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  1. Article ; Online: Hybrid Smart Strategies to Predict Amine Thermal Degradation in Industrial CO

    Azarpour, Abbas / Zendehboudi, Sohrab

    ACS omega

    2023  Volume 8, Issue 30, Page(s) 26850–26870

    Abstract: ... ...

    Abstract CO
    Language English
    Publishing date 2023-07-17
    Publishing country United States
    Document type Journal Article
    ISSN 2470-1343
    ISSN (online) 2470-1343
    DOI 10.1021/acsomega.3c01475
    Database MEDical Literature Analysis and Retrieval System OnLINE

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  2. Article: Current Status and Future Prospects of Renewable and Sustainable Energy in North America: Progress and Challenges

    Azarpour, Abbas / Mohammadzadeh, Omid / Rezaei, Nima / Zendehboudi, Sohrab

    Energy conversion and management. 2022 June 27,

    2022  

    Abstract: Energy is an important drive for the economic development and social growth. The energy demand has remarkably escalated due to technological developments in various governmental, industrial, and municipal activities. In light of such a fast growth, the ... ...

    Abstract Energy is an important drive for the economic development and social growth. The energy demand has remarkably escalated due to technological developments in various governmental, industrial, and municipal activities. In light of such a fast growth, the fuel prices and control of greenhouse gas emission are the leading driving forces for more effective enhancement in the utilization of renewable energy sources. This reflects the importance of mitigation of global energy demands and climate change, which are the most significant factors in the modern days. In this review paper, a detailed overview in the development and evolution of renewable and sustainable energy supply is provided in terms of their types, characteristics and applications, production processes, advantages, and disadvantages. Moreover, the impacts of the renewable energies on health and environment, along with the relevant policies and regulations are discussed. Further, there is a detailed focus on the emerging technologies, and theoretical and practical challenges in the development of renewable energies are analyzed. Particularly, this review provides information on renewable and sustainable energy status and prospects in North America. Central large-scale technology and distributed configuration of the renewable energies might be improved in the North American countries to effectively utilize the renewable energies to produce electricity, biomass-based fuels, and heating in both local/rural and industrial divisions. In addition to employment opportunities stemmed from manufacturing of the renewable energies, its significant impact on the economic development can be enhanced in all three nations through development of the sources.
    Keywords administrative management ; climate change ; economic development ; electricity ; employment ; energy conversion ; greenhouse gas emissions ; North America
    Language English
    Dates of publication 2022-0627
    Publishing place Elsevier Ltd
    Document type Article
    Note Pre-press version
    ZDB-ID 2000891-0
    ISSN 0196-8904
    ISSN 0196-8904
    DOI 10.1016/j.enconman.2022.115945
    Database NAL-Catalogue (AGRICOLA)

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  3. Article ; Online: Systematic energy and exergy assessment of a hydropurification process: Theoretical and practical insights

    Azarpour, Abbas / Mohamadi-Baghmolaei, Mohamad / Hajizadeh, Abdollah / Zendehboudi, Sohrab

    Energy. 2022 Jan. 15, v. 239 p.122023-

    2022  

    Abstract: Improvement of process efficiency and reduction of operation costs are of significant importance in industrial chemical plants. In this study, an effective approach is proposed to analyze a hydropurification process, focusing on energy utilization, ... ...

