Multi-Perspective: Research Progress of Probiotics on Waste Gas Treatment and Conversion
Abstract
1. Introduction
2. Mechanism of Waste Gas Conversion Driven by Microbial Metabolism
2.1. Biotransformation of Typical Waste Gases
2.2. Key Influencing Factors of Metabolic Regulation
2.3. Types of Probiotics Converting Harmful Gases
3. Genetic Characteristics of Probiotics Converting Harmful Gases
4. Environmental Application Scenarios—Multi-Domain Waste Gas Treatment Solutions
4.1. Industrial Waste Gas Pollution Control
4.2. Agricultural Source Pollution Control
4.3. Urban Waste Treatment and Formaldehyde Adsorption in New Houses
5. Engineering Design and Optimization
5.1. Mainstream Bioreactor Technology and Characteristics
5.2. Immobilization Technology of Bacteria
5.3. Multivariable Discussion of Process Design and Scale
6. Whole Life Cycle Cost Disassembly
7. Conclusions
8. Future Prospect
Author Contributions
Funding
Institutional Review Board Statement
Informed Consent Statement
Data Availability Statement
Conflicts of Interest
References
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Technical Name | Core Technology Principle | Advantages | Disadvantages |
---|---|---|---|
Adsorption method | By using the huge surface area of porous solid materials, the pollutants in the gas are captured and fixed on the surface of their pores. When the adsorbent is saturated, it needs to be replaced or regenerated. | The technology is mature, the equipment is simple, and the operation is flexible. The treatment efficiency is high, and the removal effect of low-concentration pollutants is remarkable. Valuable solvents can be recycled (by steam or thermal regeneration). | The adsorbent capacity is limited, which needs to be replaced or regenerated regularly, and the operation cost is high. It is not suitable for high concentration, high humidity, or high temperature waste gas (humidity will reduce the adsorption capacity). The waste adsorbent may become a secondary pollutant, which needs to be properly treated. It is sensitive to particulate matter, and the exhaust gas needs to be pre-dusted. |
Absorption method | The exhaust gas is in full contact with the absorption liquid, and the pollutants are transferred from the gas phase to the liquid phase by using the difference in solubility or chemical reaction activity of the pollutants in the absorption liquid, so as to achieve the purpose of purification. | The processing capacity is large, and the application range is wide. The removal efficiency of soluble pollutants is high, and the technology is mature. Specific pollutants can be treated by selecting different absorbents. | Secondary treatment is required to produce wastewater or waste absorption liquid, which increases the subsequent cost and complexity. There may also be equipment corrosion problems. The treatment effect of insoluble or insoluble VOCs is poor. High energy consumption (pump and fan power consumption). |
Thermal combustion and Catalytic combustion | The exhaust gas is heated to a high temperature (usually 760–850 °C), so that the pollutant reacts with oxygen within a sufficient residence time and is completely oxidized and decomposed into CO2 and H2O. Under the action of catalysts (such as platinum, palladium, and other precious metals), the pollutants are oxidized at lower temperatures (usually 300–450 °C). | High destruction efficiency (>99%) and thorough disposal. It can handle complex and mixed VOCs airflow. Thermal combustion can recover heat energy (through heat exchangers) and reduce operating costs. | 1. High initial investment and operating costs (fuel costs), especially thermal combustion. 2. Catalyst has a risk of poisoning (damaged by halogen, phosphorus, sulfur, heavy metals, and other substances), blockage, and wear, and the replacement cost is expensive. 3. Possibly produce secondary pollutants (such as NOx, especially at high temperatures). 4. Not suitable for the treatment of halogen-containing VOCs (which produce dioxins and acid gases). |
Type | Characteristics | Specific Strains and Functions | |
---|---|---|---|
