Combined Heat and Power from Municipal Solid Waste: Current Status and Issues in South Korea

Abstract

Municipal solid waste (MSW) is an important energy resource for combined heat and power (CHP) production. This study summarized an overview of CHP by MSW to energy (WtE) plants in South Korea and discussed the issues related to energy efficiency improvement. Given the dominant housing culture of apartment living in South Korea, the primary energy output of WtE plants has been for district heating. In 2010, approximately half of the 51 large WtE plants were CHP, while the rest produced heat. Power generation in the WtE CHP plants was estimated to be only 3.65% of the thermal input, while heat production was 60.79%. The R1 efficiency when compared to that in Europe was similar for the CHP plants and higher for heat-only plants. Improving power generation efficiency is required for new power plants producing steam at pressures higher than the current level of 20–30 bar. Over ten of the existing plants needed to increase their energy efficiency by installing new equipment such as steam turbines for excess steam. Finally, transboundary centralization of WtE plants between neighboring local authorities is essential for heat utilization since many existing small-scale plants (<50 t/day capacity) do not recover heat.

1. Introduction

Waste management with a low environmental impact is an essential element of modern society. The prioritization of waste management is expressed as the well-known hierarchy of “prevention”, “reuse”, “recycling”, “recovery” and “disposal”. Waste to energy (WtE) is the recovery of the energy content, preferably for non-recyclable wastes. This is usually achieved by combustion of the waste to release its chemical energy and then transferring this energy to water/steam in a boiler to produce heat and/or power. Compared to commercial fuels, municipal solid wastes (MSW) are low quality fuels due to their low energy content, their large variations in fuel properties and the high content of chlorine and heavy metals. However, there are established technologies available for WtE such as grate-type combustion, fluidized bed combustion and pyrolysis/ash-melting [1]. Other conversion technologies are also available to increase the fuel quality of wastes and their flexible use, such as production of solid recovered fuel (SRF) and gasification [2,3]. After recovering heat, the solid residue (bottom ash and fly ash) can be utilized as feedstock for construction [4] or safely disposed of with a minimal environmental impact [5].

One important feature of WtE is that it displaces the consumption of fossil fuels for heat and power production. Moreover, MSW contains biogenic fractions such as paper and wood, and the energy produced from those is carbon-neutral, thereby reducing greenhouse gas emissions [6]. Moreover, in many countries, WtE has been an important source of renewable energy [7,8,9].

Unlike a fossil-fuel-fired power plant, a WtE plant is usually located close to its energy source, which is often a populated urban or industrialized area. Due to this reason, WtE plants can operate in a CHP mode, that is, the residual heat in the steam after power generation is exported to a district heating (DH) system or to nearby heat demanding industries as process heat (PH). Although power generation efficiency is lower than typical power plants with a steam turbine (35%–45%), an ideal WtE plant for CHP can achieve overall energy (power and heat) efficiencies as high as 85% of the energy content in MSW [10]. Development of a district energy network to fully utilize heat from WtE together with other renewable energy sources can greatly lower the carbon emissions, as reported for the case of Sheffield, UK [11,12].

In some cases, however, achieving a high energy efficiency of WtE is not practical due to various technical and non-technical reasons. The design and operation of a WtE plant is determined primarily by the amount of MSW to be treated, not by energy demand. Therefore, utilization of the heat produced from a WtE plant needs to be considered from the planning stage of a new installation. In particular, small-scale plants in rural areas often do not have a sufficient enough need for heat, therefore in these instances installing heat recovery facilities significantly increases the capital and operation costs. Without energy recovery, waste incineration is only for easy disposal of wastes by landfill of ashes after volumetric reduction and removal of biodegradable fractions. In order to differentiate energy recovery from waste disposal, the European Union (EU) introduced a revised Waste Framework Directive (WFD, 2008/98/EC) in 2008 [13]. In the Directive, the energy efficiency of a WtE plant is evaluated using the “R1 formula”, which is the ratio of net energy output over input with equivalence factors of 2.6 multiplied for electricity production and 1.1 for heat production. New or recent WtE installations (permitted after 31 December 2008) with an R1 efficiency ≥0.65 can be classified as recovery action, while 0.60 is applied to older installations. Grosso et al. [14] reported that European WtE plants in 2004 had an average R1 efficiency of 0.71 for CHP, 0.49 for electricity and 0.64 for heat producing plants.

