission standard. In case of Hydrogen chloride, high concentration of emission from the facilities was observed. Although normal operation was performed, ineffective the operational management causedt, incomplete blockage of drug injection facilities and personnel management system. To prevent such problems, a regular maintenance of facilities is need to be installed. At the moment applied to the monitoring system (TMS) are installed in waste incinerators with the medium to large capacities, However such as a periodically monitoring system is needed to manage a small solid fuel boliers as well.

In this study proximate analysis method was applied to food waste, mold, sewage sludge, PKS, PET in considering the characteristics of individual waste. It has been observed that this proximate analysis method based on the characteristics of individual waste required to dry the waste for more than 6 hr, until the moisture contents reached the range of 105oC ~ 110oC and they reached the constant weight. Also it has been suggested that 7 min of ignition at 950oC for volatile matters and 2 ~ 3 hr of ignition at max. 815oC for ash were recommended.

In order to cope with resource depletion and global warming, many countries around the world are seeking the technicaland political alternatives and are focusing on production of refuse derived fuel (SRF) as a viable approach. SRF isclassified into pellet SRF and fluff SRF based on the shape. In domestic trend, Pellet RDF has been mainly produceduntil now, but as the quality standard of fluff SRF was set up lately, it is expected to raise supply and demand on FluffSRF after this. Fluff SRF is a solid fuel not to be processed pelletizing step, and has advantages that manufacturing processis simple and economical. In this paper, we selected 3 MBT plants to produce Pellet SRF in Korea and examined reductioneffects of energy and CO2 emission by conversion of pellet SRF to fluff SRF. As a result, the saving energy by theconversion of SRF type is 2,509 Gcal/yr (A), 1,716 Gcal/yr (B) and 1,210 Gcal/yr (C) respectively, and the reductionrate of energy consumption in full process is about 23%~26% by comparison with pellet SRF. Also, the average ofreduction of CO2 emission per unit of MSW is 0.0272 tCO2/ton. After estimating the reduction of CO2 emission of 9MBT plants in Korea, based on the results of a survey of target plants, we concluded that the reduction effect of CO2emission is created 11,374 tCO2/yr.

This paper examined energy consumption distribution by process and energy production-effect of MBT facilities inKorea. Generally, facilities that use fossil fuels for drying consumed energy about 70~80% in drying and exhaust gasestreatment process and energy distribution was heavily affected a position of drying and a kind of fuel. Energy production-effect by the ratio of input-energy to output-energy ranged from 4.54 to 9.60, however, if generation efficiency is reflected,it was standardized to low levels from 3.10~3.77. So we were able to confirm that the superiority of energy production-effect between facilities is not considerable.

This paper examined reasonable operating factor for treatment of carcass burial leachate in High Temperature Thermal Desorption (HTTD) and calculated the amount of fuel used in each device using heat and mass balance under condition of 4 scenarios. As a result, we concluded that rotary kiln for dryness and thermal desorption shoud be separated dual type and mixing ratio of sawdust and soil should be restricted no more than 1 : 14. Also, operating temperature should be kept 260, 550, 850 or higher in dryer kiln, thermal desorption kiln and secondary chamber respectively and residence time should be kept 30min in each kiln. The total amount of fuel used in each device was compared under 4 scenarios on the mixing ratio. According to a study, it showed the highest value under the scenario of 1 : 1, which showed 2.5 times higher than the scenario of 1 : 14 in terms of treatment of leachate per unit of LNG.

This study analyzed concentration and characteristics of hazardous substances in treatment of leachate from carcass burial areas by using high temperature thermal desorption (HTTD). Concentrations of pollutants emitted from HTTD treatment of leachate contaminated soil of carcass burial sites satisfied the emission standards for 11 pollutants from domestic waste incineration facilities. Dioxin concentration was 0.0060 ng I-TEQ/Sm3 and 0.0061 (0.0055-0.0070) ng ITEQ/ Sm3 in the normal operation condition and the experimental condition, respectively, which are much lower than the MSWI Standard of 0.1ng I-TEQ/Sm3. As a result, it was considered that leachate from carcass burial areas could be treated by high temperature thermal desorption (HTTD).