Bacteria | By using the huge surface area of porous solid materials, the pollutants in the gas are captured and fixed on the surface of their pores. When the adsorbent is saturated, it needs to be replaced or regenerated. | Pseudomonas | Degradation of benzene, toluene, xylene, and other aromatic compounds |
Bacillus genus | Uses organic matter as carbon source and energy source, can form spores, and has strong environmental tolerance (such as resistance to drying, resistance to temperature change). | ||
Acinetobacter genus | Good at degrading alkane compounds | ||
Thiobacillus | Hydrogen sulfide (H2S) is oxidized to sulfuric acid (H2SO3) or sulfate [11] | ||
Nitrosomonas | Oxidation of ammonia (NH3) to nitrite (NO2−) | ||
Nitrobacter genus | Nitrite (NO2−) is oxidized to nitrate (NO3−) | ||
Fungi | 1. The mycelium network greatly increases the contact area with the gas, and the absorption efficiency of hydrophobic VOCs (such as olefins, benzene series) is much higher than that of bacteria [12]. 2. It can grow in a low pH environment, which is very suitable for dealing with the system that produces acidic substances in the process of degrading H2S, etc., and can avoid the acidification and collapse of the system. 3. The requirement for moisture is lower than that of bacteria, which reduces the energy consumption and cost of humidification. | Aspergillus niger | Degradation of toluene and other benzene series, stable in low pH biofilter, is a common industrial fermentation strain |
Aspergillus wentii | Degradation of sulfur-containing malodorous gases such as ethanethiol Separated from the biological filter for treating ethanethiol, which is suitable for malodorous gas treatment | ||
Trichoderma asperellum | Degradation of nitrogen oxides (NOx), which has a certain nitrification in the denitrification tower, can oxidize nitrite (NO2−) to nitrate (NO3−) | ||
Actinobacteria | 1. Secrete antibiotics, inhibit the growth of harmful bacteria in the system, and maintain the health of the microbial community. 2. Produce extracellular enzymes to help decompose some complex organic matter that is difficult to degrade. 3 Produce soil odor; the metabolism of the ‘soil’ itself can cover up or neutralize some stench. |
Variable Category | Specific Parameters | Influence and Explanation |
---|---|---|
Operating parameters | Empty bed residence time (EBRT) | The average time that the exhaust gas stays in the packed bed. It is one of the most critical design parameters. High concentration and refractory waste gas requires longer EBRT (usually 30–100 s), otherwise it can be shortened (as low as 10–20 s). |
Temperature | Directly affects the microbial metabolic rate. The optimum temperature of mesophilic microorganisms is 25–40 °C. High temperature (>45 °C) will make the enzyme denature; too low (<10 °C) and it will greatly reduce activity. | |
pH value | Different microorganisms have their optimum pH range. Bacteria are usually 6.5–8.5, and fungi are 4–7. The treatment of sulfur-containing waste gas will produce sulfuric acid, and the treatment of nitrogen-containing waste gas will produce nitric acid. It is necessary to add buffers (such as limestone, NaOH) or nutrient solution to stabilize the pH. | |
Humidity | The filler humidity should be maintained at 40–60% (weight ratio). Too low humidity will lead to microbial inactivation and the biofilm drying; too high and it will block the pores of the filler, form an anaerobic zone, and increase the pressure drop. | |
Waste gas characteristics | Pollutant concentration and load | If the concentration is too low, the microorganism will be ‘starved to death’; too high of a concentration may lead to matrix inhibition (microbial poisoning) or too fast acid production, resulting in system pH collapse. Excessive load fluctuation will impact the stability of the system. |
Biodegradability of pollutants | Alkanes, alcohols, and phenols are easy to degrade. Aromatic hydrocarbons (benzene, xylene) and halogenated hydrocarbons (trichloroethylene) are difficult to degrade, requiring specific strains or longer acclimation time. | |
Complexity of exhaust gas composition | When multiple pollutants coexist, there is a synergistic promotion or competitive inhibition effect. Compound microbial agents are needed to cope. | |
