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. 2024 Dec 28;14:30736. doi: 10.1038/s41598-024-80297-2

Sulfonated asphaltene as a highly efficient catalyst for the Mannich reaction with excellent diastereoselectivity and recyclability

Navid Habibnejad 1, Najmedin Azizi 1,, Mohsen Hajibeygi 2
PMCID: PMC11680968  PMID: 39730466

Abstract

This study investigates the repurposing of asphaltene, a petroleum waste product, as a catalyst for organic reactions. Sulfonated asphaltene was synthesized and evaluated for its efficacy in catalyzing the Mannich reaction, displaying notable diastereoselectivity and operating effectively under mild conditions. Characterization of the catalyst’s chemical composition, structure, and thermal stability was conducted using FT-IR, TGA, XRD, CHN, BET-BJH, SEM, and EDS analyses. Employing the sulfonated asphaltene catalyst in a one-pot multi-component reaction to generate β-amino carbonyl derivatives in ethanol resulted in high product yields after 4–7 h. Notably, the catalyst exhibited recyclability, demonstrating reusability for at least 10 reaction cycles.

Supplementary Information

The online version contains supplementary material available at 10.1038/s41598-024-80297-2.

Keywords: Sulfonated asphaltene, Mannich reaction, Green chemistry, Petroleum waste

Subject terms: Environmental sciences, Chemistry

Introduction

Asphaltene (As), a supramolecular compound derived from crude oil, has historically been considered a waste product, leading to pipeline blockages1. However, recent investigations have revealed its similarities to graphene in terms of structural, physical properties, and chemical composition2. Asphaltene contains heteroatoms such as oxygen, nitrogen, and sulfur, as well as saturated and unsaturated segments, aliphatic and aromatic rings, and even transition metals like vanadium3. Just as graphene can be oxidized to graphene oxide, asphaltene can also undergo oxidation and be utilized as a catalyst4. The use of asphaltene as a catalyst offers several advantages, including lower cost compared to graphene preparation, conversion of industrial waste into a value-added product, and the potential to address environmental concerns associated with asphaltene disposal5. It can be used as a fuel additive to improve combustion properties, in asphalt production for road construction, and as a precursor for carbon materials like activated carbon and carbon nanomaterials6. Asphaltene can also serve as a feedstock for chemical production, be utilized as a catalyst or adsorbent, and play a role in environmental remediation processes7. Its versatile nature and unique properties make asphaltene a valuable resource with significant contributions to energy, infrastructure, and environmental sustainability8. It is important to note that the application of asphaltene as a catalyst in organic synthesis is still an emerging field, and currently, there are two reported examples in the literature9,10.

A one-pot multicomponent reaction (MCR) is a powerful synthetic strategy that allows for the simultaneous incorporation of multiple reactants into a single reaction vessel, resulting in the formation of structurally complex molecules in a single step1116. In these reactions, three or more starting materials react together under suitable reaction conditions, leading to the efficient formation of a single product with high efficiency and atom economy17. One-pot MCRs offer several advantages in organic synthesis, including time and resource efficiency, fewer purification steps, and the potential for the rapid generation of diverse chemical libraries18. They have found significant applications in medicinal chemistry, drug discovery, and the synthesis of complex natural products. 19 The key to a successful one-pot MCR lies in the careful selection of reactants and reaction conditions, such as temperature, solvent, and catalysts20. By judiciously choosing appropriate starting materials and reaction parameters, chemists can orchestrate multiple bond-forming events simultaneously, allowing for the rapid construction of complex molecular frameworks2123.

The Mannich reaction is a widely recognized multicomponent reaction that typically requires the presence of an acidic catalyst2427. It involves the condensation of a non-enolizable aldehyde, a primary or secondary amine, and an enolizable carbonyl compound, resulting in the formation of an aminomethylated product. 28 The enolizable carbonyl compound’s symmetry can lead to the generation of different diastereomeric isomers as products29. Notably, certain catalysts not only promote high reaction yields but also induce enantioselectivity, allowing for the production of chiral amino methylated compounds30. This capability opens up possibilities for the synthesis of complex molecules with specific stereochemical properties through the Mannich reaction3137.

