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The techniques described above are able to consistently and reproducibly precipitate silica. This is easiest to determine by the rapid onset of turbidity within the reaction vessel, which upon cessation of agitation will spontaneously settle into a thick coagulum of precipitated silica (Figure 2). The extent of reaction and hence yield can be confirmed by measuring the mass of this coagulum after separation and is typically 58 ± 6.5% (Figure 4, yellow).
Further insight into the reaction progression can be generated by adapting the molybdenum blue spectroscopic method to detect the amount of unreacted monomeric silicate species as well as those species which have reacted to form polysilicates or 'oligomers', but have not managed to reach sufficient size to coagulate (Figure 4, red and blue respectively).
This specific silica speciation data is of particular interest when comparing different titration efficiencies for the precipitation reaction - I.E. how the final reaction pH and the rate at which this is reached affects the polymerization of monomeric silica to an 'oligomer' and its subsequent coagulation to solid silica. By modifying the amount of acid added in stage 2.4 slightly, under- or over-titration of the reaction mixture can be performed (Figure 5). By measuring the silica speciation again for these two cases, a clear difference can be seen in the reaction completion (Figure 4) despite only minor changes to the titration profile of the reaction (Figure 5).
Although no difference is present between the consumption of monomeric species for the three reaction cases (remaining between 29 - 33%), there is a clear difference in the amount of oligomeric silica species which precipitate in each case. This is in agreement with traditional theory on sol-gel silicas - in the 'undershoot' case the pH is held higher for longer, allowing for individual particles to grow and hence aiding efficient coagulation; in the 'overshoot' case the coagulation is induced much faster due to the rapid titration, hence fewer of the silica species have grown to a sufficient size to coagulate and remain trapped in the colloid phase.16
Given the importance of titration upon silica formation, a priori knowledge of the appropriate titration volume is essential. Although not extractable from the reaction stoichiometry due to the complex protonation behavior of the amine additives and change in silica surface acidity on coagulation, highly reliable empirical relationships between system contents, concentrations and titer volumes are readily generated (Figure 1).
Once coagulation has been completed, material surfaces can be readily modified through the use of acid elution, as has recently been reported by the authors elsewhere.13 This allows for fine-tuning of material properties such as composition, porosity, and chemical activity of additive (Figure 6a and b).
In this study, BSA was used as an exemplar encapsulant enzyme, however, the techniques described here can be used for multiple enzymes17,18. The procedure followed for protein detection is the Bradford assay protocol,19 using the supernatants stored from each centrifugation cycle. The amount of protein in the supernatant is calculated using a calibration curve created from known amounts of BSA dissolved in the supernatant of a sample with zero protein content (Control sample). The amount of protein encapsulated into silica will be calculated by subtraction of the detected protein in supernatants from the initial amount of protein added. The only reagent needed for the assay is the Bradford Reagent (either procured or made according to standard recipes).
There are three types of assay format, depending on the sample volume, the expected amount of protein to be detected and the measurement method used. Herein, the followed format is specified for a spectrophotometer, requires disposable cuvettes of macro and of micro size and can detect from 10 µg/mL to 1.4 mg/mL of protein.
In Figure 7 the amount of protein detected after each wash (step 4.3) is shown as a % of the initial protein amount (which was 50 mg). Around ~50% of BSA was detected in the supernatant after the first centrifugation, which relates to ~50% immobilization efficiency. As there was no BSA detected in the following washes, BSA (or any other enzyme) could be securely encapsulated during silica synthesis with no leaching - this is a significant advantage of this method. In order to confirm the presence of BSA in the silica produced, Fourier Transform Infrared Spectroscopy (FTIR) analysis was performed. The presence of the characteristic bands of amide I and II in the area of 1,500/cm and 1650/cm (Figure 8) in the samples prepared in the presence of BSA, but not in the control samples (no BSA) confirmed the presence of BSA in the solids.
In addition to the method of enzyme addition described above (BSA added during neutralization of reaction mixture), there are other possible variations e.g.,BSA addition during mixing of the silicate and the additive solutions, prior to neutralization or enzyme added to the silicate or additive solution before their mixing and neutralization. Some of these possibilities were explored further and the immobilization efficiencies (mass of BSA immobilized as a percentage of enzyme added to the reaction system, calculated based on the Bradford assay) and the amount of BSA in the final silica were measured (concentration of BSA in silica as a percentage of the total composite weight produced, see Figure 9). It was clear that when BSA was added to the unreacted reagents (cases A-C in Figure 9) there were no considerable differences in the immobilization efficiency or the amount of BSA in the resulting composite. However, when BSA is added during silica formation (case D in Figure 9), immobilization efficiency and the amount of BSA in the final product were both significantly lower. Despite these differences, the average amount of silica produced remained unchanged (between 85-90 mg). These observations can be explained on the basis of the ionization (or isoelectric point) of BSA, silicate/silica and the additive. The different methods of addition allow for different interactions between the enzyme and silica precursors. As the pH at the time of the addition of the enzyme changes, the ionization of each species will determine intermolecular interactions, which in turn will control the immobilization efficiency.
| Cuvette No | Concentration of BSA (mg/mL) | Bradford reagent (mL) | Sample (mL) |
| 0 | 0 (control) | 1.5 | 0.05 |
| 1 | 0.1 | 1.5 | 0.05 |
| 2 | 0.25 | 1.5 | 0.05 |
| 3 | 0.5 | 1.5 | 0.05 |
| 4 | 0.75 | 1.5 | 0.05 |
| 5 | 1 | 1.5 | 0.05 |
| 6 | 1.25 | 1.5 | 0.05 |
| 7 | Unknown sample (X) | 1.5 | 0.05 |
Table 1: Macro Bradford assay set-up and calculated component volumes. Valid for determination range 0.1-1.4mg/mL (volumes for 1 replicate)
| Cuvette No | Concentration of BSA (ug/mL) | Bradford reagent (mL) | Sample (mL) |
| 0 | 0 (control) | 1 | 1 |
| 1 | 1 | 1 | 1 |
| 2 | 2.5 | 1 | 1 |
| 3 | 5 | 1 | 1 |
| 4 | 7.5 | 1 | 1 |
| 5 | 10 | 1 | 1 |
| 6 | Unknown sample (X) | 1 | 1 |
Table 2: Micro Bradford assay set-up and calculated component volumes. Valid for determination range 1-10 µg/mL (volumes for 1 replicate)

