1. School of Energy Science and Engineering, Harbin Institute of Technology, Harbin 150001, China 2. School of Energy and Environment, City University of Hong Kong, Hong Kong SAR, China
Microwave-assisted pyrolysis is an effective method for recycling plastic wastes into oils that can be used for aviation fuels. In this study, energy and economic analyses of aviation oil production from microwave-assisted pyrolysis of polystyrene were performed. The total energy efficiency, recovered energy efficiency, unitary cost, unitary energy economic cost, relative cost difference, and energy economic factor were detailed. And the effects of microwave power, pyrolysis temperature, microwave absorbent loading, and microwave absorbent type on these parameters were covered. It was found that pyrolysis temperature has the most significant effect on the unitary cost and unitary energy economic cost of aviation oil, and-microwave absorbent type has a significant influence on energy economic factor during the whole microwave-assisted pyrolysis process. The optimum reaction conditions at the tonnage system for pyrolysis of 1 t polystyrene were microwave power of 650 W, pyrolysis temperature of 460 °C, and silicon carbide (microwave absorbent) at a loading of 2 t (twice than feedstock loading). At these optimal conditions, the total energy efficiency, recovered energy efficiency, unitary cost, unitary energy economic cost, relative cost difference, and energy economic factor were 62.78%, 96.51%, 3.21 × 104 yuan·t–1, 779 yuan·GJ–1, 1.49, and 71.02%, respectively.
According to the price of recycled PS in the market
Electricity cost
0.51
yuan·kW–1·h–1
The electric charge standard in Harbin City, Heilongjiang Province, China
Tonnage microwave oven price
3000000
yuan
The quoted price according to evaluation by the manufacturer
Interest rate
2.75
%
Interest rate in China (year 2023)
Number of annual batches
3500
–
Calculated based on 10 batch production per day (350 days)
Microwave oven lifespan
8
year
Assumption
Tab.1
Microwave power/W
HHVoil/(GJ·t–1)
Qoil/GJ
QPS/GJ
Qelectricity/GJ
Qinput/GJ
450
41.52
35.02
42.22
28.80
71.02
550
41.78
38.21
42.22
24.60
66.82
650
41.25
40.75
42.22
22.68
64.90
750
41.35
37.26
42.22
20.16
62.38
850
41.33
36.25
42.22
23.28
65.50
Tab.2
Fig.2
Microwave power/W
UCoil/(yuan·t–1)
CED/yuan
fEC%
rEC
450
3.87 × 104
1.20 × 104
60.68
1.79
550
3.50 × 104
9.14 × 103
66.97
1.62
650
3.21 × 104
7.56 × 103
71.02
1.49
750
3.48 × 104
7.65 × 103
70.78
1.77
850
3.59 × 104
9.09 × 103
67.09
1.76
Tab.3
Fig.3
Pyrolysis temperature/°C
HHVoil/(GJ·t–1)
Qoil/GJ
QPS/GJ
Qelectricity/GJ
Qinput/GJ
340
42.17
23.62
42.22
27.36
69.58
400
41.29
33.17
42.22
21.60
63.82
460
41.25
40.75
42.22
22.68
64.90
520
40.83
37.20
42.22
21.36
63.58
580
41.17
34.90
42.22
21.72
63.94
Tab.4
Fig.4
Pyrolysis temperature/°C
UCoil/(yuan·t–1)
CED/yuan
fEC/%
rEC
340
5.79 × 104
1.51 × 104
55.09
3.18
400
3.93 × 104
9.48 × 103
66.15
2.08
460
3.21 × 104
7.56 × 103
71.02
1.49
520
3.46 × 104
8.14 × 103
69.48
1.75
580
3.73 × 104
8.99 × 103
67.32
1.92
Tab.5
Fig.5
Microwave absorbent loading/t
HHVoil/(GJ·t–1)
Qoil/GJ
QPS/GJ
Qelectricity/GJ
Qinput/GJ
1.0
40.95
33.76
42.22
24.12
66.34
1.5
41.45
38.13
42.22
22.68
64.90
2.0
41.25
40.75
42.22
22.68
64.90
2.5
41.69
38.73
42.22
25.68
67.90
3.0
41.99
35.83
42.22
30.00
72.22
Tab.6
Fig.6
Microwave absorbent loading/t
UCoil/(yuan·t–1)
CED/yuan
fEC/%
rEC
1.0
3.87 × 104
1.04 × 104
64.15
1.98
1.5
3.45 × 104
8.38 × 103
68.87
1.66
2.0
3.21 × 104
7.56 × 103
71.02
1.49
2.5
3.46 × 104
9.42 × 103
66.29
1.57
3.0
3.84 × 104
1.23 × 104
60.14
1.71
Tab.7
Fig.7
Fig.8
Microwave absorbent type
HHVoil/(GJ·t–1)
Qoil/GJ
QPS/GJ
Qelectricity/GJ
Qinput/GJ
Fe
41.33
38.07
42.22
95.88
138.10
Fe3O4
41.45
39.42
42.22
43.80
86.02
FeS2
40.23
37.28
42.22
42.51
84.73
SiC
41.25
40.75
42.22
22.68
64.90
Tab.8
Microwave absorbent type
UCoil/(yuan·t–1)
CED/yuan
fEC/%
rEC
Fe
1.52 × 105
7.08 × 104
20.75
5.60
Fe3O4
1.22 × 105
2.85 × 104
39.42
6.65
FeS2
1.24 × 105
2.79 × 104
39.90
7.14
SiC
3.21 × 104
7.56 × 103
71.02
1.49
Tab.9
Fig.9
Fig.10
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