Microorganism-related | Nutrient supply (N, P, K) | It is necessary to provide balanced nutrition (such as BOD:N:P ≈ 100:5:1) for microorganisms to grow and maintain activity. Insufficient nutrition will limit growth, and excessive nutrition may cause bacteria to over reproduce and block the system. |
Oxygen (O2) | The aerobic process requires sufficient oxygen (usually O2 > 5%). For high concentration organic waste gas, it may be necessary to supplement the air. |
Enzyme Classification and Name | Target Pollutants | Catalytic Reaction (Simplified) | Functional Background and Importance | Representative Microorganisms |
---|---|---|---|---|
Methane Monooxygenase, MMO | CH4 | CH4 + O2 + NADH → CH3OH + H2O + NAD+ | It is the starting enzyme and key enzyme of methane metabolism, which can activate the inert C-H bond at room temperature and pressure, and oxidize methane to methanol. This is the first step in methane as a carbon and energy source. | Methylococcus Methylosinus |
Toluene/Benzene Dioxygenase, TDO/BDO | Benzene, Toluene, Xylene | C6H6 + O2 + NADH → C6H6O2 + NAD+ | Starting the degradation process of the aromatic ring, catalyzing the addition of oxygen molecules to the benzene ring, and opening its stable conjugated structure is the rate-limiting step for the degradation of refractory VOCs such as BTEX [19]. Under aerobic conditions, microorganisms hydroxylate the benzene ring through monooxygenase and dioxygenase, gradually decompose it into intermediate products such as catechol, and finally completely mineralize into CO2 and H2O through the tricarboxylic acid cycle (TCA) [20]; for complex VOCs (such as polycyclic aromatic hydrocarbons) that are difficult to metabolize directly, the flora can use a simple carbon source (such as glucose) as an energy source through a co-metabolism mechanism, while secreting enzymes to decompose the target pollutant [21]. | Pseudomonas putida Ralstonia pickettii |
Ammonia Monooxygenase, AMO | NH3 | NH3 + O2 + 2H+ + 2e− → NH2OH + H2O | Oxidation of ammonia to hydroxylamine is the first step of nitrification and the starting point for the conversion of inorganic nitrogen pollutants. This enzyme is not specific to the substrate and may oxidize other substances. | Nitrosomonas |
Nitrite Oxidoreductase, NOR | NO2− | NO2− + H2O → NO3− + 2H+ + 2e− | Nitrite is responsible for the oxidation of nitrite to nitrate, which is the second step of nitrification, converting toxic nitrite to less toxic nitrate. | Nitrobacter |
Sulfite/Sulfate Reductase | SO42−/SO32− | SO42− + ATP + 8e− → SO32− → S2− | Under anaerobic conditions, it participates in the sulfate reduction process and finally reduces sulfate/sulfite to hydrogen sulfide (H2S) [22]. Note: This process is odorous and usually needs to be avoided. | Desulfovibrio [23] |
Phosphotriesterase | organic phosphorus compound | (RO)3P=O + H2O → (RO)2P=O + ROH | The P-O-C or P-F bond in organophosphorus compounds is specifically hydrolyzed. It is a key enzyme for the degradation of phosphorus-containing poisons and can be used to treat the exhaust gas of phosphorus-containing pesticides. | Pseudomonas diminuta Flavobacterium spp. |
Laccase | Phenols, Aromatic amines | Phenol + O2 → Quinone + H2O | A copper-containing polyphenol oxidase that uses molecular oxygen to oxidize a variety of phenolic and aromatic amine contaminants to produce water and unstable quinone intermediates, which are further polymerized or degraded. | Trametes versicolor Aspergillus |
Peroxidase | A variety of refractory VOCs | Substrate + H2O2 → Oxidation product + 2H2O | Relying on hydrogen peroxide (H2O2) as a co-substrate, it can oxidize and decompose refractory pollutants with complex structures such as polycyclic aromatic hydrocarbons (PAHs) and chlorinated aromatic hydrocarbons and has a strong oxidizing ability. | Phanerochaete chrysosporium |
