How Economic Theories Shape Chemical Technology Profile
Abstract
:1. Introduction
1.1. The Concept of Chemical Technologies Economics (CTE)
1.2. Chemical Industries and Economic Development
2. Chemical Technologies
3. Approaches in Chemical Technology Economics
3.1. Economic Concepts
3.1.1. Strategic Performance and Financial Controlling
Application of Game Theory in Chemical Technologies
Economic Theory | Chemical Technology | Uncertainty Analysis | Main Findings | Ref. |
---|---|---|---|---|
Game Theory | Several sludge valorization technologies were evaluated as alternative strategies, including incineration for electricity generation followed by landfill (S1), incineration for electricity generation followed by cement production (S2), biogas production from sludge digestion for electricity generation using fuel cells (S3), and biogas production from sludge digestion for electricity generation via combustion (S4). | Sensitivity Analysis | The results of the framework can enhance the sustainable decision-making process for the parties involved and facilitate more efficient agreements. | [58] |
Nash non-cooperative game theory | Wastewater discharge reduction technology | - | Developing a WPDP system requires effective management of total wastewater discharge and improved supervision of water pollution sources. Allocating wastewater discharge permits involves negotiating with stakeholders to align their interests. These negotiations among provinces can be viewed as examples of non-cooperative game behavior driven by self-interest. | [59] |
Application of Activity-Based Costing in Chemical Technologies
3.1.2. Sustainability Performance Metrics
Application of Techno-Economic Assessment, Life Cycle Assessment, and Life Cycle Cost and Cost–Benefit Analysis in Chemical Technologies
Nanomaterial Used | Chemical Technology | Economic Theory | Goal of the Study | Main Findings (Environmental and Economic Benefits) | Ref. |
---|---|---|---|---|---|
Aluminum hydroxide/oxide nanoparticles (AHNP) | Adsorption, electrocoagulation | LCA | Eco-environmental assessment Economically, the combined material and energy costs of the adsorption process were found to be nearly seven times higher than those of the electrocoagulation process. | The environmental impacts of both methods were analyzed. The results revealed that the dissolution of the aluminum electrode and electricity usage in the electrocoagulation process are major contributors to environmental impacts. The adsorption process (GWP 35.2 kg CO2 eq.) exhibits nearly eight times greater environmental impact compared to electrocoagulation (GWP 4.5 kg CO2 eq.), due to the higher adsorption capacity of in situ generated coagulant compared to pre-precipitated adsorbents. | [78] |
ZnCl2 | Adsorption, electrocoagulation | LCA | Environmental and economic impacts. The cost analysis concludes that electrocoagulation is more economically efficient than adsorption | This study conducts a life cycle assessment of both processes. The results reveal that the adsorbent production stage in the adsorption system significantly affects the environment. Recycling coproducts and recovering energy during adsorbent production helps reduce the overall energy demand. In contrast, the electrocoagulation process requires considerably less energy and raw materials, resulting in eight times lower global warming potential. Scenario analysis shows that using electricity from natural gas minimizes environmental impacts, compared to other energy sources. Sensitivity analysis, with a ±20% variation in process parameters, was also conducted. | [79] |
Nanoscale zero-valent iron (nZVI) | Iron milling, liquid chemical reduction with sodium borohydride, and chemical reduction with hydrogen gas. | LCA, LCC | The impacts of synthesizing nano-iron for remediation of contaminated sites | The LCC analysis compared the costs of different methods for synthesizing nano-iron. It found that the milling method required less funds compared to the hydrogen gas reduction method. This cost difference is due to the higher energy consumption linked with hydrogen gas reduction. | [70] |
NH2-functionalized magnetic graphene oxide | Hydrothermal method. Modified by 1st and 2nd grafting PAMAM type dendrimer. | LCA- LCC analysis, NPV, IRR | Eco-environmental assessment. | The price of mGO-NH2 was approximately USD 143.7 per kilogram, achieving an NPV of USD 21,064.8 per kilogram of mercury removed over a twenty-year lifespan. The project proved economically viable with a 64% internal rate of return (IRR) and required a capital investment of USD 742.31 per kilogram of mercury removed. This study highlights the environmental implications of mGO-NH2, paving the way for potential industrial-scale process modifications. | [80] |