WtE of MSW plays a crucial role in renewable energy production in Korea. As a country with limited natural resources, Korea imports about 98% of its energy sources from abroad [15]. Moreover, in 2010, WtE by incineration was 11.8% of total “new and renewable” energy production, while wind power and photovoltaics were 2.5% each [16]. Recognizing the importance of MSW for WtE, in 2008 the Korean government announced a new “Waste to Energy Strategic Plan” [17], which aims to increase energy recovery and utilization for all available non-recyclable wastes from the current level of 32% to 57% by 2012, and to 100% by 2020. This is one of essential elements of the National Energy Plan also announced in 2008 [18], which set ambitious national targets and introduced many new measures for sustainable development. These targets include increasing renewable energy production to 11% of the national total by 2030.

This paper reviews the current status of WtE for MSW in South Korea and analyzes the energy efficiency of large WtE plants. Raw data for analysis was collected from annual summary reports of WtE operators and official documents published by the Korean Government. The energy efficiency of the WtE plants was compared to that of European plants based on the R1 formula of the EU WFD. Based on these results, energy efficiency improvement issues are discussed.

2. Management of MSW in South Korea

Table 1 presents an overview of MSW management in Korea from 1997 to 2010 [19]. In 1995, the enforcement of regulations regarding the use of disposal bags for household waste has since resulted in a steady generation of MSW of approximately 50 kt/day or 1 kg/day/capita. In that period, the proportion of wastes recycled drastically increased from 29.0% in 1997 to 60.5% in 2010 due to the high level of segregation of recyclable wastes from households. This led to an insufficiency of MSW for incineration in some existing plants, which is discussed in Section 4.4. In the same period, however, the amount of waste incinerated increased three-fold from 7.1% in 1997 to 21.6% in 2010. High recycling rates were beneficial in raising public acceptance for incineration, since the public realized that it is applied for non-recyclable wastes they disposed in dedicated bags. The segregation of food waste and corresponding increase in the heating value of MSW also shifted the public perception and waste management policy for incineration from disposal action to energy recovery. As a result, landfill waste decreased from 63.9% to 17.9%. Compared with the average of 27 European countries [20], the proportion of recycling is 20% higher although incineration levels are similar. Overall, MSW in South Korea is managed reasonably well.

Figure 1 illustrates the trend in the fuel properties and the material breakdown of MSW averaged for the monthly analytical data measured at 40 large WtE facilities in Korea [21]. The error bars for the lower heating value (LHV) in Figure 1a represent the standard deviation. The LHV of MSW increased from 8.16 MJ/kg in 2002 to 11.92 MJ/kg in 2011, due to a gradual decrease in moisture content from 46.8 wt % to 33.2 wt %. The decrease in moisture content is largely attributed to the reduction in food waste, which has very high moisture content. Given the separate collection of food waste enforced in 2005, the proportion of food waste decreased from 36.1 wt % in 2002 to 13.0 wt % in 2011 (Figure 1b). This also led to a decrease in the bulk density from 0.292 t/m³ to 0.218 t/m³. On a dry basis, the ratio of combustibles to ash content was steady at about 4.8. The elemental composition of the combustible fraction was estimated to be 60.7% C, 8.4% H, 29.0% O, 0.8% N, 0.1% S and 1.0% Cl on a dry-ash-free basis [22]. In 2011, paper (33.9 wt %) and plastics (26.4 wt %) were the main constituents of household wastes, which provide most of the heating value.

Table 1. Summary of MSW management in South Korea.

Year		1997	2000	2003	2007	2010	EU27 2010 [20]
Generation	(t/day)	47,896	46,438	50,736	50,346	49,159
	(kg/day/capita)	1.04	0.99	1.06	1.02	0.96	1.38
Management	Recycling (%)	29.0	41.3	45.2	57.8	60.5	41.1
	Incineration (%)	7.1	11.7	14.5	18.6	21.6	21.6
	Landfill (%)	63.9	47.0	40.3	23.6	17.9	37.3

Table 1. Summary of MSW management in South Korea.

