The authors thank the financial support from the Department of Chemical and Biological Engineering (University of Sheffield) and the EPSRC (EP/L017059/1 and EP/P006892/1).

1. Preparation of Precursor Solutions (and Optional Encapsulant Solutions)
<ol>
	<li>Into a 180 mL plastic container, measure 1.5 mmol of sodium silicate pentahydrate (318.2 mg), and dissolve in 20 mL of deionized water.</li>
	<li>Similarly, in a second container, measure 0.25 mmol of pentaethylene hexamine (PEHA, 58.1 mg) and dissolve in 20 mL of deionized water.
	<ol>
		<li>When using alternative amine-containing compounds e.g.,diethylenetriamine (DETA) or triethylenetetraamine (TETA), ensure that the total Si:N mole ratio remains constant at 1 (i.e., corresponding to 0.5 mmol of DETA or 0.375 mmol of TETA in the described procedure)15.</li>
		<li>When using polymeric amine additives e.g.,poly(ethyleneimine) (PEI) or poly(allylamine hydrochloride) (PAH), maintain a concentration of 1 mg/mL (final reaction volume)15. 
		CAUTION: Handle these amines only inside a fume hood, as they are corrosive or toxic in their pure forms (especially as vapors).</li>
	</ol>
	</li>
	<li>To perform in situ encapsulation during synthesis, dissolve a pre-determined mass of protein (herein 50 mg of Bovine Serum Albumin, BSA) in 5 mL of deionized water. Subtract this amount of water from the volume of deionized water to be used for the dissolution of sodium silicate pentahydrate.
	<ol>
		<li>To ease the protein dissolution without altering its structure, once mixed with deionized water, cap the container and store at 4 &#176;C. Check occasionally on the dissolution progress, preferably without stirring.</li>
	</ol>
	</li>
</ol>
2. Silica Synthesis
<ol>
	<li>Combine the solutions of sodium silicate pentahydrate and PEHA in one of the 180 mL container and add sufficient deionized water to make the final solution volume 41 mL (or 46 if in situ encapsulation is omitted).</li>
	<li>Place the freshly-prepared mixture of sodium silicate and PEHA solutions on the top of a stirrer plate, adding a stirrer bar to provide consistent mixing.</li>
	<li>Into this vessel, suspend a pH probe and record the initial pH.
	<ol>
		<li>At this stage, optionally, remove a 750 &#181;L aliquot of the starting mixture for later determination of the initial [Si] concentration using the molybdenum blue spectrophotometric assay, as described in step 8.1.</li>
	</ol>
	</li>
	<li>Begin the synthesis by adding a predetermined quantity of 1 M HCl, as calculated from Figure 1, and observe the immediate evolution of turbidity (see Figure 2)</li>
	<li>As soon as the acid addition is over, add the encapsulant solution (if any) as quickly as possible. 
	NOTE: The final volume given these quantities is 50 mL of total reaction mixture, leading to Si and N concentrations of 30mM. This can be scaled as desired by multiplying all above quantities by a constant amount.</li>
	<li>Record the pH after 5 min to determine the reaction completion; ensure that the pH is 7 &#177; 0.05.</li>
</ol>
3. Acid Elution of the Materials
<ol>
	<li>Modify the composition of produced silica after the reaction has reached completion (either as an as-made coagulum or by resuspending a previous synthesized sample of silica) by the addition of further acid.</li>
	<li>If resuspending silica, mix approximately 150 mg as-prepared bioinspired silica with 100 mL of deionized water in a 180 mL plastic container, and place on the top of a stirrer plate.</li>
	<li>Once the suspension is well mixed, suspend a pH probe in the vessel.</li>
	<li>Titrate in further HCl until the desired pH (between 7 and 2) has been reached and allow to stabilize for ca. 1 min.</li>
	<li>Wait a further 5 min to ensure the system has fully equilibrated, and then proceed to isolate the solid silica.</li>
</ol>
4. Silica Separation and Drying
<ol>
	<li>Decant the bioinspired silica suspension into 50 mL centrifuge tubes.</li>
	<li>Centrifuge the suspension at 5,000 g for 15 min.</li>
	<li>Remove the supernatant after centrifugation and store for further analysis (e.g., Bradford assay, see below). Refill the centrifuge tubes with deionized water, and re-suspend the silica using a vortex mixer.</li>
	<li>Repeat the centrifugation, supernatant storage, and re-suspension twice.</li>
	<li>After the final centrifugation, remove the supernatant and scrape the silica into a ceramic crucible.</li>
	<li>Dry in an oven overnight at 85 &#176;C.
	<ol>
		<li>If encapsulation has taken place, use a freeze-drying facility or an oven operating under vacuum to avoid protein denaturation.</li>
	</ol>
	</li>
</ol>
5. Production of Molybdenum Blue Reagent (MBR) for [Si] Determination
<ol>
	<li>To a plastic 1 L volumetric flask, add 8 mmol (10 g) ammonium molybdate tetrahydrate in a fume cupboard.</li>
	<li>Dissolve this in 500 mL deionized water under stirring.</li>
	<li>Acidify the solution by carefully adding 60 mL of 10 M HCl solution.</li>
	<li>Adjust the final volume to 1 L.</li>
</ol>
6. Production of para-aminophenol sulfate reducing agent (RA) for [Si] determination
<ol>
	<li>Place a 500 mL glass volumetric flask in a water bath at ambient temperature on a stirrer plate in a fume- cupboard.</li>
	<li>Add 111 mmol (10 g) of anhydrous oxalic acid, 19.5 mmol (3.35 g) of para-aminophenol sulfate, and 16 mmol (2 g) of sodium sulfite, and dissolve in 250 mL water.</li>
	<li>Carefully and slowly add 92 g (50 mL) of saturated sulfuric acid while stirring and wait for the solution to cool.</li>
	<li>Finally, dilute to 500 mL with deionized water.</li>
</ol>
7. Silicomolybdic Acid Assay on Monomeric Silica Species
<ol>
	<li>In a 5 mL plastic vial, dilute 300 &#181;L of MBR produced in step 5.4 with 3 mL of deionized water.</li>
	<li>Add 10 &#181;L of a silicic acid test solution and shake to mix. 
	NOTE: This solution will slowly turn yellow.</li>
	<li>After exactly 15 min, add 1.6 mL of the reducing agent prepared from section 6 to reduce the yellow silicomolybdate complex to its blue isomer.</li>
	<li>Allow a blue color to develop for at least 2, but not more than 24 h.</li>
	<li>Measure sample absorbance at 810 nm in a UV-vis spectrophotometer and calculate [Si] against a calibration curve.</li>
</ol>
8. Silico Molybdic Acid Assay on Polymeric Silica Species
<ol>
	<li>To measure the concentration of polysilicate species using the molybdenum blue method, in a microcentrifuge tube, combine 750 &#181;L of 2 M sodium hydroxide solution with 750 &#181;L silica suspension.</li>
	<li>Seal and place in a microcentrifuge float.
	<ol>
		<li>Ensure sufficient headspace is left in the tube to prevent bursting due to pressure build up. 
		NOTE: A headspace of 500 &#181;L is usually sufficient to avoid this. Alternatively, the procedure can be carried out in open vials so long as liquid loss due to evaporation is accounted for.</li>
	</ol>
	</li>
	<li>Float the microcentrifuge tubes in a water bath heated to 80 &#176;C and leave it to dissolve for 1 h.</li>
	<li>After 1 h has elapsed, remove the microcentrifuge tubes and wipe the outside dry.</li>
	<li>Once cooled, [Si] can be determined as described above as described in steps 7.2 to 7.5.</li>
</ol>
9. Bradford Assay Procedure for Determination of Protein Concentration in Silica
<ol>
	<li>Insert a predetermined amount of (room temperature) Bradford reagent and sample in each assigned cuvette (see Table 1 and Table 2 for specific volumes). Use disposable pipette tips for every cuvette to avoid volume alterations due to the nature of the reagent and repeat each point in triplicate.</li>
	<li>Mix each cuvette by inverting 3 times and leave to develop for 10 min.</li>
	<li>Measure absorbance at 595 nm using pure supernatant as blank.</li>
	<li>Calculate the original absorbance of each cuvette by subtracting from each measurement the absorbance found for the control sample (cuvette No. 0 in both assays).</li>
	<li>Calculate the protein concentration of Unknown sample using a calibration curve (Figure 3). In case of dilution of the original sample, the dilution factor needs to be accounted for.
	<ol>
		<li>Create a calibration curve for each set of experiments by plotting measured absorbance against concentration of BSA to avoid random fluctuations that might affect the assay&#39;s sensitivity.</li>
		<li>Although this protein assay is meant to use BSA as a standard to quantify any type of protein, create a calibration curve for each specific protein of interest for improved accuracy.</li>
		<li>If the protein content of the unknown sample is expected to be higher than the covered range of the calibration curve, dilute it as needed.</li>
	</ol>
	</li>
	<li>Determine protein content for each sample during re-suspension to monitor possible protein loss.</li>
</ol>