In modern organic synthesis, the utilization of acidic catalysts stands as a cornerstone in enabling and accelerating a wide array of chemical reactions.38 These catalysts, often tailored to exhibit specific reactivity profiles, play a pivotal role in facilitating transformations that might otherwise proceed sluggishly or not at all39. Alongside acidic catalysts, heterocycle reactions form a fundamental aspect of organic chemistry, offering a diverse toolkit for constructing complex molecular frameworks40. These reactions encompass a variety of transformations, including cyclizations, ring openings, and functionalizations, each contributing uniquely to the synthesis of intricate organic compounds41. Moreover, the advent of a bio-based solvents such as Cyrene4244 and deep eutectic solvents (DESs) has revolutionized reaction media, providing environmentally friendly alternatives with tunable properties that enhance reaction efficiency and selectivity4244. Recent advancements in the synthesis of Mannich reactions have showcased novel strategies and reagents, pushing the boundaries of this versatile transformation.45 Furthermore, the development of synthesized catalysts brings both advantages and challenges, offering tailored reactivity while also requiring careful consideration of their limitations and potential drawbacks in practical applications46.

We interest lies in green chemistry-oriented reactions that have been carried out in environmentally friendly reaction media in recent years4750. This focus on sustainable practices aligns with the principles of green chemistry, emphasizing the importance of minimizing environmental impact throughout the chemical process. Conducting reactions in eco-friendly solvents not only reduces the environmental footprint but also contributes to the development of more sustainable chemical methodologies. Herein, we report for the first time, the synthesis of asphaltene-based acidic catalysts and investigate their application in the Mannich reaction. By utilizing asphaltene, a byproduct of crude oil, as a precursor for the catalyst, we aim to address the dual objectives of utilizing a renewable resource and converting an industrial waste product into a value-added material. The acidic catalysts derived from asphaltene exhibit catalytic activity in the Mannich reaction, which is a multicomponent condensation reaction involving aldehydes, amines, and carbonyl compounds.

Experimental

The crude oil was purchased from Marun petrochemical industries in Khuzestan province, Iran. Other chemical reagents, including aniline, carbonyl compounds, chlorosulfuric acids, and solvents, were purchased from suppliers. To confirm the products1, H NMR and FT-IR spectroscopy techniques were employed1. H-NMR spectra were recorded on a 500 MHz spectrometer using CDCl3 as the solvent, and chemical shifts were reported in parts per million (ppm) relative to TMS. FT-IR spectra were obtained using a Bruker Vector-22 infrared spectrometer with KBr disks. For elemental analysis, EDX studies were performed using a scanning Electron Microscope (VEGA3 TESCAN) at an operating voltage of 20 kV. Melting points were determined using a Büchi B-545 melting point apparatus. Thermal gravimetric analysis (TGA) data were recorded using a Netzsch-TGA 209 F1 instrument with a heating rate of 25 °C/min, covering the temperature range from room temperature to 800 °C. The asphaltene’s elemental analysis was determined using a CHN Perkin-Elmer 2400 II apparatus. X-ray diffraction (XRD) was revealed by using Bruker AXS-D8 Advance, and diffractometer type (Cu, Kα1:1.5405 Å). The surface area was determined by the BET (Brunauer-Emmett-Teller) and the pore size distribution was calculated by the BJH (Barrett-Joymer-Halenda) from the isotherm of the adsorption branch with the BELSORP-mini II – Microtrac instrument.

Asphaltene extraction from crude oil

100 mL of crude oil, 2 L n-heptane, and 10 mL toluene were mixed in a round-bottom flask. After 24 h the mixture was filtrated in a vacuum and the remained black-brownish residue was washed severally with n-heptane to remove impurities. The collected asphaltene was dried in an oven at 40 °C under vacuum for 5 h. (black solid, 10 mg)

Preparation of asphaltene sulfonic acid (As-SO3H)

2 g of asphaltene were mixed in 50 mL dichloromethane and the mixture was sonicated for 10 min. After the sonication process, the mixture temperature was decreased by adding 2 mL chlorosulfuric acid to an ice bath. After 5 h 10 mL methanol was added to the mixture for quenching excess chlorosulfonic acids and then filtered. The filtrated was washed with methanol and water severally and dried at 40 °C under vacuum for 5 h (Fig. 1).