    Abstract Improvement of process efficiency and reduction of operation costs are of significant importance in industrial chemical plants. In this study, an effective approach is proposed to analyze a hydropurification process, focusing on energy utilization, operating costs, environmental impact (e.g., CO₂ emissions), and exergy performance. The hydropurification process includes heat exchangers, pumps, crystallizers, reactor, and furnace. This process is operated under high pressures and temperatures; it is prone to high consumption of energy and considerable loss of work quality. The vital operating parameters affecting the system performance are chosen by employing Taguchi method. The process simulation and/or thermodynamic modeling are carried out using Aspen Plus® software, and by writing codes for the exergy calculation in MATLAB software environment. The results are in acceptable agreement with the industrial data. The optimal conditions lead to 15% reduction in the process exergy destruction. The optimal operation can be established by implementing lower minimum approach temperature (ΔTₘᵢₙ) of the reaction system feed preheaters (e.g., 5 °C), setting a higher operating pressure in the heat exchangers of the feed preparation section (e.g., 96 bar), and enhancing the performance of heat exchangers using oil as heat transfer medium (optimizing furnace operating conditions). Furthermore, the performance of the fourth and sixth heat exchangers can be enhanced by 33.3%; the performance of the fourth crystallizer can be improved up to 18.7%. The furnace, which utilizes the expensive Therminol® 66 (as the heat transfer fluid), experiences a significant exergy destruction due to significant fluctuations in temperature and thermodynamic irreversibility in the combustion process. Implementation of the proposed optimal conditions can lower the operation costs and carbon tax by 9.96% ($20.5/h) and 14.75% ($14.54/h), respectively; and the CO₂ emission rate can be decreased by 0.582 t/h. A decrease in ΔTₘᵢₙ of the heat exchangers improves the process specific energy consumption and exergy destruction. Moreover, effective control of the plant and avoidance of high fluctuations in the process parameters can lead to exergy destruction reduction.
    Keywords carbon dioxide ; carbon markets ; combustion ; energy use and consumption ; environmental impact ; exergy ; furnaces ; greenhouse gas emissions ; heat exchangers ; heat transfer ; operating costs ; pumps ; thermodynamic models ; water purification ; Energy ; Simulation ; Hydropurification process ; CO2 emissions
    Language English
    Dates of publication 2022-0115
    Publishing place Elsevier Ltd
    Document type Article ; Online
    ZDB-ID 2019804-8
    ISSN 0360-5442 ; 0360-5442
    ISSN (online) 0360-5442
    ISSN 0360-5442
    DOI 10.1016/j.energy.2021.122023
    Database NAL-Catalogue (AGRICOLA)

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  4. Article: A Review on Microalgal Biomass and Biodiesel Production through Co-cultivation Strategy

    Azarpour, Abbas / Zendehboudi, Sohrab / Mohammadzadeh, Omid / Reza Rajabzadeh, Amin / Chatzis, Ioannis

    Energy conversion and management. 2022 May 11,

    2022  

    Abstract: The adverse impacts of fossil fuels on the environment, specifically climate change, have intensified the need for finding a sustainable alternative source of energy. Numerous studies have postulated that biotechnology development, focusing on biofuel ... ...

    Abstract The adverse impacts of fossil fuels on the environment, specifically climate change, have intensified the need for finding a sustainable alternative source of energy. Numerous studies have postulated that biotechnology development, focusing on biofuel production processes, could be a suitable solution for sustainable energy production. The utilization of microorganisms, such as microalgae, is one of the basic strategies to produce biodiesel, pharmaceuticals, and nutraceuticals. Co-cultivation has overtaken mono-cultivation to improve the production of microalgae due to its endurance, foreseeability, and stability. However, further development of the co-cultivation process requires elaborate efforts to make it safe, practical, and optimal. Some dominant factors affecting the co-culture system control are the diversity of the cell groups, mass transfer, scale-up, population ratio, and time. In this review article, we will discuss some critical topics related to the co-cultivation process, such as data collection, modelling, cultivation methods, and interaction varieties. An overview of the quantification techniques for biomass concentration and lipid content is also provided. Moreover, the utilization of microalgal co-cultures will be analyzed, depicting the difficulties associated with their efficient control. As knowledge of the reactions and their entailing kinetics is elemental for analyzing the microalgal systems, which are used to synthesize intermediate products and chemicals, some studies focusing on the kinetics of microalgal biomass conversion into biofuels are presented. Moreover, since the microbial fuel cells (MFCs), as a new bioelectrochemical process, are utilized in the mixed-culture systems to treat wastewater and produce biofuels and other valuable by-products, a summary of the microalgal MFCs is also provided. Finally, arguments about the challenges and advantages of the co-cultivation systems are presented.
    Keywords administrative management ; algae culture ; biodiesel ; biomass ; climate change ; coculture ; data collection ; dietary supplements ; drugs ; energy conversion ; fuel production ; lipid content ; mass transfer ; microalgae ; mixed culture ; wastewater
    Language English
    Dates of publication 2022-0511
    Publishing place Elsevier Ltd
    Document type Article
    Note Pre-press version
    ZDB-ID 2000891-0
    ISSN 0196-8904
    ISSN 0196-8904
    DOI 10.1016/j.enconman.2022.115757
    Database NAL-Catalogue (AGRICOLA)

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  5. Article: A Dynamic Heterogeneous Dispersion Model Evaluates Performance of Industrial Catalytic Hydrotreating Systems

    Azarpour, Abbas / Sohrab Zendehboudi

    Industrial & engineering chemistry process design and development. 2018 May 24, v. 57, no. 24

    2018  

    Abstract: Catalyst deactivation is one of the main challenges in industrial reaction operations. In this paper, a dynamic heterogeneous model is developed for the crude terephthalic acid hydropurification process. The model incorporates the effects of axial mixing ...