GSH-dependent Formaldehyde Dehydrogenase, FDH Formate Dehydrogenase, FDH | Formaldehyde | HCHO + GSH + NAD+ → S-(Hydroxymethyl)GSH → S-Formyl GSH + NADH + H+ HCOOH + NAD+ → CO2 + NADH + H+ | This is the core promoter of formaldehyde degradation in eukaryotes (such as fungi) and some bacteria. Firstly, formaldehyde is spontaneously combined with intracellular antioxidant glutathione (GSH) to generate hydroxymethyl glutathione, which is then oxidized by the enzyme. Subsequently, it is converted into formic acid by intracellular formaldehyde dehydrogenase, which is further decomposed into CO2 and H2O by formate dehydrogenase to achieve complete non-toxicity [24]. The intracellular metabolic rate of high-efficiency formaldehyde-degrading bacteria can reach 0.5–2.0 mmol/(g·h), which is significantly better than the saturation capacity limit of physical adsorption materials [25]. | Candida spp. Pseudomonas putida |
Toxic and Harmful Gas | Reaction Chemical Equation |
---|---|
Hydrogen sulfide (SH2) | R1-COOH → R1-COO− + H+ |
SH2 + H+ → SH3+ (Thiosulfonium) | |
R1-COO− + SH3+ → R1-COOSH3 (Sulfonium salt) | |
Ammonia (NH3) | R2-COOH → R2-COO− + H+ |
NH3 + H+ → NH4+ (Nitrinium) | |
R2-COO− + NH4+ → R2-COONH4 (Ammonium salt) | |
Phosphine (PH3) | R3-COOH → R3-COO− + H+ |
PH3 + H+ → PH4+ (Phosphonium) | |
R3-COO− + PH4+ → R3-COOPH4 (Phosphonium salt) | |
Formaldehyde (HCHO) | R4-COOH → R4-COO− + H+ |
HCHO + H+ → HCHOH+ (Carbonium) | |
R4-COO− + HCHOH+ → R4-COOHCHOH (Carbonium salt) | |
Methane (CH4) | R5-COOH → R5-COO− + H+ |
CH4 + H+ → CH5+ (Carbonium) | |
R5-COO− + CH5+ → R5-COOCH5 (Carbonium salt) |
Influencing Factors | Influence on the Principle of Microbial Metabolism | Best Range and Examples | Consequences of Improper Control |
---|---|---|---|
pH value | 1. Enzyme activity: Most enzymes can only maintain their three-dimensional structure and active center in a specific pH range. Deviation from the optimum pH will denature and inactivate it. 2. Membrane permeability: Affecting cell membrane charge and permeability, thereby affecting nutrient absorption and waste discharge. 3. Substrate availability: Affecting the ionization state of certain pollutants (such as H2S, NH3), thereby affecting the ease of their use by microorganisms [29]. | Bacteria: near neutral (6.5–8.0) Fungi: Acidic (4.0–7.0) [30] Nitrifying bacteria: 7.5–8.5 Sulfur-oxidizing bacteria: 1.0–3.0 (extreme acidophilic) | Peracid/peralkali: Enzyme activity decreased sharply; cell membrane damage; the microbial community structure is unbalanced and the function collapses. For example, the treatment of sulfur-containing waste gas to produce sulfuric acid; if not buffered, the system pH plummets, inhibiting the vast majority of microorganisms. |
Temperature | 1. Reaction rate: For every 10 °C increase in temperature, the enzymatic reaction rate increases by about 1–2 times (Q10 law). 2. Enzyme and membrane stability: Too high temperature will cause enzyme denaturation, membrane lipid excessive flow, and disintegration; if the temperature is too low, enzyme activity will be extremely low, membrane fluidity will be poor, and metabolism will be stagnant [31]. 3. Gas phase mass transfer: It affects the solubility and diffusion rate of pollutants in gas–liquid biofilm. | Mesophilic microorganisms: 25–40 °C Thermophilic microorganisms: 50–60 °C (suitable for high temperature waste gas) Ambient temperature: usually refers to 15–30 °C | Too high: Rapid microbial inactivation, system collapse [32]. Too low: Slow metabolism, low processing efficiency, difficult to start. Excessive fluctuation: Impacts the microbial community and selects strains with poor adaptability. |
Oxygen concentration | Microorganisms need to breathe to produce energy (ATP) when degrading pollutants (as a carbon source and energy). This process requires a final electron acceptor to receive electrons produced in biochemical reactions. Oxygen (O2) is the final electron acceptor with the highest energy production efficiency. | At high concentrations, aerobic respiration is performed to degrade most VOCs (benzene, toluene, phenol, etc.) [33] and inorganic substances (H2S, NH3). Common flora such as Pseudomonas and Bacillus. | The oxygen concentration is generally required to be no less than 5–10% to ensure the smooth progress of aerobic metabolism. For high concentration organic waste gas, it is necessary to supplement air or oxygen to prevent a decrease in treatment efficiency and the generation of odorous by-products due to hypoxia. |
