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Showing papers by "Ajay K. Dalai published in 2022"


Journal ArticleDOI
15 Feb 2022-Fuel
TL;DR: In this paper, a review of regulations set for each emission type and methods used to control emissions from ships is presented, where different conventional and non-conventional desulfurization methods are discussed for treating bunker fuel to satisfy the requirements set by the IMO.

40 citations


Journal ArticleDOI
31 Aug 2022-Energies
TL;DR: In this paper , the physicochemical attributes of different biomass resources to ascertain their potential for biofuel production are discussed and the strength, weaknesses, opportunities and threats of the thermochemical conversion technologies to understand their scale-up applications and commercialization.
Abstract: Biofuels are sustainable alternatives to fossil fuels because of their renewable and low-cost raw materials, environmentally friendly conversion technologies and low emissions upon combustion. In addition, biofuels can also be upgraded to enhance their fuel properties for wide applicability in power infrastructures. Biofuels can be produced from a wide variety of biomasses through thermochemical and biological conversion processes. This article provides insights into the fundamental and applied concepts of thermochemical conversion methods such as torrefaction, pyrolysis, liquefaction, gasification and transesterification. It is important to understand the physicochemical attributes of biomass resources to ascertain their potential for biofuel production. Hence, the composition and properties of different biomass resources such as lignocellulosic feedstocks, oilseed crops, municipal solid waste, food waste and animal manure have been discussed. The properties of different biofuels such as biochar, bio-oil, bio-crude oil, syngas and biodiesel have been described. The article concludes with an analysis of the strength, weaknesses, opportunities and threats of the thermochemical conversion technologies to understand their scale-up applications and commercialization.

29 citations


Journal ArticleDOI
TL;DR: In this paper , a comprehensive overview of the employment of various types of plant oils (edible and non-edible) as feedstocks, several heterogeneous catalysts, their properties, benefits, and drawbacks for biodiesel production is presented.

20 citations


Journal ArticleDOI
TL;DR: The recent advances in various thermochemical technologies for the conversion of waste biomass to value-added biofuel products are discussed in this article , where an overview of different types and sources of biomass as well as their physicochemical properties are presented.
Abstract: Waste biomass has the potential to produce renewable fuels and fine chemicals. Biofuels derived from agricultural, forestry, and energy crop systems are promising resources to address climate change and minimize greenhouse gas emissions. The recent advances in various thermochemical technologies for the conversion of waste biomass to value-added biofuel products are discussed. A summarized outline of thermochemical technologies such as torrefaction, liquefaction, pyrolysis, and gasification is provided. An overview of different types and sources of biomass as well as their physicochemical properties is presented. The thermochemical conversion products and their environmental benefits are considered as well.

20 citations


Journal ArticleDOI
01 Sep 2022-Fuel
TL;DR: In this paper , steam gasification of pellets prepared from canola residue was carried out at varying temperatures (650-850 °C) and equivalence ratio (0.2-0.4).

17 citations


Journal ArticleDOI
TL;DR: In this article , the authors evaluated the effects of catalysts, catalyst preparation materials and methods, process conditions, nature of the feedstock, and types of the reactor on dry reforming of methane.

13 citations


Journal ArticleDOI
01 Mar 2022-Fuel
TL;DR: In this article , a sequential torrefaction and pelletization process was employed to produce high-quality fuel pellets from canola residue using the Box-Behnken design for optimal relaxed density, durability and hardness of the pellets.

12 citations


Journal ArticleDOI
TL;DR: In this article , the potential of spent coffee grounds (SCG) as a precursor for activated carbon (AC) production via prominent thermochemical conversion technologies was compared in terms of their economic viability.
Abstract: Activated carbon (AC) has gained immense popularity owing to its excellent physicochemical properties and its ability to remove carbon dioxide (CO2) from flue gas stream. This study examines the potential of spent coffee grounds (SCG) as a precursor for activated carbon (AC) production via prominent thermochemical conversion technologies. Different production routes, such as slow pyrolysis, activation, and deep eutectic solvent (DES) functionalization were compared in terms of their economic viability. Three scenarios (Scenario 1–3) involving combinations of the technologies and production routes were evaluated. Scenario 1 comprises of slow pyrolysis, CO2 activation and flue gas recycling for activation. Scenario 2 includes flue gas combustion while the third scenario comprise of flue gas combustion and DES impregnation. All processes were simulated with Aspen plus, while a detailed cash flow analysis was used to estimate the profitability parameters. The price of AC was found to be the most crucial determinant of an AC production plant’s viability and feasibility. The minimum selling price (MSP) of AC samples produced from scenarios 1,2 and 3 are U.S $0.15/kg, $0.21/kg, $0.28/kg respectively. The price of pristine AC and DES treated AC were lower than the commercially available activated carbon (U.S $0.45/kg).