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The authors declare no competing financial interest.

In the current work, we present a method for rapidly precipitating bioinspired silica materials and encapsulation of biomolecules therein. We demonstrate critical steps within the procedure, namely the amount of reaction-initiating acid to be added, and timing of addition of the biomolecule encapsulant. We show the effect of acid addition amount on both reaction progression and yield (Figure 4 and Figure 5, respectively), and demonstrated a method for tight control over synthesis conditions, allowing for consistency despite this sensitivity. Regarding active species encapsulation, although straightforward in terms of procedure, encapsulation is shown to be sensitive to the conditions of the experiment (order of addition, pH of addition, environmental conditions), however, consistency in material properties is again achievable.
The synthesis conditions can be modified through the use of different additives, many of which have been published elsewhere,15 providing a range of morphologies and porosities. Further, post-synthetic techniques to modify and chemically tailor bioinspired silica materials have been reported such as mild purification13 and surface amine decoration.20 Finally, due to the mild, aqueous nature of the synthesis, in situ encapsulation is possible for a wider range of substrates than those demonstrated here, ranging from enzymes17,18 to whole cells,21 metal salts,22 active pharmaceutical ingredients,23 and quantum dots.24
Unlike other organic-mediated silica syntheses (such as the MCM-41 or SBA-15 family of materials), the polyfunctional nature of bioinspired additives cannot produce ordered pore structures, nor highly monodisperse particle-size distributions characteristic of St&#246;ber-type silica.25 This is due to the lack of well-defined micellization behavior of bioinspired additives (outside of special cases)26 coupled with their increased catalytic activity over monofunctional amine-containing additives.26
On the other hand, this polyfunctional additive nature enables the use of shorter reaction times and milder temperature &#38; pressure compared to other organic-mediated silica syntheses. This also leads to the possibility of room-temperature additive elution as described above, which has yet to be achieved for these other silica families due to the specifics of their surface chemistry.27,28,29 Consequently, bioinspired silica materials have been shown to be both more economical and practical to produce at a larger scale, leading to easier commercialization and development.14
In summary, bioinspired silica synthesis represents a rapid, facile method for producing active species supports or gas sorbent media. Through tight control of pH during and after the reaction, a wide array of silica-amine composites can be synthesized with varying properties, which is further complemented by the possibility of in situ encapsulation of an array of different organic, inorganic, or bio-organic materials. Although independent post-synthetic modification of bioinspired additive and encapsulant concentration has yet to be achieved, these methods represent a promising step towards environmentally benign chemical processes.