This paper analyzed thermal and carbonization properties of sewage sludge in fixed bed reactor and obtained following results. The heavy metal (Pb, Ni, Mn, Cr, Cu) content of Char showed the highest level at unprocessed sewage sludge, followed by carbonized sludge at 600, 400, and 500oC. It was thought to be mainly due to the yield of char rather than the influence of temperature. Also, the migration-test results of heavy metals satisfied the landfill directive in all samples, which may be possible to use it as landfill cover materials. The concentration of dioxin by changes of pyrolysis temperature was higher in the low temperature conditions and the proportion of PCDDs was higher than that of PCDFs.

According to the statistics of the Ministry of Environment, the emission of sewage sludge is increased by 7 ~ 9% yearly. In the future, it will be increased continuously because of extension of sewage disposal plants, high class treatment for removing nitrogen and phosphorus. The objective of this study is to examine the possibility of the carbonization of the sewage sludge by pyrolysis. The pyrolysis behavior of the sewage sludge was investigated by the thermogravimetric analysis as a function of heating rate. In the pyrolysis studies measurements in weight loss was made and reported as a function of test temperature. To minimize energy consumption used for drying sewage sludge, naturally dried sludge were applied evaluate characteristics of thermal and carbonization treatment using a fixed-bed reactor. The most effective treatment temperature of carbonized material production was 400oC. The temperature of highest total yield of char and oil was 500oC. In the pyrolysis studies measurements in weight loss was made and reported as a function of test temperature. According to the result, the optimum pyrolysis temperature of sewage sludge were found to be ranged from 100oC to 600oC, respectively. About 91% of pyrolysis was completed between 100oC and 600oC. If applying the carbonization, it can be easily utilized as the replaced resource of energy(fuel) in the countries whose energy resources are insufficient, like our country.

Establishment of emission concentrations of PCDDs and PCDFs in emission gases from 85 domestic crematories were measured. The relationship between PCDDs/DFs and several factors such as structure, equipment and operational state of the crematory is discussed. Furthermore, emission of PCDDs/DFs from all crematories in korea is estimated. The following results are obtained: (1) total concentration (2,3,7,8- substituted isomers) of PCDDs/DFs was 0.113 ~ 14.34 ng/ Sm3, whose TEQ concentration was 1.815 ng-TEQ/Sm3; (2) total emission of PCDDs/DFs from crematories in korea was estimated to be 1.815 g-TEQ/yr.

Infectious diseases in domestic animals of carcase were increasing every year. According to the monthly report for infectious disease from Ministry for Food, Agriculture, Forestry and Fisheries, 11,954 heads of cattle, 518,178 heads of pig, 232,850,244 heads of bird were reported in 2011. Infectious diseases of carcase almost spread on a national scale. Dead or emergency preventive carcase are completely treated on bury. Since the treatment of carcase on bury are generating soil, underground water and source water pollution, introduction of new preventive system should be considered. In this study, literature survey and case studies to prevent the spreading of virus for infectious disease and second environmental pollution were investigated. The actual experiments using the existing incineration facilities were also performed to ensure the possibilities of safe treatment of carcase. On the other hand, the moving-type incineration are also being developed and its operation manual will be prepared. Among the investigated incinerators, stoker type incinerator was not suitable for the treatment of carcase, however, other incinerators such as fluidized-bed type incinerator, rotary kiln type incinerator ware shown to be suitable. But even for the stoker type incinerator, if the pre-treatment facilities( grinding, crushing) are installed, it will also be a suitable method. The analytical results for air pollutants(including dioxin) emitted from the final exit were all satisfied to the air pollution emission standards.

In this study, PCDDs/DFs concentrations in flue gases from 58 crematories and in fly ashes and bottom ashes (mainly bone) from several crematories were measured to grasp the present state of PCDDs/DFs emissions from crematories. The effects of several factors were discussed to prevent PCDDs/DFs emissions from crematories. Total concentration of PCDDs/DFs was ranged from 0.113 to 87.461 ng/Sm3 and toxic equivalent concentration was ranged from 0.019 to 15.347 ng-TEQ/Sm3. As the results obtained in this research, the following measures to reduce PCDDs/DFs emission are recommended for existing crematories: (1) keeping the temperature at < 800oC or < 850oC in main/secondary chambers during a whole cremation, (2) lowering the temperature in the dust collector, (3) installing the high efficiency dust collector and reducing dust concentration to less than 0.02 g/Sm3, and (4) installing the sampling point for monitoring of PCDDs/DFs.