12 citations



Journal ArticleDOI
01 Jul 2022-Fuel
TL;DR: In this paper , a state-of-the-art review was performed to discuss the impacts of catalysts on the production of biofuels and biochemicals via pyrolysis, gasification, liquefaction, Fischer-Tropsch synthesis and polysaccharides conversion.

11 citations


Journal ArticleDOI
01 Jun 2022-Fuel
TL;DR: In this article , a facile one-pot synthesis was developed to produce a series of metal-substituted TUD-1 mesoporous supports, with nominal Si/M molar ratio of 40 (where M = Al, Zr, Fe, Cu, or Ce).

Journal ArticleDOI
TL;DR: In this article , the effects of process conditions such as temperature, reaction time and feed-to-water mass ratio (1:05-1:15) were investigated to optimize the gasification process for large gas yields.

Journal ArticleDOI
TL;DR: In this article , three solid acid catalysts, namely mesoporous aluminophosphate-supported 12-tungstophosphoric heteropoly acid (HPW/MAP), mesoporus aluminosilicate-supported 6-to-12-tooth polysilicon (P2O) supported 12-topping polyethylene (Polyethylene) heteropoly acids (P3O), and gamma alumina-supported gamma alumin-supported 8-topper polyethylenes (γ-Al2O3) were prepared and characterized using a wet impregnation method.
Abstract: In this study, three solid acid catalysts, namely mesoporous aluminophosphate-supported 12-tungstophosphoric heteropoly acid (HPW/MAP), mesoporous aluminosilicate-supported 12-tungstophosphoric heteropoly acid (HPW/MAS), and gamma alumina-supported 12-tungstophosphoric heteropoly acid (HPW/γ-Al2O3) were prepared and characterized. Mesoporous aluminophosphate (MAP) and mesoporous aluminosilicate (MAS) were synthesized via sol-gel and hydrothermal methods, respectively, and 25 wt.% of 12-tungstophosphoric heteropoly acid (HPW) was immobilized on the support materials using the wet impregnation method. The features of the fabricated catalysts were comprehensively investigated using various techniques such as BET, XRD, NH3-TPD, TGA, and TEM. The surface area of the supported catalysts decreased after HPW impregnation according to BET results, which indicates that HPW loaded on the supports and inside of their pores successfully. The density and strengths of the acid sites of the support materials and the catalysts before reaction and after regeneration were determined by the NH3-TPD technique. Accordingly, an increase in acidity was observed after HPW immobilization on all the support materials. The catalytic performance of the catalysts was studied through alcoholysis reaction using unrefined green seed canola oil as the feedstock. The maximum biodiesel yield of 82.3% was obtained using 3 wt.% of HPW/MAS, with a methanol to oil molar ratio of 20:1, at 200 °C and 4 MPa over 7 h. The reusability study of HPW/MAS showed that it can maintain 80% of its initial activity after five runs.

Journal ArticleDOI
TL;DR: In this paper , the main routes including carboxylation, oxidation, etherification, hydrogenolysis, esterification, and dehydration to convert glycerol to value-added products are investigated.
Abstract: Utilization of biofuels generated from renewable sources has attracted broad attention due to their benefits such as reducing consumption of fossil fuels, sustainability, and consequently prevention of global warming. The production of biodiesel causes a huge amount of by-product, crude glycerol, to accumulate. Glycerol, because of its unique structure having three hydroxyl groups, can be converted to a variety of industrially valuable products. In recent decades, increasing studies have been carried out on different catalytic pathways to selectively produce a wide range of glycerol derivatives. In the current review, the main routes including carboxylation, oxidation, etherification, hydrogenolysis, esterification, and dehydration to convert glycerol to value-added products are investigated. In order to achieve more glycerol conversion and higher desired product selectivity, acquisition of knowledge on the catalysts, the type of acidic or basic, the supports, and studying various reaction pathways and operating parameters are necessary. This review attempts to summarize the knowledge of catalytic reactions and mechanisms leading to value-added derivatives of glycerol. Additionally, the application of main products from glycerol are discussed. In addition, an overview on the market of glycerol, its properties, applications, and prospects is presented.