The use of silica as a structural support for industrial catalysts is well established, allowing for the improved catalyst activity, stability and processability,1 hence potentially reducing the operating cost. These benefits are compounded in the case of enzyme immobilization, as storage within a silica pore system can confer significant benefits on the enzyme lifetime over its free counterpart. Accordingly, much effort has been expended in finding the best method to attach enzymes to silica species, with multiple reviews comparing investigations using different methods of immobilization on siliceous solid supports.2,3,4
Enzymes are typically attached via physisorption or covalent bonding, in addition to encapsulation within a porous material.5 However, there are significant drawbacks related to each method: physisorption relies on transient surface interactions between the silica and biomolecule, which can very easily be weakened by the reaction conditions leading to the unacceptable enzyme leaching. The much stronger covalent attachment usually results in lower activity due to the reduced conformational freedom of the active species. Encapsulation can result in reduced activity due to the enzyme inaccessibility or diffusional limitations.6
Recent developments in the field of milder (often dubbed &#39;bioinspired&#39;) silica syntheses have established the in situ encapsulation of biomolecules and other active species during the material synthesis.7,8,9 This method negates many of the drawbacks of conventional immobilization - unlike chemisorption approaches the conformational freedom of the biomolecule is maintained by the use of weaker noncovalent interactions but as the pore cavity forms around the biomolecule, leaching is still prevented. Indeed, encapsulation has been demonstrated to work for a range of biomolecules and even whole cells,10 and through encapsulation in bioinspired silica effects such as deactivation due to harsh process conditions can be avoided.7,11
The goal of the method described herein is to prepare a porous silica with controllable properties, under ambient conditions, by using a bioinspired organic additive. The method can be easily modified to include encapsulation of either inorganic or bioorganic molecules, a selection of which shall be shown. We further show a facile method for modifying the as-synthesised materials to achieve desired bulk properties and purification by removing the organic template through acid elution.
Compared to the traditional synthesis of templated porous silica supports (e.g.,silica materials templated through supramolecular surfactant assemblies like MCM-41 or SBA-15)12 this method is significantly faster and milder, enabling tailored, in situ encapsulation without the need for numerous immobilization steps and laborious purification. Furthermore, the use of acid elution rather than calcination opens the possibility of organic surface functionalization.
This method is highly applicable to those working in active species immobilization who have found physisorption or covalent immobilization to be ineffective. It is also useful for those researching process scale-up as the bioinspired synthesis is uniquely positioned for industrialisation compared to conventional templated silica materials.13,14 This method is not recommended for applications which require an ordered array of pores within the material e.g.,for photonics, as the material structure is disordered despite any similarity in bulk properties.

