Life Cycle Assessment and Economic Analysis of Biomass Energy Technology in China: A Brief Review
Abstract
:1. Introduction
2. Current Situation of Major Biomass Power Generation Technologies in China
2.1. Biomass Direct Combustion Power Generation
2.2. Biomass Gasification Power Generation
2.3. Biomass Mixed-Combustion Power Generation
2.4. Biomass Biogas Power Genzeration
3. Environmental Benefit Analysis of Domestic Biomass Power Generation Technologies
3.1. Goal and Scope
3.2. Inventory Analysis
3.3. Environmental Impact Assessment
3.3.1. Environmental Impact Potential Value Calculation
- EP(j): Contribution of product environmental impact potential value j;
- EPi(j): Contribution of the pollutant i to the environmental impact j;
- Qi: Emissions of pollutant i;
- EFi(j): Equivalent factor of the pollutant i to the environmental impact category j;
- and the characterization results of different power generation processes are shown in Table 3.
3.3.2. Normalization and Weighting Analysis
3.4. Results Analysis
4. Economic Analysis of Domestic Biomass Power Generation Technologies
4.1. Capital Inflow–Outflow List Analysis
4.2. Economic Evaluation
- Pt′: Discounted Pay-back (10%) period
- CI: Cash inflow
- CO: Cash outflow
- (CI–CO)t: Net cash flow in year t
- n: Years
- ic: Base earning rate
- NPV: Net present valuei1: Low discount rate
- i2: High discount rate
4.3. Results Analysis
5. Conclusions
- (1)
- This paper discussed the process flow and characteristics of four leading biomass power generation technologies, including biomass direct combustion power generation, biomass gasification power generation, biomass mixed-combustion power generation, and biomass biogas power generation.
- (2)
- According to the environmental impact assessment of coal-fired power generation and different biomass power generation technologies, the latter has better environmental benefits, among which biomass gasification power generation has the best environmental benefits, with environmental loads of 1.05 × 10−5. Compared with coal-fired power generation, the emission reduction rate of biomass gasification power generation is 97.69%, followed by biomass biogas power generation (79.69%), biomass direct combustion power generation (72.87%), and biomass mixed-combustion power generation (14.56%).
- (3)
- According to the economic evaluation of different biomass power generation technologies, when the dynamic pay-back period and IRR are used as evaluation indexes, the biomass direct combustion power generation has the best pay-back period (7.71 years) and IRR (19.16%), followed by biomass biogas power generation (12.03 years and 13.49%, respectively). The dynamic pay-back period and IRR of biomass gasification and mixed-combustion power generation technologies are longer and lower, respectively. When taking the NPV as the evaluation index, biomass biogas power generation technology has the highest NPV (1,497,276 pound/MW), followed by biomass direct combustion power generation technology (763,686 pound/MW), and the NPV of biomass mixed-combustion and gasification power generation are lower. Compared with coal-fired power generation, direct combustion power generation and biogas power generation have more obvious economic benefits.
Author Contributions
Funding
Acknowledgments
Conflicts of Interest
References
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Technology | CO2 | CO | CH4 | NOx | PM | SO2 |
---|---|---|---|---|---|---|
direct combustion | 7.48 × 10−2 | 2.50 × 10−4 | 5.29 × 10−5 | 3.04 × 10−3 | 2.24 × 10−4 | 3.26 × 10−3 |
gasification | 4.70 × 10−2 | 8.30 × 10−5 | 4.71 × 10−5 | 1.11 × 10−4 | 3.37 × 10−4 | 2.58 × 10−4 |
mixed-combustion | 8.71 × 10−1 | 1.29 × 10−3 | 2.09 × 10−3 | 5.78 × 10−3 | 1.62 × 10−2 | 8.60 × 10−3 |
biogas | 5.11 × 10−1 | 1.03 × 10−3 | 5.37 × 10−5 | 8.72 × 10−4 | 1.69 × 10−4 | 3.18 × 10−3 |
Coal-fired | 1.07 | 1.55 × 10−3 | 2.60 × 10−3 | 6.46 × 10−2 | 2.02 × 10−2 | 9.93 × 10−3 |
Impact Categories | Unit | Key Parameters |
---|---|---|
