Abstract
Amide formation through the Ritter reaction remains a valuable transformation in pharmaceutical and materials chemistry, yet conventional protocols rely heavily on corrosive homogeneous acids and non-green conditions. In this study, a magnetite nanoparticles/graphitic carbon nitride/ nitrilotri(methylphosphonic acid (Fe3O4/g-C3N4/NTMPA) magnetic nanocomposite (MNC) was synthesized via a co-precipitation method and employed as an efficient and recyclable solid acid catalyst for solvent-free Ritter reactions at 80 °C. Structural and morphological analyses using FT-IR, XRD, FE-SEM, TEM, DLS, and EDX confirmed successful incorporation of NTMPA and uniform distribution of Fe, C, N, O, and P throughout the composite. BET analysis showed a surface area of 11.421 m2/g, pore volume of 0.0588 cm³/g, and mean pore diameter of 20.593 nm, indicating a mesoporous structure conducive to catalytic accessibility. TGA revealed a major decomposition step of 23.88% between 500 and 600 °C corresponding to g-C3N4 degradation, confirming appropriate thermal stability. The catalyst demonstrated broad substrate applicability, converting tertiary alcohols and benzylic alcohols to the corresponding amides in high to excellent yields in 1.25–6 h. Aromatic nitriles consistently delivered yields above 90% within 5–6 h, with electron-withdrawing substituents further enhancing reactivity and aliphatic nitriles provide the related amides in 87–98% yields within 1.5–5.5 h. The catalyst retained over 90% activity after six cycles, with post-reaction analyses confirming structural integrity. These results highlight Fe3O4/g-C3N4/NTMPA as a robust, magnetically recoverable, and environmentally compatible catalyst for green amide synthesis.
Supplementary Information
The online version contains supplementary material available at 10.1038/s41598-026-35371-2.
Keywords: Magnetite nanoparticles, Graphitic carbon nitride, Nitrilotri(methylphosphonic acid, Ritter reaction, Amide synthesis, Heterogeneous acid catalyst, Solvent-free catalysis, Green chemistry
Subject terms: Chemistry, Environmental sciences, Materials science
Introduction
Amides are fundamental organic compounds that hold a central place in both natural and synthetic chemistry due to their structural and chemical versatility. Characterized by a carbonyl group (C = O) linked to a nitrogen atom, they are essential building blocks in proteins, forming peptide bonds that link amino acids and serve as the structural units of living organisms1. Beyond their biological significance, amides are critical intermediates in the synthesis of pharmaceuticals, agrochemicals, and polymers, featuring prominently in bioactive molecules from small-molecule drugs to complex peptide-based therapeutics2. Amide bonds are integral to the backbone of many therapeutic agents, including antibiotics, anticancer drugs, and pain relievers2. In materials science, amides contribute to the development of advanced materials like nylons and aramids, valued for their chemical stability, mechanical properties, and resistance to hydrolysis3. Furthermore, amides play a significant role in various industrial applications, such as in the production of plastics, lubricants, dyes, cosmetics, and surfactants. This broad utility across fields highlights the importance of developing efficient and sustainable methods for amide synthesis, making it a priority in both organic synthesis and industrial chemistry4.
Amides have been synthesized through various methods, Fig. 1, including direct acylation of amines (Fig. 1A)5, the Schmidt reaction (Fig. 1B)6, transamidation (Fig. 1C)7, Ritter reaction (Fig. 1D)8, aminocarbonylation (Fig. 1E)9, oxidative amidation (Fig. 1F)10, hydrolysis of nitriles (Fig. G)11, reductive amination (Fig. 1H)12, [1,3]-acyl shift of n-carboxyanhydrides which is the reaction of carboxylic acid with isocyanate followed by a [1,3]-acyl shift (Fig. 1I)13, and biocatalytic amide bond formation (Fig. 1J)14. Among these, transamidation, oxidative amidation, and aminocarbonylation represent more modern approaches. However, these methods often require harsh reaction conditions or toxic reagents, making them less favorable in terms of green chemistry.
Fig. 1.
Different routes for the synthesis of amides.
The Ritter reaction is one of the most powerful and versatile methods for synthesizing amides from nitriles and alcohols or alkenes, often under mild conditions8. This reaction proceeds through the generation of a carbocation intermediate, which reacts with the nitrile to form a nitrilium ion, eventually yielding an amide upon hydrolysis. The major advantages of the Ritter reaction are its broad substrate scope and its ability to form amides in a single step without requiring pre-functionalization of the starting materials. It also tolerates a wide variety of functional groups, making it a highly adaptable method for both academic and industrial applications15. Despite its benefits, the traditional Ritter reaction often relies on strong acids, such as sulfuric acid or hydrochloric acid, posing environmental and operational challenges, particularly in catalyst recovery and reuse. Thus, the exploration of more sustainable and efficient catalytic systems within the framework of the Ritter reaction remains a significant area of research in the pursuit of greener methodologies for amide synthesis.
Recent advancements in the Ritter reaction have shifted focus toward more sustainable acidic catalytic systems, moving away from traditional strong acids such as sulfuric acid and hydrochloric acid16. Various Lewis and Brønsted acid catalysts have been explored, including sulfated tungstate17, sulfonic acid-functionalized silica18,and ionic liquids like [BSmim]CuPW12O4019. Notable examples also include zeolite Y nanoparticles (NPs)20, sulfonic acid-functionalized (bio)materials21, and sulfated polyborate catalysts22. Additionally, nafion/layered double hydroxide nanohybrids23 and m-phenolsulfonic acid-formaldehyde resin24, and amberlyst15(H)25 have shown promise as effective catalysts. Moreover, metal-organic frameworks (MOFs) like copper-MOF10, and magnetic CoFe2O4 nanoparticle (NP) immobilized N-propyl diethylenetriamine sulfamic acid26 have been employed for enhanced catalytic performance. Finally, TFA/TfO27 represent additional catalytic systems investigated for their effectiveness in the Ritter reaction. These developments reflect the ongoing efforts to refine catalytic systems in the Ritter reaction, aiming to achieve greater sustainability and operational convenience in amide synthesis28.
