| Literature DB >> 36161096 |
Robert Pilling1, Siddharth V Patwardhan1.
Abstract
Global specialty silica production is over 3 million tonnes per annum with diverse applications across sectors and an increasing demand for more complex material structures and surface chemistries. Commercial manufacturing of high-value silica nanomaterials is energy and resource intensive. In order to meet market needs and mitigate environmental impacts, new synthesis methods for these porous materials are required. The development of the bioinspired silica (BIS) product system, which is the focus of this review, provides a potential solution to this challenge. BIS is a versatile and greener route with the prospect of good scalability, attractive process economics and well controlled product materials. The potential of the system lies not only in its provision of specific lead materials but also, as itself, a rich design-space for the flexible and potentially predictive design of diverse sustainable silica nanomaterials. Realizing the potential of this design space, requires an integrative mind-set, which enables parallel and responsive progression of multiple and dependent research strands, according to need, opportunities, and emergent knowledge. Specifically, this requires development of detailed understanding of (i) the pathways and extent of material diversity and control, (ii) the influences and mechanisms of scale-up, and (iii) performance, economic and environmental characteristics and sensitivities. Crucially, these need to be developed for the system overall, which sits in contrast to a more traditional research approach, which focuses initially on the discovery of specific material leads at the laboratory scale, leaving scale-up, commercialization, and, potentially, pathway understanding to be considered as distinctly separate concerns. The intention of this review is to present important recent advances made in the field of BIS. Specifically, advances made along three research themes will be discussed: (a) particle formation pathways, (b) product design, and (c) scale-up and manufacture. These advances include first quantitative investigation of synthesis-product relationships, first structured investigation of mixing effects, preparation of a broad range of functionalized and encapsulated silica materials and continued industrial engagement and market research. We identify future challenges and provide an important foundation for the development of new research avenues. These include the need to develop comprehensive and predictive product design models, to understand markets in terms of product cost, performance and environmental considerations, and to develop capabilities enabling rapid prototyping and scale-up of desired nanomaterials.Entities:
Year: 2022 PMID: 36161096 PMCID: PMC9490786 DOI: 10.1021/acssuschemeng.2c02204
Source DB: PubMed Journal: ACS Sustain Chem Eng ISSN: 2168-0485 Impact factor: 9.224
Figure 1Bioinspired silica development pipeline. Image reproduced with permission from Patwardhan, S. V.; Staniland, S. S.[8]
Figure 2System-based product design research framework.
Figure 3Overview of BIS synthesis, formation pathways, their compositional subtypes, and particle structures. (a) The chemical formation of bioinspired silica (image reproduced with permission from Dewulf et al.)[16] and (b) the physical formation of bioinspired silica. (c) Three compositional subtypes of bioinspired silica. (d) Multiscale particle structure of bioinspired silica showing a representative SEM image (left) and TEM image (middle) of as-made BIS. Right schematic shows the primary particles and the additives aggregated. Image adapted with permission from Entwistle et al.[17]
Figure 4(a–d) Porosity of bioinspired silica when using different additives (a–c). (d) Removal of the additives/purification via Calcination (C), acid elution (A) or acid elution followed by calcination (A+C). Images reproduced with permission from Routoula (a–c) and Manning et al. (d).[23,25] Note that the difference between samples denoted C and A (or A+C) in Figure d is from the method, not the extent of removal (which is ∼100% for both). Calcination is known to create local “explosions” with the additives burning and leading to fracturing some pore walls/damaging pores, hence higher specific surface area.
Figure 5Selected characteristics mapped to a broad depiction of the BIS material design space.
Figure 6Schematic showing control of the properties of biosinspired silica with an example of ethyleneamine additives. Properties in red colored text can be tuned by varying parameters in blue text. an denotes the number of repeat units in the ethyleneamine additives used. bRoom temperature acid elution removes additives (fully for smaller and partially for larger additives, for details, see refs (23 and 26)). cCalcination is used for fully removing larger additives. *Refers to internal porosity and excludes external porosity arising from interparticle pores.