Figure 1: Required titer volume against silica concentration for reaction systems using either DETA or PEHA as the additive. Silica was synthesized at varying concentrations while maintaining an [N]:[Si] ratio of 1, for two different additive chemicals. Error bars are one standard deviation around the mean.

Figure 2: Photographs of silica coagulum in the reaction vessel (a) during and (b) after agitation, demonstrating the solution turbidity and settling that are indicative of an optimal reaction.

Figure 3: Exemplar calibration curve for Bradford macro assay. Supernatant from bioinspired silica synthesis in absence of BSA is mixed with a known amount of the protein, after which Bradford analysis is performed as described in step 9.1.

Figure 4: Final polymerization states of silica species for different reaction conditions. Silica is synthesized using optimal (baseline) conditions, as well as with over- or under-titration, after which relative silica concentration is quantified for monomeric or dimeric silicates (red), polysilicate 'oligomers' (blue) and unstable coagulating silica (yellow).

Figure 5: Progression of pH through reaction system as a function of initial titer volume. Acid is immediately dosed after ca. 38s of mixing, causing the pH to rapidly drop to below 8. Afterward, further quantities of acid are automatically dosed such that the pH was 7.0 ± 0.05 300s after initial addition. In the case of over-titrating, this was not achievable, as the initial dose was sufficient to drop the pH below 7, reaching pH 6.65 after 300s. Initial HCl volume added for 'undershoot,' 'baseline,' and 'overshoot' was 6.90, 7.05, and 7.20mL respectively.

Figure 6: Representative property changes upon acidification of coagulated silica material. (a) Change of additive concentration with respect to pH, and (b) change of silica porosity with respect to pH. Reproduced from Manning et al. 13 under Creative Commons license.

Figure 7: BSA concentration in bioinspired silica synthesis supernatants. Bradford assays were carried out on reaction supernatants after centrifugation, from which the relative amount remaining (therefore occluded from the synthesized silica) was determined.

Figure 8: FTIR analysis on bioinspired silica with and without active species encapsulation. Spectra showed: black line: bioinspired silica, gray line: pure BSA, blue line: bioinspired silica loaded with BSA. Vertical dashed lines indicate characteristic amide bands.

Figure 9: Immobilization efficiency and the amount of BSA in the composite for silica produced using PEHA. BSA was added (A) in the PEHA solution before mixing with silicate, (B) in the silicate solution before mixing with PEHA, (C) after initial mixing of PEHA and silicate solutions, and (D) after mixing PEHA and silicate solutions and neutralizing. Efficiency is measured as% BSA encapsulated from the reaction mixture as a proportion of total BSA added, while BSA in silica signifies% concentration of BSA in final silica composite by mass. Error bars are one standard deviation around the mean.