Research Article | Open Access
Thomas Macher, Jennifer Sherwood, Yaolin Xu, Min Lee, Grayson Dennis, Ying Qin, Daniel Daly, Richard P. Swatloski, Yuping Bao, "Scalable Production of Iron Oxide Nanowhiskers", Journal of Nanomaterials, vol. 2015, Article ID 376579, 8 pages, 2015. https://doi.org/10.1155/2015/376579
Scalable Production of Iron Oxide Nanowhiskers
We reported the scalable production of iron oxide nanowhiskers from 250 mL laboratory scale to 10 L reactor reaction. During the scale-up process, the reaction time was found to be a critical parameter to adjust for the production of iron oxide nanowhiskers with similar quality to that of the laboratory scale. Based on transmission electron microscopy and magnetometry analysis, the size, size distribution, and magnetic properties of the large scale products were comparable to those produced on laboratory scale. Subsequently, these nanowhiskers were transferred from organic solvents to aqueous solution using a 38-liter stainless steel tank. These water soluble nanowhiskers were well dispersed in water and the surface chemistry was confirmed by Fourier transform infrared spectroscopy.
Iron oxide nanoparticles have shown great potential in many applications, including contrast agents for magnetic resonance imaging (MRI) , iron deficiency therapy , drug delivery [3, 4], soil and groundwater remediation , and photocatalysts [6, 7]. Iron oxide nanoparticles (magnetite or maghemite) are an inverse phase spinel crystal structure and their magnetic properties are strongly size- and shape-dependent [8, 9]. Most of these applications have been focused on spherical nanoparticles with a few reported on nanocubes [10–12]. The formation of one dimensional (1D) structures was limited to iron oxide nanobars , nanowires , and iron oxide nanochains [14, 15]. Recently, it was shown that nonspherical iron oxide nanoparticles could greatly improve their usefulness for biomedical applications, such as extremely high r2 relaxivity  and high value of the specific absorption rate of iron oxide nanocubes , long blood circulation time, and enhanced retention at tumor sites of nanoworms . These studies suggested that shape control of iron oxide nanoparticles could potentially lead to further advancement in biomedical applications. We and other groups have recently reported the synthesis of ultrathin 1D iron oxide nanostructures [19, 20]. We recently demonstrated that these nanowhiskers can be used as novel positive contrast agents for MRI . For any type of potential applications, large scale production is an important factor, such as the scaled production of spherical iron oxide nanoparticles for direct coal liquefaction [22, 23].
Here, we reported the scalable production of ultrathin iron oxide nanowhiskers using a selective heating method. The synthesis was scaled up from laboratory scale of a 250 mL reaction flask to a 10 L reactor. During this process, we discovered that the reaction time was a key parameter to be adjusted in order to achieve a similar quality product, mainly because of the alteration of heat/mass transfer rates for large volume reactions. Interestingly, the prolonged reaction time did not greatly affect the morphology and property of the nanowhiskers. The transmission electron microscopy (TEM) images showed similar morphologies of the nanowhiskers and the Fourier transform infrared spectroscopy (FTIR) spectra indicated the formation of magnetic ferrite structure. Furthermore, the phase transfer strategy from organic solvent to aqueous solution developed at laboratory scale was successfully applied to large scale (38-liter tank) to prepare water soluble iron oxide nanowhiskers. The scalability of the selective heating method and surface functionalization approach will open up further opportunities to explore the applications of iron oxide nanowhiskers.
Reagents were purchased from VWR, unless otherwise indicated, including iron chloride (FeCl3, ACROS, 98%), sodium oleate (TCI America, 95%), oleylamine (TCI America, minimum 50%), oleic acid (OA, Fisher, 95%), trioctylphosphine oxide (TOPO, Sigma Aldrich 90%), 1-octadecene (ACROS 90%), and polysorbate 80 (Tween 80, AMRESCO, reagent grade).
2.2. Preparation of the Iron Oleate/Oleylamine Complex
Iron-ligand complex precursor was prepared in a 10 L reactor using sodium oleate and oleylamine as mixed ligands following our previously developed procedures on laboratory scale with slight modification [9, 24–26]. The reaction volume was first scaled up 100 times. In brief, iron chloride (140 g, 0.85 mol), oleylamine (289 mL), and sodium oleate (536 g, 1.76 mol) were reacted in a solvent mixture (deionized (DI) water, 880 mL; hexane, 3 L; and ethanol, 1.8 L) at 60°C for 8 h. After reaction, the reaction mixture was separated into two phases with organic phase on the top and aqueous phase on the bottom. The aqueous phase was drained off using the bottom drain of the reactor, and the organic phase containing the precursor was washed with DI water three times and dried under vacuum overnight. The obtained brown waxy product was then collected for subsequent characterization and nanowhisker synthesis.
