1 Introduction

Diesel engines have become the predominant choice for global commercial transportation, primarily due to their high thermal efficiency, substantial power output, and low fuel consumption. In addition, they play a pivotal role in agriculture, industrial applications, and energy production [1]. Diesel engines produce approximately 80 times more particulate matter than gasoline engines [2]. According to the World Health Organization (WHO), individuals in underdeveloped and develo** countries are exposed to air pollution levels that surpass WHO’s recommended limits [3]. Consequently, the pursuit of carbon neutrality has emerged as a worldwide imperative.

Diesel particulate filters (DPF) are the most efficient technique for controlling particulate matter emissions. Constant soot removal is crucial to prevent DPF clogging due to soot accumulation [4]. The usage of a catalyst for soot oxidation is a promising method to prevent filter clogging. The efficiency of soot oxidation is greatly influenced by the degree of interaction between the soot and the catalyst, making it necessary to consider the contact conditions in this solid–solid interaction [5]. Furthermore, the resilience of the catalyst and its activity for soot oxidation in the exhaust environment is crucial, as it is subjected to temperature fluctuations and thermal degradation (due to the formation of localized hotspots), leading to a decline in catalyst activity [6]. Chemical deactivation poses a further threat to the catalyst’s long-term activity. While using noble metals as catalysts, such as Pt, has shown promising results in reducing the oxidation temperature and soot accumulation in DPF, scarcity and high costs of other platinum-group metals necessitate the exploration of alternative solutions [7].

Ceria-based catalysts [8, 9], noble metals [10,11,12,13,14,15], perovskites [16, 17], alkali-based catalysts [18, 19], and 3 DOM [20] catalysts have been extensively researched, but there is still a need to explore more materials to meet regulatory standards. Among the metal oxides, manganese-based oxides are promising candidates for various oxidative reactions (e.g., CO and VOCs) due to multivalent oxidation states. Octahedral molecular sieves, a type of manganese oxide called K-OMS-2, form a 2 × 2 structure in their most stable state [21, 22]. This structure consists of MnO6 octahedrons stacked to form a square-like tunnel structure with sides measuring 4.6 Å. The potassium atom in the centre helps balance the charge and stabilize the structure. K-OMS-2 exhibits high mobility due to weak interactions with the framework. Various oxidation states of MnOx contribute to its excellent redox properties [23].

Studies report that K-OMS-2 can be tuned by substituting K or Mn ions with single or multiple valence state ions to improve catalytic efficiency and oxygen vacancies [24, 25]. Ag-doped catalysts have been extensively researched for catalytic oxidation reactions (e.g., methanol, ethanol, toluene, CO, and formaldehyde) [26,27,28,29]. Yu et al. [30] investigated that adding Ag produced more surface oxygen vacancies and lattice defects, contributing to excellent catalytic oxidation of methanol. Furthermore, Liu et al. [31] have reported that Ag can enhance the regeneration and generation of active oxygen species with enhanced mobility, thus exhibiting improved catalytic performance with long-term stability. To our knowledge, Ag-doped K-OMS-2 for soot oxidation has not been reported.

This study aims to demonstrate and explain the soot oxidation activity of Ag/K-OMS-2. The hydrothermal synthesis method is employed to prepare K-OMS-2 and silver-doped K-OMS-2. Characterization methods such as XRD, FESEM, FTIR, Raman, and Soot TPR are utilized. A TGA instrument is used to analyze soot catalytic activity. Calculation of the soot oxidation activation energy provides a better understanding of the catalytic performance of the synthesized catalyst.

2 Experimental section

2.1 Materials

Potassium permanganate (99%) and manganese sulfate monohydrate (99%) from Sigma-Aldrich, silver nitrate (99%) and nitric acid (65%) from Merck are used as procured without any additional purifications.

2.2 Preparation of K-OMS-2 catalyst

2.89 g of KMnO4 dissolved in 50 ml of double distilled water was added to a mixture containing 4.12 g of MnSO4 and 1.5 ml nitric acid, with 15 ml double distilled water dropwise and stirred continuously at room temperature for fifteen minutes. This mixture was then transferred into an autoclave (100 ml) and heated in an air oven set at 100 °C for 24 h. The precipitate obtained was washed to neutralize its pH level up to 7 using distilled water before drying it in a hot air oven set at 80 °C. The dried sample is calcined at 600 °C in a muffle furnace for 4 h.

For do** of 5% Ag into K-OMS-2, the following procedure is followed: 2.89 g of KMnO4 in 50 ml double distilled water are added dropwise to a mixture containing 4.12 g MnSO4, an appropriate amount of Ag(NO3)2 and 1.5 ml HNO3 in 15 ml of double distilled water while stirring constantly at room temperature for 15 min. The mixture is put into a 100 ml autoclave and placed inside a hot air oven set at 100 °C for 24 h. The rest of the process was carried out in the same for the undoped sample.

XRD analysis was done using Rigaku Mini Flex 600 to analyze the structure and phase purity of the samples. The wavelength of 1.54 Å was used, with angles ranging from 10° to 70°. Surface morphology was analyzed using FESEM (Carl Zeiss, Germany) with an accelerating voltage of 200 kV. An excitation wavelength of 785 nm was used to record the Raman spectra using a Compact Raman Spectrometer, Renishaw (UK). With a gas flow rate of 60 mL/min (soot TPR was performed in a nitrogen atmosphere). TGA instrument was loaded with the mixed sample (catalyst and soot), which was heated between 50 and 800 °C. It facilitates locating the oxygen radicals that are actively promoting soot oxidation.