    Abstract Catalyst deactivation is one of the main challenges in industrial reaction operations. In this paper, a dynamic heterogeneous model is developed for the crude terephthalic acid hydropurification process. The model incorporates the effects of axial mixing and deactivation of the commercial catalyst of palladium supported on carbon on efficiency of the hydropurification operation. The transport phenomena governing equations lead to a series of partial differential equations which are simultaneously solved. The model validation is accomplished using the industrial data. The proposed model satisfactorily simulates the real process, and it is more accurate than the plug flow model to forecast the process behaviors. A decline in the catalyst particle size improves the catalyst performance; an increase in the catalyst porosity prolongs the catalyst lifetime, while maintaining an acceptable pressure drop in the catalyst bed. It is concluded that the effective control of p-xylene oxidation reactor (in terms of process conditions) and inlet temperature rise lead to more efficient purification process.
    Keywords carbon ; catalysts ; differential equation ; mixing ; model validation ; models ; oxidation ; palladium ; particle size ; porosity ; process design ; purification methods ; temperature ; xylene
    Language English
    Dates of publication 2018-0524
    Size p. 8267-8282.
    Publishing place American Chemical Society
    Document type Article
    ZDB-ID 1484436-9
    ISSN 1520-5045 ; 0888-5885
    ISSN (online) 1520-5045
    ISSN 0888-5885
    DOI 10.1021/acs.iecr.8b01135
    Database NAL-Catalogue (AGRICOLA)

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  6. Article: Dynamic Modeling Strategy To Assess Impacts of Hydrodynamic Parameters on Industrial Hydropurification Process by Considering Catalyst Deactivation

    Azarpour, Abbas / Nima Rezaei / Sohrab Zendehboudi

    Industrial & engineering chemistry process design and development. 2018 Sept. 11, v. 57, no. 41

    2018  

    Abstract: In this study, modeling and simulation of the dynamic behavior of an industrial-scale trickle bed reactor (TBR) with application to a hydropurification process for production of purified terephthalic acid (PTA) are carried out. The impacts of ... ...

    Abstract In this study, modeling and simulation of the dynamic behavior of an industrial-scale trickle bed reactor (TBR) with application to a hydropurification process for production of purified terephthalic acid (PTA) are carried out. The impacts of hydrodynamic parameters such as reactor bed porosity, liquid hourly space velocity (LHSV), and liquid–solid and gas–liquid mass transfer coefficients on the industrial hydropurification TBR performance (in particular, on the catalyst lifetime) are analyzed. As the palladium supported on carbon (Pd/C) catalyst deactivates with time, the concentration of impurities in the product, especially 4-carboxybenzaldehyde (4-CBA) as the main impurity of PTA, increases. The three-phase dynamic mathematical model developed in this research work is validated against the plant data, and an average relative error of 2.2% is obtained for the concentration of 4-CBA. The lifetime of the catalyst based on plant data is 348.2 ± 5.0 days; this value is estimated to be 365.1 days from the simulation results, showing a 4.8% error. According to the sensitivity analysis on the model parameters, the effects of LHSV and bed porosity are in the same direction and magnitude, while the effects of the liquid–solid and gas–liquid mass transfer coefficients are in the opposite direction, and their impacts are also less significant. These parameters are disturbed in a range of up to ±15%, compared to the normal operating conditions that results in an absolute catalyst lifetime change of 2.9%–14.2%. The maximum and minimum variations in the catalyst lifetime are obtained when LHSV is disturbed by ±10%, exhibiting a catalyst lifetime change of 14.2% at a −10% disturbance (416.9 days) and −6.5% at a +10% disturbance (341.3 days). A +15% disturbance in the liquid–solid mass transfer coefficient increases the catalyst lifetime by 2.9% (375.8 days), and a −15% disturbance decreases this vital parameter by 3.7% (351.8 days). Eventually, the findings of this study might be applied to the relevant industrial sectors, providing the required close and meticulous control of the process.
    Keywords carbon ; catalysts ; dynamic models ; hydrodynamics ; liquids ; mass transfer ; mathematical models ; palladium ; porosity ; process design
    Language English
    Dates of publication 2018-0911
    Size p. 13671-13688.
    Publishing place American Chemical Society
    Document type Article
    ZDB-ID 1484436-9
    ISSN 1520-5045 ; 0888-5885
    ISSN (online) 1520-5045
    ISSN 0888-5885
    DOI 10.1021/acs.iecr.8b03235
    Database NAL-Catalogue (AGRICOLA)