MgO Nanoparticles | Sol–Gel | Gross Profit Margin, Internal Rate Return, Break Even Point, Payback Period, and Cumulative Net Present Value | Economic Feasibility of magnesium oxide (MgO) nanoparticles using the sol–gel method | The Payback Period analysis reveals that profitability is achieved after a period exceeding three years. From an economic standpoint, it is evident that this project holds significant potential, despite potential losses resulting from deviations from optimal conditions. These study findings are anticipated to provide a framework for the development of economically efficient and commercially viable MgO nanoparticle production projects. | [77] |
Fe-Cu nanoparticle | Coagulation and adsorption | Capital expenditures (CAPEX) and operating expenses (OPEX) | To evaluate the viability and effectiveness of the pilot prototype system using Fe-Cu nanoparticles | The overall cost of treatment (incorporating annual capital expenditures and operational expenditures) per cubic meter in the suggested system was USD 4.5, aimed at reusing treated textile wastewater for irrigating forest trees. This research demonstrates that the innovative multistage treatment approach (beginning with coagulation followed by adsorption using Fe/Cu nanoparticles) effectively addresses real textile wastewater at a competitive cost. | [75] |
MoS2 nanoparticles | solvothermal method | The life cycle assessment (LCA) was conducted using a combination of Aspen Plus and LCIA IMPACT 2002+ from cradle-to-gate, with a functional unit defined as 1 kg of MoS2 ENM. | To evaluate the environmental and health impacts of scaling up the production of MoS2 NPs | The study proposes replacing LiOH with NaOH (sodium hydroxide) to alleviate resource scarcity and reduce associated environmental impacts during processing. This substitution has the potential to decrease estimated impacts by up to 56%. The findings provide valuable guidance for scientific committees and stakeholders, aiding informed decisions in selecting and developing nanomaterial production processes, specifically for MoS2. | [81] |
- | Coagulants derived from chemicals (alum) and bio-sources (neem leaves) | CBA | To assess the efficacy of chemical-based and bio-based coagulants in treating real aquaculture wastewater. | Neither scenario proves economically viable for generating profit, whereas employing neem coagulant provides benefits for water reuse and sludge utilization. | [82] |
- | Membrane bioreactor (MBR) technology | CBA | The study evaluated the cost-effectiveness, environmental benefits, net earnings, and effectiveness of MBRs using economic methodologies such as cost analysis, CBA, and data envelopment analysis (DEA) with non-radial directional distance function (NDDF). Data from 35 large-scale MBR installations were analyzed to assess investment and operational aspects. | The economic feasibility of 35 large-scale MBR plants, each with a capacity of more than 10 k m3/d, was assessed using techno-economic methods. CBA, which included shadow pricing of environmental benefits, indicated that the MBRs yielded positive net profits, averaging approximately USD 4.9/m3. This analysis affirmed the feasibility of Membrane bioreactor (MBR) technology from a techno-economic standpoint. | [83] |
- | Moving bed biofilm reactor (MBBR) | CBA | An evaluation of the feasibility of improving wastewater treatment systems in an area of North Macedonia. | According to their economic analysis, they concluded that it is justified to invest in the WWTP project. | [10] |
3.1.3. Sustainability at a Macro Level
Sustainable, Green, Circular, and Low Carbon Chemistry
- Green Chemistry and Atom Economy
- Atom Economy
Economic Theory | Chemical Technology | Main Findings | References |
---|---|---|---|
Atom economy | Synthesis | AQ reagent-free, 100% atom-economic, scalable, and sustainable synthetic method for the highly regio- and stereoselective iodosulfenylation of alkynes. This method utilizes only iodine and disulfides to produce important classes of stereodefined alkenes, such as (E)-β-iodoalkenyl sulfides, with moderate to excellent yields of up to 96%. | [94] |
Atom economy | Synthesis | Dichloromeldrum’s acid is introduced as a bench-stable, non-volatile reagent for the dichloroacetylation of anilines and alkyl amines, yielding α,α-dichloroacetamides, which are key motifs in medicinal chemistry. The products are obtained in good to excellent yields using reagent-grade solvents, and since the only byproducts are acetone and CO2, no column chromatography is necessary. This reagent offers a practical, efficient, and environmentally friendly approach for the dichloroacetylation of primary amines. | [92] |