2.3. Synthesis of Iron Oxide Nanowhiskers
The iron oxide nanowhiskers were synthesized in the large reactor by varying the reaction volumes. First, a scale-up reaction (100 times of the laboratory reaction scale) was performed under the same reaction conditions as laboratory scale (e.g., chemical molar ratios and reaction times); then the same reaction was performed at an increased reaction time; finally, the scale-up reaction at the full capacity of the reactor was carried out. The reaction volume of the full capacity reaction was about 450 times of the laboratory scale. In brief, iron oleate/oleylamine complex (720 g, 1.2 mol) was first dissolved in 6 L of 1-octadecene followed by the addition of a mixture of capping ligands (TOPO: 90 g, 0.225 mol; OA: 45 mL, 0.145 mol). The reaction mixture was then heated at 150°C for 18 h under inert gas (argon) blanket. After the reaction mixture was cooled down to room temperature, the nanowhiskers were cleaned with a hexane/ethanol solution and precipitated out of solution by centrifugation (Avanti J26) and dried under vacuum for 30 min. The powder was weighed and characterized. For phase transfer, the nanowhiskers were dispersed in hexane (50 mg/mL) under sonication and stored as stock solution.
2.4. Phase Transfer Process of the Iron Oxide Nanowhiskers
The iron oxide nanowhiskers were transferred from organic solvents to aqueous solution using a second layer encapsulation method. Briefly, 5 L of iron oxide nanowhisker hexane solution (1 mg/mL) was mixed with 10 L DI water in the 38-liter stainless steel tank. After addition of 250 mL of polysorbate 80 (final concentration of 0.15 mM), the reaction mixture was sonicated for 10 min using a high powered sonicator (Q1375 with booster probe, 20 kHz). The resulting solution was kept under vacuum overnight to completely evaporate the organic solvent. Finally, light brown nanowhiskers water solution was obtained, which are stable for months without any noticeable precipitation.
The formation of the iron-ligand complex precursor and the inverse phase spinel structure of the iron oxide nanowhiskers were confirmed by FTIR [19, 27]. The samples were prepared by mixing powder sample with KBr to form a KBr pallet and then measured on a PerkinElmer Spectrum 100 FT-IR spectrometer (Bucks, UK), equipped with an attenuated total reflectance (ATR) cell by accumulation of 4 scans, with a resolution of 2 cm−1. The size and morphology of the ultrathin nanowhiskers were examined on a FEI Tecnai F-20 TEM. The magnetic property of the nanowhiskers in dry powder form was tested by alternating gradient magnetometer (AGM) at room temperature. The hydrodynamic size and size distribution of the iron oxide nanowhiskers in aqueous solution were measured by using a Zetasizer nanoseries dynamic light scattering (DLS) to ensure uniform size distribution.
3. Results and Discussions
The synthesis of ultrathin iron oxide nanowhiskers was originally developed on laboratory scale using a selective heating method . The entire synthetic process involves preparation of the precursor, iron-ligand complex, synthesis of ultrathin iron oxide nanowhiskers, and subsequent phase transfer from organic solvent to aqueous solution. Here, the precursor preparation and nanowhisker synthesis were scaled up to 10 L reactors and the phase transfer was carried out in a 38-liter tank. Figure 1 shows the experimental setup of the 10 L reactors and the 38-liter stainless steel tank. The 10 L reactors for precursor preparation and nanowhisker synthesis are identical, which are equipped with a digitally controlled and programmable heater in a temperature range of 20–1000°C. The 0.5 horse power (HP) motor with attached stir rod allows continuous agitation of up to 15 L at a constant rate of 200 RPM to ensure full mixing and effective heat transfer. The see-through glass reactor also makes it easy to monitor the reactions. Additionally, the bottom drain assures the easy recovery of the product after reaction with almost no loss of product due to transfer or spills. The removable motor and reactor lids allow easy cleanup after reaction.
The 38-liter surface functionalization tank contains an agitator for mixing, a vacuum control system, and a bottom drain valve for easy product collection. The tank also has an airtight function, allowing the reaction to take place in a chemically confined environment. After the reaction, the product recovery can be achieved by placing a magnetic collector near the bottom drain while draining the solvents. Cleaning the tank can be done following the same procedure used for our reactors; clean with solution and flush with water.