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  7. Article: Performance analysis of crude terephthalic acid hydropurification in an industrial trickle-bed reactor experiencing catalyst deactivation

    Azarpour, Abbas / Zahedi, Gholamreza

    Chemical engineering journal. 2012 Oct. 15, v. 209

    2012  

    Abstract: In this work, a dynamic model of an industrial trickle-bed reactor for hydrogenation reactions of 4-carboxybenzaldehyde has been developed. In this case, a heterogeneous plug-flow model has been considered to predict the dynamic behavior of the catalytic ...

    Abstract In this work, a dynamic model of an industrial trickle-bed reactor for hydrogenation reactions of 4-carboxybenzaldehyde has been developed. In this case, a heterogeneous plug-flow model has been considered to predict the dynamic behavior of the catalytic hydropurification reactor of Purified Terephthalic Acid production plant. Furthermore, deactivation model of carbon coated palladium catalyst of the reactor (0.5wt.% Pd/C, type D3065, supplied by Chimet SpA) has been devised based on the actual plant data. The catalyst of the proposed industrial reactor is deactivated after 360days. The simulation results indicate that the concentration of 4-carboxybenzaldehyde is very influential. In addition, concentration of para-toluic is not as destructive as that of 4-carboxybenzaldehyde so that it lessens the lifetime of catalyst about 40days if its concentration in normal operation builds up more than 1.6 times. Besides, the concentration of reactor feed should not be increased to boost the rate of production since this makes the lifetime of the catalyst shorter. If the production rate enhances about 18%, the lifetime of the catalyst drops more than 6months. The hydropurification reactor control is the most crucial part of the purification unit operation. Thus, in addition to the reactor operation assessment, this dynamic model can be used to evaluate the purification section performance at any time to continue producing on-spec product. Also, it might be used in future in the formulation of model based control strategies for the reactor control.
    Keywords carbon ; chemical engineering ; hydrogenation ; models ; palladium
    Language English
    Dates of publication 2012-1015
    Size p. 180-193.
    Publishing place Elsevier B.V.
    Document type Article
    ZDB-ID 2012137-4
    ISSN 1873-3212 ; 1385-8947
    ISSN (online) 1873-3212
    ISSN 1385-8947
    DOI 10.1016/j.cej.2012.07.140
    Database NAL-Catalogue (AGRICOLA)

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  8. Article: Prediction of Pd/C Catalyst Deactivation Rate and Assessment of Optimal Operating Conditions of Industrial Hydropurification Process

    Azarpour, Abbas / Abdul Manan Zainuddin / Madooli Behbehani Mazyar / Nejad Ghaffar Borhani Tohid / Wan Alwi Sharifah Rafidah

    Industrial & Engineering Chemistry Research. 2015 July 22, v. 54, no. 28

    2015  

    Abstract: One of the key concerns of the purification section of a purified terephthalic acid (PTA) production plant is the deactivation of palladium supported on carbon (Pd/C) catalyst. In this work, the deactivation rate model of 0.5 wt % Pd/C catalyst has been ... ...

    Abstract One of the key concerns of the purification section of a purified terephthalic acid (PTA) production plant is the deactivation of palladium supported on carbon (Pd/C) catalyst. In this work, the deactivation rate model of 0.5 wt % Pd/C catalyst has been developed considering temperature, active surface area, and residual catalytic activity. Moreover, the optimal operating conditions of the industrial hydropurification process have been investigated. The results show that PTA production rate (PPR) can be improved by 5.4% through 18% increase in hydrogen flow rate. Furthermore, PPR can be increased by 7.6% via the temperature rise in the reaction mixture. The optimization results further reveal that PPR can be enhanced by 17.3% by improving the feed concentration under the normal operation by means of limiting the inlet 4-carboxybenzaldehyde concentration. The research findings can be applied in the actual working plant to enhance the efficiency of the hydropurification process.
    Keywords carbon ; catalysts ; catalytic activity ; engineering ; hydrogen ; models ; palladium ; prediction ; temperature
    Language English
    Dates of publication 2015-0722
    Size p. 7067-7082.
    Publishing place American Chemical Society
    Document type Article
    ZDB-ID 1484436-9
    ISSN 1520-5045 ; 0888-5885
    ISSN (online) 1520-5045
    ISSN 0888-5885
    DOI 10.1021%2Facs.iecr.5b00925
    Database NAL-Catalogue (AGRICOLA)