- Sustainable Chemistry
- Circular Chemistry and Circular Economy
- Low-Carbon Chemistry
4. Challenges and Future Perspectives
5. Conclusions
Author Contributions
Funding
Data Availability Statement
Conflicts of Interest
References
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Category | Environmental Chemical Technology | Environmental Chemical Technologies Considerations | Economic Considerations |
---|---|---|---|
Physical Methods | Adsorption | Non-destructive process. Use of a solid material [7]. An effective method with significant potential for recovering, reusing, and recycling adsorbent materials [32]. Challenges related to adsorbent disposal and regeneration [33]. | A low-cost technology [34,35]. While regeneration is cost-effective, the regenerating process can be expensive [36]. |
Membranes | Membrane technology generates stable water with less sludge and requires no chemicals for separating solid wastes from wastewater. However, it is energy-intensive [36]. | Operation and maintenance costs are high [36]. | |
Coagulation/Flocculation | Coagulation and flocculation are low-energy processes but managing the volume of sludge (large flocs) they produce can be challenging [36]. | Coagulation and flocculation are advantageous due to their low capital costs [7]. | |
Chemical Methods | Fenton | Fenton processes utilize less hazardous substances, simpler equipment, and recycle reactants with significant environmental impact [37]. The low energy requirement for activating Fenton’s reagent makes it more advantageous compared to many physicochemical solutions [38]. | The Fenton process is recognized as a cost-efficient choice [39]. |
Precipitation | Chemical precipitation transforms dissolved metal ions into solid particles, aiding their sedimentation [40]. | Chemical precipitation is an economically viable method [7]. Hydroxide precipitation was adopted for its cost-effectiveness, simplicity, and ability to adjust pH [40]. | |
Ozonation | No chemicals are required [7]. Ozone-based processes produce strong oxidants but can result in stable byproducts, such as formaldehyde. Challenges include ozone’s limited solubility in water, affecting mass transfer at gas–liquid interfaces, and its tendency to self-decompose [37,41]. | The ozonation process has high operational costs [31]. | |
Biological Methods | Aerobic-Anaerobic | Anaerobic treatment can manage high organic loads, produce limited amounts of stable sludge, and generate methane as an end-product [42], although it requires time to complete [43]. | The process is notable for its low costs [44]. Aerobic digestion (AD) is Aerobic digestion (AD) is regarded as a cost-effective solution while minimizing environmental impact [45]. |
Activated sludge | The activated sludge process, a suspended growth biological treatment method, is known for its high flexibility, it can be adapted to treat wastewaters with diverse compositions [46]. | It is the most cost-effective method and is capable of producing high-quality effluent that meets increasingly stringent standards [47]. | |
Constructed wetlands | Constructed wetlands (CW) have been used as a waste management option since the 1950s [48]. They function by saturating the substrate, creating oxygen-poor conditions that limit vegetation to species adapted to low-oxygen environments [49]. They are efficient in reducing a wide range of waterborne pollutants [48]. A key challenge lies in understanding the complex relationships between pollutant extraction rates and factors like temperature, influent loads, and species [50]. | Affordable and efficient wastewater treatment technology [51]. |
Economic Theory | Chemical Technology | Main Findings | References |
---|---|---|---|
Activity-based costing (ABC) | Membranes | The Total Cost of Ownership (TCO) approach is an activity-based process that relies heavily on Activity-Based Costing (ABC) principles to document and evaluate costs. This study used the ABC methodology due to its suitability for managing laboratory activities. The model was applied to both the synthesis and physicochemical characterization processes. The quantitative analysis showed that the key cost drivers for synthesis were accident-related and energy expenses, while energy costs were the most significant factor in the physicochemical characterization process. | [64] |
Economic Theory | Chemical Technology | Main Findings | References |
---|---|---|---|