Fig. 1.

Fig. 1

The step-by-step preparation As-SO3H from As.

General procedure

In a test tube with a magnetic stirring bar, aldehyde (0.5 mmol), aniline (0.5 mmol), enolizable carbonyl (0.5 mmol), ethanol (0.2 mL), and 20 mg As-SO3H were mixed in a flask at room temperature for 5–7 h. The reaction completion was monitored by thin layer chromatography (TLC) (mobile phase 1:5 ethyl acetate: n-hexane) After this time had elapsed the reaction was quenched by adding water (5 mL) and ethyl acetate (5 mL) and As-SO3H was isolated by centrifugation and washed Twice times with ethyl acetate (5 mL) to reuse again. The organic phase was separated and the ethyl acetate was evaporated by a rotary evaporator and the resulting residue was purified by recrystallizing with a suitable solvent column chromatography using silica gel to give a pure product. All synthesized compounds are known and compared with literature melting point.

Selected data

2-(phenyl(phenylamino)methyl)cyclohexanone (B14): 0.5mmol (0.051 mL) benzaldehyde, 0.5 mmol (0.046mL) aniline, 0.5 mmol (0.052 mL) cyclohexanone 20 mg As-SO3H and 0.2 mL ethanol were mixed in test tube for 6 h at room temperature. The reaction was monitored by TLC and after 6 h the reaction was quenched by adding 5 mL water and 5 mL ethyl acetate. The catalyst was separated by centrifugation and the organic layer was evaporated by rotary evaporator. Remained residue recrystallized in ethanol. Melting point 114–116 °C.

δH: (500 MHz; CDCl3; Me4Si): 1.69–1.98 (6 H, m, aliphatic H), 2.34–2.39 (1 H, m, aliphatic H), 2.44–2.50 (1 H, m, aliphatic H), 2.77–2.81 (1 H, m, aliphatic H), 4.66–4.67 (1 H, d, J = 6.82 Hz, aliphatic H, anti-isomer), 4.77 (0.73, broad, N-H, D2O exchangeable), 6.56–6.58 (2 H, d, J = 8.31 Hz, aromatic H), 6.66–6.68 (1 H, t, J = 7.32 Hz, aromatic CH), 7.08–7.11 (2 H, dd, J = 8.30 Hz - J = 7.32 Hz, aromatic H), 7.23–7.26 (1 H, t, J = 7.33 Hz, aromatic H), 7.32–7.35 (2 H, dd, J = 7.8 Hz – J = 7.34 Hz, aromatic H), 7.40–7.42 (2 H, d, J = 7.8 Hz, aromatic H).

2-(phenyl(phenylamino)methyl)cycloheptanone (B15): 0.5mmol (0.051mL) benzaldehyde, 0.5 mmol (0.046) aniline, 0.5 mmol (0.059mL) cycloheptanone 20 mg As-SO3H and 0.2 mL ethanol were mixed in test tube for 6 h at room temperature. The reaction was monitored by TLC and after 6 h the reaction was quenched by adding 5 mL water and 5 mL ethyl acetate. The catalyst was separated by centrifugation and the organic layer was evaporated by rotary evaporator. Remained residue recrystallized in ethanol. Melting point 139–141 °C.

δH: (500 MHz; CDCl3; Me4Si): 1.27–1.73 (5 H, m, aliphatic H), 1.85–1.92 (4 H, m, aliphatic H), 2.01–2.10(2 H, m, aliphatic H), 2.27–2.56 (2 H, m, aliphatic H), 2.74–2.79 (1 H, m, aliphatic H), 2.90–2.97 (1 H, m, aliphatic H), 4.55–4.57 (0.54 H, d, J = 7.67 Hz, aliphatic H, anti-isomer), 4.68–4.69 (0.46 H, d, J = 4.84 Hz, aliphatic H, syn isomer), 5.48( 0.6 H, broad, D2O exchangeable, N-H), 6.57–6.60 (2 H, t, J = 7.1 Hz, aromatic H), 6.65–6.68 (1 H, t, J = 7.46 Hz, aromatic H), 7.09–7.13 (2, dd, J = 7.46 Hz – J = 7.1 Hz, aromatic H), 7.25–7.43 (7 H, m, aromatic H).