Using this reactor, iron-ligand complex precursor was successfully prepared with a rough yield of 94% with the production of 160 g per batch. The iron-ligand complex has three coordination ligands, but at this selective temperature, two of the weakly bounded ligands decompose first, leaving the third one to direct the formation of the iron oxide whiskers. Here, the modification was the addition of oleylamine as a coligand during precursor preparation with oleate to oleylamine ratio of 2 to 1. We have previously shown that the amine functional group had a stronger binding to iron atom. The design was that the two oleate ligands will decompose first, leaving the tightly bounded oleylamine as a soft template for nanowhisker formation, which potentially allows for better control of the reaction. Compared to our previous data, this modification allowed producing iron oxide nanowhiskers with a more uniform diameter and length. The appearance and morphology of the precursor were very similar to that synthesized on laboratory scale (Figures 2(a) and 2(b)). The chemical structure of the precursors was analyzed using FTIR spectroscopy, which is a great tool to study the metal-ligand coordination. The spectra of the small scale and large scale samples were almost identical (Figure 2(c)).
The presence of the oleylamine ligand was confirmed by the broad –NH2 absorption band at 3400 cm−1 for both samples. The oleate coordination was evident from the asymmetric and symmetric COO− vibration at 1530 and 1430 cm−1. Further, the frequency difference of 100 cm−1 between the asymmetrical (-1530 cm−1) and symmetrical (-1430 cm−1) COO− vibration models indicated the formation of bidentate coordination [28, 29]. Compared to the large scale sample, the signal of the asymmetric COO− vibration at 1530 cm−1 was slightly higher; we attributed this to partial contribution of –COOH groups. This is consistent with the higher –C=O vibration at 1713 cm−1 for the small scale sample. The bands at lower frequency (690 and 430 cm−1) are related to the iron-oxygen coordination bands [27, 29], where the 690 cm−1 bands refer to the Fe–O vibration with tetrahedral coordination and 430 cm−1 with octahedral coordination. The similar morphology and chemical structure of the iron complex precursors from small and large scales suggested that the scale-up process did not alter the quality of the product and further scale-up is highly feasible.
Using the precursors produced from the 10 L large reactor, the nanowhisker synthesis was performed in a 10 L reactor at various experimental conditions. The first reaction was conducted under the same reaction conditions (e.g., chemical molar ratios and reaction times) as laboratory scale, but the reaction volume was increased 100 times. The TEM image of the product showed very dark background, which is likely from the unreacted precursors (Figure 3(a)), indicating that the reaction was not complete. By keeping all the experimental parameters the same and simply increasing the reaction time from 2.5 to 6 h, uniform iron oxide nanowhiskers were obtained (Figure 3(b)). When increasing the reaction volume to the full capacity of the reactor (about 450 times of the laboratory volume), it took about 18 hours for all the precursors to decompose and obtain uniform iron oxide nanowhiskers. The full capacity reaction can generate about 60 g of nanowhiskers per batch and the prolonged heating did not alter the morphology of the product (Figure 3(c)). The high resolution TEM image of the nanowhiskers from the full capacity reaction indicated their crystalline crystal structures (Figure 3(d)). Compared to the laboratory scale reaction, the reaction time was the only parameter to be adjusted to ensure completion of the reaction. The need of the larger reaction time can be understood due to the change in heat and mass transfer properties from the addition of more reactants.
The magnetic property is one of the key parameters to evaluate a magnetic material for their potential applications. The room temperature magnetization versus applied magnetic field (M-H) curve of the nanowhiskers from large scale was similar to the laboratory scale samples, but more paramagnetic, as shown in Figure 4(a). These nanowhiskers exhibited strong paramagnetic signals, indicated by the straight lines of the M-H curves (Figure 4(a)). The high paramagnetic signal is due to the high surface to volume () ratios of these nanowhiskers.
Both surface capping molecules and spin canting contributed to the paramagnetic signal. The functional groups of the ligands cause misaligned spins at the particle surface because of the broken exchange bonds from the reduced coordination of Fe surface ions while the spin-canting effects were because of the presence of disordered Fe vacancies. Surface spin-canting effects for nanostructures of high ratios are significantly enhanced to minimize the magnetostatic energy at the surface . The canted spins on the surface of a nanostructure with high ratios do not respond to the external fields as bulk spins and significantly reduce the magnetization. The slight difference in the M-H curves between small and large scale samples was attributed to the diameter uniformity of the nanowhiskers. Compared to the small scale sample, the diameter of the large scale sample is more uniform without thicker regions as in small scale sample. The small percentage of the superparamagnetic signal mainly resulted from these larger diameter regions. For certain application, paramagnetic signal is more preferred, such as the use of positive MRI contrast agents in our recent publications .