Carbon nitrogen phosphorus ratio (C:N:P) | 1. Cell synthesis: Microbial synthesis of their own cytoplasm needs to follow a certain nutritional ratio. Nutrient imbalance limits microbial growth. 2. Enzyme synthesis: C, N, and P are the basic elements of key metabolites such as synthetase, ATP, and NADH [34]. | Classical ratio: BOD:N:P = 100:5:1 (When treating inorganic waste gas such as H2S, an additional carbon source is needed) [35]. | C high and N/P low: Malnutrition, poor growth of zoogloea, treatment efficiency decreased. High N/P and low C: Overgrowth of microorganisms may lead to sludge bulking or excessive biofilm thickness, resulting in blockage. |
cofactor | 1. Enzyme function core: Many enzymes (especially the key enzymes for degradation of special pollutants) require cofactors to perform catalytic functions. 2. Energy metabolism: Coenzymes (such as NAD+, FAD) are involved in electron transfer and energy (ATP) production. | Trace elements: Fe, Mo, Mg, Co, Ni, Cu, etc. (are part of many coenzymes) [36] Vitamins: Such as B vitamins, as coenzyme precursors [37]. | Deficiency: Key metabolic pathways are disrupted, and pollutants cannot be degraded even in the presence of bacteria. This is a common but easily overlooked reason for poor system performance. |
Substrate inhibition | High concentration substrates (pollutants) may cause the following: 1. Toxic effects: Direct destruction of cell membranes, enzyme saturation inactivation, or interference with central metabolism. 2. Osmotic stress: High concentrations of organic matter lead to a decrease in water activity and cause cell dehydration. | It varies with microorganisms and pollutants. For example, VOC concentrations >5–10 g/m3 may inhibit many bacteria. | Performance: When the inlet concentration suddenly increases (impact load), the treatment efficiency does not rise but falls, or even drops, to zero. Microorganisms need a long recovery time. |
Product inhibition | Accumulation of metabolites may cause the following: 1. Feedback inhibition: Terminal products inhibit the activity of key enzymes at the front end of the metabolic pathway. 2. Change the pH of the environment: Such as degradation of chlorine, sulfur, and nitrogen waste gas to produce HCl, H2SO2, and HNO3, resulting in system acidification. | For example, the accumulation of H2S produced by sulfate-reducing bacteria inhibits its own activity. | Performance: The initial effect of the system is good, but with the operation, the efficiency continues to decline. It is often accompanied by dramatic changes in pH. |
Name of Bacteria | Convertible Gas Name | Transformation Mechanism | Biotransformation Products | Reaction Conditions | Ref |
---|---|---|---|---|---|
Acidithiobacillus thiooxidans | H2S | Under aerobic conditions, H2S is gradually oxidized by sulfur oxidase system, and the electron transfer chain drives energy metabolism to produce sulfuric acid or elemental sulfur. | S0, SO42− | The optimum temperature is 28–30 °C; the optimum pH is 1.0–3.5; chemoautotrophic bacteria; aerobic metabolism. | [38] |
Vibrio natriegens | BTEX, PAHs | Synthetic biology modified chassis bacteria, integrated 5 degradation gene clusters, expressed benzene ring lyase, oxygenase, etc., and directly mineralized aromatic hydrocarbons into small molecules. | CO2, H2O | The optimum temperature is 30–37 °C; the optimum pH is 7.0–8.5; aerobic metabolism. | [39] |
Bacillus amyloliquefaciens T-5 | VOCs | It secretes antibacterial VOCs (such as aldehydes and ketones), destroys the virulence genes of R. solanacearum, and weakens its biofilm formation ability. | Non-toxic small molecule metabolites | The optimum temperature is 30–37 °C; the optimum pH is 6.5–7.5; the optimum C/N ratio is 20:1; aerobic metabolism. | [40] |
Pseudomonas | VOCs | Mineralization of n-butyl acetate and other pollutants with VOCs as a carbon source. | O2, H2O | The optimum temperature is 20–30 °C; the optimum pH is 6.5–7.5; the optimum C/N ratio is 5:1; aerobic metabolism. | [41] |
Alcaligenes faecalis UA | H2SO4 | Secretes acid-resistant urease, decomposes urea to produce alkali and neutralize acidic wastewater, and precipitates heavy metal ions. | Carbonate, heavy metal precipitates | The optimum temperature is 30–37 °C; the optimum pH is 7.0–8.0; aerobic metabolism. | [42] |
