Ultralight Silica Foams with a Hierarchical Pore Structure via a

Aug 8, 2018 - Efficient Propulsion and Hovering of Bubble-Driven Hollow Micromotors underneath an Air–Liquid Interface. Langmuir. Wang, Chen, Zhang ...
1 downloads 0 Views 4MB Size
Subscriber access provided by Kaohsiung Medical University

Interface Components: Nanoparticles, Colloids, Emulsions, Surfactants, Proteins, Polymers

Ultralight silica foams with a hierarchical pore structure via a surfactant-free high internal phase emulsion process Shuhua Tu, Yongliang Zhao, Haotian Tan, Heng Yu, Xiaomin Zhu, and Haitao Wang Langmuir, Just Accepted Manuscript • DOI: 10.1021/acs.langmuir.8b02094 • Publication Date (Web): 08 Aug 2018 Downloaded from http://pubs.acs.org on August 13, 2018

Just Accepted “Just Accepted” manuscripts have been peer-reviewed and accepted for publication. They are posted online prior to technical editing, formatting for publication and author proofing. The American Chemical Society provides “Just Accepted” as a service to the research community to expedite the dissemination of scientific material as soon as possible after acceptance. “Just Accepted” manuscripts appear in full in PDF format accompanied by an HTML abstract. “Just Accepted” manuscripts have been fully peer reviewed, but should not be considered the official version of record. They are citable by the Digital Object Identifier (DOI®). “Just Accepted” is an optional service offered to authors. Therefore, the “Just Accepted” Web site may not include all articles that will be published in the journal. After a manuscript is technically edited and formatted, it will be removed from the “Just Accepted” Web site and published as an ASAP article. Note that technical editing may introduce minor changes to the manuscript text and/or graphics which could affect content, and all legal disclaimers and ethical guidelines that apply to the journal pertain. ACS cannot be held responsible for errors or consequences arising from the use of information contained in these “Just Accepted” manuscripts.

is published by the American Chemical Society. 1155 Sixteenth Street N.W., Washington, DC 20036 Published by American Chemical Society. Copyright © American Chemical Society. However, no copyright claim is made to original U.S. Government works, or works produced by employees of any Commonwealth realm Crown government in the course of their duties.

Page 1 of 33 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

Langmuir

Ultralight silica foams with a hierarchical pore structure via a surfactant-free high internal phase emulsion process Shuhua Tu,† Yongliang Zhao,‡ Haotian Tan,† Heng Yu,† Xiaomin Zhu,*,§ Haitao Wang*,† †

State Key Laboratory of Molecular Engineering of Polymers, Collaborative

Innovation Center of Polymers and Polymer Composite Materials, Department of Macromolecular Science, Fudan University, Shanghai 200433, China ‡

Shanghai Dilato Materials Co., Ltd, Shanghai 200433, China

§

DWI-Leibniz-Institute for Interactive Materials e.V. and Institute for Technical and

Macromolecular Chemistry of RWTH Aachen University, Aachen 52056, Germany

1

ACS Paragon Plus Environment

Langmuir 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

Page 2 of 33

ABSTRACT: Ultralight silica aerogel is among the most versatile materials available for technical applications; however, it remains a huge challenge to reduce its manufacturing cost. Here we report on a simple approach for preparation of silica foam monoliths with ultrahigh porosity up to 99.5% and specific surface area as high as 755 m2 g-1, which are similar to those of aerogel. Our strategy is based on the effective stabilization of water-in-oil high internal phase emulsions by a hydrophobic silica

precursor

polymer,

hyperbranched

polyethoxysiloxane,

due

to

its

hydrolysis-induced amphiphilicity. After conversion of this precursor polymer to silica, the emulsions are solidified without significant volume shrinkage. Thus mechanically strong macroporous silica monoliths are obtained after removal of its liquid components. According to nitrogen sorption data the resulting silica foams exhibit a high specific surface area and a foam skeleton consisting of both micropores (< 2 nm) and mesopores (2 - 50 nm). The pore size, porosity as well as surface area can be regulated by varying pH as well as the concentration of the silica precursor in the oil phase. In addition, the pore size can be adjusted by controlling shear force during emulsification. This work opens a new avenue for producing ultralight porous materials amenable to numerous applications.