A critical factor in enhancing the practical applicability of catalytic systems in the Ritter reaction is their ability to be easily recovered and reused, which aligns with the principles of green chemistry through reducing wastes and costs in large-scale applications26. Catalysts that can be efficiently separated from the reaction mixture, especially those that avoid complex purification steps, are highly valued in the industry29–31. Among the various systems, magnetic acidic catalysts have gained attention due to their facile recovery through magnetic separation, simplifying the catalyst handling and reuse process32. Several recent studies have reported successful applications of magnetic catalysts in organic reactions, including Cu-supported amine-functionalized Fe3O4 for coupling reaction33, Fe3O4@gC3N4@Thiamine for the synthesis of spirooxindole-pyran derivatives and 2-amino-4H-pyrans34. Additional reported systems are Fe3O4@Zein-copper(II) for the synthesis of novel fluorescent 1,4-disubstituted-1,2,3-triazoles35, Fe3O4@EDA-SO3H for the synthesis of synthesis of quinoxalines, benzothiazoles and benzoxazoles36, Fe3O4@SiO2-S-Bu-SO3H for the synthesis of benzothiazole derivatives37, Fe3O4@Glycerol‑Cu in the green synthesis of 2‑amino‑4H‑chromenes38, Fe3O4@ZIF-8@Glycerol-Ni in the synthesis of dihydropyrimidinones39, Fe3O4@CPTMS@Asp@Ni in the synthesis of substituted acridines40, and Ni catalyst anchored on Fe3O4@MIL-101 has shown excellent efficiency in one-pot Suzuki–Miyaura coupling41 have demonstrated effective reusability and high catalytic performance in organic synthesis, underscoring the potential of these systems in sustainable organic synthesis.
NTMPA exhibits strong acidic properties due to the presence of three phosphonic acid groups that making it a strong Brønsted acid catalyst in various acid-catalyzed transformation in organic synthesis42. NTMPA is one of the most important family of aminopolyphosphonic acids as strong chelating agents toward metal ions, enabling stable binding to metal oxide surfaces such as Fe3O4, thereby reducing leaching and enhancing catalyst durability43. Third, phosphonic acids show excellent anchoring affinity to oxide and graphitic supports, creating robust hybrid materials suitable for heterogeneous catalysis44. Fourth, NTMPA is non-volatile, thermally stable, and widely used in environmentally benign applications (e.g., scale inhibition, water treatment), aligning well with green chemistry principles45. Finally, despite its strong acidity and stability, NTMPA has not previously been reported as a catalytic component for the Ritter reaction, offering both novelty and functional advantages in designing recyclable, magnetically recoverable solid acid catalysts.
Coating Fe3O4 NPs with different materials serves several purposes, such as improving stability, enhancing functionality, preventing aggregation, and allowing specific surface modifications for various applications46,47. Some commonly used coatings are silica (SiO₂) coating46, polymer coatings such as polyethylene glycol (PEG)48, carbon coatings like graphene49, organic acid coatings like oleic acid50, and g-C3N451. The g-C3N4 coating provides a protective layer around Fe3O4 NPs, increasing their resistance to chemical degradation and oxidation51. Additionally, the magnetic nature of Fe3O4 enables easy recovery of the catalyst with an external magnetic field, which simplifies the recycling process and makes the material suitable for repeated use in heterogeneous catalysis32.
This study focuses initially on synthesizing a novel, heterogeneous, magnetically separable Fe3O4/g-C3N4/NTMPA MNC for the efficient catalysis of the Ritter reaction under mild and benign conditions (Fig. 2). By integrating the magnetic properties of Fe3O4 with the protective and conductive characteristics of g-C3N4 and the strong acidity of NTMPA to develop a sustainable and reusable catalytic system that aligns with green chemistry principles. Then it is employed in a green, solvent-free approach for amide formation via the Ritter reaction, while specifically addressing key limitations of earlier methods such as prolonged reaction times, harsh conditions, and difficult catalyst recovery by providing a more efficient, recoverable, and environmentally friendly alternative.
Fig. 2.
Synthesis of amide derivatives through Ritter reaction catalyzed by an efficient magnetically Fe3O4/g-C3N4/NTMPA MNC.
Experimental
Chemicals
All solvents and chemicals were purchased from Merck, and Sigma-Aldrich chemical companies and were applied with no further purification. The following chemicals were purchased from Sigma-Aldrich to synthesize Fe3O4/g-C3N4/NTMPA MNC: melamine, iron (III) chloride hexahydrate (FeCl3.6H2O), iron (II) chloride tetrahydrate (FeCl2.4H2O). Ammonium hydroxide (NH4OH) and potassium bromide (KBr) were bought from Merck company. The solvents were used with no more purification.
Characterization instruments
The spectra of 1H NMR at 400 MHz and 13C NMR at 100 MHz were reported by a Bruker Avance DPX spectrometer in pure deuterated chloroform (CDCl3) and deuterated dimethyl sulfoxide (DMSO-d6) solutions. All ¹H and ¹³C NMR spectra were recorded with TMS as an internal standard. Chemical shifts (δ) are reported in ppm, coupling constants (J) in Hz, and splitting patterns are indicated as s (singlet), d (doublet), t (triplet), q (quartet), m (multiplets), or br (broad). The FT-IR spectra of the materials were recorded on a Shimadzu FT-IR 8300 spectrometer using a potassium bromide pellet. The phase composition and the crystalline structure of MNPs were investigated by Bruker AXS D8-Advance X-ray diffractometer with Cu Kα radiation (λ = 1.5418). The magnetization of NPs was measured by using an instrument model BHV-55 vibrating sample magnetometer. The thermal stability of the catalyst was determined by thermal gravimetric analysis (TGA) using a TA Q600 device. The Field emission scanning electron microscopy (FE-SEM) image of the catalyst was performed by MIRA3 TESCAN and HITACHI S-4160, and the elemental characterization was conducted by energy-dispersive X-ray (EDX) spectroscopy accessory to FE-SEM. The Transmission Electron Microscopy (TEM) images were recorded using the Zeiss- EM10C and Philips EM208 transmission electron microscope operated at 100 kV accelerating voltage. The specific surface area of the nanocatalyst was determined through Brunauer Emmett Teller (BET) analysis measured on a Microtrac Bel Corp-Belsorp mini II device. The size distribution of the NPs was measured by the Dynamic light scatterings (DLS) technique using a HORIBA-LB 550 particle size analyzer. The loading amount of Cu in the nanocatalyst and the leaching amount were measured by the Varian Vista-pro ICP analyzer. The reaction progress and purity of the products were monitored by thin-layer chromatography (TLC) on Merck silica gels 60 F254 aluminum plates and visualized under UV light (254 nm). TLC solvent systems typically consisted of n-hexane/ethyl acetate mixtures in ratios ranging from 8:2 to 6:4 (v/v), depending on product polarity. Column chromatography was carried out on silica gel (230–400 mesh), using gradient mixtures of n-hexane/ethyl acetate as the mobile phase unless otherwise stated. Fractions were monitored via TLC, combined, and concentrated under reduced pressure. The UV-Vis absorption spectra were recorded using a PerkinElmer Lambda 25 UV-Vis spectrophotometer. The melting points of products were determined in open capillaries using an Electrothermal 9100 apparatus and were compared with literature values.