Year		1997	2000	2003	2007	2010	EU27 2010 [20]
Generation	(t/day)	47,896	46,438	50,736	50,346	49,159
	(kg/day/capita)	1.04	0.99	1.06	1.02	0.96	1.38
Management	Recycling (%)	29.0	41.3	45.2	57.8	60.5	41.1
	Incineration (%)	7.1	11.7	14.5	18.6	21.6	21.6
	Landfill (%)	63.9	47.0	40.3	23.6	17.9	37.3

Figure 1. (a) Components and LHV of MSW and (b) material breakdown in 2002–2011 analyzed at large incineration plants.

Figure 1. (a) Components and LHV of MSW and (b) material breakdown in 2002–2011 analyzed at large incineration plants.

3. Energy production and Efficiencies of WtE from MSW in Korea

3.1. Energy Production from MSW

As of 2011, 53 large WtE plants for MSW are in operation in Korea with a capacity ranging from 50–900 t/day [23]. Plants with a capacity larger than 300 t/day typically comprise of two or three identical units each with a capacity of 100, 150, 200, 300 or 400 t/day. The total capacity of the plants is 14,192.5 t/day. Among them, 46 plants incorporate grate type furnaces, three fluidized bed and four pyrolysis/melting type. These plants burned 3439 kt of wastes in 2010, which represents 88.7% of MSW incinerated in the country. Small-scale (<50 t/day) plants located in rural areas or in small cities treated the remaining MSW.

Figure 2 shows the amount of heat and power produced from WtE plants since 2002 [21]. The heat recovered by steam was used mostly as heat. On-site heat consumption was the largest in 2002, equivalent to 57% (7482 TJ) of total heat use (13,063 TJ). This heat was used for various purposes such as reheating flue gas for selective catalytic reactors and the prevention of white smoke, preheating of combustion air, and on-site hot water supply. The amount of on-site heat consumption was steady throughout the period despite the growth in the number of plants, which was due to the efforts to efficiently utilize the heat at the plants. The amount of heat exported for DH or PH exceeded the on-site consumption in 2006 and continued to increase. The fraction of heat exported for PH is small compared to DH, which was done at eight out of 51 plants in 2010. It is important to note that Korea has a unique housing culture in that apartments are the main residential form in urban areas. According to the 2010 national population and housing census, 47.1% of all homes were apartments [15]. Therefore, it is relatively easy to install district heating systems that supply heat and hot water in an apartment district. The heat exported to DH is sold typically to public DH corporations at 27% of the customer price [21]. The heat used at subsidiary facilities refers to hot water or steam for swimming pools or food waste treatment facilities collocated with a WtE plant, which was at 16 out of 51 plants in 2010. In 2011, power generation was very small compared to that of heat production (943 TJ) and was used mostly on-site. However, electricity export to grid significantly increased from 11 TJ in 2002 to 302 TJ in 2011, representing about a third of all electricity produced. Overall, heat is the dominant form of energy produced from WtE plants in Korea due to the large demand for heat while efficient power generation requires much higher capital costs. Details of technical data including energy efficiencies and steam pressures are discussed later.

Figure 2. Energy production and use at WtE plants in 2002–2011.

Figure 2. Energy production and use at WtE plants in 2002–2011.

3.2. Korean WtE Energy Efficiencies

Table 2 lists the status and efficiencies of energy production in selected years by large WtE plants for which detailed technical data is available [21,23]. The number of plants increased significantly in 2002–2010, but the ratio between CHP and heat-only remained similar. Waste throughput per site is larger for CHP plants because recently installed CHP plants have larger capacities (100–300 t/day) than the heat-only plants (mostly 50 t/day) located at small cities.

Table 2. Summary of status and gross efficiency for heat and power production in 2002 and 2010 from WtE plants.

Year		2002	2010
Combined Heat and power	Number of plants	13	25
	Annual waste throughput (kt)	1,307	1,899
	Thermal input of MSW (TJ)	10,662	22,265
	Heat production efficiency, ηheat (%)	63.1	60.8
	Power generation efficiency, ηpower (%)	3.2	3.6
Heat-only production	Number of plants	14	26
	Annual waste throughput (kt)	867	1,494
	Thermal input of MSW (TJ)	7,073	17,511
	Heat production efficiency, ηheat (%)	89.2	74.9

Table 2. Summary of status and gross efficiency for heat and power production in 2002 and 2010 from WtE plants.