3-(Phenyl(phenylamino)methyl)tetrahydro-4-pyranone (B16): 0.5mmol (0.051mL) benzaldehyde, 0.5 mmol (0.046) aniline, 0.5 mmol (0.046 mL) Tetrahydro-4 H-pyran-4-one 20 mg As-SO3H and 0.2 mL ethanol were mixed in test tube for 7 h at room temperature. The reaction was monitored by TLC and after 7 h the reaction was quenched by adding 5 mL water and 5 mL ethyl acetate. The catalyst was separated by centrifugation and the organic layer was evaporated by rotary evaporator. Remained residue recrystallized in ethanol. Melting point 186–187 °C.

δH: (500 MHz; CDCl3; Me4Si): 2.47–2.81 (3 H, m, aliphatic CH), 3.71–3.90 (3 H, m, aliphatic H), 4.17–4.19 (1 H, m, aliphatic H), 4.82–4.84 (1 H, d, J = 9.31 Hz, anti-isomer), 4.97 (0.7 H, s, D2O exchangeable, N-H), 6.60–6.61 (2 H, d, J = 6.51 Hz aromatic H), 6.60–6.71 (1 H, t, J = 6.87 Hz, aromatic H), 7.08–7.12 (2 H, dd, J = 6.87 Hz- J = 6.51 Hz, aromatic H), 7.34–7.45 (5 H, m).

Result and discussion

The characterization of As and As-SO3H were performed using various methods, with the first method being FT-IR. The FT-IR spectrum of As and As-SO3H are shown in Figs. 2 and 3. As FT-IR (Fig. 1) has just revealed two important absorption bands. a strong absorption band at 2926 cm− 1 is related to C-H saturated stretching and two weak absorption bands at 1457 cm− 1 and 1606 can be attributed to aromatic C = C ring stretch absorption. As-SO3H has also shown various absorption bands that were observed in important regions, providing valuable information about the compound’s functional groups. The broadband observed from 2996 cm− 1 to 3700 cm− 1, with a centrality at 3435 cm− 1, can be attributed to the O-H stretching vibration. The absorption band at 2918 cm− 1, which can be attributed to C-H stretching. This suggests the presence of carbon-hydrogen bonds in the compound. The two strong absorption bands at 1601 cm− 1 and 1440 cm− 1 are related to the C = C aromatic ring stretch absorption. These bands indicated the presence of an aromatic ring structure in the compound. The strong absorption band at 1168 cm− 1 corresponds to the O = S = O asymmetric stretching band, indicating the presence of a sulfur dioxide group. Additionally, another strong absorption band at 1027 cm− 1 is observed, which is related to the stretching of the C-S bond. These bands indicate the presence of a sulfur-oxygen and carbon-sulfur bond. Furthermore, three important absorptions were identified in the As-SO3H compound.

Fig. 2.

Fig. 2

FT-IR spectrum of As.

Fig. 3.

Fig. 3

FT-IR spectrum of As-SO3H.

The XRD pattern of As-SO3H, as depicted in Fig. 4, did not exhibit any distinct or notable reflection. This characteristic suggests that As-SO3H lacks crystalline structures and is instead an amorphous solid. Amorphous materials do not possess long-range order in their atomic arrangement, resulting in the absence of sharp diffraction peaks in XRD patterns. The absence of distinct reflections in the XRD pattern provides further evidence supporting the amorphous nature of As-SO3H.

Fig. 4.

Fig. 4

XRD Diagram of As-SO3H.

The TGA thermogram curve and its first derivative (DTG), as shown in Fig. 5; Table 1, exhibit distinct decomposition events for the As-SO3H compound. The first mass loss occurs at 98 °C, which can be attributed to the evaporation of solvents and water. This initial weight reduction suggests that the sample may contain residual moisture or volatile organic compounds that are easily vaporized at relatively low temperatures. The second and the third mass loss are observed at 210 °C and 456 °C respectively, and they are associated with the decomposition of the SO3H group. This indicates that the sulfonic acid groups present in the As-SO3H compound undergoes thermal decomposition at this temperature range. The fourth main mass loss can be attributed to the decomposition of aliphatic and aromatic components of the compound. This suggests that both aliphatic and aromatic moieties present in the As-SO3H compound undergo thermal decomposition at higher temperatures.

