Waste Compositions
The composition of MSW has a crucial effect on the waste management system. It could be adopted as raw information to define the ability of MSW recycling and recovering. Moreover, it signifies the environmental emissions associated with waste disposal, or any probable treatments and recycling processes. Population density, life expectancy, income per capita, level of education, and development are the highly important factors affecting the quantity and compositions of the generated MSW (Azam et al., 2020).
Landfills waste composition information in Muscat is collected every three months by the landfill’s operators under normal operations. The latest municipal solid waste composition data of both covered landfills in this study are listed in Figs. 6 and 7.
*WEEE: Waste Electrical and Electronic Equipment
The three main waste categories in Al Amerat landfill are plastic with 24% out of the total waste received in the landfill, followed by food waste with 20% contribution, paper and cardboard waste portion was 16% out of the total MSW.
*WEEE: Waste Electrical and Electronic Equipment
The concentration of different plastic grades waste in Barka landfill makes up the highest percentage, at around 33% out of the total MSW, followed by paper and cardboard of 15% and then food waste of 10%.
From Figs. 6 and 7, it is obvious that the food waste dumped in Al Amerat landfill is double the one in Barka landfill. This mainly could be because of the population lifestyle and concentration of food industry. The area served by Al Amerat landfill has more hotels and restaurants which are responsible for high food waste. The wood portion out of total MSW in Barka is twice that of Al Amerat landfill. Wood recovery could be the key aspect behind this because Muscat municipality wood and green waste are employed in the compost production in Al Amerat.
Overall, Muscat municipal solid waste is characterized by high proportions of recyclable waste in both landfills. However, currently there is no recycling industry and almost all waste is still dumped in the engineered landfills. Among the recycled waste, plastic waste is the highest portion representing about 30% of the total MSW. Most plastic waste is non-biodegradable materials. Non-biodegradable plastic wraps which almost constitute 20% of the total MSW are not appropriate for both composting and combustion procedure and desire to be separated before waste feeds to these processes.
The plastics industry in Oman is supposed to increase sharply shortly which might bring about more plastic waste. Mechanical recycling is the most ecofriendly accessible solution to deal with the huge plastic waste produced and already used widely (Gu et al., 2017). Recycled plastics can be considered as a renewable origin of plastic. Furthermore, in terms of the economic benefits, its price will be less by 20–50% of virgin plastic (Gu et al., 2016). A low cost and high quality of recycling plastic will inspire industry owners to exert it especially in large production and construction (Al-Maaded et al., 2012). Thus, plastic recycling feasibility is worth to be studied further. There is also a possibility to recycle paper and cardboard which represent about 17% of the total waste. This will thus reduce Oman’s dependence on importing of these materials or at least covering the hoped high demand in this field.
The biodegradable waste ratio which primarily consists of food, green, wood, paper, cardboard, and the biodegradable plastic waste is the dominant segment of waste. Thus, biological treatment feasibility could be considered for additional studies.
Landfills hazardous wastes quantity is low because most hospitals waste is directed to incineration facilities somewhat than engineered landfills and there are special industrial waste landfills. These variation in the waste compositions is the evidence of the MSW heterogeneous nature and any solid waste management decisions should be based on a reliable data of each country itself and their long-term plans.
Moisture Content (MC)
Moisture content (MC) is a critical parameter for the degradation of solid waste in landfills. MSW moisture content can be quantified using reported literature moisture contents of the waste categories and their compositions out from the waste separation campaign and can be measured in the laboratory using 103°C ovens for an hour. As it can be seen in Fig. 8, a clear difference in MC for the collected samples in Al Amerat and Barka locations. The main reasons for moisture contents variances are waste content, weather conditions, and the season in which the samples were collected (Hui et al., 2006).