Year		2002	2010
Combined Heat and power	Number of plants	13	25
	Annual waste throughput (kt)	1,307	1,899
	Thermal input of MSW (TJ)	10,662	22,265
	Heat production efficiency, ηheat (%)	63.1	60.8
	Power generation efficiency, ηpower (%)	3.2	3.6
Heat-only production	Number of plants	14	26
	Annual waste throughput (kt)	867	1,494
	Thermal input of MSW (TJ)	7,073	17,511
	Heat production efficiency, ηheat (%)	89.2	74.9

The energy efficiencies in Table 2 were calculated, based on the total heat and electricity use (Figure 2) and the average LHV (Figure 1a). The gross efficiencies for heat production (η_heat) and power generation (η_power) are defined, respectively, as follows:

η_heat (%) = 100 × E_heat/E_waste

(1)

η_power (%) = 100 × E_elec/E_waste

(2)

where E_waste refers to the thermal input calculated by waste throughput times the LHV. E_heat and E_elec represent total heat use and power generation including on-site consumption, respectively. Table 2 shows that η_heat and η_power in 2010 were 60.8% and 3.6%, respectively. The net power generation became as low as 1.0% of the thermal input, which is for the electricity exported to grid. Surprisingly, the overall efficiencies were lower than in 2002. This is due to a large uncertainty in the LHV of the input wastes, which is always an issue due to its heterogeneous nature. Detailed analysis for individual WtE plants revealed that the values of LHV in 2002 were significantly underestimated. Figure 3 plots the boiler efficiency (= heat output as steam / E_waste) vs. LHV for individual plants in 2002 and 2010. If the LHV is underestimated, it leads to an overestimation of the boiler efficiency. In 2002, 14 out of 27 plants are above 100%, which is thermodynamically impossible. One plant in Figure 3a even has a boiler efficiency estimated as high as 169%. The actual boiler efficiency is limited by the residual enthalpy in flue gas at the boiler exit (typically at 150–200 °C), radiation loss and unburned carbon. The practical upper limit of boiler efficiency would be about 85%. The highest boiler efficiency of WtE plants in Europe was 84.2% with average of 81.2% [24]. Figure 3a also shows that the plants that reported a LHV lower than the average tended to have a higher efficiency and vice versa. In 2010 (Figure 3b), three of those are still above 100%. Note that in 2007 there were eight plants with efficiencies above 100% by the same analytical method [22]. This suggests that the uncertainty involved in the analysis of waste properties was considerably reduced in 2010. Overall, it is not very reliable to analyze the energy efficiencies using the LHV at this stage. However, it would be reasonable to say that the efficiencies in Table 2 for 2010 would be close to the true values.

Figure 3. Steam production efficiency based on the reported LHVs for WtE plants in (a) 2002 and (b) 2010.

Figure 3. Steam production efficiency based on the reported LHVs for WtE plants in (a) 2002 and (b) 2010.

Figure 4 shows R1 efficiencies of EU WFD evaluated for 37 large WtE plants in Korea using the operation data in 2010 for comparison with EU WtE plants. R1 efficiency in WFD is defined as:

R1 efficiency = E_prod − (E_fuel + E_import)/0.97 (E_waste + E_fuel)
where E_prod = 1.1 E_heat + 2.6 E_elec

(3)

For the energy produced (E_prod), an equivalence factor of 1.1 is multiplied for heat produced (E_heat) and 2.6 for electricity (E_elec) each of which is based on the average efficiency in European power plants (38%) and heat plants (91%) [25]. Energy output excludes the input from other fuels (E_fuel) and imported (E_import). A factor of 0.97 is multiplied to the thermal input for waste (E_waste) and other fuels (E_fuel) to account for the energy loss due to bottom ash and radiation during thermal conversion. In the calculation, the use of auxiliary fuels for E_fuel and E_import in individual plants was included with a LHV of 39.9 MJ/m³ for LNG and 36.0 MJ/L for light fuel oil.

Figure 4. R1 efficiencies of WtE plants in Korea in 2010.