<table border="0" cellpadding="0" cellspacing="0" style="width:672px;" width="670">
	<tbody>
		<tr height="21">
			<td height="21" style="height:21px;width:139px;">Silica synthesis</td>
			<td style="width:223px;"></td>
			<td style="width:123px;"></td>
			<td style="width:188px;"></td>
		</tr>
		<tr height="42">
			<td height="42" style="height:42px;width:139px;">Sodium silicate pentahydrate</td>
			<td style="width:223px;">Fisher scientific</td>
			<td style="width:123px;">10070470</td>
			<td></td>
		</tr>
		<tr height="42">
			<td height="42" style="height:42px;width:139px;">Pentaethylene hexamine (PEHA)</td>
			<td style="width:223px;">Sigma-Aldrich</td>
			<td>292753</td>
			<td></td>
		</tr>
		<tr height="42">
			<td height="42" style="height:42px;width:139px;">Diethylenetriamine (DETA)</td>
			<td style="width:223px;">Sigma-Aldrich</td>
			<td style="width:123px;">D93856</td>
			<td>Toxic</td>
		</tr>
		<tr height="42">
			<td height="42" style="height:42px;width:139px;">Triethylenetetraamine (TETA)</td>
			<td style="width:223px;">Sigma-Aldrich</td>
			<td style="width:123px;">90460</td>
			<td></td>
		</tr>
		<tr height="42">
			<td height="42" style="height:42px;width:139px;">Poly(ethyleneimine) (PEI)</td>
			<td style="width:223px;">Polysciences</td>
			<td style="width:123px;">6088</td>
			<td>1.2K MW</td>
		</tr>
		<tr height="63">
			<td height="63" style="height:63px;width:139px;">Poly(allylamine hydrochloride) (PAH)</td>
			<td style="width:223px;">Sigma-Aldrich</td>
			<td style="width:123px;">283215</td>
			<td>17.5k MW</td>
		</tr>
		<tr height="42">
			<td height="42" style="height:42px;width:139px;">Bovine Serum Albumin (BSA)</td>
			<td style="width:223px;">Sigma-Aldrich</td>
			<td style="width:123px;">A2153</td>
			<td></td>
		</tr>
		<tr height="43">
			<td height="43" style="height:43px;width:139px;">Hydrochloric acid (HCl) 1M</td>
			<td style="width:223px;">Fisher Scientific</td>
			<td style="width:123px;">10487830</td>
			<td></td>
		</tr>
		<tr height="42">
			<td height="42" style="height:42px;width:139px;">Silicomolybdic acid assay</td>
			<td style="width:223px;"></td>
			<td style="width:123px;"></td>
			<td></td>
		</tr>
		<tr height="63">
			<td height="63" style="height:63px;width:139px;">Ammonium molybdate tetrahydrate</td>
			<td style="width:223px;">Sigma-Aldrich</td>
			<td style="width:123px;">A7302</td>
			<td>Product replaced by M1019</td>
		</tr>
		<tr height="42">
			<td height="42" style="height:42px;width:139px;">Hydrochloric acid (HCl) 37.0%wt</td>
			<td style="width:223px;">Fluka Analytical</td>
			<td>84436</td>
			<td></td>
		</tr>
		<tr height="42">
			<td height="42" style="height:42px;width:139px;">Anhydrous oxalic acid</td>
			<td style="width:223px;">Sigma-Aldrich</td>
			<td style="width:123px;">75688</td>
			<td></td>
		</tr>
		<tr height="42">
			<td height="42" style="height:42px;width:139px;">Para-aminophenol sulphate</td>
			<td style="width:223px;">Fisher Scientific</td>
			<td style="width:123px;">10446880</td>
			<td></td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:139px;">Sodium sulphite</td>
			<td style="width:223px;">Fisher Scientific</td>
			<td style="width:123px;">10234400</td>
			<td></td>
		</tr>
		<tr height="22">
			<td height="22" style="height:22px;width:139px;">Sulphuric acid</td>
			<td style="width:223px;">Sigma-Aldrich</td>
			<td style="width:123px;">84727</td>
			<td></td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:139px;">Bradford assay</td>
			<td style="width:223px;"></td>
			<td style="width:123px;"></td>
			<td></td>
		</tr>
		<tr height="22">
			<td height="22" style="height:22px;width:139px;">Bradford reagent</td>
			<td style="width:223px;">Sigma-Aldrich</td>
			<td style="width:123px;">B6916</td>
			<td></td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:139px;">Equipment</td>
			<td style="width:223px;"></td>
			<td style="width:123px;"></td>
			<td></td>
		</tr>
		<tr height="42">
			<td height="42" style="height:42px;width:139px;">Autotitrator Titrando 902</td>
			<td style="width:223px;">Metrohm</td>
			<td style="width:123px;">2.902.0010</td>
			<td></td>
		</tr>
		<tr height="42">
			<td height="42" style="height:42px;width:139px;">801 magnetic stirrer plate</td>
			<td style="width:223px;">Metrohm</td>
			<td style="width:123px;">2.801.0040</td>
			<td>For use with above</td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:139px;">800 Dosino</td>
			<td style="width:223px;">Metrohm</td>
			<td style="width:123px;">2.800.0010</td>
			<td>For use with above</td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:139px;">Aquatrode Plus</td>
			<td style="width:223px;">Metrohm</td>
			<td style="width:123px;">6.0253.100</td>
			<td>For use with above</td>
		</tr>
		<tr height="42">
			<td height="42" style="height:42px;width:139px;">Centrifuge Sorvall ST16</td>
			<td style="width:223px;">Thermo Scientific</td>
			<td style="width:123px;">11814243</td>
			<td>Code is for Fisher scientific</td>
		</tr>
		<tr height="64">
			<td height="64" style="height:64px;width:139px;">UV-Vis spectrophotometer Genesys 10A</td>
			<td style="width:223px;">Thermo scientific</td>
			<td style="width:123px;">12104972</td>
			<td>Code is for Fisher scientific</td>
		</tr>
	</tbody>
</table>

preparation of functional silica using a bioinspired method

The goal of the protocols described herein is to synthesize bioinspired silica materials, perform enzyme encapsulation therein, and partially or totally purify the same by acid elution. By combining sodium silicate with a polyfunctional bioinspired additive, silica is rapidly formed at ambient conditions upon neutralization. 
The effect of neutralization rate and biomolecule addition point on silica yield are investigated, and biomolecule immobilization efficiency is reported for varying addition point. In contrast to other porous silica synthesis methods, it is shown that the mild conditions required for bioinspired silica synthesis are fully compatible with the encapsulation of delicate biomolecules. Additionally, mild conditions are used across all synthesis and modification steps, making bioinspired silica a promising target for the scale-up and commercialization as both a bare material and active support medium.
The synthesis is shown to be highly sensitive to conditions, i.e., the neutralization rate and final synthesis pH, however tight control over these parameters is demonstrated through the use of auto titration methods, leading to high reproducibility in reaction progression pathway and yield. 
Therefore, bioinspired silica is an excellent active material support choice, showing versatility towards many current applications, not limited to those demonstrated here, and potency in future applications.