Circular Economy | Coagulation, Flocculation, Adsorption | The industrial-scale initiative successfully implemented achieved significant water savings of 5 m3/h and fulfilled all the cooling tower’s water needs. The project anticipates recovering its initial investment within 16 months post-installation, accounting for regular monthly maintenance and replacing the activated carbon bed in the third year. The strategy of employing regenerated water as part of the circular economy approach could be readily applied to other food industry plants using peracetic acid for disinfection in their processes. | [105] |
Circular Economy | Adsorption AOP | A green biochar method was developed by integrating biochar production, adsorption, and regeneration within the framework of circular economy principles. Initially, the effects of operational conditions on the adsorption capacity of the produced biochar were analyzed. The optimal biosorbent was then characterized, and the adsorption process for both pollutants was optimized. The regeneration of spent biochar, a critical aspect in designing an effective treatment system, was studied using pollutant desorption and advanced oxidation processes. | [106] |
Circular Economy | Adsorption | The effectiveness of using demolition waste as an adsorbent for removing three metal cations (Copper, Nickel, and Zinc) from industrial effluents was evaluated, with copper showing the highest removal efficiency when all metals are present simultaneously. This type of waste shows potential as a low-cost material for industrial effluent treatment, aligning with circular economy principles. Once saturated with metals, the waste can be reused in construction. The study also demonstrated that the spent adsorbent could replace part of the sand used in mortar production, creating a new loop within the concrete life cycle. This incorporation reduces the need for new raw materials, enhancing the eco-efficiency of the process as a step towards a circular economy. | [107] |
Circular Economy | adsorption | Rice husk, modified using a circular economy approach with effluent from the alkaline scouring of cotton, was investigated for its ability to adsorb Congo Red dye. The study examined equilibrium, kinetics, thermodynamics, and the adsorption mechanism by varying the initial dye concentration, contact time, temperature, and adsorbent dosage. The results demonstrated the effectiveness of this method in producing an efficient adsorbent for direct dye removal. This approach highlights the feasibility of using the circular economy to create an effective adsorbent without consuming extra chemicals or energy, paving the way for a continuous process of rice husk modification and textile industry effluent purification. | [108] |
Circular Economy | Adsorption | This literature review highlights the potential of agricultural, fisheries, and timber industry biowaste as biosorbents for metal removal within the circular economy framework. These biowastes contain functional groups (such as carboxyl, hydroxyl, amide and amine) that effectively bind metals, offering an environmentally friendly and cost-effective alternative to conventional metal removal methods. While selecting the right biosorbent requires research, their high efficiency, low cost, and renewability make them promising solutions. | [109] |
Circular Economy | Adsorption | This study introduced torrefied coco-peat biochar, treated at 200 °C, as an effective adsorbent for norfloxacin (NFX) removal from water. The biochar had a high carbon content (36.45%), with significant levels of K2O (27.73%) and chlorine (7.49%). NFX desorption reached 89.19% efficiency using 80% ethanol, and 87.76% of the drug was recovered as crude crystals. NFX removal was highly efficient across various water types, including tap, seawater, and river water. A techno-economic analysis revealed that biochar production costs USD 0.82/kg, with profitability achieved by selling recovered NFX at USD 6/kg. The study demonstrated a zero-waste, self-sustaining, and profitable water treatment process in line with circular economy principles. | [110] |
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Gkika, D.A.; Mitropoulos, A.C.; Kyzas, G.Z. How Economic Theories Shape Chemical Technology Profile. ChemEngineering 2024, 8, 91. https://doi.org/10.3390/chemengineering8050091
Gkika DA, Mitropoulos AC, Kyzas GZ. How Economic Theories Shape Chemical Technology Profile. ChemEngineering. 2024; 8(5):91. https://doi.org/10.3390/chemengineering8050091
Chicago/Turabian StyleGkika, Despina A., Athanasios C. Mitropoulos, and George Z. Kyzas. 2024. "How Economic Theories Shape Chemical Technology Profile" ChemEngineering 8, no. 5: 91. https://doi.org/10.3390/chemengineering8050091
APA StyleGkika, D. A., Mitropoulos, A. C., & Kyzas, G. Z. (2024). How Economic Theories Shape Chemical Technology Profile. ChemEngineering, 8(5), 91. https://doi.org/10.3390/chemengineering8050091