The measured moisture content of MSW samples varied from one sample to another which is normal due to MSW heterogeneous nature. Actual MCs might be higher than this because the analysis was done after days of the fresh waste collection, and the raw sample preparation was done manually because of the unavailability of the shredder machine. However, these results are higher than MCs reported by Baawain in 2017 for Al Amerat landfill waste sample collected in 2015 which ranges from 10.6–14.7% because samples were kept under the sun for many days before the analysis.
MSW moisture contents reported in the literature for Europe normally lower than 30% and it is higher than 60% for East Asia. For example, Hui in 2006 reported values of 53.6–64.1% for mixed waste in Chongqin, whereas Gidarakos in the same year reported 36.72% for the island of Crete in Greece (Hui et al., 2006 and Gidarakos et al., 2006).
Overall, fresh waste moisture content expected to be closed to the reported values. MSW with high MC tends to erode the incineration systems (Hui et al., 2006). While it is required for MSW bioreactor technology (Guérin et al., 2004).
Volatile Content and Loss of Ignition
Volatile content and loss of ignition are both important characteristics to comprehend waste nature. The volatile content (VC) has direct influences on the MSW incineration efficiency. The higher the volatile matter content, the simpler the ignition of MSW will be and more waste fraction can be removed in the incineration process (Azam et al., 2020). In pyrolysis and gasification processes, volatile content impacts production, composition and yield. High volatility leads to more gas pyrolysis and gasification (Zhou et al., 2014).
Volatile contents were investigated in this study through the weight loss of residue from moisture contents measurement ignited at a temperature of 550°C. The proportions of the measured MSW volatility as a dry base in these experiments, as it is shown in Fig. 9, varied from 47.0-82.4%. Volatile contents results were closed to the values reported for Lahor in 2020 which were in the range of 75–93% (Azam et al., 2020). Compared with the aforementioned percentages, the volatile contents acquired by Baawain were within the ranges of 28–33% (Baawain et al., 2017), mostly because there are ongoing variations in the MSW properties with the composition changes.
MSW loss on ignition was also investigated by burning residue samples from volatile content under 1000°C for an hour. The loss ignition was measured in the range of 56.2–91.0% which is higher than the study was conducted in 2015 for Al Amerat landfill MSW (Baawain et al., 2017).
High volatile contents and loss on ignition values show that Muscat dried MSW can be a good feed for incineration plants which is extensively used in modern countries. It is also good feed for both pyrolysis and gasification processes where high feed volatility is necessitated.
Total Oxides
MSW samples oxides have been investigated using metal concentration in samples. Aluminum, Calcium, Iron, and Magnesium concentrations were measured using Flame Atomic Absorption Spectrometer which is known for its high precision and capability to detect trace elements amount. Sodium and Potassium concentration were measured using Flame Atomic Absorption Spectrometer. The measured metals concentration with the mount of Silica is shown in Fig. 10.
Metals concentration were then utilized to estimate the percentage of the metal oxides present in each sample using the proportion of the molecular weight between the metal oxide to the metal. Final metal oxides in the samples are presented in Fig. 11.
Figure 11 shows that the total oxides ratio in the MSW was within the range of 12.4–44.06%. Silica is the highly prominent oxide in all MSW samples followed by Calcium Oxide. The major sources of Silica in the MSW are cement, concrete, bricks, stones, ...etc. There were about 6% of the total MSW in both landfills as fine particulates. Calcium oxide is usually produced from the thermal decomposition of limestone or any other materials containing Calcium Carbonate.
The sample collected from Barka landfill in March shows a higher total oxide, almost twice the amount in other samples. This could be due to waste heterogeneous nature or any variation in the sample preparation procedure. In general, Barka MSW samples have higher amounts of total oxides than Al Amerat samples.
Elemental Analysis
The elemental composition of MSW is extremely significant for heating energy calculations that indicate the quantity of recoverable energy in the waste. Perkin-Elmer 2400 Series II CHNS/O Elemental Analyzer was applied in determining the weight percent of Carbon, Hydrogen, Nitrogen, Sulphur, and Oxygen in each waste sample. The experiment result mass percentage of the MSW samples are shown in Fig. 12. It can be concluded that the most dominant compositions in all mixed waste samples are Carbon and Oxygen. Al Amerat February sample has the highest C content (48.7%w) and Barka March sample has the lowest C content (16.0% w) among mixed waste samples. The Sulfur percentage is the lowest in all samples compared to other elements. Nitrogen content in these samples is within the range of 0.7- 3.0%w.