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 &#177; 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 &#39;oligomers&#39;, 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 &#39;oligomer&#39; 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 &#39;undershoot&#39; case the pH is held higher for longer, allowing for individual particles to grow and hence aiding efficient coagulation; in the &#39;overshoot&#39; 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 &#181;g/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.
<table border="1" fo:keep-together.within-page="1" fo:keep-with-next.within-page="always">
	<tbody>
		<tr>
			<td>Cuvette No</td>
			<td>Concentration of BSA (mg/mL)</td>
			<td>Bradford reagent (mL)</td>
			<td>Sample (mL)</td>
		</tr>
		<tr>
			<td>0</td>
			<td>0 (control)</td>
			<td>1.5</td>
			<td>0.05</td>
		</tr>
		<tr>
			<td>1</td>
			<td>0.1</td>
			<td>1.5</td>
			<td>0.05</td>
		</tr>
		<tr>
			<td>2</td>
			<td>0.25</td>
			<td>1.5</td>
			<td>0.05</td>
		</tr>
		<tr>
			<td>3</td>
			<td>0.5</td>
			<td>1.5</td>
			<td>0.05</td>
		</tr>
		<tr>
			<td>4</td>
			<td>0.75</td>
			<td>1.5</td>
			<td>0.05</td>
		</tr>
		<tr>
			<td>5</td>
			<td>1</td>
			<td>1.5</td>
			<td>0.05</td>
		</tr>
		<tr>
			<td>6</td>
			<td>1.25</td>
			<td>1.5</td>
			<td>0.05</td>
		</tr>
		<tr>
			<td>7</td>
			<td>Unknown sample (X)</td>
			<td>1.5</td>
			<td>0.05</td>
		</tr>
	</tbody>
</table>
Table 1: Macro Bradford assay set-up and calculated component volumes. Valid for determination range 0.1-1.4mg/mL (volumes for 1 replicate)
<table border="1" fo:keep-together.within-page="1" fo:keep-with-next.within-page="always">
	<tbody>
		<tr>
			<td>Cuvette No</td>
			<td>Concentration of BSA (ug/mL)</td>
			<td>Bradford reagent (mL)</td>
			<td>Sample (mL)</td>
		</tr>
		<tr>
			<td>0</td>
			<td>0 (control)</td>
			<td>1</td>
			<td>1</td>
		</tr>
		<tr>
			<td>1</td>
			<td>1</td>
			<td>1</td>
			<td>1</td>
		</tr>
		<tr>
			<td>2</td>
			<td>2.5</td>
			<td>1</td>
			<td>1</td>
		</tr>
		<tr>
			<td>3</td>
			<td>5</td>
			<td>1</td>
			<td>1</td>
		</tr>
		<tr>
			<td>4</td>
			<td>7.5</td>
			<td>1</td>
			<td>1</td>
		</tr>
		<tr>
			<td>5</td>
			<td>10</td>
			<td>1</td>
			<td>1</td>
		</tr>
		<tr>
			<td>6</td>
			<td>Unknown sample (X)</td>
			<td>1</td>
			<td>1</td>
		</tr>
	</tbody>
</table>
Table 2: Micro Bradford assay set-up and calculated component volumes. Valid for determination range 1-10 &#181;g/mL (volumes for 1 replicate)
<img alt="Figure 1" class="xfigimg" src="/files/ftp_upload/57730/57730fig1.jpg" /> 
Figure 1:&#160;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.
<img alt="Figure 2" class="xfigimg" src="/files/ftp_upload/57730/57730fig2.jpg" /> 
Figure 2:&#160;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.&#160;
<img alt="Figure 3" class="xfigimg" src="/files/ftp_upload/57730/57730fig3.jpg" /> 
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.
<img alt="Figure 4" class="xfigimg" src="/files/ftp_upload/57730/57730fig4.jpg" /> 
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 &#39;oligomers&#39; (blue) and unstable coagulating silica (yellow).
<img alt="Figure 5" class="xfigimg" src="/files/ftp_upload/57730/57730fig5.jpg" /> 
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 &#177; 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 &#39;undershoot,&#39; &#39;baseline,&#39; and &#39;overshoot&#39; was 6.90, 7.05, and 7.20mL respectively.&#160;
<img alt="Figure 6" class="xfigimg" src="/files/ftp_upload/57730/57730fig6.jpg" /> 
Figure 6:&#160;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.&#160;
<img alt="Figure 7" class="xfigimg" src="/files/ftp_upload/57730/57730fig7.jpg" /> 
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.&#160;
<img alt="Figure 8" class="xfigimg" src="/files/ftp_upload/57730/57730fig8.jpg" /> 
Figure 8:&#160;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.&#160;
<img alt="Figure 9" class="xfigimg" src="/files/ftp_upload/57730/57730fig9.jpg" /> 
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.

Watch this Scientific Journal Video about Preparation of Functional Silica Using a Bioinspired Method at JoVE.com

Preparation of Functional Silica Using a Bioinspired Method

Here, we present a protocol to synthesize bioinspired silica materials and immobilize enzymes therein. Silica is synthesized by combining sodium silicate and an amine &#39;additive&#39;, which neutralize at a controlled rate. Material properties and function can be altered either by in situ enzyme immobilization or post-synthetic acid elution of encapsulated additives.

The goal of the protocols described herein is to synthesize bioinspired silica materials, perform enzyme encapsulation therein, and partially or totally ...

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17.0K Views.  University of Sheffield. Here, we present a protocol to synthesize bioinspired silica materials and immobilize enzymes therein. Silica is synthesized by combining sodium silicate and an amine 'additive', which neutralize at a controlled rate. Material properties and function can be altered either by in situ enzyme immobilization or post-synthetic acid elution of encapsulated additives.

