Study on Volatile Organic Compound (VOC) Emission Control and Reduction Potential in the Pesticide Industry in China
Abstract
:1. Introduction
2. Materials and Methods
2.1. Study Objects
2.2. Data Collection
2.3. Methodology
2.3.1. Collection Rate of Exhaust Gas
2.3.2. Facility Removal Rate
2.3.3. Facility Commissioning Rate
2.3.4. Comprehensive Facility Removal Rate
2.4. Design Scenario
3. Results and Discussion
3.1. Characteristics of VOC Pollution in the Pesticide Manufacturing Industry
3.2. List of Key VOC Substances in Pesticide Manufacturing Industry
3.3. VOC Treatment Technologies in Pesticide Manufacturing Industry
3.3.1. Proportion of VOC Treatment Technologies Used
3.3.2. Facility Removal Rates of VOCs
3.3.3. Collection Rate of Exhaust Gas
3.3.4. Emission Reduction Benefit and Economic Evaluation
3.4. VOC Emission Reduction Potential of the Pesticide Manufacturing Industry
4. Conclusions and Prospects
Supplementary Materials
Author Contributions
Funding
Institutional Review Board Statement
Informed Consent Statement
Data Availability Statement
Acknowledgments
Conflicts of Interest
References
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Target Levels | Proportion of Factories (%) | ||
---|---|---|---|
Benchmark | Moderate | Poor | |
Low | 20 | 65 | 15 |
Moderate | 30 | 60 | 10 |
High | 40 | 58 | 2 |
Process | Generating Point | Cause | Emission Characteristics | Emission Form | Discharge Concentration after Collection and Treatment (mg/m3) |
---|---|---|---|---|---|
Feeding | Feeding port | The feeding port is connected to the reactor | Normal temperature and pressure, intermittent discharge | Organized/fugitive emissions | <10 |
Reaction | Reactor, washing kettle, etc. | Displacement, purging and other processes | High temperature, atmospheric or high pressure, intermittent discharge | Organized emissions | 5~110 |
Refining | Distillation tower, rectification tower, crystallization tank, etc. | Discharge during replacement, purging, material in- and outflow, etc. | High temperature, atmospheric pressure, intermittent discharge | Organized emissions | 5~110 |
Separation | Filter presses, stratification facilities | Processes such as open filter presses | Normal temperature, normal pressure, intermittent discharge | Organized/fugitive emissions | 5~110 |
Filling | Discharge port, product filling, etc. | Product discharge | Normal temperature, normal pressure, intermittent discharge | Organized/fugitive emissions | <10 |
Storage | Breathing valve of the organic liquid storage tank at atmospheric pressure | Tank breathing | Normal temperature, normal pressure, intermittent discharge | Organized/fugitive emissions | <10 |
Wastewater treatment | Open liquid surface in wastewater treatment facilities | Liquid escape | Normal temperature, normal pressure, continuous discharge | Organized/fugitive emissions | <10 |
Loading | Open mouths of tankers etc. | Exhaust gas discharge due to internal and external gas phase balance | Normal temperature, normal pressure, intermittent discharge | Organized/fugitive emissions | <10 |
Hazardous waste storage | Hazardous waste warehouse, raw material warehouse | Escape caused by poor packaging | Normal temperature, normal pressure, continuous discharge | Organized/fugitive emissions | <10 |
Vacuum system | Wet vacuum system, circulating water tank | VOC escape from circulating water | Normal temperature, normal pressure, continuous discharge | Organized/fugitive emissions | Fugitive emissions caused by improper management >3000 |
Circulating water system | Open circulating water equipment | VOC escape from circulating water | Normal temperature, normal pressure, continuous discharge | Fugitive emissions | High VOC emissions caused by improper management |
Type | Key VOC Substances | Origins | Screening Evidence |
---|---|---|---|
Alkanes | Cyclohexane, n-hexane, n-heptane, methylcyclohexane | Intermediates, raw materials | Refer to active substance lists [30,31,32,33] |