Synthesis of Fe3O4/g-C3N4/NTMPA MNC
Synthesis of Fe3O4/g-C3N4
The g-C3N4 powder was synthesized by directly heating melamine at 520 ˚C for 4 h in a tube furnace under ambient air52. The Fe3O4@g-C3N4 MNC was subsequently prepared via chemical co-precipitation. In this process, 0.125 g of g-C3N4 was dispersed in a 500-mL beaker containing ethanol/water mixture (1:2) and subjected to ultrasonic treatment for 5 h at room temperature. Then, 1.83 g of FeCl3·6 H₂O and 0.7 g of FeCl₂·4 H₂O were added to the g-C3N4 solution after being dissolved in 20 mL of distilled water separately. The mixture was stirred at 80 °C for 30 min before the gradual addition of ammonia solution (NH4OH 25%) until the pH reached 10. The reaction proceeded under continuous stirring for an additional 30 min. Upon completion, the resulting product was cooled and subjected to successive washes with ethanol and distilled water. Finally, the product was dried at 80 °C53.
Synthesis of Fe3O4/g-C3N4/NTMPA MNC
An amount of 0.25 g of Fe3O4/g-C3N4 was dispersed in 10 mL of distilled water. Meanwhile, NTMPA (0.23 g, in a 1:1 molar ratio relative to the initially used melamine) was dissolved in 5 mL of distilled water and subsequently introduced into the suspension. The mixture was stirred for 3 h at room temperature. The resulting brown precipitate was then separated using an external magnetic field, washed thoroughly with deionized water and ethanol, and dried at 60 °C for 5 h.
General procedure for the synthesis of amides via the Ritter reaction using Fe3O4/g-C3N4/NTMPA as a heterogeneous acid catalyst
To a mixture of nitrile (1.0 mmol) and alcohol (1.0 mmol), 0.06 g of the acid catalyst Fe3O4/g-C3N4/NTMPA was added, and the reaction mixture was stirred at 80 °C under solvent-free conditions for the appropriate time. The progress of the reaction was monitored by TLC using n-hexane/ethyl acetate as the eluent. Upon completion, ethanol was added to the reaction mixture to dissolve the precipitated amide product, leaving the catalyst behind as a brown, ethanol-insoluble solid. The catalyst was magnetically separated from this ethanolic solution and washed with ethanol. The two ethanolic solutions were then combined and evaporated under reduced pressure. The crude product, obtained as a solid, was purified either by recrystallization from ethanol or ethanol/water mixtures depending on product solubility or by column chromatography using silica gel and a gradient mixture of n-hexane/ethyl acetate (from 8:2 to 6:4). The structures of pure products were identified by comparing their melting point, FT-IR and ¹H- and C-NMR NMR spectra with those have been reported in the literature.
Characteristic data for N-(1-phenylethyl)benzamide (3a) (Table 3, entry 1): White solid; Yield: 95%; Mp:104–106 °C; FT-IR (KBr) ῡ: 3356.6, 3057.9, 2973.0, 2929.9, 1634.6, 1602.9, 1521.7, 1451.5, 1361.8, 1321.9, 1073.9, 760.6, 700.6 cm− 1; 1H NMR (400 MHz, CDCl3) δ: 1.63 (d, J = 6.8 Hz, 3 H), 5.37 (m, 1H), 6.36 (s, 1H), 7.28–7.34 (m, 2 H), 7.41–7.36 (m, 3 H), 7.44–7.49(m, 2 H), 7.47–7.53 (m, 1H), 7.80 (d, J = 7.3 Hz, 2 H) ppm; 13C NMR (100 MHz, CDCl3) δ: 21.8, 49.2, 126.4, 126.9, 127.5, 128.6, 128.8, 131.5, 134.5, 143.1, 166.6 ppm.
Table 3.
Synthesis of amides via Ritter reaction using Fe3O4/g-C3N4/NTMPA MNC.
|
| ||||||||
|---|---|---|---|---|---|---|---|---|
| Entry | Alcohol | Nitrile | Product | Time (h) | Yieldb (%) | TONc | TOFd | M.P.e/˚C (Ref.) |
| 1 |
|
|
|
5.0 | 95 | 15.83 | 3.17 | 104–106 (104–106)56 |
| 2 |
|
|
|
4.5 | 93 | 15.50 | 3.44 | 153–155 (152–154)57 |
| 3 |
|
|
|
5.5 | 92 | 15.33 | 2.79 | 75–77 (75–77)58 |
| 4 |
|
|
|
5.5 | 90 | 15.00 | 2.73 | 70–72 (70–72)58 |
| 5 |
|
|
|
5.25 | 92 | 15.33 | 2.92 | 138–140 (136–139 )59 |
| 6 |
|
|
|
5.5 | 92 | 15.33 | 2.79 | 163–164 (162–165 )57 |
| 7 |
|
|
|
6.0 | 86 | 14.33 | 2.39 | 148–151 (156–157)57 |
| 8 |
|
|
|
4.5 | 94 | 15.67 | 3.48 | 134–137 (136–139)60 |
| 9 |
|
|
|
4.75 | 91 | 15.17 | 3.19 | 208–210 (208–210)61 |
| 10 |
|
|
|
4.0 | 93 | 15.50 | 3.87 | 148–150 (148–150)57 |
| 11 |
|
|
|
5.5 | 93 | 15.050 | 2.82 | 104–106 (106–108)57 |
| 12 |
|
|
|
5.5 | 91 | 15.17 | 2.76 | 108–110 (110–111)57 |
| 13 |
|
|
|
3.0 | 97 | 16.17 | 5.39 | 130–133 (131–133)62 |
| 14 |
|
|
|
4.0 | 95 | 15.83 | 3.96 | 137–139 (136–137)8 |
| 15 |
|
|
|
3.5 | 95 | 15.83 | 4.52 | 131–133 (131–133)8 |
| 16 |
|
|
|
5.0 | 82 | 13.67 | 2.74 | 103–106 (104–105)8 |
| 17 |
|
|
|
5.5 | 86 | 14.33 | 2.61 | 156–157 (156–157)63 |
| 18 |
|
|
|
6.0 | 90 | 15.00 | 2.50 | 108–110 (112 °C)57 |
| 19 |
|
|
|
6.5 | 86 | 14.33 | 2.20 | 120–123 (120–123)57 |
| 20 |
|
|
|
1.25 | 98 | 16.33 | 13.06 | 159–161 (158–163)64 |
| 21 |
|
|
|
1.50 | 97 | 16.17 | 10.78 | 148–150 (148–150)21 |
| 22 |
|
|
|
1.75 | 96 | 16.00 | 9.14 | 145–147 (144–145)8 |
| 23 |
|
|
|
2.0 | 87 | 14.50 | 7.25 | 119–122 (119–120)57 |
| 24 |
|
|
|
2.0 | 92 | 15.33 | 7.66 | 156–158 (156–158)8 |
| 25 |
|
|
|
2.0 | 85 | 14.17 | 7.08 | 123–125 (123–125)57 |
aReaction conditions: Alcohol (1mmol), nitrile (1mmol), Fe3O4/g-C3N4/NTMPA MNC (0.06 g), 80 °C, solvent-free.
bIsolated yield.
cmmol product / g catalyst.
d(mmol product / g catalyst)/ h.
eThe melting point of the products was compared to those in the literature.