Video: Preparation of Functional Silica Using a Bioinspired Method

Preparation of Silica Nanoparticles Through Microwave-assisted Acid-catalysis

Microwave-assisted synthetic techniques were used to quickly and reproducibly produce silica nanoparticle sols using an acid catalyst with nanoparticle diameters ranging from 30-250 nm by varying the reaction conditions. Through the selection of a microwave compatible solvent, silicic acid precursor, catalyst, and microwave irradiation time, these microwave-assisted methods were capable of overcoming the previously reported shortcomings associated with synthesis of silica nanoparticles using microwave reactors. The siloxane precursor was hydrolyzed using the acid catalyst, HCl. Acetone, a low-tan &#948; solvent, mediates the condensation reactions and has minimal interaction with the electromagnetic field. Condensation reactions begin when the silicic acid precursor couples with the microwave radiation, leading to silica nanoparticle sol formation. The silica nanoparticles were characterized by dynamic light scattering data and scanning electron microscopy, which show the materials&#39; morphology and size to be dependent on the reaction conditions. Microwave-assisted reactions produce silica nanoparticles with roughened textured surfaces that are atypical for silica sols produced by St&#246;ber&#39;s methods, which have smooth surfaces.

Silica nanoparticles were prepared using acid-catalysis of a siloxane precursor and microwave-assisted synthetic techniques resulting in the controlled growth of nanomaterials ranging from 30-250 nm in diameter. The growth dynamics can be controlled by varying the initial silicic acid concentration, time of the reaction, and temperature of reaction.

Microwave-assisted synthetic techniques were used to quickly and reproducibly produce silica nanoparticle sols using an acid catalyst with nanoparticle ...

Preparing Silica Aerogel Monoliths via a Rapid Supercritical Extraction Method

A procedure for the fabrication of monolithic silica aerogels in eight hours or less via a rapid supercritical extraction process is described. The procedure requires 15-20 min of preparation time, during which a liquid precursor mixture is prepared and poured into wells of a metal mold that is placed between the platens of a hydraulic hot press, followed by several hours of processing within the hot press. The precursor solution consists of a 1.0:12.0:3.6:3.5 x 10-3 molar ratio of tetramethylorthosilicate (TMOS):methanol:water:ammonia. In each well of the mold, a porous silica sol-gel matrix forms. As the temperature of the mold and its contents is increased, the pressure within the mold rises. After the temperature/pressure conditions surpass the supercritical point for the solvent within the pores of the matrix (in this case, a methanol/water mixture), the supercritical fluid is released, and monolithic aerogel remains within the wells of the mold. With the mold used in this procedure, cylindrical monoliths of 2.2 cm diameter and 1.9 cm height are produced. Aerogels formed by this rapid method have comparable properties (low bulk and skeletal density, high surface area, mesoporous morphology) to those prepared by other methods that involve either additional reaction steps or solvent extractions (lengthier processes that generate more chemical waste).The rapid supercritical extraction method can also be applied to the fabrication of aerogels based on other precursor recipes.

This article describes a rapid supercritical extraction method for fabricating silica aerogels. By utilizing a confined mold and hydraulic hot press, monolithic aerogels can be made in eight hours or less.

A procedure for the fabrication of monolithic silica aerogels in eight hours or less via a rapid supercritical extraction process is described. The ...

Synthesis and Catalytic Performance of Gold Intercalated in the Walls of Mesoporous Silica

As a promising catalytically active nano reactor, gold nanoparticles intercalated in mesoporous silica (GMS) were successfully synthesized and properties of the materials were investigated. We used a one pot sol-gel approach to intercalate gold nano particles in the walls of mesoporous silica. To start with the synthesis, P123 was used as template to form micelles. Then TESPTS was used as a surface modification agent to intercalate gold nano particles. Following this process, TEOS was added in as a silica source which underwent a polymerization process in acid environment. After hydrothermal processing and calcination, the final product was acquired. Several techniques were utilized to characterize the porosity, morphology and structure of the gold intercalated mesoporous silica. The results showed a stable structure of mesoporous silica after gold intercalation. Through the oxidation of benzyl alcohol as a benchmark reaction, the GMS materials showed high selectivity and recyclability.

Here, we present a protocol with a sol-gel process to synthesize gold intercalated in the walls of mesoporous materials (GMS), which is confirmed to possess a mesoporous matrix with gold intercalated in the walls imparting great stability and recyclability.

As a promising catalytically active nano reactor, gold nanoparticles intercalated in mesoporous silica (GMS) were successfully synthesized and properties ...

Real-time Monitoring of Reactions Performed Using Continuous-flow Processing: The Preparation of 3-Acetylcoumarin as an Example

By using inline monitoring, it is possible to optimize reactions performed using continuous-flow processing in a simple and rapid way. It is also possible to ensure consistent product quality over time using this technique. We here show how to interface a commercially available flow unit with a Raman spectrometer. The Raman flow cell is placed after the back-pressure regulator, meaning that it can be operated at atmospheric pressure. In addition, the fact that the product stream passes through a length of tubing before entering the flow cell means that the material is at RT. It is important that the spectra are acquired under isothermal conditions since Raman signal intensity is temperature dependent. Having assembled the apparatus, we then show how to monitor a chemical reaction, the piperidine-catalyzed synthesis of 3-acetylcoumarin from salicylaldehyde and ethyl acetoacetate being used as an example. The reaction can be performed over a range of flow rates and temperatures, the in-situ monitoring tool being used to optimize conditions simply and easily.