Journal ArticleDOI
TL;DR: In this article , microwave-assisted (MAE) and Soxhlet extraction techniques were attempted to obtain the extractives from sea buckthorn pomace and seed using low (n-hexane) and medium (ethanol) polar solvents aiming at higher extraction yield.

Journal ArticleDOI
TL;DR: In this article , the Ni-La/SBC materials not only realized the reuse of SBC but also effectively promoted the hydrothermal gasification of agricultural wastes, and approximately 90% H2 yield was obtained under optimized conditions (360 °C, 0.5 g NiLa catalyst loading and 10 min) by an orthogonal design with NiLa/spent bleaching clay (SBC) materials.

Journal ArticleDOI
TL;DR: In this paper , the main objective of CFD simulation for Fischer-Tropsch synthesis (FTS) can be summarized in three points (1) to analyze the conservation laws (mass, heat, and momentum transport) coupled with the catalytic reactions in the reactor, (2) to optimize the operating conditions to maximize the catalyst activity and selectivity to desired products, and (3) to support the reactor design and engineering.
Abstract: Increasing the global energy demand motivates the search for renewable and clean energy resources. Fischer-Tropsch synthesis (FTS) is one of these sources, which converts syngas (a mixture of CO and H2) to a wide range of hydrocarbons . Liquid transportation fuels produced via FTS from biomass-derived syngas introduce an attractive, clean, carbon-neutral, and sustainable energy source. Reactor and catalyst designs play a significant role in the improvement of FTS efficiency. Flow hydrodynamics coupled with reaction kinetics makes this process challenging. Numerical methods such as computational fluid dynamics (CFD) can help us effectively understand the fluid dynamics within FT reactor. The main objective of CFD simulation for FTS can be summarized in three points (1) to analyze the conservation laws (mass, heat, and momentum transport) coupled with the catalytic reactions in the reactor, (2) to optimize the operating conditions to maximize the catalytic activity and selectivity to desired products, and (3) to support the reactor design and engineering. A CFD code consists of four steps: geometry generation, meshing, solver, and post-processing. Emerging data-driven techniques were also reviewed in this work to analyze the fluid dynamics of FTS. FTS is mainly operated in fixed bed, slurry bubble column, fluidized bed, micro-structured, and membrane reactors. This review aims to analyze the capability of CFD simulation in predicting the FTS performance in different reactor types and address the present challenges.

Journal ArticleDOI
TL;DR: In this article , a two-level full factorial design was applied for K and/or Mo-promoted Fe/CNTs catalyst to investigate the effects of synthesis conditions including Mo/K mass ratio, ultrasonic time, and iron loading on light olefins' yield.
Abstract: Light olefins' (C2-C4) production from syngas (H2 +CO) through Fischer-Tropsch synthesis (FTS) benefits from Fe-based catalysts supported on carbon nanotubes (CNTs). Two-level full factorial design was applied for K and/or Mo-promoted Fe/CNTs catalyst to investigate the effects of synthesis conditions including Mo/K mass ratio, ultrasonic time, and iron loading on light olefins' yield. These catalysts were characterized to perform an in-depth study of Mo/K binary promoter effects on Fe/CNTs catalyst in Fischer-Tropsch to light olefins. CO chemisorption and TEM revealed that molybdenum plays a significant role in metal dispersion, leaving structural defects on CNTs support. Additionally, H2-TPR confirmed that K as promoter facilitates reducibility of Fe/CNTs catalysts, which promoted CO conversion in FTS. Compared with the un-promoted Fe/CNTs catalysts, addition of molybdenum as a promoter increased light olefins' selectivity by 33.4%, while potassium led to an increase in CO conversion by 96.3%. The optimum formulation (0.5K5Mo10Fe/CNTs) obtained olefins' yield of 35.5%.