Results and discussion
As described in the experimental section, the synthesis of Fe3O4/g-C3N4/NTMPA was performed through three steps as illustrated in Fig. 3.
Fig. 3.
The preparation steps of Fe3O4/g-C3N4/NTMPA MNC.
Characterization of the Fe3O4/g-C3N4/NTMPA MNC
FT-IR analysis
The FT-IR spectra of (a) NTMPA, (b) g-C3N4 powder, (c) Fe3O4/g-C3N4, and (d) the Fe3O4/g-C3N4/NTMPA MNC are depicted in Fig. 4. The IR spectrum of NTMPA shows sharp band at 900–1000 cm− 1 that belongs to asymmetric stretching vibrations of the P-OH group. Peak at 1150 cm− 1 corresponds to P = O stretching, and a weak peak around 3500 cm− 1 is attributed to O-H stretching (Fig. 4a)42. In the FT-IR spectrum of g-C3N4 (Fig. 4b), a broad absorption band observed in the range of 3000–3400 cm− 1 is indicative of the stretching vibrations associated with NH and NH2 functional groups present in the g-C3N4 framework. Furthermore, the bands appearing within the range of 1230–1640 cm− 1 are attributed to the stretching modes of carbon-nitrogen (C-N) bonds, encompassing both single and double bonds in the g-C3N4 structure51. A distinctive feature for the identification of graphitic carbon nitride is the sharp peak at 815 cm− 1, which can be assigned to the vibrational modes of the s-triazine ring51. In the spectrum of Fe3O4/g-C3N4 (Fig. 4c), a pronounced peak at 570 cm− 1 corresponds to the Fe-O stretching vibrations characteristic of Fe3O4. The FT-IR spectrum of the Fe3O4/g-C3N4/NTMPA MNC (Fig. 4d) exhibits characteristic peaks consistent with those observed for Fe3O4/g-C3N4, exhibiting a slight shift due to interactions. Notably, peaks around 950 and 1150 cm− 1 are associated with P-OH and P = O stretching vibrations, respectively. Additionally, a broad band at 3500 cm− 1 is detected, which is indicative of O-H stretching vibrations34.
Fig. 4.
FT-IR spectra of (a) NTMPA, (b) g-C3N4, (c) Fe3O4/g-C3N4, and (d) Fe3O4/g-C3N4/NTMPA, and XRD patterns of (e) Fe3O4 (f) Fe3O4/g-C3N4, and (g) Fe3O4/g-C3N4/NTMPA.
XRD analysis
Figure 4e-g illustrate the XRD patterns for (a) Fe3O4 (Fig. 4e), (b) Fe3O4/g-C3N4 (Fig. 4f), and (c) Fe3O4/g-C3N4/NTMPA (Fig. 4g). All three samples exhibit distinct diffraction peaks at 2θ values of 30.4°, 35.5°, 43.6°, 53.4°, 57.0°, and 62.8°, corresponding to the (220), (311), (400), (422), (511), and (440) indices, respectively. These peaks confirm the presence of the cubic spinel structure of Fe3O4, consistent with standard magnetite XRD patterns reported in the literature (Fig. 4e)34. The XRD patterns of Fe3O4/g-C3N4 (Fig. 4f) and Fe3O4/g-C3N4/ NTMPA (Fig. 4g) exhibit a broad, featureless peak at low diffraction angles (2θ = 10–20°), indicative of the amorphous nature of g-C3N434. These findings indicate that the surface functionalization of Fe3O4 NPs does not induce any phase transformation. The reduced intensity of the diffraction peaks in the composite samples compared to the bare Fe3O4 is likely due to the g-C3N4 coating.
FE-SEM, TEM and DLS analyses
The SEM image of bulk g-C3N4 illustrates the microstructure and surface morphology of this layered compound (Fig. 5a). The g-C3N4 exhibits a solid agglomerate form with particle sizes ranging from hundreds of nanometers to several micrometers, characterized by a crumpled sheet-like structure (Fig. 5a). The FE-SEM images of Fe3O4/g-C3N4 and Fe3O4/g-C3N4/NTMPA are depicted in Fig. 5b,c, respectively. The surface characteristics and morphology of these MNCs were assessed using FE-SEM micrographs, which reveal a two-dimensional (2D) lamellar structure with well-dispersed spherical particles. These micrographs indicate uniformity in the Fe3O4/g-C3N4 and Fe3O4/g-C3N4/NTMPA MNCs with average particle sizes of approximately 10–12 nm and 17–22 nm, respectively (Fig. 5b,c).
Fig. 5.
SEM image of (a) Bulk-g-C3N4, and FE-SEM images (b) Fe3O4/g-C3N4, and (c) Fe3O4/g-C3N4/NTMPA.
The evaluation of TEM micrographs for the Fe3O4/g-C3N4/NTMPA MNC clearly shows the presence of attached NTMPA molecules and the deposition of dark Fe3O4 NPs on the surfaces of g-C3N4 (Fig. 6a,b). Furthermore, the transparent, thin, sheet-like structure of g-C3N4 is observable in the TEM images confirming the 2D morphology observed in FE-SEM.
Fig. 6.
TEM images of (a,b) Fe3O4/g-C3N4/NTMPA MNC, and (c) the size distribution of Fe3O4/g- C3N4/NTMPA.
DLS technique was also used to determine the hydrodynamic diameter of particle size. The size distribution of Fe3O4/g-C3N4/NTMPA MNC is centered at a value of 34 nm (Fig. 6c). The DLS result further confirms the presence of nanoscale particles, which aligns with the observations obtained from FE-SEM and TEM analyses, indicating the successful synthesis of the MNC and its uniform dispersion in the solvent. This is critical for evaluating the material’s potential applications in catalysis and nanotechnology54.
EDX analysis
The purity of the Fe3O4/g-C3N4/NTMPA MNC was confirmed through the EDX spectrum with weight% and atom% values of the synthesized MNC. As illustrated in Fig. 7a, the distinct peaks indicate the presence of the expected elements. The spectrum for the Fe3O4/g-C3N4/NTMPA MNC exhibits characteristic peaks for nitrogen (N), oxygen (O), phosphorus (P), carbon (C), and iron (Fe) (Fig. 7a). These results confirm the successful integration of Fe3O4 and NTMPA into the graphitic carbon nitride framework. Moreover, elemental mapping performed via EDX analysis provides insight into the spatial distribution of these elements within the MNC. The mapping results demonstrate a homogeneous distribution of Fe, C, N, O, and P throughout the sample, indicating a well-dispersed composite structure (Fig. 7b). This uniform distribution is critical for enhancing the catalytic properties of the MNC, as it ensures optimal interaction between the components during chemical reactions.
Fig. 7.