Keywords: polyethoxysiloxane, silica monoliths, ultralight nanomaterials, ultrahigh porosity, aerogel, thermal insulation

2

ACS Paragon Plus Environment

Page 3 of 33 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

Langmuir

INTRODUCTION Porous solid materials that are often referred to as cellular solids or solid foams appear widely in nature, forming e.g. the most abundant load-bearing structures such as wood, bone and coral. This has inspired and driven remarkable development of synthetic porous structures. Controlled introduction of porosity into a solid can significantly reduce the density, meanwhile maintaining material properties or even imparting additional functionalities.1,2 Foams can be formed by a large variety of materials, and organic polymer foams are probably the best known examples, and they penetrate into all aspects of our daily life for insulation, cushion, absorption, packaging, etc.3-6 Techniques now exist not only for foaming polymers, but also for metals7 and ceramics.8 In the foam manufacturing process, blowing agents are mostly used. They include gases that expand during the pressure release, liquids that develop to cells while evaporated, and chemical agents that react to generate a gas. A sol-gel method is a process to generate oxide materials from molecular precursors at low temperature, and meso- and microporosity is an inherent feature of the resulting amorphous gels.9 Any kind of structure-directing agents can be added during solidification as porogen to induce the formation of extra pores.10 Examples are molecular species,11 surfactant assemblies,12 emulsion droplets13,14 or solid particles.15 Sol-gel technology can be combined with foaming processes to obtain ceramic foams with big pores.16,17 Among the various porous materials aerogel is probably the most exciting one derived by means of a sol-gel process.18-21 Aerogel designates a gel, in which the liquid dispersed phase has been replaced with a gas.22 It is a solid with a 3

ACS Paragon Plus Environment

Langmuir 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

Page 4 of 33

very high relative pore volume, extremely low density and large surface area. Aerogel can be made from different materials and the first reported one was silica aerogel,23 which is now the most versatile materials available for technical applications.24 The straightforward and most promising application of silica aerogel is thermal insulation due to its extremely low thermal conductivity.25,26 In addition, it can be used in catalysis, sensors, nuclear particle detection, waste management, optics, electronic devices, etc.21,24 The production of silica aerogel often involves the solvent exchange, hydrophobization of silica skeletons, and supercritical drying in order to maintain the porous texture of the wet stage, thus leading to its high price that limits the application field. High internal phase emulsion (HIPE) templating is another route toward well-defined porous materials.27-33 HIPEs are an interesting class of emulsions characterized by an internal phase volume fraction exceeding 74%, the volume ratio of uniform, undistorted spherical droplets in the most compact arrangement.34 The conventional method for manufacturing HIPEs consists of dissolving a suitable emulsifier (a surfactant34-36 or solid particles37-42) in the component constituting the continuous phase followed by stepwise addition of the dispersed phase under continuous moderate stirring. Macroporous materials with embedded emulsion droplets are then obtained by solidification of the continuous phase. By polymerization of water-in-monomer HIPEs polymer foams with a very low density of significantly less than 0.1 g cm-3 can be formed. Inorganic porous materials may also be synthesized by means of HIPE templating. For instance, monodisperse 4