2.3 Soot catalytic activity

TGA instrument TA 50 Discovery was used to investigate catalytic soot oxidation. In a 10:1 ratio, the catalyst and soot were combined. The temperature was ramped from ambient to 700 °C while the gas flow rate (O2 flow) was set at 60 mL/min.

3 Results and discussion

3.1 X-ray diffraction (XRD)

Figure 1 depicts the XRD patterns of both K-OMS-2 and silver-doped K-OMS-2 samples. The diffraction peaks at 2θ correspond to K-OMS-2. Notably, the XRD pattern of the silver-doped K-OMS-2 sample does not exhibit peaks indicative of other forms of silver. This observation has been corroborated by FTIR analysis, which confirms the complete integration of silver ions into the lattice framework (see Fig. 1b).

Fig. 1
figure 1

XRD pattern of all catalysts and lattice structure of a K-OMS-2, b 5-Ag/K-OMS-2

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A reduction of the peak intensity is observed upon adding silver ions. This decrease in peak intensity can be attributed to the thorough incorporation of silver ions into the tunnel structure of K-OMS-2. However, it is essential to note that the XRD pattern also indicates the presence of the orthorhombic phase of α-Mn2O3, known as bixbyite. The formation of α-Mn2O3 has been previously explained in our earlier work [32]. Details regarding the lattice parameters are presented in Table 1.

Table 1 Crystallite and lattice parameters
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3.2 FESEM

Figure 2 illustrates the morphology of the synthesized samples. Both samples exhibit a rod-like structure. The average rod length and width for the pure and 5% Ag-doped sample were 290 nm and 32 nm, and 213 nm and 26 nm, respectively. The elongation growth of the particles is partially inhibited, which can be attributed to the incorporation of Ag+ ions into the lattice of K-OMS-2 [33].

Fig. 2
figure 2

FESEM of a K-OMS-2; b 5-Ag/K-OMS-2

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3.3 FTIR

Figure 3 displays the FTIR spectra of K-OMS-2 and 5-Ag/K-OMS-2. The obtained FTIR spectra exhibit slight variations from the reported peaks, which can be attributed to factors such as grain size effects, the synthesis process, and temperature influences [3. T50% of this work is compared with the literature and is tabulated in Table 2. From Fig. 6, Ti for K-OMS-2 and silver-doped K-OMS-2 are 229 and 233 °C, whereas the Ti for bare soot was significantly higher at 530 °C.

Table 3 Active oxygen radicals and soot conversion parameters
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Although Ti for the Ag-doped sample is slightly higher than the undoped sample, T50% and Tmax are lower than the undoped. This observation can be explained as the silver-doped samples exhibited higher surface- and lattice-adsorbed oxygen radicals, which is observed in soot TPR results. The direct contact between soot and the catalyst enhances the exchange of surface-adsorbed oxygen radicals, which accounts for the lower T50% and Tmax observed in the Ag-doped sample. Surface-adsorbed oxygen radicals are generated by absorbing oxygen through crystal defects. These species are highly reactive and readily desorb at lower temperatures compared to lattice and bulk oxygen radicals. The redox properties of the metal ions in the catalyst facilitate the transfer of oxygen radicals from the lattice to the catalysts surface. In contrast, bulk oxygen radicals become active oxygen radicals only at much higher temperatures [50, 51].

3.7 Activation energy for soot catalytic oxidation

Activation energy is a critical parameter for assessing the type of reaction process occurring in a system. Figure 7 presents the Osawa method’s kinetic results [57]. The activation energy was calculated using Eq. 1; the values are summarized in Table 4. The activation energy of Ag-doped K-OMS-2 is significantly lower compared to that of K-OMS-2, implying that soot undergoes oxidation more readily when the activation energy is reduced [53] (Table 4):

$${\text{Log }}\beta [\beta + 0.{476 }E/{\text{RT}}] = K,$$
(1)

where ß is the heating rates, E is the activation energy, R is the gas constant, T is the measuring temperature.

Fig. 7
figure 7

Kinetics of catalytic reaction at T50% conversion

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Table 4 Activation energy calculated through the Osawa method
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3.8 Thermal aging

Thermal ageing studies measure catalysts prolonged stability and effectiveness within practical operational settings. Through subjecting catalysts to elevated temperatures over an extended duration, any changes in their catalytic activity, selectivity, and durability can be monitored [58]. The thermal stability of the catalyst is shown in Fig. 8. The aged samples showed similar activity compared to that of fresh catalysts. The T50% of Ag-doped K-OMS-2 had an increase of about ~ 21 °C compared to the fresh catalyst, and no significant changes in the crystal structure were seen in the XRD graph.

Fig. 8
figure 8

Thermal stability and XRD pattern of the catalyst and aged samples

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4 Conclusion

In summary, we successfully synthesized K-OMS-2 and Ag-doped K-OMS-2 through hydrothermal methods. XRD analysis revealed that the prepared samples exhibited a tetragonal phase. FESEM images displayed a nanorod-like morphology, with Ag-doped K-OMS-2 samples showing smaller-sized nanorods. This size reduction can be attributed to the inhibitory effect of Ag+ ions on nanoparticle growth. Raman and FTIR results indicated the absence of additional phases, such as silver oxides, confirming the full integration of Ag+ ions into the framework. The Soot Temperature Programmed Reduction (TPR) results showed that the Ag-doped sample exhibited higher surface-adsorbed oxygen and lattice oxygen radicals, which translates to superior catalytic activity (T50% = 370 °C). Furthermore, as calculated using the Ozawa method, the activation energy was lower for the Ag-doped sample, a crucial factor contributing to its enhanced catalytic activity.