(a) EDX spectrum of Fe3O4/g-C3N4/NTMPA MNC and (b) the element mapping of Fe3O4/g-C3N4/NMPA MNC.
BET and BJH analyses
The data obtained from the BET and BJH analyses of the synthesized Fe3O4/g-C3N4/NTMPA MNC are presented in Table 1. The BET surface area was measured at 11.421 m2/g, indicating a significant potential for adsorption applications. The total pore volume at a relative pressure (p/p0) of 0.990 was determined to be 0.0588 cm3/g, reflecting the material’s capacity to accommodate various substances within its pore structure. Additionally, the mean pore diameter was calculated to be 20.593 nm, suggesting a mesoporous structure conducive to enhanced diffusion and accessibility for reactants.
Table 1.
Surface area and pore size measurements of Fe3O4/g-C3N4/NTMPA MNC.
| BET plot | ||
| V m | 2.6241 | [cm3(STP) g−1] |
| as, BET | 11.421 | [m2 g−1] |
| Total pore volume(p/p0 = 0.990) | 0.0588 | [cm3 g−1] |
| Mean pore diameter | 20.593 | |
| BJH plot | ||
| Vp | 0.059142 | [cm3 g−1] |
| rp, peak(Area) | 1.21 | |
| ap | 13.543 | [m2 g−1] |
In conjunction with the BJH analysis, the total pore volume was found to be 0.059142 cm³/g, with the peak pore radius at 1.21 nm. The BJH adsorption surface area was calculated to be 13.543 m2/g, which highlights the effectiveness of the synthesized MNC in providing ample active sites for chemical interactions. The combination of a high surface area and optimal pore structure suggests that the Fe3O4/g-C3N4/NTMPA MNC exhibits promising characteristics for various applications, including catalysis, adsorption, and drug delivery.
TGA and VSM analyses
The thermal properties of the Fe3O4/g-C3N4/ NTMPA MNC was investigated using TGA and DSC as shown in Fig. 8. TGA is an analytical technique commonly employed to assess a material’s thermal stability by monitoring changes in weight as the MNC is heated at a controlled rate. In this study, the thermal stability of the Fe3O4/g-C3N4/NTMPA nanocomposite was evaluated by heating the sample from 0 to 800 °C at a rate of 20 °C/min.
Fig. 8.
(a) Thermogravimetric analysis of Fe3O4/g-C3N4/NTMPA, (b) DSC of Fe3O4/g-C3N4/NTMPA, magnetization curves of (c) Fe3O4/g- C3N4, (d) Fe3O4/g- C3N4/NTMPA MNC, and (e) magnetically separation property of Fe3O4/g- C3N4/NTMPA MNC.
The TGA curve (Fig. 8a) exhibited a two-step thermal decomposition process. The initial weight loss observed in the range of 100–300 °C, which be attributed to the evaporation of physically adsorbed solvents, the desorption of moisture, and the removal of surface hydroxyl groups along with potential intermolecular condensation of phosphonic acid units55. The second major weight loss, 23.88%, occurs between 500 and 600 °C, which corresponds to the decomposition of g-C3N4 sheets. Notably, the loading of Fe3O4 and NTMPA onto the g-C3N4 sheets leads to a decrease in thermal stability compared to pristine g-C3N4, which is happened from 609 to 761 °C. This reduction in thermal stability may result from the combination of NTMPA, the iron oxide, and the g-C3N4 matrix, which alters the decomposition pathway.
The DSC analysis, shown in Fig. 8b, provides crucial information about the thermal behavior of Fe3O4/g-C3N4/NTMPA MNCs. The DSC curve reveals multiple thermal transitions, indicating the material’s thermal stability and composition. The first endothermic peak observed at 125.88 °C is attributed to the removal of adsorbed water or other volatile substances from the composite, a typical behavior for materials containing organic components. The subsequent endothermic transition at 261.97 °C is associated with the intermolecular condensation of phosphonic acid units, which begins to decompose at this temperature. A more prominent endothermic peak at 331.07 °C corresponds to further decomposition, likely of the NTMPA component, as it breaks down at higher temperatures. These thermal events provide valuable insight into the material’s stability under thermal stress, confirming that the Fe3O4/g-C3N4/NTMPA MNC can withstand elevated temperatures before significant degradation occurs. This characteristic is essential for its potential use in high-temperature catalytic reactions, as it indicates that the catalyst will maintain structural integrity and performance during prolonged exposure to heat.
The VSM analysis presented in Fig. 8c,d reveals the magnetic properties of the Fe3O4/g-C3N4 and Fe3O4/g-C3N4/NTMPA MNCs. Both composites exhibit typical superparamagnetic behavior, with the Fe3O4/g-C3N4/NTMPA MNC (Fig. 8d) showing a slightly enhanced magnetization relative to Fe3O4/g-C3N4 (Fig. 8c). The saturation magnetization values for the Fe3O4/g-C3N4 and Fe3O4/g-C3N4/NTMPA MNCs are approximately 40 emu/g and 45 emu/g, respectively. This indicates that the Fe3O4/g-C3N4/NTMPA MNC possesses a marginally higher magnetization, which is beneficial for magnetic separation applications. Such properties are advantageous for catalytic applications, particularly in enabling the easy recovery of the catalyst from reaction mixtures, as demonstrated by the visual evidence in Fig. 8e. The VSM analysis confirms that the Fe3O4/g-C3N4/NTMPA MNC retains adequate magnetic properties for effective recovery, making it a promising candidate for recyclable catalysis in industrial processes.
Catalytic performance of Fe3O4/g-C3N4/NTMPA MNC for amide synthesis via the Ritter reaction
The Ritter reaction is a pivotal method for the formation of carbon-nitrogen bonds and is widely applied in the synthesis of amides, which serve as key intermediates in pharmaceutical and medicinal chemistry16. Traditionally, the reaction involves the interaction between nitriles and benzylic or tertiary alcohols, facilitated by concentrated sulfuric acid, a process known as the classical Ritter reaction. Due to the harsh conditions and corrosive nature of this method, numerous alternative approaches have been explored to develop milder and more environmentally friendly reaction conditions16. Consequently, there is a strong demand for efficient, sustainable, and versatile catalysts that can perform under milder conditions while maintaining high yields and selectivity.
Table 2 presents the optimization of reaction conditions for the Ritter reaction, highlighting the effect of various factors such as catalyst amount, solvent choice, reaction time, and temperature on the yield of amides.
Table 2.