Figure 7(Left) Process flow diagram and (right) photo of larger scale BIS production apparatus operated in a 5 L continuous stirred tank reactor. The units are marked as follows. A, B - feedstock tanks (TK-01, TK-02); C, E - pumps (P-01, P-02); D - reactor (R-01); F - filtration (S-01, S-02); G - waste filtrate tank (TK-03); H - overflow tank; H-01 - drying oven. Images reproduced with permission from Manning.[27]
Comparison of BIS with MCM-41 as a Current Benchmark Material, Adapted from Ref (10)
| Reaction conditions | ||||||||||
|---|---|---|---|---|---|---|---|---|---|---|
| Silica type | Reagents | Solvents | pH | Byproducts | Yield | Finishing | Cost (£/kg) | |||
| Mesoporous - MCM-41[ | Silicate, CTAB, ammonia | Water | 2–6days | 20–120 | ∼9 | Alcohol, NO | 12 (60, 900) | 17 | Calcination (550 °C, 6 h) | >1000 |
| Bioinspired | Silicate and additive | Water | 5–20min | 20 | 7 | NaCl | 5 (30, 85) | Up to 38 | Centrifuge, dry | 1.5–5 |
Silicate = sodium silicate or water glass, CTAB = cetyltrimethylammonium bromide.
Calculated from representative internal results; numbers in parentheses include reaction solvent, reaction solvent + washing/purification solvent.
Chemical Reaction Space for Bioinspired Silica Preparation
| Chemistry | Relevant range/options | Notes |
|---|---|---|
| Amine additive | Varying origins (natural, biological, synthetic), molecular sizes (small, polymeric), architectures (linear, branched), and chemistries (N substitution, modifications). | There is a huge range of additives used, and additive “type” has a profound influence on silica formed. |
| Silicon precursor | Alkoxysilane, sodium silicates, Si-catecholate complex, modified silanes | Need to consider what trigger is required to start the reaction, effects on reactions/products, scalability, sustainability, and costs. |
| Ratio of precursor to additive | [Si]:[N] = 0.5–16 | Main focus has been on the ratio of 1, but some studies used <0.5. |
| Reagent concentration | [Si] = 20–100 mM | There are also studies at <20 (8 and even 1 mM) and >100 mM (up to 660 mM). |
| pH | 6–8, some at as low as 4 | Generally controlled with a buffer (if not using sodium silicate) or simply by neutralization. |
| Others | Use of cosolvents and the type of acids used for hydrolysis | |
Physical Reaction Space for Bioinspired Silica Preparation
| Physics | Relevant range/options | Notes |
|---|---|---|
| Reaction time | Typically 5–60 min | Also <1 min and >1 h (to a day or more) |
| Temperature | ∼20 °C | This is generally kept constant but can be easily varied |
| Addition order/rate | Rarely studied | We found the order makes
a difference (e.g., acid added to Si-source or amine or after mixing
Si and N).[ |
| Mixing type/rate | Rarely studied/completely unknown | Preliminary
work shows that
flow ( |
| Reactor type | Batch, micro- and milli-fluidic devices, plug flow reactor | Very little understanding available |
| Others | Separation and drying also has an impact on the properties of silica produced. |
Figure 8Three-dimensional response surfaces for (a) the silica yield and (b) the Brunauer, Emmett, and Teller (BET) surface area. (c) Overlaid contour plot of the model for silica yield (blue) and silica BET surface area (red) for optimization of both responses simultaneously. The gray region enables to synthesize silica with the constraints that the yield should exceed 60 mol % and the BET surface area should exceed 100 m2/g. Figures reproduced with permission from Dewulf et al.[16]
Figure 9(a) Schematic representation of mixing and reaction kinetics change with scales. (b) Sensitivity of bioinspired silica products to scale-up.
Figure 10Discrete sol–gel silica product families. Using a variety of additives, most commonly amine-based organic molecules, several families of silica materials developed are shown with controlled particle and pore morphology on multiple length scales. Image reproduced with permission from Manning et al.[28]
Figure 11Schematic showing (from left to right) how the knowledge gained from BIS, when applied to discrete sol–gel silica materials, helped unify them into a single sol–gel silica family with clarity on overlaps and intersections. Image in the right is reproduced with permission from Manning et al.[28]
Market Segmentation and Prospects for Bioinspired Silica Products
| Product | Typical properties | Cost and volume | Comparative
BIS cost | Prospects | Progress | Outlook |
|---|---|---|---|---|---|---|
| Industrial precipitated silica (IPS) | Surface area 100–300 m2/g | Low < £1/kg | Comparable £1.5–2.0/kg | Direct substitution (tires): BIS materials offer comparable cost and performance in traditional applications, the largest of which is in the manufacture of tires. | Early promise in the tire sector, with BIS offering potential for a new supplier to enter an otherwise IP protected market. | Investment hurdles appear insurmountable for traditional applications, at least in the medium term. BIS cost would need to drop further for this calculus to change. |
| Pore volume (not generally reviewed) | High Mt/y | |||||
| Advanced materials (batteries):
An important and emerging new application is that of Li-ion batteries.