Carbon content in the sub waste categories is high in four waste groups: paper and cardboard, plastic, textile, and wood. Plastic has the highest C content above (51.9% w) in all samples followed by textile with C content above 40.5% weight in all tested samples.
Oxygen is the second main component in most of the waste samples. The highest content of O was observed in wood, textile, paper, and cardboard. Metal and Glass waste have the lowest O content; except glass samples from Al Amerat landfill which could be because the sample was contaminated with another types of wastes.
Nitrogen content in almost all samples is low, mainly lower than 3%. There was one abnormal N content in the wood sample from the Al Amerat landfill with 15% N content.
Sulfur content in all mix and separated waste samples are low. Wood sample from Al Amerat landfill sample is also an exception in S content with the value of 36.2% which could be a consequence of the sample contamination with other wastes.
Overall, the sub waste categories elemental analysis is satisfactory for samples collected from a mixed waste. This indicates the importance of the waste source separations to minimize the amount of waste contaminations and for more easy and efficient recycling processes. The elemental analysis is mainly required to know the waste chemical compositions which will be used further for waste calorific value computations.
Chemical Content
Waste streams energy are available for some regions around the world and the data unavailability has heightened in low and middle-income countries. This initiates the necessity for reliable models and techniques to evaluate the approximate waste energy before any waste utilization or treatment processes adoption. Researchers use the available literature values for energy computation and exert developed models based on the waste physical and chemical properties to estimate the energy content. In this research, Dulong and modified Dulong equations (Kuleape et al., 2014) were used for the proximate municipal solid waste analysis.
The computation approach started with the waste chemical composition calculation for each kind of waste excluding other waste which includes (Other compositable, Non-compositable, Hazard, Weef, and Complex) wastes, and using the dry mass base. The moisture of the sample was converted to Oxygen and Hydrogen using their molar mass ratios. Moles of each element were then computed by dividing the element mass by their molar mass. After that, normalized moles ratio was calculated with Sulfur and without Sulfur content. Four different chemical formulas were developed for each sample set, two for the mixed waste sample and another two using mass percent of each waste streams. All results are presented in Tables 1 to 6. Normal used approach in most of the literature is waste streams compositions. However, an added chemical formula based of direct elemental assessment of mixed waste sample to test the difference and if there is opportunity to adopt such easier way because working with solid waste is intricate and consume a lot of time.