Figure 4. R1 efficiencies of WtE plants in Korea in 2010.

In Figure 4, the average R1 efficiency of 21 CHP plants is 0.716, which is comparable to those in Europe (0.71) [14]. The number of plants under the threshold of 0.6 is 9, in which the heat produced is used mostly on-site including three plants without any heat export to DH or PH. Electricity producing plants in the EU have been reported to have an average R1 efficiency of 0.49 [14]. For 16 plants producing only heat, the R1 efficiency (0.936) is much higher than that of the EU (0.64). This is because plants export all extra heat to DH or PH. Regarding the uncertainties in LHV analysis, the same calculation was carried out for E_waste based on steam output instead of LHV. Assuming that steam output is 83.1% (average boiler efficiency in Figure 3b) of thermal input, the average R1 efficiency becomes 0.737 for CHP plants and 0.905 for heat producing only plants. Therefore, the results are overall similar between the two approaches.

4. Issues of WtE in Korea

4.1. Increase in LHV

Most existing WtE plants in Korea were designed for a reference LHV of 7.1 MJ/kg (1700 kcal/kg) with operational limits ranging from 4.2 to 10 MJ/kg (1000–2400 kcal/kg). Due to the continuing increase in the LHV of wastes, however, the present values are well over the design limits for many plants. This has caused serious operation problems. For example, excessively high temperature damages furnace walls and the increased need for maintenance lowers plant availability. In addition, waste throughput is kept low in order to control for heat input to the boiler. Only several plants built recently can properly treat the wastes with a high LHV. Therefore, retrofit of the furnace and boiler is required for existing plants with a sufficient life-time remaining. A successful example for this is the plant at Yangchun, Seoul (operated by Hankook Seghers Co. Ltd., Seoul, Korea; two units of 200 t/day capacity; commissioned in 1996) which replaced the existing refractory wall in the lower part of the furnace with membrane wall to increase the heat absorption of the boiler. Similar to most old plants, the refractory wall in the lower furnace was originally designed to achieve quick ignition and good burn-out of the waste with high moisture content. The heat recovery by membrane walls started from the level of secondary air injection in the mid-level of the furnace. Installing the membrane wall in the lower part of the furnace in 2010 enabled 20% increase in the waste throughput for a reference LHV of 11.3 MJ/kg (2700 kcal/kg) [26].

4.2. Steam Pressure and Power Generation Efficiency for a New Plant

Power generation efficiency of Korean WtE CHP plants in 2010 was very low with a gross value of 3.65% and net 1.03%. This was due to low steam pressures in boilers. Table 3 details the technical data for steam produced at four representative WtE plants. Most large CHP or heat-only plants have designed steam pressures of 16–21 bar with temperatures of 200–240 °C which are close to saturated steam. The highest steam pressure is about 40 bar with a temperature of 400 °C at two heat-only plants located in Seoul (Gangnam and Nowon). The steam is exported to a nearby CHP facility that supplies heat for district heating. A recently built plant in Ichon has the highest steam pressure of 30 bar for WtE CHP in Korea. Small-scale plants such as the one in Nonsan, have a steam pressure of 7–10 bar and temperature 160–183 °C for heat production. The reason for such low steam pressures and temperatures is due to the large heat demand for DH and also the minimization of corrosion in heat exchangers. In contrast, WtE plants in Japan commissioned since the year 2000 mostly have steam temperatures around 400 °C and power generation efficiency as high as 23% [27]. Most plants in the EU also have steam temperatures of about 400 °C and above with steam pressures of about 40 bar [10,28]. A state-of-the-art WtE plant at the Netherlands achieves 30% of net power generation efficiency with a steam pressure of 125 bar and temperature 440 °C [29]. Therefore, increasing the power generation efficiency with higher steam pressures is essential for new WtE installations in Korea. The configuration of steam pressures, turbines and energy efficiencies for WtE has been reviewed by Pavlas et al. [30].

Table 3. Design properties of steam at four representative WtE plants.