Fig. 5.

Fig. 5

TGA curve of As-SO3H.

Table 1.

Thermal decomposition data of As-SO3H in N2 atmosphere.

Sample T5 (°C) T10(°C) T max1 (°C) Tmax2 (°C) Tmax3 (°C) Char yield (800 °C) (%)
As-SO3H 137 207 210 456 537 2.8

The CHN analysis was employed to determine the carbon, hydrogen, and nitrogen content of the asphaltene sample, as indicated in Table 2. Furthermore, the accuracy and precision of the EDS analysis were validated by confirming the carbon content. In this case, the carbon content was compared between the CHN method and the EDS analysis, and the agreement between the two methods confirmed the accuracy and precision of the EDS analysis.

Table 2.

CHN analysis of As-SO3H.

Sample %C %H %N
As 78.51 6.61 0.75
As-SO3H 42.55 4.41 0.42

Moreover, the results from the EDS analysis demonstrated an increase in the sulfur content due to the sulfonation process. Additionally, it was observed that the weight% of carbon decreased as a result of the sulfonation process. These findings, presented in Table 3, provide evidence that the sulfonation process was successfully conducted on the asphaltene sample. The EDS analysis revealed an increase in sulfur content and a decrease in carbon weight%, indicating the successful sulfonation process. The data presented in Tables 2 and 3 support these conclusions.

Table 3.

EDS data of as and As-SO3H.

Sample C (Weight%) O (Weight%) S (Weight%) N (Weight%)
As 60.97 21.22 12.24 5.56
As-SO3H 40.27 36.97 18.76 3.99

The surface morphology of As and As-SO3H was studied using SEM, offering crucial insights into their morphology and surface characteristics (Figs. 6 and 7). The SEM images of as suggest a nearly uniform morphology with slight agglomeration and an absence of porosity. In contrast, the SEM images of As-SO3H exhibit a distinct morphology compared to As, confirming surface modification.

Fig. 6.

Fig. 6

SEM images of As.

Fig. 7.

Fig. 7

SEM images of As-SO3H.

The N2 adsorption–desorption diagram in BET and BJH shows pore size, surface area, and pore volume are shown in Fig. 8. The radius pore was reported 1.86 nm, surface area in BET was reported 3.8477 m2/g.

Fig. 8.

Fig. 8

The adsorption/desorption isotherm of As-SO3H (left) and BJH pore size distribution of As-SO3H.

To optimize the reaction conditions, various parameters were investigated in the model reaction, and the results are presented in Table 4 to identify the most suitable solvent for the reaction. Different types of solvents, including polar, non-polar, protic, and aprotic ones, were investigated. The highest yield of 98% was achieved with ethanol (Table 4, entry A22). While the lowest yield of 57% was observed with CH2Cl2 (Table 4, entry A3). Other solvents such as chloroform (Table 4, entry A6), dimethylformamide (DMF) (Table 4, entry A1), dimethyl sulfoxide (DMSO) (Table 4, entry A2), water (Table 4, entry A8), and others were also examined during the optimization process. Regarding the amount of As-SO3H catalyst, it was found that adding 20 mg of the catalyst significantly improved the reaction yield, resulting in optimal yield. However, increasing the amount of catalyst beyond this point did not further enhance the yield.

Table 4.

Monitoring solvent and temperature on the model reaction.

graphic file with name 41598_2024_80297_Figa_HTML.gif
Entry Solvent Volume (mL) Catalyst loading (mg) Temperature (°C) Yield (%)
A1 DMF 0.5 40 60 80
A2 DMSO 0.5 40 60 79
A3 CH2Cl2 0.5 40 Reflux 57
A4 Methanol 0.5 40 60 90
A5 Acetonitrile 0.5 40 60 86
A6 CHCl3 0.5 40 Reflux 66
A7 Ethyl acetate 0.5 40 50 70
A8 Water 0.5 40 60 79
A9 Solvent-free - 40 60 67
A10 THF 0.5 40 Reflux 59
A11 PEG-200 0.5 40 60 91
A12 Glycerol 0.5 40 60 88
A13 Ethanol 0.5 40 60 98
A14 Ethanol 0.5 30 60 98
A15 Ethanol 0.5 20 60 98
A16 Ethanol 0.5 15 60 91
A17 Ethanol 0.5 20 40 98
A18 Ethanol 0.5 20 R.T* 98
A19 Ethanol 0.5 20 Reflux 98
A20 Ethanol 0.4 20 R.T 98
A21 Ethanol 0.3 20 R.T 98
A22 Ethanol 0.2 20 R.T 98
A23 Ethanol 0.1 20 R.T 89