Journal ArticleDOI
TL;DR: In this article , the authors present an updated report on slow pyrolysis of lignocellulosic biomass, impact of different pyroplysis parameters and degradation pathway involved in the evolution properties of biomass.
Abstract: The excessive dependency on fossil fuel resources could be curtailed by the efficient conversion of lignocellulosic biomass. Biochar, a porous carbonaceous product synthesized exploiting thermochemical conversion pathway, could be an environment-friendly replacement of fossil fuel resources. Slow pyrolysis, a sub-class among various thermochemical conversion techniques, has gained immense popularity owing to its potential to convert biomass to biochar. Furthermore, biochar obtained as the by-product of slow pyrolysis has attracted enormous popularity due to its proven role and application in the multidisciplinary areas of engineering and environmental remediation applications. The physicochemical quality of biochar and its performance is significantly dependent on the feedstock type and pyrolysis process parameters. Therefore, further experimental research and investigations in terms of lignocellulose biomass type and pyrolytic process parameters (temperature, heating rate and reaction time) are essential to produce biochar with desired physicochemical features for effective utilization. This review presents an updated report on slow pyrolysis of lignocellulosic biomass, impact of different pyrolysis parameters and degradation pathway involved in the evolution properties of biomass. The influence of the feedstock type and lignocellulosic composition on the biochar properties are also discussed meticulously. The co-relationship between biochar yield at different pyrolysis temperatures and the development of textural properties provides valuable information for their effective utilization as a functional carbon material. Additionally, an extensive study was undertaken to collate and discuss the excellent physicochemical characteristics of biochar and summarizes the benefits of biochar application for diverse industrial purposes. Biochar is acknowledged for its excellent physicochemical properties owing to the thermal treatment and as a result its prospective diverse industrial applications such as for soil treatment, carbon sequestration, adsorbent (wastewater treatment or CO2 capture), producing activated carbon for gold recovery, energy storage and supercapacitor are summarized systematically in this review paper. For instance, biochar when applied in soil have shown improvement in soil respiration by 1.9 times. Furthermore, biochar when used to capture CO2 from flue gas stream under post-combustion scenario has demonstrated superior capture performance (2.8 mmol/g) compared to commercial activated carbon. This paper identified the knowledge gaps and outlooks in the field of the advancements of biochar from slow pyrolysis for targeted engineering applications mainly in the field of environmental remediation and energy harvesting.

Journal ArticleDOI
TL;DR: A review of state-of-the-art research on hydrothermal flames including the impacts of process parameters on flame ignition is presented in this paper, where the authors highlight some technical considerations relating to hydrotherm flames such as the choice of organic solvent and its characteristics.

Journal ArticleDOI
TL;DR: In this paper , the authors used the Box-Behnken design approach based on response surface methodology to optimize H2-rich fuel gas yield from canola hull pellet via supercritical water gasification at variable temperatures (375-575 °C), biomass-to-water ratio (1:5-1:20), and residence time (10-60 min).

Journal ArticleDOI
TL;DR: In this paper , the 3D graphene oxide hydrogel was synthetized using two different cross-linking agents, p-phenylene diamine (PPD) and ethylene diamines tetra acetic acid (EDTA), and then magnetized by insitu co-participation of Fe3O4.

Journal ArticleDOI
TL;DR: In this article , a two-step glycerol dehydration-hydrogenation process was considered and the activation energy for the dehydration and hydrogenation steps was found to be 57.73 ± 10 kJ/mol and 156.6 ± 8.9kJ/m from the Eley-Rideal kinetic model, respectively.

Journal ArticleDOI
TL;DR: In this paper , the optimal operating conditions were determined in a CVD reactor for maximal yield and purity of carbon nanotubes (CNTs) for light olefins production using synthesis gas in Fischer-Tropsch synthesis.

Journal ArticleDOI
TL;DR: In this article , the effect of pressure (200-400 bar) and temperature (300-400 °C) on the yield and composition of bio-oil and biochar was investigated in semi-batch mode.