Table 1
Chemical composition of Al Amerat MSW samples-Feb. 2020
|
Dry mass (kg)
|
Composition (kg)
|
|
|
C
|
H
|
N
|
S
|
O
|
Mix waste
|
78.5
|
37.9
|
4.6
|
1.3
|
0.5
|
11.1
|
Food
|
6.9
|
1.0
|
0.3
|
0.1
|
0.0
|
0.6
|
Paper & Cardboard
|
17.7
|
6.3
|
0.7
|
0.4
|
0.1
|
5.2
|
Plastics
|
23.9
|
12.4
|
1.9
|
0.2
|
0.2
|
0.0
|
Glass
|
4.9
|
0.0
|
0.0
|
0.0
|
0.0
|
1.8
|
Metal
|
2.8
|
0.0
|
0.0
|
0.0
|
0.0
|
0.1
|
Textile
|
4.7
|
1.9
|
0.1
|
0.2
|
0.0
|
1.9
|
Wood
|
1.1
|
0.4
|
0.1
|
0.2
|
0.4
|
0.2
|
Trimming Garden
|
1.9
|
0.9
|
0.1
|
0.0
|
0.0
|
0.8
|
Sanitary
|
3.5
|
1.3
|
0.1
|
0.0
|
0.0
|
0.6
|
Fines & Dust
|
6.0
|
0.5
|
0.0
|
0.0
|
0.0
|
1.2
|
Moisture
|
|
|
3.0
|
|
|
23.7
|
Total Mass (kg)
|
68.8
|
24.7
|
6.2
|
1.1
|
0.7
|
36.0
|
Mass (%)
|
|
35.9
|
9.0
|
1.7
|
1.0
|
52.4
|
Molar Mass (kg/mol)
|
|
12.0
|
1.0
|
14.0
|
32.1
|
16.0
|
Moles
|
|
3.0
|
9.0
|
0.1
|
0.0
|
3.3
|
Molar Ratio with S
|
|
94
|
280
|
4
|
1
|
102
|
Molar Ratio without S
|
|
25
|
75
|
1
|
0
|
27
|
Table 2
Chemical composition of Al Amerat mixed waste sample- Feb. 2020
|
Composition
|
|
C
|
H
|
N
|
S
|
O
|
Total Mass (kg)
|
37.9
|
7.0
|
1.3
|
0.5
|
30.2
|
Mass (%)
|
49.3
|
9.1
|
1.6
|
0.6
|
39.3
|
Molar Mass (kg/mol)
|
12.0
|
1.0
|
14.0
|
32.1
|
16.0
|
Moles
|
4.1
|
9.0
|
0.1
|
0.0
|
2.5
|
Molar Ratio with S
|
215
|
473
|
6
|
1
|
128
|
Molar Ratio without S
|
35
|
78
|
1
|
0
|
21
|
Chemical formulas of Al Amerat using different waste streams samples are chemical formula with S: C
94 H
280 O
102 N
4 S and chemical formula without S: C
25 H
75 O
27 N. While chemical formulas of Al Amerat landfill mixed waste sample using the data in Table
2 analysis are chemical Formula with S: C
215 H
473 O
128 N
6 S and chemical Formula without S: C
35 H
78 O
21 N. From these formulas it is obvious that Carbon and Oxygen are the main chemical compositions in Al Amerat municipal solid waste. Formulas are deviated significantly from each other.
It can be seen that the chemical formulas of Barka Feb. 2020 landfill samples using the data in Table 3 are chemical Formula with S: C125 H376 O99 N3 S and chemical formula without S: C40 H121 O32 N.
On the other hand, the chemical formulas of Barka Feb. 2020 (Table 4) landfill mixed waste sample analysis are chemical formula with S: C77H606 O187 N8 S and chemical formula without S: C10 H79 O25 N.
It showed different chemical formulas of Barka Mar. 2020 landfill samples (Table 5) with S: C191 H436 O109 N2 S and chemical formula without S: C80H183 O46 N.
For the same landfill Barka in Mar. 2020 for mix waste the samples analysis derives the chemical formula with S: C142 H587 O330 N5 S and chemical formula without S: C27 H110 O62 N.