ACS Paragon Plus Environment

Page 5 of 33 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

Langmuir

macroporous materials of silica, titania, and zirconia were prepared by first mixing a monodisperse oil-in-formamide HIPE with a metal oxide sol in formamide followed by gelling the continuous sol phase and subsequent heat treatment.43 This procedure was modified for silicone oil-in-water HIPEs, and macroporous silica with a non-uniform pore size distribution was obtained.44 The combination of HIPE at the macroscale and micellar templates at the mesoscale can lead to materials with dual meso/macroporous structures. In a two-step method organic macroporous foam was first prepared, and it imbibed a sol-gel solution containing inorganic oxide precursor and surfactant molecules, which co-assembled to form an ordered mesostructure.45 The resulting composite material was then dried and calcined in air to obtain the meso/macroporous inorganic material. A single-step method that makes use of the common structure of HIPEs containing micellar aggregates located in the continuous phase has been developed as well.46 By this means silica with a specific surface area as high as 800 m2 g-1 associated with a very low bulk density of 80 mg cm-3 was obtained. However, the oil-in-water (O/W) procedure needs a large amount of organic solvent as the dispersed phase and leads to powder rather than monoliths at volume fractions of the internal phase above 80%. A simple way for preparing porous silica materials is to evaporate liquid components of emulsions stabilized by silica particles alone, i.e. Pickering emulsions.47 The resulting macroporous silica reported so far has a pretty high density. Recently we reported on the stabilization of both O/W48-51 and water-in-oil (W/O)51 miniemulsions using a silica precursor polymer, hyperbranched polyethoxysiloxane 5

ACS Paragon Plus Environment

Langmuir 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

Page 6 of 33

(PEOS). PEOS is a highly hydrophobic liquid, which becomes amphiphilic upon hydrolysis at the oil/water interface. The interfacial tension between an organic solution containing PEOS and water is significantly lower than that arising from the pure solvent/water interface. In this study we attempt to utilize PEOS as the sole stabilizer to form HIPEs, which can in turn be converted to porous silica after condensation of PEOS and evaporation of liquid components. In order to achieve very low density coupled with mechanical integrity, the PEOS-containing oil component should compose the minor continuous phase to form W/O HIPEs. It was investigated under which conditions such kind of emulsions can be formed. Another key question is whether the conversion of PEOS leads to phase inversion and eventually collapse of HIPEs. Finally, the influence of preparation conditions on the morphology of resulting silica materials was studied.

RESULTS AND DISCUSSION When the internal phase volume in an emulsion exceeds a critical limit, phase inversion tends to take place, i.e. an O/W type emulsion becomes a W/O emulsion and vice versa. This can in principle be avoided by proper choice of a surfactant which is completely insoluble in the dispersed phase of the emulsion.27 PEOS can be a perfect candidate to stabilize W/O HIPEs, since it is soluble in most organic solvents, but insoluble in water even after its hydrolysis at the oil/water interface.52 Nevertheless, W/O HIPEs can only be formed by adding water into a PEOS solution in toluene, and the resulting mixture should be shaken for at least 2 min before emulsification using a 6

ACS Paragon Plus Environment

Page 7 of 33 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

Langmuir

high-speed rotor-stator homogenizer. Addition of the PEOS solution into water or high-speed homogenization without prior shaking results only in O/W emulsions. Water droplets are formed while adding water into the oil phase (Figure 1a). However, it takes a certain time for PEOS molecules to hydrolyze at the interface to form a stabilizing layer around the water droplets. High-speed homogenization then reduces the size of the water droplets, meanwhile the phase inversion from W/O to O/W is prevented by the tough PEOS layer at the interface. Figure 1b shows a photo of a water-in-toluene/PEOS HIPE, which is stable and remains liquid for at least 1 h at room temperature before it is converted to a solid material. Optical fluorescent microscopy of the HIPE confirms the formation of water droplets with a mean diameter of 18.6 ± 5.4 µm in the oil phase, although water composes the major phase (Figure 1c).

7

ACS Paragon Plus Environment

Langmuir 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

Page 8 of 33

Figure 1. (a) Liquid mixture formed by adding water of pH 7 into a toluene solution of PEOS. (b) HIPE obtained after high-speed homogenization under circumferential speed of 15000 rpm (Entry 3 in Table 1). (c) Fluorescence optical micrograph of HIPE. Blue color shows the aqueous phase labeled with fluorescein sodium salt.