Real-time monitoring allows for fast optimization of reactions performed using continuous-flow processing. Here the preparation of 3-acetylcoumarin is used as an example. The apparatus for performing in-situ Raman monitoring is described, as are the steps required to optimize the reaction.

By using inline monitoring, it is possible to optimize reactions performed using continuous-flow processing in a simple and rapid way. It is also possible ...

Layer-by-layer Synthesis and Transfer of Freestanding Conjugated Microporous Polymer Nanomembranes

CMP as large surface area materials have attracted growing interest recently, due to their high variability in the incorporation of functional groups in combination with their outstanding thermal and chemical stability, and low densities. However, their insoluble nature causes problems in their processing since usually applied techniques such as spin coating are not available. Especially for membrane applications, where the processing of CMP as thin films is desirable, the processing problems have hindered their commercial application.
Here we describe the interfacial synthesis of CMP thin films on functionalized substrates via molecular layer-by-layer (l-b-l) synthesis. This process allows the preparation of films with desired thickness and composition and even desired composition gradients.
The use of sacrificial supports allows the preparation of freestanding membranes by dissolution of the support after the synthesis. To handle such ultra-thin freestanding membranes the protection with sacrificial coatings showed great promise, to avoid rupture of the nanomembranes. To transfer the nanomembranes to the desired substrate, the coated membranes are upfloated at the air-liquid interface and then transferred via dip coating.

In this paper we describe the interfacial synthesis of conjugated microporous polymers (CMP) on sacrificial substrates, and the dissolution of the substrate for the preparation of freestanding CMP nanomembranes. In addition, we will describe how the fragile nanomembranes can be transferred to other substrates.

CMP as large surface area materials have attracted growing interest recently, due to their high variability in the incorporation of functional groups in ...

Preparation of Biopolymer Aerogels Using Green Solvents

Although the first reports on aerogels made by Kistler1 in the 1930s dealt with aerogels from both inorganic oxides (silica and others) and biopolymers (gelatin, agar, cellulose), only recently have biomasses been recognized as an abundant source of chemically diverse macromolecules for functional aerogel materials. Biopolymer aerogels (pectin, alginate, chitosan, cellulose, etc.) exhibit both specific inheritable functions of starting biopolymers and distinctive features of aerogels (80-99% porosity and specific surface up to 800 m2/g). This synergy of properties makes biopolymer aerogels promising candidates for a wide gamut of applications such as thermal insulation, tissue engineering and regenerative medicine, drug delivery systems, functional foods, catalysts, adsorbents and sensors. This work demonstrates the use of pressurized carbon dioxide (5 MPa) for the ionic cross linking of amidated pectin into hydrogels. Initially a biopolymer/salt dispersion is prepared in water. Under pressurized CO2 conditions, the pH of the biopolymer solution is lowered to 3 which releases the crosslinking cations from the salt to bind with the biopolymer yielding hydrogels. Solvent exchange to ethanol and further supercritical CO2 drying (10 - 12 MPa) yield aerogels. Obtained aerogels are ultra-porous with low density (as low as 0.02 g/cm3), high specific surface area (350 - 500 m2/g) and pore volume (3 - 7 cm3/g for pore sizes less than 150 nm).

A new way for the production of biopolymer-based aerogels by carbon dioxide (CO2) induced gelation is shown. The technique utilizes pressurized carbon dioxide (5 MPa) for the production of biopolymer hydrogels and supercritical CO2 (12 MPa) to convert gels into aerogels. The only solvents needed besides CO2 are water and ethanol.

Although the first reports on aerogels made by Kistler1 in the 1930s dealt with aerogels from both inorganic oxides (silica and others) and biopolymers ...

Sediment Core Extrusion Method at Millimeter Resolution Using a Calibrated, Threaded-rod

Aquatic sediment core subsampling is commonly performed at cm or half-cm resolution. Depending on the sedimentation rate and depositional environment, this resolution provides records at the annual to decadal scale, at best. An extrusion method, using a calibrated, threaded-rod is presented here, which allows for millimeter-scale subsampling of aquatic sediment cores of varying diameters. Millimeter scale subsampling allows for sub-annual to monthly analysis of the sedimentary record, an order of magnitude higher than typical sampling schemes. The extruder consists of a 2 m aluminum frame and base, two core tube clamps, a threaded-rod, and a 1 m piston. The sediment core is placed above the piston and clamped to the frame. An acrylic sampling collar is affixed to the upper 5 cm of the core tube and provides a platform from which to extract sub-samples. The piston is rotated around the threaded-rod at calibrated intervals and gently pushes the sediment out the top of the core tube. The sediment is then isolated into the sampling collar and placed into an appropriate sampling vessel (e.g., jar or bag). This method also preserves the unconsolidated samples (i.e., high pore water content) at the surface, providing a consistent sampling volume. This mm scale extrusion method was applied to cores collected in the northern Gulf of Mexico following the Deepwater Horizon submarine oil release. Evidence suggests that it is necessary to sample at the mm scale to fully characterize events that occur on the monthly time-scale for continental slope sediments.

An extrusion method using a calibrated threaded-rod is presented, which allows for mm scale subsampling of aquatic sediment cores. Millimeter-scale sampling is necessary to fully characterize recent event stratigraphy in sediment records.