Bacillus subtilis yb-1 | NH3, H2S | Reduce pH to reduce odor production. | Short-chain fatty acid | The optimum temperature is 30–37 °C; the optimum pH is 6.5–7.5; the optimum C/N ratio is 25:1; aerobic metabolism. | [43] |
Acinetobacter pittii | H2S | H2S can be converted to SO42−. | SO42− | The optimum temperature was 30–35 °C; the optimum pH was 6.5–7.5; the optimum C/N ratio was 5:1; and strict aerobic metabolism was carried out. | [44] |
Microbial Name | Key Genetic Characteristics |
---|---|
Acidithiobacillus thiooxidans | 1. Chemoautotrophic-related gene cluster: There is a complete Calvin–Benson–Bassham cycle gene for fixing CO2 as a carbon source. 2. Sulfur oxidation gene cluster: There is the sox gene cluster (soxXYZABCD), doxDA, etc., encoding the key enzyme system that oxidizes reducing sulfide (H2S, S0) to sulfuric acid (H2SO4). 3. Extreme acid resistance mechanism: The genome contains a strong proton pump system, cell membrane, and enzyme adapted to an extremely low pH environment, allowing it to survive in high acidity. |
Vibrio natriegens | 1. Natural high-speed metabolic gene background: It has a very high number of ribosomal RNA operons, supporting its ultra-fast protein synthesis and growth rate. 2. Integration of exogenous degradation pathways: Through plasmid or genome integration, the degradation gene clusters of specific VOCs (such as benzene series) (such as tod or tom operons from Pseudomonas) were introduced. 3. Artificial optimization elements: The introduced genes are usually controlled by strong promoters to maximize expression; it may also contain resistance markers and stability elements. |
Bacillus amyloliquefaciens T-5 | 1. Antibacterial substance synthesis gene cluster: It has a non-ribosomal synthase (NRPS) gene cluster that encodes the synthesis of antimicrobial lipopeptides (such as surfactin, iturin, and fengycin). 2. Substrate degradation related genes: Genes encoding extracellular enzymes (such as proteases, amylases, and possibly specific oxygenases) that degrade complex organic matter. 3. Spore-forming gene: It has a complete spo gene cluster, which enables it to form spores with strong resistance. |
Pseudomonas spp. | 1. A large library of degradation plasmids: Usually carrying a variety of mobile genetic elements (such as plasmids, transposons), which carry a variety of degradation operons (such as tod for toluene, alk for alkanes, nah for naphthalene). The regulatory network is complex: There are complex regulatory genes (such as xyIR, todS/todT) that can sense the presence of substrates and fine-tune the expression of degradation genes. 3. Environmental adaptation genes: It has genes encoding a variety of efflux pumps and membrane proteins to help it resist organic solvents and heavy metal stress. |
Alcaligenes faecalis UA | 1. Denitrification-related genes: The amoCAB gene cluster, which is used to oxidize ammonia (NH3) to hydroxylamine, and the nitrite oxidoreductase (nxr) gene, which was used to oxidize nitrite (NO2−) to nitrate (NO3−). 2. Aerobic/facultative anaerobic metabolism: Some strains have nitrate reductase (nar) gene, which can be denitrified under anoxic conditions. |
Bacillus subtilis yb-1 | 1. Spore-forming genes: Having a complete spo gene cluster is the basis of its stress resistance. 2. Antibacterial peptide synthesis genes: Usually have genes encoding a variety of antimicrobial peptides (such as subtilin). 3. Substrate degradation genes: There are abundant genes encoding extracellular hydrolases. |
Acinetobacter pittii | 1. Alkane hydroxylase gene: alkB gene encodes a key enzyme that hydroxylates the end of alkane, which is the first step in the degradation of long-chain alkane. 2. Biofilm formation related genes: It has genes encoding pilus, extracellular polysaccharides, etc., so that it can strongly adhere to form biofilms. 3. Drug resistance gene island: The mobile drug resistance gene island is often integrated into the genome, which is the source of its hospital infection ability but has little effect on waste gas treatment. |
Industry Category | Main Exhaust Gas Components | Evaluated Microbial Treatment Technologies | Core Functional Microorganisms | Technical Advantages and Precautions |