Plant (City)		Gangnam, Seoul	Jeonju	Ichon	Nonsan
Capacity (t/h)		300 × 3 units	200 × 2 units	150 × 2 units	50 × 1 units
Design properties of steam	Pressure (bar, gauge)	40	21	30	7
	Temp (°C)	400	216	300	170
	Flow rate (t/h)	131.4	59.3	60.6	6.6
Energy production		Heat-only	CHP	CHP	Heat-only
Note		Heat exported to CHP system	Typical at large- scale plants for CHP or heat-only		Typical at small scales

Table 3. Design properties of steam at four representative WtE plants.

Plant (City)		Gangnam, Seoul	Jeonju	Ichon	Nonsan
Capacity (t/h)		300 × 3 units	200 × 2 units	150 × 2 units	50 × 1 units
Design properties of steam	Pressure (bar, gauge)	40	21	30	7
	Temp (°C)	400	216	300	170
	Flow rate (t/h)	131.4	59.3	60.6	6.6
Energy production		Heat-only	CHP	CHP	Heat-only
Note		Heat exported to CHP system	Typical at large- scale plants for CHP or heat-only		Typical at small scales

4.3. Improving the Energy Efficiency at Existing Plants

Energy efficiency improvement of existing plants can be achieved by installing a steam turbine or by installing an additional heat export system to a nearby site if the demand for heat exists. Another way is to co-locate new waste management facilities with heat demand (e.g., food waste treatment or drying of sewage sludge for fuel production) at an existing WtE plant. Reduction in consumption of auxiliary fuels and electricity is also necessary to improve efficiency. However, such measures are appropriate only for plants with excess heat and sufficiently long life-times. According to study by the Korean Ministry of Environment [31], installing a steam turbine for power generation was economically feasible in nine plants with a capacity larger than 50 t/day and five smaller plants. These plants had over six years of life-time remaining and most had >3 t/h of excess steam not utilized. The energy efficiency of these plants is expected to increase since the government has initiated several projects to install additional energy recovery facilities.

4.4. Transboundary Centralization of a WtE Plant

Currently, there are over 100 incineration plants with capacities smaller than 50 t/day across Korea. These small-scale plants are usually located in rural areas and do not recover heat. Instead, water is sprayed at the furnace exit to quench the combustion gas for prevention of PCDD/Fs formation. The main reasons for not recovering energy from wastes are: (i) to lower the capital costs; (ii) nearby heat demanding sites are not available; and (iii) difficulties in maintaining continuous operation. In order to increase energy recovery from small-scale plants, governmental policy should include transboundary centralization of new WtE plants between neighboring local authorities. One effective approach would be to provide government subsidies to cover the capital costs of centralized WtE plants with heat recoveries above a certain thresholds such as the R1 formula of the EU WFD. In order to be eligible for the subsidies (30%–50% of capital costs), the current legislation for waste management in Korea requires a new WtE plant to have energy recovery/utilization and transboundary treatment of MSW. However, no thresholds are set in the legislation on the efficiency of energy recovery.

Old WtE plants also require transboundary approach of MSW management to increase plant availability and energy production. Good examples can be found in Seoul. Among four plants in the capital, three were built in 1996–2001 only for the MSW generated from the districts where they are located. The plants had a waste throughput ranging only from 20% to 30% of the capacity until 2006, due to a decrease in the amount of waste as a result of increased recycling rate and separation of food waste from combustibles. However, the plant availability has increased to about 60%–80% since transboundary waste treatment began in 2007 [26]. Such a progress was possible by raising public acceptance on incineration after improving the removal efficiency of PCDD/Fs in the plants to a level of 0.01 ng-TEQ/m³ (average of 0.003 ng-TEQ/m³ in 2011), far below the emission regulation (0.1 ng-TEQ/m³). The latest plant (Mapo) in Seoul was built in 2005 with a planning for transboundary waste treatment. The four plants currently treat MSW from 22 districts out of 25 in the capital.

