Although MTNs have been widely prepared by so-gel bulk methods [
27], generating MTNs with smaller size and regular morphology remains a challenge. In this study, we developed a sequential system through ordered combination of two MIVMs to fabricate MTNs at a short time scale (
Scheme 1A). In the first MIVM, titanium precursor and surfactant were co-injected to produce MTNs without surface modification. Then, such raw nanomaterials were immediately transferred into the second MIVM with the aid of PEG-functionalized silane to stop the growth of TiO
2. We systematically investigated into how the concentration of titanium precursors, PEG-silane and pH affect the size and morphology of MTNs (Figs. S1–S3 in Supporting information). We found that increasing the concentration of titanium precursors from 0.075 mmol/mL to 0.5 mmol/mL induced very different size and morphology, the middle concentration (0.3 mmol/mL) led to the most regular morphology with the smallest size. The concentration of PEG-silane at 0.15 mmol/mL made more uniform morphology of MTNs. After tuning the pH from 5 to 10, we demonstrated the optimized pH for the best nanoparticulate size and morphology was 8. Collectively, the regulation of the concentrated titanium precursors, PEG-silane and pH were crucial in achieving uniform particle size. Moreover, we investigated how velocity ratios between surfactant and titanium precursors in the first MIVM affect the size of products (Fig. S4 in Supporting information). We confirmed that the size of MTNs was decreased with the increasing the velocity ratios from 1:1 to 5:1, providing the optimal condition of surfactant/titanium precursors ratio at 5:1. Based on these findings, we prepared the outperforming MTNs with the optimal concentration of titanium precursors (0.3 mmol/mL) and PEG-silane (0.15 mmol/mL), pH 8, and surfactant/titanium precursors ratio (5:1). After calcination at 500 ℃ for 4 h, the FNC-based MTNs (referred to as "MTNs" for simplicity) were obtained. In parallel, we prepared control MTNs through single MIVM or bulk method (referred to as "BULK" for simplicity) (Fig. S5 in Supporting information). Scanning electron microscopy (SEM) and transmission electron microscope (TEM) revealed the outperforming MTNs to be uniformly spherical with a size of approximately 31.5 nm with a mesoporous structure (
Figs. 1A and
B). In contrast, both single MIVM- and BULK-based MTNs exhibited irregular size and morphology including uneven size distribution, morphology collapse and severe aggregation. X-ray diffraction (XRD) patterns indicated the presence of both anatase (JCPDS No. 21–1272) and rutile (JCPDS No. 21–1276) phases (
Fig. 1C), which have better photocatalytic activity. The nitrogen adsorption-desorption isotherms of MTNs belongs to typical type IV adsorption curve, showed bimodal mesopore distributions with high surface area and pore volume, as calculated using the Brunauer-Emmett-Teller (BET) method. The BET surface area and pore volume of outperforming MTNs were 461.9 m
2/g and 0.59 cm
3/g (
Fig. 1D), respectively, which were significantly higher than those of single MIVM-based MTNs (167.8 m
2/g and 0.27 cm
3/g), BULK (180.4 m
2/g and 0.34 cm
3/g), as well as commercial P25 (85.7 m
2/g and 0.23 cm
3/g). The pore size of MTNs, calculated using the Barrett-Joyner-Halenda (BJH) model, revealed the presence of pores with diameters centered at 6.5 nm (the inset in
Fig. 1D), which was considerably larger than that of single MIVM-based MTNs (0.9 nm), BULK (1.2 nm), and P25 (1.5 nm) (Fig. S5). Taken together, these findings demonstrated the advantages of sequential FNC-based MTNs in the regular size, morphology and pore properties, indicating their outstanding performance on photocatalytic and antibacterial activities. Drawing on prior investigations and existing theories surrounding MTNs preparation, we presented a coherent conceptualization of the growth mechanism underlying the formation of MTNs. In the first MIVM, the formation of template micelle was initiated by the violent mixing of hydrophobic tetrabutyl titanate (TBOT) molecules in ethanol phase and
N-hexadecyltrimethylammonium chloride (CTAC) in aqueous phase within MIVM's minuscule mixing chamber, resulting in the formulation with TBOT/ethanol phase inside and water outside. Subsequently, the TBOT molecules inside the cores of templates diffused out and underwent hydrolysis at the outside water-rich interface. In view of the high hydrolysis and condensation rate of TBOT, the hydrolysis reaction must be terminated swiftly to produce MTNs with small and controllable particles in the second MIVM. Thus, we introduced the capping agent PEG-silane in the second step to prevent TBOT from further contact with water, ultimately bringing the entire reaction to an end to generate MTNs. For the single MIVM-based production, the hydrolysis, condensation, and termination of the titanium precursor occur at the same time when CTAC and TBOT were concurrently present within single MIVM device, leading to the irregular growth of MTNs due to the immediately disturbance of PEG-silane. For the BULK-based production, the titanium precursor might hydrolyze completely before the introduction of PEG-silane due to the rapid hydrolysis rate of titanium precursor, resulting in the overgrowth of MTNs. Different from these two methods, our sequential MIVM-based production separated the process of hydrolysis, condensation and terminalization in different MIVMs, offering strong and interference-free driving force for the sophisticated fabrication of MTNs with regulated size, morphology and pore structures.