Table 3
Chemical composition of Barka MSW samples-Feb. 2020
|
Dry mass (kg)
|
Composition
|
|
|
C
|
H
|
N
|
S
|
O
|
Mix waste
|
56.7
|
14.6
|
4.9
|
1.7
|
0.5
|
9.1
|
Food
|
2.0
|
0.2
|
0.2
|
0.0
|
0.0
|
0.2
|
Paper & Cardboard
|
20.7
|
6.5
|
1.1
|
0.4
|
0.1
|
7.7
|
Plastics
|
36.7
|
21.8
|
4.1
|
0.4
|
0.4
|
10.0
|
Glass
|
3.7
|
0.0
|
0.0
|
0.0
|
0.0
|
0.1
|
Metal
|
3.6
|
0.1
|
0.0
|
0.0
|
0.0
|
0.1
|
Textile
|
6.4
|
3.3
|
0.6
|
0.1
|
0.1
|
1.9
|
Wood
|
3.1
|
0.6
|
0.1
|
0.0
|
0.0
|
0.9
|
Trimming Garden
|
0.7
|
0.2
|
0.0
|
0.0
|
0.0
|
0.2
|
Sanitary
|
3.6
|
0.1
|
0.5
|
0.0
|
0.0
|
0.4
|
Fines & Dust
|
4.9
|
0.8
|
0.2
|
0.1
|
0.0
|
1.1
|
Moisture
|
|
|
1.6
|
|
|
13.0
|
Total Mass kg
|
79.4
|
33.6
|
8.5
|
1.0
|
0.7
|
35.6
|
Mass (%)
|
|
42.3
|
10.7
|
1.2
|
0.9
|
44.8
|
Molar Mass (kg/mol)
|
|
12.0
|
1.0
|
14.0
|
32.1
|
16.0
|
Moles
|
|
3.5
|
10.6
|
0.1
|
0.0
|
2.8
|
Molar Ratio with S
|
|
125
|
376
|
3
|
1
|
99
|
Molar Ratio without S
|
|
40
|
121
|
1
|
0
|
32
|
Table 4
Chemical composition of Barka landfill mixed waste sample- Feb. 2020
|
Composition
|
|
C
|
H
|
N
|
S
|
O
|
Total Mass (kg)
|
14.6
|
9.7
|
1.7
|
0.5
|
47.6
|
Mass (%)
|
19.7
|
13.1
|
2.3
|
0.7
|
64.2
|
Molar Mass (kg/mol)
|
12.0
|
1.0
|
14.0
|
32.1
|
16.0
|
Moles
|
1.6
|
13.0
|
0.7
|
0.0
|
4.01
|
Molar Ratio with S
|
77
|
606
|
8
|
1
|
187
|
Molar Ratio without S
|
10
|
79
|
1
|
0
|
25
|
Table 5
Chemical composition of Barka MSW samples-Mar. 2020
|
Dry mass (kg)
|
Composition
|
|
|
C
|
H
|
N
|
S
|
O
|
Mix waste
|
77.9
|
12.5
|
1.9
|
0.5
|
0.2
|
18.9
|
Food
|
3.1
|
0.9
|
0.1
|
0.1
|
0.0
|
0.5
|
Paper & Cardboard
|
14.3
|
7.2
|
1.3
|
0.0
|
0.1
|
5.2
|
Plastics
|
37.5
|
24.2
|
3.3
|
0.2
|
0.3
|
3.7
|
Glass
|
3.9
|
0.1
|
0.0
|
0.0
|
0.0
|
0.0
|
Metal
|
2.9
|
0.1
|
0.0
|
0.0
|
0.0
|
0.2
|
Textile
|
5.5
|
3.1
|
0.4
|
0.1
|
0.0
|
1.2
|
Wood
|
2.8
|
1.1
|
0.2
|
0.1
|
0.0
|
1.2
|
Trimming Garden
|
1.7
|
0.1
|
0.0
|
0.0
|
0.0
|
0.1
|
Sanitary
|
3.6
|
0.5
|
0.1
|
0.0
|
0.0
|
0.4
|
Fines & Dust
|
6.5
|
0.5
|
0.1
|
0.1
|
0.0
|
1.2
|
Moisture
|
|
|
2.0
|
|
|
16.1
|
Total Mass (kg)
|
76.4
|
37.9
|
7.6
|
0.6
|
0.5
|
29.8
|
Mass (%)
|
|
49.6
|
9.5
|
0.7
|
0.7
|
37.6
|
Molar Mass (kg/mol)
|
|
12.0
|
1.0
|
14.0
|
32.1
|
16.0
|
Moles
|
|
4.1
|
9.4
|
0.1
|
0.0
|
2.3
|
Molar Ratio with S
|
|
191
|
436
|
2
|
1
|
109
|
Molar Ratio without S
|
|
80
|
183
|
1
|
0
|
46
|
Table 6
Chemical composition of Barka mixed waste sample- Mar. 2020
|
Composition
|
|
C
|
H
|
N
|
S
|
O
|
Total Mass (kg)
|
12.5
|
4.3
|
0.5
|
0.2
|
38.5
|
Mass (%)
|
22.2
|
7.7
|
1.0
|
0.4
|
68.7
|
Molar Mass (kg/mol)
|
12.0
|
1.0
|
14.0
|
32.1
|
16.0
|
Moles
|
1.9
|
7.6
|
0.1
|
0.0
|
4.3
|
Molar Ratio with S
|
142
|
587
|
5
|
1
|
330
|
Molar Ratio without S
|
27
|
110
|
1
|
0
|
62
|
From the chemical formulas analysis for the two landfill, it can be argued that there is no clear association between the waste collection area and the waste chemical formulas. The Table 7 shows that, the MSW formula of Al Amerat is closed to Barka March sample formula. The variation in the chemical formulas is significant between the mixed waste sample chemical formulas and the formulas established by using the landfill waste stream elemental mass percentages. Thus, the mixed waste samples are not typical of the overall waste chemical formula and not adequate to evaluate the solid waste chemical formula. Waste streams elemental analysis are required for accurate results regardless of their complexity.