global warming potential (GWP) | kg CO2 eq | CO2 = 1, CO = 2, CH4 = 25, NOx = 320 [77] |
acidification potential (AP) | kg SO2 eq | SO2 = 1, NOx = 0.7 [78,79] |
creation of photochemical ozone potential (POCP) | kg Ethene eq | SO2 = 0.048, NOx = 0.028, CO = 0.04, CH4 = 0.007 [79,80] |
human toxicity potential (HTP) | kg CO eq | SO2 = 100, NOx = 65, CO = 1 [73,81] |
soot potential (SP) | kg PM eq | PM = 1 [81] |
Technologies | GWP/kg CO2 eq | AP/kg SO2 eq | POCP/kg Ethene eq | HTP/kg CO eq | SP/kg PM eq |
---|---|---|---|---|---|
direct combustion | 1.05 | 5.39 × 10−3 | 2.49 × 10−4 | 5.24 × 10−1 | 2.24 × 10−4 |
gasification | 8.39 × 10−2 | 3.36 × 10−4 | 1.80 × 10−5 | 3.31 × 10−2 | 3.37 × 10−4 |
mixed-combustion | 2.77 | 1.26 × 10−2 | 6.24 × 10−4 | 1.24 | 1.62 × 10−2 |
biogas | 7.93 × 10−1 | 3.79 × 10−3 | 2.05 × 10−4 | 3.76 × 10−1 | 1.69 × 10−4 |
Coal-fired | 3.21 | 1.45 × 10−2 | 7.18 × 10−4 | 1.41 | 2.02 × 10−2 |
Impact | Baseline [72,82] | Normalized Result | ||||
---|---|---|---|---|---|---|
Direct Combustion | Gasification | Mixed-Combustion | Biogas | Coal-Fired | ||
GWP | 8700 kg CO2 eq | 1.21 × 10−4 | 9.64 × 10−6 | 3.19 × 10−4 | 9.12 × 10−5 | 3.68 × 10−4 |
AP | 36 kg SO2 eq | 1.50 × 10−4 | 9.32 × 10−6 | 3.51 × 10−4 | 1.05 × 10−4 | 4.01 × 10−4 |
POCP | 0.65 kg Ethene eq | 3.83 × 10−4 | 2.78 × 10−5 | 9.60 × 10−4 | 3.16 × 10−4 | 1.10 × 10−3 |
HTP | 9100 kg CO eq | 5.76 × 10−5 | 3.63 × 10−6 | 1.36 × 10−4 | 4.13 × 10−5 | 1.55 × 10−4 |
SP | 18 kg PM eq | 1.24 × 10−5 | 1.87 × 10−5 | 9.00 × 10−4 | 9.39 × 10−6 | 1.12 × 10−3 |
Weighting | Global Warming | Acidification | Photochemical Ozone Creation | Human Toxicity | Soot |
---|---|---|---|---|---|
Global warming | 1 | 3 | 6 | 5 | 4 |
Acidification | 1/3 | 1 | 3 | 6 | 5 |
Photochemical ozone creation | 1/6 | 1/3 | 1 | 3 | 6 |
Human toxicity | 1/5 | 1/6 | 1/3 | 1 | 3 |
Soot | 1/4 | 1/5 | 1/6 | 1/3 | 1 |
Weight | Global Warming | Acidification | Photochemical Ozone Creation | Human Toxicity | Soot |
---|---|---|---|---|---|
Value | 0.48 | 0.25 | 0.05 | 0.13 | 0.09 |
Technology | Direct Combustion | Gasification | Mixed-Combustion | Biogas | Coal-Fired |
---|---|---|---|---|---|
Value | 1.23 × 10−4 | 1.05 × 10−5 | 3.88 × 10−4 | 9.21 × 10−5 | 4.56 × 10−4 |
Technology | Scale | Initial Investment | Operation Investment | Operation Profit | Annual Profit |
---|---|---|---|---|---|
direct combustion | 30 MW | 33,607,200 | 8,878,320 | 15,518,250 | 6,639,930 |
gasification | 4 WM | 7,255,644 | 1,205,094 | 2,069,100 | 864,006 |
mixed-combustion | 300 WM | 150,323,250 | 110,918,808 | 116,403,804 | 5,484,996 |
biogas | 2 MW | 12,079,782 | 407,550 | 2,178,198 | 1,770,648 |
Coal-fired | 1320 MW | 661,426,062 | 337,885,284 | 425,765,604 | 87,880,320 |
Technology | Scale | Dynamic Pay-Back Period/Year | NPV/Pound·MW−1 | IRR/% |
---|---|---|---|---|
direct combustion | 30 MW | 7.71 | 763,686 | 19.16 |
gasification | 4 MW | 19.28 | 25,080 | 10.20 |
mixed-combustion | 300 MW | >20.00 | 155,496 | −2.83 |
biogas | 2 MW | 12.03 | 1,497,276 | 13.50 |
Coal-fired | 1320 MW | 14.50 | 566,808 | 11.88 |
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Chen, S.; Feng, H.; Zheng, J.; Ye, J.; Song, Y.; Yang, H.; Zhou, M. Life Cycle Assessment and Economic Analysis of Biomass Energy Technology in China: A Brief Review. Processes 2020, 8, 1112. https://doi.org/10.3390/pr8091112
Chen S, Feng H, Zheng J, Ye J, Song Y, Yang H, Zhou M. Life Cycle Assessment and Economic Analysis of Biomass Energy Technology in China: A Brief Review. Processes. 2020; 8(9):1112. https://doi.org/10.3390/pr8091112
Chicago/Turabian StyleChen, Shuangyin, He Feng, Jun Zheng, Jianguo Ye, Yi Song, Haiping Yang, and Ming Zhou. 2020. "Life Cycle Assessment and Economic Analysis of Biomass Energy Technology in China: A Brief Review" Processes 8, no. 9: 1112. https://doi.org/10.3390/pr8091112
APA StyleChen, S., Feng, H., Zheng, J., Ye, J., Song, Y., Yang, H., & Zhou, M. (2020). Life Cycle Assessment and Economic Analysis of Biomass Energy Technology in China: A Brief Review. Processes, 8(9), 1112. https://doi.org/10.3390/pr8091112