Reaction conditions: benzaldehyde, (0.5 mmol, 0.051 mL), aniline (0.5 mmol, 0.046 mL), cyclohexanone (0.5 mmol, 0.052 mL), As-SO3H (15–40 mg), and solvent (0.1–0.5 mL) for 6 h.

After successful optimization in the Mannich reaction with As-SO3H as a catalyst, the reaction was further studied using various benzaldehyde derivatives (with electron-donating groups (EDG) and electron-withdrawing groups (EWG)) and different enolizable ketones. The catalyst effectively promoted the reaction, regardless of the presence of either EWGs or EDGs. Although aldehydes with EDGs (methoxy and methyl) and amines with EWGs (NO2, Cl) do not have an outstanding yield in the Mannich reaction, some amines with EWGs and aldehydes with EDGs exhibit acceptable yields with this catalyst (B11, B13). The highest yields belonged to benzaldehyde and aldehydes with EWGs (B1, B4 and B5). One notable advantage of this catalyst is diastereoselectivity. The catalyst produces a specific diastereomer with 100% (anti) diastereoselectivity (B14-B16) and 54/46% (syn/anti) (B15) (Table 5).

Table 5.

Synthesis of β-aminocarbonyl derivatives in ethanol.

graphic file with name 41598_2024_80297_Figb_HTML.gif
Entrya Ar1 (aldehyde) Ar2 (amine) Ar3 (enolizable carbonyl) Yield (%) Time (h) Syn/anti or Rfb Melting point (°C)
Found Reported(ref)
B1 C6H5 C6H5 Acetophenone 98 6 0.50 165–167 167-16951
B2 4-Cl C6H4 C6H5 Acetophenone 91 6 0.41 118–120 118-12051
B3 4-MeO C6H4 C6H5 Acetophenone 78 7 0.45 150–151 150-15151
B4 3-NO2 C6H4 C6H5 Acetophenone 95 5 0.31 140–142 141-14252
B5 4-NO2 C6H4 C6H5 Acetophenone 93 5 0.28 107–108 107-10951
B6 4-Br C6H4 C6H5 Acetophenone 92 6 0.43 137–139 138-13951
B7 4-Me C6H4 C6H5 Acetophenone 95 7 0.49 132–134 133-13451
B8 C6H5 4-Cl C6H5 Acetophenone 91 6 0.38 165–166 167-16951
B9 4-NO2 C6H4 4-Cl C6H5 Acetophenone 90 6 0.22 128–129 127-13053
B10 4-Me C6H4 4-Cl C6H5 Acetophenone 87 7 0.37 161–163 160-16254
B11 4-MeO C6H5 4-Cl C6H4 Acetophenone 88 6 0.46 120–122 123-12555
B12 4-Me C6H4 4-NO2 C6H4 Acetophenone 81 6 0.46 160–162 165-16557
B13 C6H5 C6H5 4-Cl acetophenone 86 6 0.41 133–134 132-13358
B14 C6H5 C6H5 Cyclohexanone 91 6 0/100
B15 C6H5 C6H5 Cycloheptanone 85 6 54/46
B16 C6H5 C6H5 Tetrahydro-4 H-pyran-4-one 82 7 00/100
B17 C6H5 3-Me C6H4 Cyclohexanone 84 7 0/100
B18 4-ClC6H4 C6H5 Cycloheptanone 78 7 52/48
B19 4-ClC6H4 C6H5 Cyclohexanone 79 7 0/100
B20 C6H5 3-MeC6H4 Cycloheptanone 76 7 68/32
B21 4-ClC6H4 4-BromoC6H4 Cyclohexanone 81 7 69/31
B22 4-BrlC6H4 C6H5 Cyclohexanone 75 7 30/70

aReaction conditions: aldehyde (0.5 mmol), aniline (0.5 mmol), an enolizable ketone (0.5 mmol), ethanol (0.2 mL), and 20 mg As-SO3H were mixed in a flask at room temperature for 5–7 h.