Journal ArticleDOI
TL;DR: In this paper , the authors used deep eutectic solvent (DES) to optimize the surface functionalities of the pristine and DES-functionalized activated carbon (DES-AC) samples.
Abstract: Spent coffee grounds have been selected as a potential feedstock to synthesize activated carbon (AC) through physical activation. The activation parameters were optimized by employing the Box-Behnken design method. The impact of input activation parameters included the activation temperature (600-800 ℃), holding time (60-120 mins) and CO 2 flow rate (150-250 mL/min). Accordingly, at the optimum conditions obtained at 800 ℃, 90 min and 150 mL/min, the predicted response of specific surface area (1202.1 m 2 /g) was in good agreement with the actual response 1224 m 2 /g. Furthermore, deep eutectic solvent (DES) has been used to tailor the surface functionalities of the optimized AC (pristine). The change in textural characteristics, surface chemistry and morphology of the pristine and DES-AC samples were characterized by using complementary analytical techniques, including ultimate analysis, ash content, textural characteristics, XRD, CO 2 -TPD, TGA, XPS and SEM analyses. The studies highlighted change in physicochemical properties after the impregnation. For instance, the surface area of the DES-functionalized AC reduced to 1033 m 2 /g, but more basic functional moieties developed on the surface. The DES-AC has shown adequate CO 2 capture performance of 5.5 mmol/g compared to pristine AC (4.34 mmol/g) at 25 ℃ and 15 vol % of CO 2 (in N 2 ). Furthermore, DES functionalized AC has shown excellent selectivity in a dynamic mixture stream of CO 2 /N 2 and facile regeneration (92% retention) after multiple adsorption-desorption runs. Hence, preparing AC from SCG via physical activation and DES impregnation could be proposed as a promising valorization strategy to alleviate the CO 2 emission problem. • The potential of spent coffee grounds to synthesize activated carbon was investigated. • The preparation conditions were optimized using the Box Behnken Design method. • Deep eutectic solvent (DES) was used to functionalize the activated carbon. • The functionalized activated carbon displayed maximum CO 2 adsorption capacity of 5.5 mmol/g. • The DES functionalized activated carbon displayed thermal stability for industrial use.

Journal ArticleDOI
TL;DR: In this paper , an integrated hydrothermal process was used to remove hemicellulose and lignin through the integrated H2O2 process, which increased the crystallinity index and thermal stability of the cellulose fibers.
Abstract: Cannabis indica stems were hydrolyzed with subcritical water at various temperatures, reaction times, and feed concentrations. The highest total yield of reducing sugars of 16.4 wt % was obtained at 190 °C in 37.5 min with a feed concentration of 3.5 wt %. Solid residues from the optimized process were treated with 0.5 M NaOH (pulping) and 0.5–3 % H2O2 (bleaching) to isolate cellulose fibers. The maximum yield of cellulose was 34.8 wt % with lowest lignin content of 0.5 wt %. With the removal of hemicellulose and lignin through the integrated hydrothermal processes, the crystallinity index and thermal stability of the cellulose fibers increased.

Journal ArticleDOI
TL;DR: In this paper , the supercritical CO2 extraction (SCCO2) extraction of Indian cannabis (Cannabis indica) leaves was optimized through a central composite design using CO2 pressure (150-250 bar), temperature (30-50 °C) and time (1-2 h).
Abstract: Supercritical CO2 extraction (SCCO2) extraction of cannabis oil from Indian cannabis (Cannabis indica) leaves was optimized through a central composite design using CO2 pressure (150–250 bar), temperature (30–50 °C) and time (1–2 h). From the regression model, the optimal CO2 pressure, extraction temperature and time were 250 bar, 43 °C and 1.7 h, respectively resulting in the experimental yield of 4.9 wt% of cannabis oil via SCCO2 extraction. The extract contained cannabidiol, tetrahydrocannabivarin, Δ9-tetrahydrocannabinol and Δ8-tetrahydrocannabinol as well as two terpenoids such as cis-caryophyllene and α-humulene. Besides SCCO2 extraction of cannabis oil, the raffinate biomass was utilized to extract polyphenols using water as the extraction medium. Cannabis oil and water extractive were investigated for their half-maximal inhibitory concentration (IC50) values, which were found to be 1.3 and 0.6 mg/mL, respectively. This is comparable to the commercially available antioxidant such as butylated hydroxytoluene with an IC50 value of 0.5 mg/mL. This work on SCCO2 extraction of cannabinoids and other valuable bioactive compounds provides an environmentally sustainable technique to valorize cannabis leaves.