---|---|---|---|---|
Petrochemical industry | Benzene, toluene, xylene (BTEX), and other volatile organic compounds (VOCs). | Biotrickling filter, biofilter | Pseudomonas, Bacillus | It has good removal effect on a variety of VOCs; attention should be paid to the possible impact of fluctuations in exhaust gas concentration. |
Printing, spraying | VOCs such as ketones (such as acetone), esters, benzene series, etc. | Biotrickling filter, biological scrubber | Nocardia, Mycobacterium | It is suitable for low-concentration and high-air-volume exhaust gas; the treatment effect of VOCs with poor water solubility may be limited, and composite microbial agents or pretreatment can be used. |
Food processing, fermentation | Ethanol, organic acids (such as acetic acid), aldehydes, odorous gases | Biofilter | Yeast (such as Candida), lactic acid bacteria, compound microbial agents | The operation cost is low; however, the exhaust gas may contain fungicides or high concentrations of salt, which requires screening of tolerant strains and control of environmental conditions (such as pH, humidity). |
Pharmaceutical industry | Solvent VOCs (such as dichloromethane), sulfur-containing or nitrogen-containing organic matter, fermentation tail gas | Biotrickling filter (domesticated strains for specific compounds), composite biological treatment (combined with other technologies) | Specific domesticated degrading bacteria (such as some Pseudomonas) and fungi (such as Aspergillus) | Exhaust gas may contain biological inhibitory substances or antibiotics, which are highly toxic to microorganisms and require long-term domestication or physicochemical pretreatment. |
Leather, papermaking | Hydrogen sulfide (H2S), mercaptan, total reduced sulfur (TRS), formaldehyde | Biotrickling filter, biofilter | Sulfur-oxidizing bacteria (such as Thiobacillus), formaldehyde-degrading bacteria (such as Hyphomicrobium) | The waste gas contains odorous substances with strong hydrophobicity (such as thiols), and the mass transfer efficiency is the key. Segmented treatment or surfactant addition can be used to promote microbial absorption. |
Industry Category | Main Exhaust Gas Components | Evaluated Microbial Treatment Technologies | Core Functional Microorganisms | Technical Advantages and Precautions |
---|---|---|---|---|
Livestock and poultry breeding, composting | Malodorous gases such as ammonia (NH3), hydrogen sulfide (H2S), volatile organic acids, phenols, etc. | Biological filter (commonly used organic filler) | Nitrifying bacteria, sulfur-oxidizing bacteria, actinomycetes | The investment operation cost is relatively low; the composition of exhaust gas is complex, and the concentration fluctuates greatly. It has high requirements for the compound degradation ability of microorganisms, and it is necessary to ensure sufficient residence time. |
Industry Category | Main Exhaust Gas Components | Evaluated Microbial Treatment Technologies | Core Functional Microorganisms | Technical Advantages and Precautions |
---|---|---|---|---|
Sewage treatment, waste treatment | Malodorous gases such as hydrogen sulfide (H2S), ammonia (NH3), and thiols. | Biological filter (commonly used organic filler) | Acidithiobacillus thiooxidans, Nitrifying bacteria/denitrifying bacteria | The removal efficiency of inorganic odors such as H2S and NH3 is high (often ≥98%). Acidic substances may be produced during the treatment process, and attention should be paid to pH control and filler maintenance. |
Pollutant Type | Process Conditions (Temperature, pH, Residence Time, etc.) | Reactor/Technology Type | Removal Rate | Core Microorganisms (If Specified) |
---|---|---|---|---|
VOCs mixed gas (alcohol, phenol, aldehyde, ketone, etc.) | pH: 6.5–7.5 Temperature: 25–28 °C DO: ≥0.3 mg/L Contact time: 15–20 s | Two-stage biological contact purification tower (including specific filler) | H2S: close 100% (160 → 0.1 mg/m3) NH3: ~73% (6 → 1.6 mg/m3) VOCs: ~98% (1200 → 22) | Pseudomonas, Bacillus, Arthrobacter, and other dominant flora |