BIS materials are an attractive precursor for silicon anodes, showing
higher performance than alternative silica materials with comparable
cost. | BIS materials have been shown as a viable source for LiB anodes, with the scale-up of Si for anodes demonstrated. | BIS materials show significant promise for emerging application in the manufacturer of LiB anodes; development work continues. | ||||
| Porous sol and gel silicas (SGS) | Surface area 200–600 m2/g | Medium £1–10/kg | Comparable or Lower £1.5–2.0/kg | Enhanced access/performance (various): BIS materials offer comparable or reduced cost combined with a broader range of performance options, especially for applications requiring larger pore sizes, or functionalized or encapsulated forms, which do not compromise porosity or increase tortuosity. Therefore, the greatest opportunities lie with improving access to less well established products or to establishing entirely new ones (either within this value bracket or extending it upward). | BIS porous gels have been demonstrated for applications in decontamination of air and water via pollutant adsorption. They have also been tested for hosting catalysts and biocatalysts. They show excellent performance in drug delivery. | Development work continues, focused on specific target markets (environmental) with a view to demonstrating efficacy and value using industry accepted performance testing and protocols. |
| Pore volume up to 1.7 cc/g | Medium kt/y | |||||
| Ordered
mesoporous silica
(OMS) | Surface area 500–1000 m2/g | High > £1000/kg | Disruptively low £5–10/kg | Market transformation
(drug delivery): Ordered mesoporous silica is a specialist subset
of SGS with applications, for example, in drug delivery.[ | n/a | BIS has potential to transform this nascent market due to its disruptively low cost, ease of scale-up, and excellent environmental profile. Although, analogous materials have not yet been reported, there is potential for novel strategies, utilizing the BIS driving forces, to direct and enable break-through discovery. |
| Pore volume ∼ 0.5–1 cc/g | Low t/y |
BIS costs are based on data obtained at the lab scale process (unpublished). It is reasonably anticipated that, as for any process, scale-up will reduce costs further.
Laboratory studies report advanced performance, further investigations of the phenomena and its hypothesized structural explanation are ongoing.[10]
OMS may be considered as a specialist subset of SGS.
Figure 12Bioinspired silica nanomaterials: selected material properties, corresponding target applications, and market outlook.
Summary of Recent Advances Made with BIS, Discussed in This Review, Listed with Corresponding External References
| Advances | Summary | Ref. | |
|---|---|---|---|
| 1 | Demonstrated scalability | Preparation of BIS materials has been demonstrated successfully from 2 mL to 40 L scale. 1–100 g quantities of material can be now made, which unlocked research on silicon/silica anodes and testing for other commercial applications. | ( |
| 2 | Enhanced purification | After the core amine mediated process, the amines may be removed via the new discovery of a mild room temperature acidification to provide pure silica products with associated recovery of the valuable amines for reuse. This invention is important from TEA and LCA perspectives. | ( |
| 3 | Synthesis–product relationships | First steps toward quantitative and systematic insight of BIS reactions and products, including important pH dependencies. Also, methodological development, including a sequential DoE strategy and GSA machine learning. | ( |
| 4 | Mixing effects | A first systematic study of mixing effects revealed that nucleation and aggregation steps are sensitive to meso-mixing. | ( |
| 5 | Functionalized and encapsulated silicas | Prior to purification, amine additives remain incorporated within and on the surface of the BIS nanomaterials, thereby offering a single step route to functionalized silica. With modification to the process (i.e., including metal catalysts, biologicals, drug molecules, etc.), in situ encapsulated silicas may also be formed. | ( |
| 6 | Mechanistic studies | A combination of experimental and computational studies established the mediating role of charge-matching between amines and silicates within the formation mechanism with important implications for system understanding, reaction control, and product design. | ( |
| 7 | Characterization studies | Advanced characterization identified significant association between the additives and fully condensed silicon species, leading to higher levels of condensation and greater hydrothermal stability. There are important implications for product performance and mechanistic understanding. | ( |
| 8 | Unified mechanism | A first joined-up mechanistic view of the wider amine-mediated sol–gel silica family. Enables translation of knowledge between the component subtypes and offers the prospect of new, extended, or hybrid materials. | ( |
| 9 | Identification of future challenges | Review paper laying out the sustainability challenges for modern nanomaterials and solutions offered by the bioinspired approach. | ( |
| 10 | Methodology | A reference text for the bioinspired synthesis and sustainable manufacture of inorganic nanomaterials, which includes a widely applicable methodology for discovery to market for green nanomaterials. | ( |
Figure 13Bioinspired silica nanomaterials: recent advances and systematic research challenges. The text is color coded to match the colors of the boxes.