Olefins | Acrylonitrile | Raw materials | High MIR value [34,35]; pungent odour |
Propylene, isoprene, ethylene, 1-pentene, cyclopentene, trans-3-heptene, trans-1,3-dichloropropene, cyclohexene, styrene, isopentene | Intermediates, raw materials | Refer to active substance lists [30,31,32,33] | |
Aromatic hydrocarbons | Benzene series (benzene, toluene, xylene) | Raw materials, solvents, contaminants | Benzene: carcinogenicity class I (high toxicity) Toluene: high MIR value; large amount used as solvent Xylene: high MIR value; large amount used as solvent [34,35] |
m/p-xylene, o-xylene, m-diethylbenzene, naphthalene | Intermediates, raw materials | Refer to active substance lists [30,31,32,33] | |
Oxygenated hydrocarbons | Formaldehyde | Raw materials and byproducts | Carcinogenicity class I; high MIR value; inhalation toxicity class I; low olfactory threshold [34,35] |
Glyoxal, propionaldehyde, acrolein, n-butyraldehyde, n-butanol, n-hexanal, 3-methoxy-1-butanol, methyl isobutyl ketone, ethanol, cyclohexanone, n-propyl acetate, Methyl tert-butyl ether, methanol, ethyl acetate, isopropanol | Intermediates, raw materials | Refer to active substance lists [30,31,32,33] | |
Halogenated olefins | Trichloroethylene | Intermediates, raw materials | Refer to active substance lists [30,31,32,33] |
Phenols | Phenols | Raw materials | Industry standard requirements, no MIR value yet |
Chlorobenzenes | Chlorobenzenes | Byproduct | Industry standard requirements, no MIR value yet |
Facility | Coverage Rate | Facility Removal Rates of VOCs (In Terms of Total Nonmethane Hydrocarbons) (%) | ||
---|---|---|---|---|
Concentration I (>250 mg/m3) | Concentration II (20~250 mg/m3) | Concentration III (<20 mg/m3) | ||
Incineration (RTO) | 23.3% | 98 | 82 | 53 |
Multistage absorption and adsorption | 64.14% | 95 | 65 | 35 |
Multistage absorption | 71.99% | 85 | 51 | 16 |
Specific Pollutants | Recommended Combination Process | Removal Rate/% |
---|---|---|
Benzene | One-stage alkali absorption + RTO | 99 |
Acrylonitrile | Alkali absorption | 95 |
Xylene | Two-stage falling film + two-stage lye absorption + one-stage activated carbon adsorption | 90 |
Two-stage 5 °C water-cooled treatment +activated carbon adsorption and desorption | 90 | |
One-stage absorption with water spray + one-stage alkali absorption + one-stage activated carbon adsorption | 95 | |
Phosgene | Alkali absorption + RTO | 99 |
Two-stage absorption with falling water film + two-stage hot water catalytic light breaking absorption + one-stage absorption with falling water film + one-stage alkali absorption in packed tower | 95 | |
Toluene | Activated carbon adsorption | 98 |
Condensation absorption | 80 | |
Secondary falling film absorption + activated carbon adsorption | 95 | |
Formaldehyde | One-stage alkali absorption + RTO | 98 |
Water absorption | 90 | |
Secondary falling film absorption + activated carbon adsorption | 95 |
Collection Method | Coverage Rate % | Collection Rate % | The Conditions that Must Be Met to Reach the Upper Limit Efficiency, Otherwise the Limit Is Calculated |
---|---|---|---|
Direct connection to the exhaust gas outlet of the equipment | Approximately 80% | 80~95 | The equipment has a fixed discharge pipe (or port) directly connected to the air duct. The equipment is completely sealed, leaving only the product inlet and outlet open, and there are exhaust gas collection measures at the inlet and outlet. When the collection system is running, hardly any VOCs are emitted around it. |
Confined collection in workshop or closed room | Approximately 40% | 80~95 | The roof is cast in place, and the surrounding walls, doors, and windows have good airtightness. The total air volume collected ensures a slight negative pressure at the opening (the suction wind speed at the open section is not less than 0.5 m/s), and exhaust gas is not leaked. |