Optimization of reaction conditions for the model reaction.
|
| ||||||
|---|---|---|---|---|---|---|
| Entry | Catalyst | Amount (g) | Solvent | Temp. (°C) | Time (h) | Yield (%)b |
| 1 | Fe3O4/g-C3N4/NTMPA | 0.06 | n-Hexane | Reflux | 24 | 10 |
| 2 | Fe3O4/g-C3N4/NTMPA | 0.06 | CH2Cl2 | Reflux | 24 | 20 |
| 3 | Fe3O4/g-C3N4/NTMPA | 0.06 | H2O | Reflux | 8 | 72 |
| 4 | Fe3O4/g-C3N4/NTMPA | 0.06 | Toluene | 80 | 8 | 78 |
| 5 | Fe3O4/g-C3N4/NTMPA | 0.06 | THF | Reflux | 24 | 15 |
| 6 | Fe3O4/g-C3N4/NTMPA | 0.06 | DMF | 80 | 24 | Trace |
| 7 | Fe3O4/g-C3N4/NTMPA | 0.06 | CHCl3 | Reflux | 24 | 18 |
| 8 | Fe 3 O 4 /g-C 3 N 4 /NTMPA | 0.06 | Solvent-free | 80 | 5 | 95 |
| 9 | Fe3O4/g-C3N4/NTMPA | ----- | Solvent-free | 80 | 24 | Trace |
| 10 | NTMPA | 0.035 | Solvent-free | 80 | 5 | 92 |
| 11 | Fe3O4/g-C3N4/NTMPA | 0.03 | Solvent-free | 80 | 5 | 55 |
| 12 | Fe3O4/g-C3N4/NTMPA | 0.09 | Solvent-free | 80 | 5 | 95 |
| 13 | Fe3O4/g-C3N4/NTMPA | 0.12 | Solvent-free | 80 | 5 | 88 |
| 14 | Fe3O4/g-C3N4/NTMPA | 0.06 | Solvent-free | R.T | 12 | 50 |
| 15 | Fe3O4/g-C3N4/NTMPA | 0.06 | Solvent-free | 110 | 6 | 78 |
| 16 | g-C3N4 | 0.01 | Solvent-free | 80 | 5 | --- |
| 17 | Fe3O4 | 0.01 | Solvent-free | 80 | 5 | --- |
| 18 | Fe3O4@g-C3N4 | 0.02 | Solvent-free | 80 | 5 | --- |
aReaction conditions: 1-Phenylethanol (1a) (1.0 mmol, 0.12 mL), benzonitrile (2a) (1.0 mmol, 0.1 mL), Fe3O4/g-C3N4/NTMPA MNC, and solvent (2.0 mL).
bIsolated yield.
Optimization was performed using 1-phenylethanol (1a) and benzonitrile (2a) as a model system. The first set of experiments was conducted using a fixed catalyst amount (0.06 g) with different solvents. Solvent choice significantly influenced the reaction efficiency. N-hexane (Table 2, entry 1) and CH2Cl2 (Table 2, entry 2) under reflux conditions resulted in low yields of 10% and 20%, respectively, even after 24 h of reaction time. Using water as a solvent (Table 2, entry 3) improved the yield to 72% with a reduced reaction time of 8 h. This suggests that the polarity of water aids in better reaction efficiency. Toluene (Table 2, entry 4) at 80 °C further increased the yield to 78%, indicating that higher temperatures and moderate polarity solvents enhance performance. THF (Table 2, entry 5) and CHCl3 (Table 2, entry 7) showed similarly low yields (15 and 18%, respectively) as non-polar solvents, emphasizing the importance of solvent selection for optimal reaction conditions. DMF (Table 1, entry 6) resulted in only trace product formation, likely due to its high boiling point, which could be detrimental to this reaction under the given conditions. The solvent-free reaction at 80 °C (Table 2, entry 8) produced a highly significant yield of 95% within just 5 h, demonstrating that eliminating the solvent improves both reaction efficiency and yield. This condition was selected as the best option, which avoids the use of harmful solvents, making the process greener and more cost-effective. In the next step of optimization, the role of the catalyst under solvent-free conditions at 80 °C was explored. Running the reaction without any catalyst (Table 2, entry 9) resulted in only trace amounts of product, confirming the critical role of the Fe3O4/g-C3N4/NTMPA MNC catalyst in the reaction. A slight reduction in the catalyst amount (0.03 g) (Table 2, entry 11) decreased the yield to 55% while increasing the amount to 0.09 g (Table 2, entry 12) resulted in the same maximum yield of 95% as 0.06 g (Table 2, entry 8). A further increase to 0.12 g (Table 2, entry 13) led to a slight drop in yield (88%), indicating that increasing the catalyst beyond 0.09 g may not significantly enhance the reaction but instead decrease the efficiency, possibly due to agglomeration or other factors. Also, using NTMPA alone as a homogeneous acid catalyst provided excellent yields (Table 2, entry 10) but lacked the recyclability of the MNC, which is a key feature aligned with green chemistry principles. The recyclability of the Fe3O4/g-C3N4/NTMPA MNC makes it a valuable catalyst in sustainable chemistry. So, 0.06 g was chosen as the best optimum amount of Fe3O4/g-C3N4/NTMPA for the reaction.
Temperature optimization revealed that 80 °C was ideal for maximizing conversion, producing a 95% yield within 5 h (Table 2, entry 8). Also, performing the reaction at room temperature (R.T) (Table 2, entry 14) for 12 h yielded only 50%, indicating that heat plays a crucial role in driving the reaction forward. Increasing the temperature to 110 °C (Table 2, entry 15) resulted in a 78% yield after 6 h, suggesting that while higher temperatures accelerate the reaction, they may not necessarily produce a better yield compared to the optimized condition at 80 °C (Table 2, entry 8). The reaction was also repeated at 80 °C for 5 h in the presence of g-C3N4, Fe3O4, and Fe3O4@C3N4 separately, which are the precursor components of the catalyst, in order to evaluate their individual contributions to the catalytic activity. TLC monitoring of these reactions revealed that all starting materials remained intact (Table 2, entries 16–18).
The optimal conditions for the Ritter reaction were identified as follows: 0.06 g of Fe3O4/g-C3N4/NTMPA, solvent-free at 80 °C, and a reaction time of 5 h. These conditions deliver excellent yields while minimizing environmental impact through the use of a recyclable catalyst and eliminating the need for solvents. The MNC’s performance under these conditions highlights its potential for scalable and sustainable amide synthesis.
After determining the optimized conditions, the capability of the catalyst in preparing a range of amide derivatives was explored. Table 3 provides the results for the synthesis of a diverse array of amide derivatives through the Ritter reaction under solvent-free conditions, catalyzed by Fe3O4/g-C3N4/NMPA at 80 °C. The study examines various alcohol substrates, including benzylic, tertiary, primary, allylic, and diphenyl alcohols (1a–1 h) and nitriles (2a–2i) as starting substrates to produce their corresponding amide products (Table 3, entries 1–25) with the yields predominantly exceeding 80%, indicating the efficacy of the catalyst in promoting the formation of amides. The catalytic activity was further quantified by determining the turnover number (TON) and turnover frequency (TOF) under optimized conditions, with the calculated values confirming the high intrinsic efficiency of the Fe3O4/g-C3N4/NTMPA system in promoting the Ritter reaction.