H2S, NH3, mercaptan and other odorous gases | pH: 6–7 Temperature: 26–34 °C | Biofilter, biotrickling filter, and a variety of combined processes (such as biotrickling filter–chemical absorption, –activated-carbon adsorption, –photocatalysis) | Odorous substances: >95% TVOCs: >90% | Composite functional flora screened for representative pollutants |
The stench of stale landfill waste (H2S, NH3, CH4, VOCs) | Comprehensive application of a technology system (direct injection of pile body, fog gun, drone spraying, biological filter) | MPI environmental control probiotic integrated control technology system (not a single reactor) | CH4: 92.7% H2S: 100% Odor concentration: 62.85–88.24% NH3: 89.37% (7.9 → 0.84 mg/m3) | MPI environmental control probiotics (compound microbial agent) |
Antibiotic production tail gas (Complex VOCs, odor, dust, high temperature, and high humidity) | A large-scale integrated system with an investment of more than 1.6 billion yuan (87 washing towers, 13 molecular sieve units, 11 combustion units, etc.) | Integrated process of ‘negative pressure collection + pretreatment + molecular sieve adsorption concentration + high temperature oxidation combustion’ technology | VOCs and stench: ≥95% | Domesticated microbial communities |
Organic waste gas | pH: 6–7 Temperature: 30 ± 4 °C (26–34 °C) | Airlift packed bioreactor | Effectively degraded | Domesticated microbial communities |
Cost Item | Specific Content | Cost Range (Ten Thousand Yuan) | Proportion |
---|---|---|---|
Reactor equipment | Biofilter/trickling filter main body, air distribution/spray system | 80–150 | 50–60% |
Carrier material | Volcanic rock/activate-carbon/modified straw | 20–50 | 15–20% |
Monitoring and control system | pH meter, temperature sensor, fan, frequency converter | 15–30 | 10–15% |
Fungi culture and domestication equipment | Laboratory shake flask, seed tank (on demand) | 5–15 | 5–10% |
Installation and debugging | Pipeline connection, system test run | 10–20 | 5–10% |
Cost Item | Calculation Basis | Cost Range (Yuan/m3 Waste Gas) | Proportion |
---|---|---|---|
Fungi and nutrition supplement | Monthly supplementation (100–200 yuan/kg agent), nutrients. | 0.1–0.3 | 10–15% |
Energy consumption | Fan (0.5–1.0 kW·h/m3), spray pump (0.2–0.5 kW·h/m3), heating (on demand) | 0.3–0.8 | 40–50% |
Manual maintenance | 1–2 people/class (monitoring parameters, cleaning carrier) | 0.1–0.2 | 10–15% |
Carrier replacement | Replaced every 1–3 years (based on 1/3 of carrier cost) | 0.05–0.15 | 5–10% |
Wastewater/waste treatment | Regular discharge of spray liquid (to be treated to meet the standard) | 0.1–0.3 | 15–20% |
Factors | Description and Optimization Direction |
---|---|
Exhaust gas complexity | The cost of single pollutant (such as toluene) is low (0.5–1.0 CNY/m3). Mixed pollutants (such as VOCs + H2S + NH3) require a variety of bacteria, and the cost increases by 20–30%. |
Processing scale | When the scale is greater than 50,000 m3/h, the unit cost can be reduced by 15–25% (scale effect). |
Carrier reusability | Degradable carriers such as modified straw need to be replaced frequently, while ceramic carriers can be reused for 3–5 years, with lower long-term costs. |
Parameter control accuracy | Automatic control systems (such as AI regulating pH and temperature) can reduce energy consumption and bacterial waste and reduce operating costs by 10–15%. |
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Song, Y.; Cai, R.; Wei, C.; Xu, H.; Liu, X. Multi-Perspective: Research Progress of Probiotics on Waste Gas Treatment and Conversion. Sustainability 2025, 17, 8642. https://doi.org/10.3390/su17198642
Song Y, Cai R, Wei C, Xu H, Liu X. Multi-Perspective: Research Progress of Probiotics on Waste Gas Treatment and Conversion. Sustainability. 2025; 17(19):8642. https://doi.org/10.3390/su17198642
Chicago/Turabian StyleSong, Yingte, Ruitao Cai, Chuyang Wei, Huilian Xu, and Xiaoyong Liu. 2025. "Multi-Perspective: Research Progress of Probiotics on Waste Gas Treatment and Conversion" Sustainability 17, no. 19: 8642. https://doi.org/10.3390/su17198642
APA StyleSong, Y., Cai, R., Wei, C., Xu, H., & Liu, X. (2025). Multi-Perspective: Research Progress of Probiotics on Waste Gas Treatment and Conversion. Sustainability, 17(19), 8642. https://doi.org/10.3390/su17198642