b(Rf for n-hexane-ethyl acetate = 5:1);

The successful recycling of the catalyst for multiple reaction cycles highlights its potential for practical applications, as it offers sustainability and cost-effectiveness. The ability to reuse the catalyst without a loss in catalytic activity enhances the overall efficiency and economic feasibility of the reaction process. As a heterogeneous catalyst, As-SO₃H, demonstrates the ability to be recycled. After each reaction cycle in the model reaction (B1), ethyl acetate (5 mL) were added and the catalyst was isolated via centrifugation. The isolated catalyst was then washed with ethanol (0.5 mL) for reuse in subsequent cycles. The recycling performance of the catalyst was assessed over a total of 10 consecutive cycles (Fig. 9). The FTIR spectrum of the used catalyst after 10 cycles (Fig. 10) indicates that its spectrum is similar to sulfonated asphaltene without any major changes. Therefore, based on this FTIR analysis, it can be concluded that after 10 uses, this catalyst possesses the appropriate functional groups required for catalytic activity.

Fig. 9.

Fig. 9

Recyclability of As-SO3H catalyst on model reaction (B1).

Fig. 10.

Fig. 10

FT- IR spectrum of Recycled As-SO3H.

The proposed mechanism of this reaction on this catalyst is illustrated in Fig. 11. In the proposed one-pot synthesis of β-amino carbonyl derivatives utilizing the As-SO3H catalyst, a conceivable reaction mechanism was envisioned. Initially, the As-SO3H catalyst initiates the reaction by activating the carbonyl compound through protonation, rendering it more susceptible to nucleophilic attack. Subsequently, an amine nucleophile was added to the activated carbonyl, forming an imine intermediate. This intermediate then undergoes further transformation, possibly attack of the enol derived from the ketone on the protonated imine, ultimately yielding the desired β-amino carbonyl derivative. Proton transfers and potential rearrangements may also play a role in the process, leading to the final product. Throughout these steps, the As-SO3H catalyst is likely involved in facilitating the reactions and may undergo regeneration to sustain catalytic activity in the synthesis process.

Fig. 11.

Fig. 11

The proposed mechanism of synthesis β-amino carbonyl with As-SO3H as a recyclable catalyst.

Conclusion

In summary, this study showcases the successful repurposing of asphaltene waste as a catalyst for organic transformations, with sulfonated asphaltene proving to be a highly efficient catalyst for the Mannich reaction. The notable diastereoselectivity and recyclability of the catalyst, along with its performance under mild conditions, underscore its potential in green chemistry applications. The comprehensive characterization of the catalyst through various analytical techniques further validates its suitability for catalytic processes. Using the As-SO3H catalyst resulted in high yields of the desired products and demonstrated excellent diastereoselectivity. The reaction process was straightforward and efficient, making it a practical and efficient method for synthesizing β-amino carbonyl derivatives. Furthermore, the catalyst offered significant advantages in terms of its reusability. It could be recycled and reused for at least 10 consecutive reaction cycles without any noticeable decrease in catalytic activity.

Electronic supplementary material

Below is the link to the electronic supplementary material.

Acknowledgements

Financial support for this work by the Chemistry and Chemical Engineering Research Center of Iran (CCERCI) is gratefully appreciated.

Author contributions

Navid Habibnejad performed material preparation, data collection, and analysis. Mohsen Hajibeygi wrote the first draft of the manuscript. Najmedin Azizi supervised and Writing- review & editing. All authors reviewed the manuscript.

Funding

The authors declare that no funds, grants, or other support were received during the preparation of this manuscript.

Data availability

All data generated during this study are included in this published article.

Declarations

Competing interests

The authors declare no competing interests.

Footnotes

Publisher’s note

Springer Nature remains neutral with regard to jurisdictional claims in published maps and institutional affiliations.

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