4.5. Renewable Energy from WtE

International standards for renewable energy such as that of EU Renewable Energy Directive (2009/28/EC) differentiate biogenic fractions of MSW from non-biogenic fractions. However, the energy from MSW in Korea is classified as “new and renewable energy”, together with other wastes such as residual gas from oil refineries, waste tires, waste woods and integrated gasification combined cycle (IGCC) of coal. Although the statistics of MSW includes the breakdown of materials in MSW (as shown in Figure 1b), no standard has yet been established to estimate the energy and CO₂ emission from non-biogenic and biogenic fractions. Table 4 summarizes a study by the Korea Energy Economics Institute that estimated the proportion of energy from biogenic fractions of MSW for two cases of LHV. Based on the US Energy Information Administration (EIA) method [32], about 40% of energy can be classified as renewable. Note that the component of textile/leather (TL) is classified as biogenic in the EIA method for simplification, although it may include a certain fraction of synthetic materials. In contrast, the European standard (EN 15440) for manual sorting assumes 50% biogenic for fabric and 80% for leather [33]. The error involved in such simplifications could be significant. Therefore, further investigations are required to determine the LHV and biogenic fractions of individual materials for domestic MSW in Korea [24]. Recognizing the renewable portion of power from MSW, raising its price could be an effective way to achieve higher power generation efficiency from WtE plants. The current incentive on the electricity from a WtE plant is not significant as it is sold at a system marginal price (SMP, average of about 120 KRW/kWh in 2011) plus a fixed rate of 5 KRW/kWh.

Table 4. Estimation of energy contribution from biogenic fractions in MSW.

Components in MSW	Paper	Wood	Food	TLa	Plastics	Incomb.	Misc.
wt %	33.9	7.9	13.0	8.1	26.4	7.3	3.4
Biogenic fraction b	1.0	1.0	1.0	1.0	0.0	-	0.0
LHV case 1b (MJ/kg)	7.07	10.55	0.93	14.78	26.31	-	0
LHV fractions (%)	20.9	7.2	1.1	10.4	60.4	-	0
Total biogenic LHV fraction	39.6%
LHV case 2c	9.79	9.74	1.82	14.18	29.24	-	12.67
LHV fractions (%)	24.4	5.6	1.7	8.5	56.7	-	3.1
Total biogenic LHV fraction	40.2%

Notes: ^a Textile/Leather; ^b Data from US Energy Information Administration [32], LHV for food is annual average in Seoul [22]; ^c Analytical data from Sudokwon Landfill Site, Korea, in 2000 [22].

Table 4. Estimation of energy contribution from biogenic fractions in MSW.

Components in MSW	Paper	Wood	Food	TLa	Plastics	Incomb.	Misc.
wt %	33.9	7.9	13.0	8.1	26.4	7.3	3.4
Biogenic fraction b	1.0	1.0	1.0	1.0	0.0	-	0.0
LHV case 1b (MJ/kg)	7.07	10.55	0.93	14.78	26.31	-	0
LHV fractions (%)	20.9	7.2	1.1	10.4	60.4	-	0
Total biogenic LHV fraction	39.6%
LHV case 2c	9.79	9.74	1.82	14.18	29.24	-	12.67
LHV fractions (%)	24.4	5.6	1.7	8.5	56.7	-	3.1
Total biogenic LHV fraction	40.2%

Notes: ^a Textile/Leather; ^b Data from US Energy Information Administration [32], LHV for food is annual average in Seoul [22]; ^c Analytical data from Sudokwon Landfill Site, Korea, in 2000 [22].

4. Conclusions

The status of MSW energy recovery in Korea was reviewed and its issues related to achieving a high energy efficiency were discussed. The proportions of MSW recycled and incinerated have significantly increased to reach 60.5% and 21.6% in 2010, respectively. With a decrease in the fraction of food waste, the LHV of MSW has also gradually increased to 11.9 MJ/kg. In 2010, about half of large WtE plants were CHP while the rest produced heat alone. Heat production was dominant in the energy output due to the large demand for DH. The proportion of on-site consumption of heat and power produced was significant, but the amount of heat exported for DH/PH and that of power to grid were gradually increasing. Although the power generation efficiency was very low, the R1 efficiency of WtE CHP plants in the country was comparable to the average of European plants. For the heat producing plants, the efficiency was higher.

To further improve energy efficiency, power generation efficiency needs to be increased by the installation of boilers with steam pressures above 20–30 bar. Transboundary centralization of WtE plants between neighboring local authorities is an essential element of waste management policy that would to prevent development of new small-scale plants with low energy efficiencies. Evaluating the renewable fraction of energy from MSW is required to promote efficient energy recovery of WtE plants and also to comply with international standards for energy statistics.