Journal ArticleDOI
TL;DR: In this paper , the authors presented a method of valorizing liquid effluents produced from the torrefaction of oat hull and canola hull via microwave irradiation, which was carried out at 375-525 °C for 15-60 min with 1:5 and 1:10 feed-to-water ratios under 22-25 MPa pressure to optimize the operating parameters of the process.
Abstract: A significant amount of aqueous liquids rich in organic, inorganic contents and leached metals is produced during torrefaction of biomass, which requires additional remediation before disposal. Hydrothermal gasification can produce H 2 -rich syngas from organic wastes, especially from feedstocks with high-water content. This study presents a novel method of valorizing liquid effluents produced from the torrefaction of oat hull and canola hull via microwave irradiation. Hydrothermal gasification of the liquid effluents (feedstock) was carried out at 375-525 °C for 15-60 min with 1:5 and 1:10 feed-to-water ratios under 22-25 MPa pressure to optimize the operating parameters of the process. Hydrothermal gasification of torrefaction effluents from canola hull and oat hull produced total gas yields of 6.6 mmol/g and 8.7 mmol/g, respectively without the addition of water at optimized conditions (525 °C and 45 min). However, with the addition of water (i.e., 1:10 feed-to-water ratio), the total gas yield increased to 12 mmol/g and 16.1 mmol/g from oat hull and canola hull effluents, respectively. The highest H 2 yields (7.8 mmol/g) and carbon gasification efficiency (51%) were obtained at 525 °C in 60 min with a 1:10 feed-to-water ratio. Homogeneous catalysts including KOH, K 2 CO 3 and Na 2 CO 3 were used to improve the gas yields from torrefaction effluents from oat hull at optimal conditions. H 2 gas yield increased by 58%, 65% and 66% in presence of K 2 CO 3 , Na 2 CO 3 and KOH, respectively. KOH led to maximum H 2 yield, hydrogen selectivity and carbon gasification efficiency of 12.8 mmol/g, 89% and 98%, respectively. • Renewable H 2 production from torrefied liquid effluent from supercritical water is feasible. • Impacts of process conditions such as temperature, reaction time and feed to water ratio on products yield were studied in-depth. • The major torrefied liquid chemical species were identified as aldehydes, ketones, organic acids, esters, and aromatics. • Homogeneous catalyst KOH improved the gas yields and hydrogen selectivity by 61% and 36%, respectively. • Anti-coking ability can be enhanced by using feedstock with low carbon contents.

Journal ArticleDOI
TL;DR: In this article , industrial hemp seeds were subjected to three different extraction techniques-advanced extraction techniques like microwave and ultrasound extraction and primitive extraction technique like mechanical cold pressing in order to extract oils.
Abstract: Industrial hemp hearts were subjected to three different extraction techniques-advanced extraction techniques like microwave and ultrasound extraction and primitive extraction technique like mechanical cold pressing in order to extract oils. The extraction yield varied between 41.0 ± 2.1% (w/w) and 54.0 ± 2.7% (w/w). Linoleic acid (LA) was reported to be the major polyunsaturated fatty acid (PUFA) followed by α−Linolenic acid (ALA). The ratio of LA to ALA was found to be close to 3:1 which is considered optimal for nutrition. The ratio of unsaturated fatty acids (UFA) to saturated fatty acids (SFA) was in the range of 6.7 to 9.1. Several minor compounds like ɣ-Sitosterol, stigmasterol, rhodoxanthin, carotene, and methyl cholate as well as antioxidants like β-Carotene and ɣ-Tocopherol have been identified in the oils. The physicochemical properties of the oils like the acid value, iodine value, and oxidative stability indicated that they have higher quality and that the level of unsaturation was very high. Furthermore, free radical scavenging activity of the oils revealed that the oils exhibited 94% of activity in the first 2 h. A perfect combination of unsaturated fatty acids and saturated fatty acids, an appropriate medley of different antioxidants not only qualifies hemp seed oil as an excellent source of nutrition but also as an important plant-based (vegetable) oil for the higher value nutraceutical and pharmaceutical industries.