Aquatic sediment core subsampling is commonly performed at cm or half-cm resolution. Depending on the sedimentation rate and depositional environment, ...

Determination of Carbonyl Functional Groups in Bio-oils by Potentiometric Titration: The Faix Method

Carbonyl compounds present in bio-oils are known to be responsible for bio-oil property changes upon storage and during upgrading. Specifically, carbonyls cause an increase in viscosity (often referred to as &#39;aging&#39;) during storage of bio-oils. As such, carbonyl content has previously been used as a method of tracking bio-oil aging and condensation reactions with less variability than viscosity measurements. Additionally, carbonyls are also responsible for coke formation in bio-oil upgrading processes. Given the importance of carbonyls in bio-oils, accurate analytical methods for their quantification are very important for the bio-oil community. Potentiometric titration methods based on carbonyl oximation have long been used for the determination of carbonyl content in pyrolysis bio-oils. Here, we present a modification of the traditional carbonyl oximation procedures that results in less reaction time, smaller sample size, higher precision, and more accurate carbonyl determinations. While traditional carbonyl oximation methods occur at room temperature, the Faix method presented here occurs at an elevated temperature of 80 &#176;C.

Here we present a potentiometric titration technique for accurately quantifying carbonyl compounds in pyrolysis bio-oils.

Carbonyl compounds present in bio-oils are known to be responsible for bio-oil property changes upon storage and during upgrading. Specifically, carbonyls ...

Preparation and Evaluation of 99mTc-labeled Tridentate Chelates for Pre-targeting Using Bioorthogonal Chemistry

Pre-targeting combined with bioorthogonal chemistry is emerging as an effective way to create new radiopharmaceuticals. Of the methods available, the inverse electron demand Diels-Alder (IEDDA) cycloaddition between a radiolabeled tetrazines and trans-cyclooctene (TCO) linked to a biomolecule has proven to be a highly effective bioorthogonal approach to imaging specific biological targets. Despite the fact that technetium-99m remains the most widely used isotope in diagnostic nuclear medicine, there is a scarcity of methods for preparing 99mTc-labeled tetrazines. Herein we report the preparation of a family of tridentate-chelate-tetrazine derivatives and their Tc(I) complexes. These hitherto unknown compounds were radiolabeled with 99mTc using a microwave-assisted method in 31% to 83% radiochemical yield. The products are stable in saline and PBS and react rapidly with TCO derivatives in vitro. Their in vivo pre-targeting abilities were demonstrated using a TCO-bisphosphonate (TCO-BP) derivative that localizes to regions of active bone metabolism or injury. In murine studies, the 99mTc-tetrazines showed high activity concentrations in knees and shoulder joints, which was not observed when experiments were performed in the absence of TCO-BP. The overall uptake in non-target organs and pharmacokinetics varied greatly depending on the nature of the linker and polarity of the chelate.

Preparation and Evaluation of 99mTc-labeled Tridentate Chelates for Pre-targeting Using Bioorthogonal Chemistry

Here, we describe a protocol for radiolabeling and in vivo testing of tridentate 99mTc(I) chelate-tetrazine derivatives for pre-targeting and bioorthogonal chemistry.

Pre-targeting combined with bioorthogonal chemistry is emerging as an effective way to create new radiopharmaceuticals. Of the methods available, the ...

Surface Properties of Synthesized Nanoporous Carbon and Silica Matrices

In this work, we report the synthesis and characterization of ordered nanoporous carbon material (also called ordered mesoporous carbon material [OMC]) with a 4.6 nm pore size, and ordered silica porous matrix, SBA-15, with a 5.3 nm pore size. This work describes the surface properties of nanoporous molecular sieves, their wettability, and the melting behavior of D2O confined in the differently ordered porous materials with similar pore sizes. For this purpose, OMC and SBA-15 with highly ordered nanoporous structures are synthesized via impregnation of the silica matrix by applying a carbon precursor and by the sol-gel method, respectively. The porous structure of investigated systems is characterized by an N2 adsorption-desorption analysis at 77 K. To determine the electrochemical character of the surface of synthesized materials, potentiometric titration measurements are conducted; the obtained results for OMC shows a significant pHpzc shift toward the higher values of pH, relative to SBA-15. This suggests that investigated OMC has surface properties related to oxygen-based functional groups. To describe the surface properties of the materials, the contact angles of liquids penetrating the studied porous beds are also determined. The capillary rise method has confirmed the increased wettability of the silica walls relative to the carbon walls and an influence of the pore roughness on the fluid/wall interactions, which is much more pronounced for silica than for carbon mesopores. We have also studied the melting behavior of D2O confined in OMC and SBA-15 by applying the dielectric method. The results show that the depression of the melting temperature of D2O in the pores of OMC is about 15 K higher relative to the depression of the melting temperature in SBA-15 pores with a comparable 5 nm size. This is caused by the influence of adsorbate/adsorbent interactions of the studied matrices.

Here we report the synthesis and characterization of ordered nanoporous carbon (with a 4.6 nm pore size) and SBA-15 (with a 5.3 nm pore size). The work describes the surface and textural properties of nanoporous molecular sieves, their wettability, and the melting behavior of D2O confined in the materials.

In this work, we report the synthesis and characterization of ordered nanoporous carbon material (also called ordered mesoporous carbon material [OMC]) ...