Semi-closed hood or fume hood | Approximately 60% | 65~85 | At the point (surface) of pollutant generation, the controlled wind speed towards the suction port shall not be less than 0.5 m/s. |
Hot upper suction hoods | Approximately 30% | 30~60 | At the point (surface) of pollutant generation, the controlled wind speed towards the suction port shall not be less than 0.5 m/s. “Hot” refers to the temperature of the gas emitted by the pollution source, which must be ≥60 °C. |
Cold upper suction hoods | >90% | 20~50 | At the point (surface) of pollutant generation, the controlled wind speed towards the suction port shall not be less than 0.5 m/s. “Cold” refers to the temperature of the gas emitted by the pollution source, which must be <60 °C. |
Side suction hoods | >90% | 20~40 | At the point (surface) of pollutant generation, the controlled wind speed towards the suction port shall not be less than 0.5 m/s, and the distance between the suction hood and the far end of the pollution source shall not be greater than 0.6 m. |
Technology | Depreciation Cost (Ten Thousand US Dollars) | Operating Cost (Ten Thousand US Dollars) | Comprehensive Cost (Ten Thousand US Dollars) | VOC Treatment Amount (t/a) | Unit VOC Reduction Cost (US dollars/ton) |
---|---|---|---|---|---|
RTO (low cost) | 31.08 | 8.88 | 39.96 | 88.2 | 4530.28 |
RTO (high cost) | 68.08 | 34.04 | 102.12 | 187.51 | 5446.40 |
Multistage absorption and adsorption | 6.66 | 3.7 | 10.36 | 32.47 | 3190.88 |
Multistage absorption | 5.92 | 0.74 | 6.66 | 20.06 | 3319.64 |
Evaluation Node | Proportion of VOC Pollution | Estimated Exhaust Gas Collection Rate/Type of Factory | Estimated Facility Commissioning Rate/Type of Factory | Estimated Facility Removal Rate/Type of Factory | Estimated Comprehensive Removal Rate/Type of Factory | ||||||||
---|---|---|---|---|---|---|---|---|---|---|---|---|---|
B | M | P | B | M | P | B | M | P | B | M | P | ||
Preparation, feeding and reaction process | 5% | 95% | 75% | 0 | 95% | 80% | 50% | 95% | 75% | 30% | 86% | 45% | 0% |
Solid–liquid separation | 20% | 95% | 75% | 60% | 95% | 80% | 50% | 95% | 75% | 30% | 86% | 45% | 9% |
Drying | 30% | 95% | 85% | 75% | 95% | 80% | 50% | 95% | 75% | 30% | 86% | 51% | 11% |
Solvent recovery, vacuum system | 35% | 98% | 95% | 85% | 95% | 80% | 50% | 95% | 75% | 30% | 88% | 57% | 13% |
Packaging | 3% | 95% | 85% | 0 | 95% | 80% | 50% | 95% | 75% | 30% | 86% | 51% | 0% |
Solvent storage and transportation | 2% | 95% | 75% | 50% | 95% | 80% | 50% | 95% | 95% | 0 | 86% | 57% | 0% |
Sewage station | 2% | 90% | 75% | 10% | 95% | 80% | 50% | 90% | 60% | 30% | 77% | 36% | 2% |
Others | 3% | 90% | 75% | 0 | 95% | 80% | 50% | 95% | 60% | 30% | 81% | 36% | 0% |
Whole plant evaluation | 86% | 51% | 10% |
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Wang, N.; Shi, M.; Wu, S.; Guo, X.; Zhang, X.; Ni, N.; Sha, S.; Zhang, H. Study on Volatile Organic Compound (VOC) Emission Control and Reduction Potential in the Pesticide Industry in China. Atmosphere 2022, 13, 1241. https://doi.org/10.3390/atmos13081241
Wang N, Shi M, Wu S, Guo X, Zhang X, Ni N, Sha S, Zhang H. Study on Volatile Organic Compound (VOC) Emission Control and Reduction Potential in the Pesticide Industry in China. Atmosphere. 2022; 13(8):1241. https://doi.org/10.3390/atmos13081241
Chicago/Turabian StyleWang, Na, Mali Shi, Shengmin Wu, Xinyan Guo, Xiaohui Zhang, Ni Ni, Sha Sha, and Houhu Zhang. 2022. "Study on Volatile Organic Compound (VOC) Emission Control and Reduction Potential in the Pesticide Industry in China" Atmosphere 13, no. 8: 1241. https://doi.org/10.3390/atmos13081241
APA StyleWang, N., Shi, M., Wu, S., Guo, X., Zhang, X., Ni, N., Sha, S., & Zhang, H. (2022). Study on Volatile Organic Compound (VOC) Emission Control and Reduction Potential in the Pesticide Industry in China. Atmosphere, 13(8), 1241. https://doi.org/10.3390/atmos13081241