Table 7
Chemical formulas of solid waste samples
Location
|
Sample
|
Formulas with S
|
Formulas without S
|
Al Amerat
(Feb. 2020)
|
MSW
|
H280 O102 N4 S
|
C25 H75 O27 N
|
Mixed waste
|
C215 H473 O128 N6
|
C35 H78 O21 N
|
Barka
(Feb. 2020)
|
MSW
|
C125 H376 O99 N3
|
C40 H121 O32 N
|
Mixed waste
|
C77H606 O187 N8 S
|
C10 H79 O25 N
|
Barka
(Mar. 2020)
|
MSW
|
C191 H436 O109 N2
|
C80H183 O46 N
|
Mixed waste
|
C142 H587 O330 N5
|
C27 H110 O62 N
|
Energy Content
Waste energy computation of MSW is important to evaluate the viability of any energy recovery initiative (Azam et al., 2020). To evaluate the overall MSW energy content, each waste stream energy was quantified separately. Table 8 shows the waste calculated energy. Waste categories composition of the latest separation of each landfill was used for the waste stream energy calculation.
Table 8
Energy content of MSW samples using waste composition from Be’ah and waste streams energy
|
Wet Mass (kg)
|
Energy (kJ/kg)*
|
Total Energy (kJ)
|
|
Al Amerat
Feb. 2020
|
Barka
Feb. 2020
|
Barka
Mar.2020
|
Al Amerat
Feb. 2020
|
Barka
Feb. 2020
|
Barka
Mar. 2020
|
Mix waste
|
100.0
|
100.0
|
100.0
|
10500
|
106,328
|
31,205
|
48,783
|
Food
|
22.9
|
6.7
|
10.5
|
4650
|
309,953
|
361,768
|
250,826
|
Paper & Cardboard
|
18.8
|
21.9
|
15.2
|
16525
|
793,530
|
1,219,362
|
1,247,969
|
Plastics
|
24.3
|
37.4
|
38.3
|
32600
|
743
|
561
|
603
|
Glass
|
5.0
|
3.7
|
4.0
|
150
|
1,992
|
2,618
|
2,109
|
Metal
|
2.8
|
3.7
|
3.0
|
700
|
91,939
|
124,780
|
107,115
|
Textile
|
5.3
|
7.2
|
6.1
|
17450
|
25,479
|
71,617
|
64,353
|
Wood
|
1.4
|
3.9
|
3.5
|
18600
|
31,507
|
11,441
|
26,842
|
Trimming Garden
|
4.8
|
1.8
|
4.1
|
6500
|
41,096
|
42,354
|
41,295
|
Sanitary
|
8.2
|
8.5
|
8.3
|
5000
|
45,732
|
36,964
|
49,219
|
Fines & Dust
|
6.5
|
5.3
|
7.0
|
7000
|
106,328
|
31,205
|
48,783
|
Total
|
|
|
|
|
1,448,298
|
1,902,671
|
1,839,113
|
*(Peavy te al., 1985) |
The highest energy content was observed in four waste categories: plastics, wood, textile, paper, and cardboard which represent almost more than 50% of the total MSW in all collected samples. Other wastes consist of hazard waste, non-combustible and other combustible, weef and complex waste; energy calculations were avoided because most of them were non-combustible.