Regarding alcohols, 1-phenylethanol (1a) yielded amides (3a-3 g) with excellent yields, with most reactions completing within 4.5–6 h (Table 3, entries 1–7). (4-Chlorophenyl) methanol (1b) incorporates an electron resonance-donating chlorine substituent at the para position, yielding similar efficiency with amide products (3 h-3 L) and yields ranging from 91 to 94% within 4–5.5 h (Table 3, entries 8–12). 2-Methylpropan-2-ol (1c) exhibited exceptionally high yields (up to 97%) with shorter reaction times (3–4 h) across several nitrile substrates to produce related amides (3 m-3o). The stability of the tertiary carbocation intermediates contributes to the enhanced reactivity (Table 3, entries 13–15). Phenylmethanol (1d), a primary alcohol, resulted in an amide product (3p) with a respectable yield of 82% over a reaction time of 5 h. The absence of electron-withdrawing or donating groups on the phenyl ring suggests that this substrate provides a baseline reactivity (Table 3, entry 16). The presence of the electron-withdrawing nitro group on the para position of the phenyl ring significantly decreases the reactivity of (4-nitrophenyl) methanol (1e). This resulted in a yield of 86% (3q) over a slightly higher reaction time of 5.5 h. The nitro group destabilizes the carbocation, decreasing the tendency of nitrile attack (Table 3, entry 17). The o-tolyl methanol substrate (1f), which contains a methyl group in the ortho position relative to the hydroxyl group, produced an amide (3r) with a yield of 90% after 6 h. The presence of the methyl group, an electron-donating substituent, seems to affect the reaction time, likely through stabilization of the carbocation intermediate. The yield reflects the balance between steric hindrance from the ortho substituent and the overall electronic effects, showcasing that even with substituents that could hinder reactivity, the reaction remains efficient (Table 3, entry 18). The allylic alcohol, prop-2-en-1-ol (1 g), resulted in a yield of 86% for amide product (3s) after 6.5 h. The reaction may proceed through the formation of a more stable carbocation due to the allylic nature of the alcohol. While the yield is slightly lower than some of the other entries, it still demonstrates the high potential of this substrate in the Ritter reaction (Table 3, entry 19). Diphenylmethanol (1 h) was particularly effective, producing high yields of products (3t-3y) ranging from 85 to 98% across a variety of nitriles with remarkably short reaction times (1.25–2 h). The structure of diphenylmethanol, with its two phenyl rings, increases the stability of the carbocation intermediate formed during the Ritter reaction, leading to improved reaction efficiency (Table 3, entries 20–25).
In respect of nitriles, most reactions with aromatic nitriles were completed within 5–6 h and yielded high percentages (generally above 90%). This trend underscores the effectiveness of aromatic nitriles in the Ritter reaction. Benzonitrile, as a baseline nitrile, produced good yields across various alcohol substrates. Nitriles like 4-(trifluoromethyl)benzonitrile exhibited excellent yields, demonstrating the positive influence of electron-withdrawing groups on reactivity (Table 3, entry 2). Nitriles bearing electron-donating groups have less electrophilicity, resulting in a slightly longer reaction time (Table 3, entries 4–7). Entries featuring aliphatic nitriles (like acetonitrile and butyronitrile) showed that while they are less effective compared to their aromatic counterparts, they still provided acceptable yields when reacted with appropriate alcohols (Table 3, entries 3, 4, 11, 12, 21, 22, 23 and 25).
As a result, the Fe3O4/g-C3N4/NTMPA catalyst exhibited remarkable efficiency in promoting the Ritter reaction, providing high yields across a wide range of alcohol and nitrile substrates. Its ability to facilitate reactions under mild, solvent-free conditions further highlights its potential as a versatile and environmentally friendly catalyst for organic transformations.
The plausible mechanism of the Ritter reaction for the synthesis of amides from alcohols and nitriles catalyzed by the Fe3O4/g-C3N4/NTMPA MNC involves several key steps as follows (Fig. 9). In the first step, the Fe3O4/g-C3N4/NTMPA catalyst protonates and helps subsequent dehydration of the alcohol I, forming a highly reactive carbocation II. This step is particularly favorable due to the catalyst’s acidic sites, which enhance the formation of the carbocation intermediate. The nitrile undergoes nucleophilic addition to the carbocation, forming an intermediate nitrilium ion III, which is converted to the amide by reacting with the produced water in situ via the intermediate IV and regenerates the catalyst62,64.
Fig. 9.
A plausible mechanism of amid formation via the Ritter reaction catalyzed by Fe3O4/g-C3N4/NTMPA MNC.
The MNC’s ability to be recycled and reused is crucial in light of both environmental and economic concerns. We assessed the magnetically heterogeneous Fe3O4/g-C3N4/NTMPA MNC performance, which has been effectively applied in subsequent reactions. Therefore, under optimum model reaction conditions, the MNC’s recyclability was investigated. Under solvent-free conditions at 80 °C, the MNC catalyst (0.06 g) catalyzed the Ritter reaction between 1-phenylethanol (1a) (1.0 mmol), and benzonitrile (2a) (1.0 mmol). After the reaction was finished, the MNC was separated from the reaction mixture using an external magnetic field, demonstrating both the MNC’s magnetic behavior and its ease of retrieval. After being thoroughly washed with ethanol and deionized water, the MNC was dried for 5 h at 60 °C before being used for the subsequent reactions under optimal conditions. The recovered MNC demonstrated steady activity in the reaction during seven runs, as seen in Fig. 10a. Fe3O4/g-C3N4/NTMPA has remarkable stability and recyclability up to six cycles, as indicated by the favorable yields of the isolated product.
Fig. 10.
(a) Recyclability of Fe3O4/g-C3N4/NTMPA MNC (Reaction conditions: 1-phenylethanol (1a) (1.0 mmol), benzonitrile (2a) (1.0 mmol), 0.06 g Fe3O4/g-C3N4/NTMPA NMC, solvent-free conditions at 80 °C); (b) TEM and (c) FE-SEM images of the recovered Fe3O4/g-C3N4/NTMPA MNC after 6 cycles of reaction.
The TEM and FE-SEM images were recorded after seven runs of the reaction to demonstrate the size and morphology of the Fe3O4/g-C3N4/NTMPA nanocomposite (Fig. 10b and c). The analysis of TEM micrographs for the Fe3O4/g-C3N4/NTMPA demonstrates the deposition of dark Fe3O4 NPs on the surfaces of g-C3N4 as well as the presence of NTMPA molecules (Fig. 10b). The SEM image depicts that the surface morphology of the Fe3O4/g-C3N4/NTMPA did not significantly alter after being used in six cycles of reaction, demonstrating the nanocatalyst’s stability and identity (Fig. 10c).