The FTIR spectra of the nanowhiskers from small and large scales both showed the typical absorption bands of spinel structures around 590 and 445 cm−1, where the 590 cm−1 band refers to the Fe–O vibration in the tetrahedral (A) site and 445 cm−1 was assigned to the Fe–O vibration in the octahedral (B) sites. The carboxylic groups on the nanoparticle surface showed an asymmetric (COO−) vibration at 1533 cm−1 and symmetric vibration of (COO−) vibration at 1436 cm−1. The frequency difference of 97 cm−1 between the asymmetric and symmetric absorption bands suggested bidentate binding of carboxylic groups on nanowhiskers surfaces. Because of the bidentate binding (two oxygen atoms to one iron atom) and significant amount of surface atoms of the nanowhiskers, the Fe–O band frequency shifts to higher frequency compared to typical spinel absorption bands. The chemical nature of the large scale sample was also very similar to laboratory scale sample with a frequency difference of 99 cm−1. Both samples showed the broad absorption band of –NH2 groups around 3440 cm−1, suggesting the presence of oleylamine on the nanowhisker surfaces. Samples from both laboratory scale and large scale were capped with mixed ligands oleate and oleylamine. Therefore, we believe that the scaling process did not affect the synthetic process except for the increased reaction times. For example, the reaction time was increased for the precursor preparation from laboratory scale (4 h) to 10 L reactor (8 h) without any noticeable change to the properties of the nanowhiskers.
The as-synthesized nanowhiskers are capped with oleate and oleylamine and only soluble in organic solvents; they must be transferred into aqueous solution for biological or biomedical applications. The mixed ligand coated iron oxide nanowhiskers were transferred into aqueous solution through a second layer encapsulation approach . The capping molecule for second layer encapsulation was polysorbate 80 (Tween 80), an amphiphilic biocompatible polymer. During mixing under sonication, the hydrophobic region of Tween 80 interacts with the hydrophobic tail of the original capping molecules on the nanowhisker surfaces, leaving the ethylene oxide polymers exposed for water solubility and biocompatibility. Before encapsulation, DLS plots of nanowhiskers in toluene were routinely measured to ensure the solution was free of aggregation. The excess Tween 80 molecules were removed by 4 h dialysis. Figure 5(a) shows the TEM image of Tween 80 coated iron oxide nanowhiskers from a typical large scale reaction. After phase transfer and dialysis, the nanowhiskers were well dispersed based on the TEM image. However, the DLS plot in Figure 5(b) did show an elongated tail compared to the laboratory scale sample. The long tail indicated some aggregation of the nanowhiskers by simply increasing the exchange volume. Experimental parameters need to be adjusted accordingly to achieve well-dispersed samples, such as sonication power, time, or Tween 80 concentration. The zeta-potential of large scale sample showed slightly more negatively charged compared to the laboratory scale sample.
The surface chemistry of the Tween 80 coated iron oxide nanowhiskers produced at large scale was studied using FTIR (Figure 6). The spectrum showed typical stretching bands of –C–O–C (1115 cm−1) and 1735 cm−1 band from –C=O stretching of the ester bond from hydrophilic portion of Tween 80. The much broader band around 3444 likely included the contribution from the –OH group of Tween 80 and the –NH2 group from the original oleylamine coating. The asymmetric (1644 cm−1) and symmetric (1462 cm−1) vibration of COO− groups could be assigned to the original oleic acid coating. The iron oxide vibration became one broad band at 560 cm−1. This study confirms the presence of Tween 80 on the nanowhisker surfaces. The water soluble nanowhiskers are stable for months without evident precipitations.
In conclusion, ultrathin iron oxide nanowhiskers were successfully prepared using 10 L reactors. The quality of the nanowhiskers, in terms of size, size distribution, and magnetic properties, is comparable to the samples synthesized at laboratory scale. During the scale-up process, the reaction time was found to be a critical parameter to adjust, mainly because of the slower material transfer at the large volumes. Further, the nanowhiskers were transferred from organic solvent to aqueous solution using Tween 80 as a capping molecule followed by a second layer encapsulation method. This reported scale-up study offers valuable information for future pilot studies.
Conflict of Interests
The authors declare that there is no conflict of interests regarding the publication of this paper.
This work is in part supported by DMR1149931 and NSF SBIR-1248947. The authors acknowledge the UA Central Analytical Facility (CAF) and the Biological Science Department for the use of TEM. The authors would like to acknowledge the support provided by UA’s Office for Technology Transfer within the Office of the Vice President for Research and Alabama Innovation and Mentoring of Entrepreneurs Center at the University of Alabama.
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