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  9. Article: Performance analysis of crude terephthalic acid hydropurification in an industrial trickle-bed reactor experiencing catalyst deactivation

    Azarpour, Abbas / Zahedi, Gholamreza

    Chemical engineering journal

    Volume v. 209

    Abstract: In this work, a dynamic model of an industrial trickle-bed reactor for hydrogenation reactions of 4-carboxybenzaldehyde has been developed. In this case, a heterogeneous plug-flow model has been considered to predict the dynamic behavior of the catalytic ...

    Abstract In this work, a dynamic model of an industrial trickle-bed reactor for hydrogenation reactions of 4-carboxybenzaldehyde has been developed. In this case, a heterogeneous plug-flow model has been considered to predict the dynamic behavior of the catalytic hydropurification reactor of Purified Terephthalic Acid production plant. Furthermore, deactivation model of carbon coated palladium catalyst of the reactor (0.5wt.% Pd/C, type D3065, supplied by Chimet SpA) has been devised based on the actual plant data. The catalyst of the proposed industrial reactor is deactivated after 360days. The simulation results indicate that the concentration of 4-carboxybenzaldehyde is very influential. In addition, concentration of para-toluic is not as destructive as that of 4-carboxybenzaldehyde so that it lessens the lifetime of catalyst about 40days if its concentration in normal operation builds up more than 1.6 times. Besides, the concentration of reactor feed should not be increased to boost the rate of production since this makes the lifetime of the catalyst shorter. If the production rate enhances about 18%, the lifetime of the catalyst drops more than 6months. The hydropurification reactor control is the most crucial part of the purification unit operation. Thus, in addition to the reactor operation assessment, this dynamic model can be used to evaluate the purification section performance at any time to continue producing on-spec product. Also, it might be used in future in the formulation of model based control strategies for the reactor control.
    Keywords models ; palladium ; chemical engineering ; carbon ; hydrogenation
    Language English
    Document type Article
    ISSN 1385-8947
    Database AGRIS - International Information System for the Agricultural Sciences and Technology

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  10. Article: Optimization of biodiesel production from waste cooking oil using ion-exchange resins

    Kolyaei, Maryam / Zahedi, Gholamreza / Nasef, Mohamed Mahmoud / Azarpour, Abbas

    International journal of green energy

    Volume v. 13,, Issue no. 1

    Abstract: Waste cooking oil is a potential substitution of refined vegetable oil for the production of biodiesel due to the low cost of raw material and for solving their disposal problem. In this study, optimization of esterification process of free fatty acids ... ...

    Abstract Waste cooking oil is a potential substitution of refined vegetable oil for the production of biodiesel due to the low cost of raw material and for solving their disposal problem. In this study, optimization of esterification process of free fatty acids in artificially acidified soybean oil with oleic acid has been carried out using methanol as an agent and ion exchange resin as a heterogeneous catalyst. The esterification reaction has been investigated based on the mass balance of the developed model. The model has been validated against experimental data and effects of temperature and catalyst weight have been analyzed. Thereafter, optimization process has been fulfilled for two different objective functions as conversion of acid oil and benefit. Optimization results indicated that the maximum conversion of acid is 95.95%, which is achievable at 4.48-g catalyst loading and reaction temperature of 120°C. Maximum benefit was obtained as US$0.057 per batch of reaction at a catalyst amount of 1 g and temperature of 120°C.
    Keywords cooking fats and oils ; oleic acid ; esterification ; catalysts ; methanol ; temperature ; vegetable oil ; free fatty acids ; models ; soybean oil ; biodiesel ; raw materials ; ion exchange resins ; ion exchange
    Language English
    Document type Article
    ISSN 1543-5083
    Database AGRIS - International Information System for the Agricultural Sciences and Technology

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