There are distinctive peaks for N, O, P, C, and Fe along with weight% and atom% values in the EDX spectrum for the recovered Fe3O4/g-C3N4/NTMPA NMC, which indicates the maintained elemental composition of the MNC after the recovery process (Fig. 11a). In comparison to the fresh MNC, which has an average size of 34 nm (Fig. 6c), the DLS analysis results show a little increase in the size of the reused MNC, with an average size of 36 nm, which suggests a small amount of NP aggregation during the recycling processes (Fig. 11b). The excellent deposition of Fe3O4 NPs and preservation of the crystalline structure during the reusing process are confirmed by the similarity of the XRD characteristic peaks in the reused MNC (Fig. 11c) to that in the fresh MNC (Fig. 4f). The recovered MNC’s FT-IR spectrum also shows the primary vibration bands associated with the Fe-O, P-O, C-N, and O-H bonds at 570, 1250, 1630, and 3400 cm− 1, respectively (Fig. 11d). The preserved structure of the MNC is confirmed by the similar bands in the recovered (Fig. 11d) and fresh MNC (Fig. 4c).
Fig. 11.
(a) EDX image; (b) DLS image; (c) XRD pattern; and (d) FT-IR spectrum of Fe3O4/g-C3N4/NTMPA MNC after six reaction cycles.
A comparative study of catalysts for the preparation of amides through the Ritter reaction was conducted, highlighting the efficiency, reaction conditions, yield, and reusability of six catalysts (Table 4). Al(HSO4) 3 (0.16 g) produced a moderate yield of 85% under reflux with CH3NO₂ in 2.5 h but lacked reusability (Table 4, entry 1). Multiwalled carbon nanotube bearing a p-toluenesulfonyl group (MWCNT-CSP) (0.05 g) demonstrated a low yield of 50% at 100 °C, requiring a prolonged reaction time of 24 h, indicating limited efficiency (Table 4, entry 2). Fe(NO3) 3·9 H₂O (0.2 g), under milder conditions at 80 °C, delivered a high yield of 96% in 3 h but was not reusable (Table 4, entry 3). Pentafluorophenylammonium triflate (PFPAT) (0.028 g), notable for its low catalyst loading and solvent-free conditions at 90 °C, achieved a good yield of 92% in 3 h (Table 4, entry 4). The γ-Fe₂O3@SiO₂-HClO4 (0.05 g) stood out with a yield of 97% under neat conditions at room temperature in 3 h and demonstrated reusability for five cycles, highlighting its stability and energy efficiency (Table 4, entry 5). Finally, Fe3O4/g-C3N4/NTMPA MNC (0.12 g) showed the best overall performance, achieving the highest yield of 98% in the reaction time of 5 h under solvent-free conditions at 80 °C. Moreover, it demonstrated excellent reusability over six cycles (Table 4, entry 6). This comparison underscores Fe3O4/g-C3N4/NMPA’s superiority in efficiency, sustainability, and practicality, making it a promising catalyst for the Ritter reaction.
Table 4.
Brief report of the efficiency of catalysts published in the literature and Fe3O4/g-C3N4/NTMPA MNC for the Preparation of amide 3a through the Ritter reaction.
| Entry | Catalyst | Reaction Conditions | Time (h) | Yielda (%) | Cycleb | Refs. |
|---|---|---|---|---|---|---|
| 1 | Al(HSO4)3 (0.16 g) | CH3NO2/reflux | 2.5 | 85 | 0 | 62 |
| 2 | MWCNT-CS (0.05 g) | 100 °C | 24 | 50 | 0 | 21 |
| 3 | Fe(NO3)3.9H2O (0.2 g)c | 80 °C | 3 | 96 | 0 | 58 |
| 4 | PFPAT (0.028 g) | Solvent free/90 °C | 3 | 92 | 0 | 65 |
| 5 | γ-Fe2O3@SiO2-HClO4 (0.05 g) | Neat condition/R.T | 3 | 97 | 5 | 66 |
| 6 | Fe3O4/g-C3N4/NTMPA (0.12 g) | Solvent free/80 °C | 5 | 98 | 6 | This work |
1-Phenylethanol (1a) (1.0 mmol) and benzonitrile (2a) (1.0 mmol) were used as substrates unless otherwise stated.
aIsolated yield.
bNumber of cycles reusing the catalyst.
c1-Phenylethanol (0.5 mmol) and benzonitrile (30 mmol) were used.
Conclusion
The Fe3O4/g-C3N4/NTMPA magnetic nanocomposite developed in this work demonstrates strong potential as a heterogeneous solid acid catalyst for green amide synthesis via the Ritter reaction. Comprehensive structural analyses (FT-IR, XRD, FE-SEM, TEM, DLS, BET, TGA, and EDX) confirmed the successful assembly of a thermally stable, uniformly functionalized composite containing Fe, C, N, O, and P. Catalytic evaluations revealed that the MNC efficiently promotes carbocation formation even under solvent-free and mild conditions, enabling high conversions for a wide variety of alcohols and nitriles. Notably, tertiary alcohols afforded yields up to 97%, while benzylic and diarylmethyl alcohols produced amides in 82–98% yields across relatively short reaction times. This performance highlights the catalyst’s ability to maintain homoselectivity—that is, selective activation of the alcohol substrate without promoting undesirable side reactions such as rearrangements, over-alkylation, or hydrolysis—due to the controlled acidity provided by NTMPA and the stable microenvironment created by the g-C3N4 matrix. The catalyst further exhibited excellent operational stability, preserving more than 90% of its activity over six consecutive cycles with negligible structural degradation. This behavior confirms that the reaction proceeds via a true heterogeneous pathway, supported by post-reaction FT-IR, XRD, DLS, and EDX analyses showing no detectable leaching of active species. These attributes—high efficiency, substrate compatibility, structural robustness, and magnetic recoverability—position Fe3O4/g-C3N4/NTMPA as a compelling alternative to conventional homogeneous acids in sustainable amide synthesis.
This NTMPA-functionalized magnetic nanocomposite can be explored in future studies, for broader catalytic applications beyond the Ritter reaction, particularly in other acid-catalyzed organic transformations such as esterification, dehydration, and multicomponent reactions. Detailed kinetic and mechanistic investigations, including computational studies, could provide deeper insight into the role of NTMPA and the Fe3O4/g-C3N4 interface in facilitating carbocation formation. Furthermore, scaling up the process and evaluating catalyst performance in continuous-flow or industrially relevant conditions would enhance its practical applicability. The structural flexibility of NTMPA also opens opportunities to design next-generation phosphonic acid-based magnetic nanocatalysts with tunable acidity and improved recyclability.
Supplementary Information
Below is the link to the electronic supplementary material.
Acknowledgements
We thank the Shiraz University Research Council for the financial support of this work.
Author contributions
H.K.: Resources, Validation, Data Curation, Visualization. Methodology, Formal analysis, Investigation, Writing-original draft. A. R. S.: Resources, Methodology, Conceptualization, Supervision, Investigation, Writing − review & editing.
Data availability
Data is provided within the supplementary information file.
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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