The total waste energy content for the wet base is within the range from 1.4 to 1.9 Mn kJ which is in the high range of waste energy content. As for the dry base waste, computations were done using measured waste moisture in Fig. 8. Unit energy was also assessed after normalizing the new total waste without the other waste stream. The outcome of these computations are listed in Table 9.
Table 9
Unit energy content of MSW samples
|
Total Energy (kJ)
|
|
Al Amerat
Feb. 2020
|
Barka
Feb. 2020
|
Barka
Mar. 2020
|
Total Energy (kJ)
|
1448298.2
|
1902670.5
|
1839112.7
|
Total Mass (kg)
|
100.0
|
100.0
|
100.0
|
Unit Energy (kJ/kg)
|
14483.0
|
19026.7
|
18391.1
|
Moisture (%)
|
21.5
|
43.3
|
22.1
|
Energy on Dry basis
(kJ/kg)
|
18449.7
|
33556.8
|
23608.6
|
The energy unit of the MSW samples on the dry base is within the range from 18450 to 33560 kJ/kg. The dry energy content of Muscat MSW estimated by Baawain et al., 2017 was within the range from 15243 to 23779 kJ/kg which are close to the estimated values in this study. MSW typical unit energy as indicated in Peavy, 1985 for wet mix waste is 10500 kJ/kg which is associated with about 14000 kJ/kg for dry base calculations.
MSW incineration as a waste disposal option is debated throughout history because of its high costs and associated air pollution. However, the low and limited economic values of MSW separation and recycling in the past positioned the incineration procedure as the suitable choice for waste disposal for a long time (McKay, 2002). The incineration procedure reduces MSW volume to 80% of its original volume, the cost of the facility can be offset by energy sale, and an efficient flue gas treatment system could control pollutants in air discharge to a satisfactory level (McKay, 2002).
The waste-to-Energy project approved in 2019 at Barka planned to generate between 120 to 160 MW of electricity on yearly basis (Prabhu, 2019). From Table 9, the average unit energy on a dry basis of Muscat mixed waste without any separation was calculated 25205 kJ per kg of MSW. Thus, the planned unit will be necessary to process 479904 kg of MSW per day which is almost a quarter of the residential solid waste produced in Muscat.
One of the major limitations of MSW combustion reported through history is the greenhouse gas (GHG) production which is interrelated with the MSW characteristics and the procedure technology. For example, plastic waste which has high LHV also generates an increment in CO2 emission (Yang et al., 2012). Another main GHG is CH4 and N2O (Hwang et al., 2017). However, mixed MSW incineration contribution to global warming was observed to be less compared to landfilling. This is because generated energy is largely used for electricity production which is usually produced from non-renewable petroleum resources (Hupponen et al., 2015). Thus, adopting incineration in the integrated management system necessitated to investigation all these perspectives in detail based on the Muscat MSW compositions, characteristics, and the region's long-term plans which might affect the compositions.
High Heating Value Content
High heating value (HHV) calculation based on the material elemental analysis has been approved for coal by Dulong (1785–1838) before the availability of a calorimetric bomb which has been then employed for more exact measurement. The formula has been appraised and modified for coal since that time. The first instance of using the equation for MSW HHV estimation was in 1980 and has been reviewed and modified several times for a large number of samples which corroborates its validity (Maksimuk et al., 2020).
Where, C: Carbon (%), H: Hydrogen (%), O: Oxygen (%), S: Sulfur (%) and N: Nitrogen (%)