Even at room temperature hydrolysis and condensation of PEOS can still take place as indicated by continuous increase of the emulsion viscosity, and the PEOS-stabilized HIPEs are eventually solidified. This process can be accelerated by raising the reaction temperature. In this work a HIPE is placed into a cylindrical Teflon® mold, which is then sealed in a metallic container. After heating in an oven at 60 °C for 12 h, the HIPE is converted to a piece of solid, which is rinsed with acetone to remove both water and toluene. Subsequent drying in a vacuum oven at 80 °C results in a porous silica monolith, i.e. a silica foam. In Figure 2 the FT-IR spectra of PEOS, silica foams and silica foams calcined at 800 °C for 30 min are compared. The characteristic peaks for alkyl groups at 2800 - 2900 cm-1 disappeared after the 8

ACS Paragon Plus Environment

Page 9 of 33 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

Langmuir

conversion of PEOS to silica. The spectra of silica foams before and after calcination are similar, and all absorption bands are characteristic for pure silica, indicating a complete conversion of PEOS even at a low reaction temperature. The reduction of the intensity of the absorbance band at 3500 cm-1 after calcination can be accounted for by loss of absorbed water and further condensation of silanol groups. Any shape change, volume shrinkage as well as variation of pore structure are not observed during the calcination, indicating an outstanding thermal stability. Remarkably, the silica foams are extremely light and highly porous. Their density is clearly below the typical density range of silica aerogels21-24 and can reach values as low as 10 mg cm-3 (cf. Table 1).

9

ACS Paragon Plus Environment

Langmuir 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

Page 10 of 33

Table 1. Recipes for preparation of HIPEs with 16 g of water. Entry

PEOS (g)

Toluene

Aqueous

(g)

pH

Speeda)

Mean water

Densityc)

(rpm)

droplet sizeb)

-3

(mg cm )

Porosityd)

Mean

(%)

macropore sizee)

(µm)

(µm) 1

2.00

1.96

11

15000

--

--

--

--

2

2.00

1.96

9

15000

21.5 ± 7.3

--

--

9.2 ± 3.2

3

2.00

1.96

7

15000

18.6 ± 5.4

24

98.9

6.9 ± 2.5

4

2.00

1.96

5

15000

15.5 ± 4.3

26

98.8

4.9 ± 1.9

5

2.00

1.96

3

15000

10.4 ± 3.9

30

98.6

3.8 ± 1.8

6

2.00

1.96

1

15000

4.9 ± 2.6

33

98.5

2.9 ± 1.4

7

0.80

2.87

7

15000

22.1 ± 4.6

10

99.5

11.2 ± 1.5

8

1.60

2.27

7

15000

19.7 ± 3.8

20

99.1

7.3 ± 1.2

9

2.40

1.67

7

15000

7.2 ± 2.7

30

98.6

2.4 ± 0.9

10

2.00

1.96

7

12000

20.9 ± 7.5

24

98.9

7.2 ± 2.5

11

2.00

1.96

7

18000

13.8 ± 4.1

24

98.9

4.8 ± 1.7

a)

circumferential speed of the rotor-stator homogenizer.

b)

Mean size of water droplets was estimated by averaging diameter of 1000 water droplets in

fluorescent microscope images. c)

Density of silica foams (ρ) was determined by measuring volume and mass of monoliths

obtained in a cylindrical form. d)

Porosity was calculated using the following equation: Porosity = (1 - ρ/ρs) × 100%

Where ρ is the density of silica foam and ρs is the density of amorphous silica that equals 2.2 g cm-3.53 e)

Mean size of macropores was estimated by averaging diameter of 1000 pores in field-emission

scanning electron micrographs.

10

ACS Paragon Plus Environment

Page 11 of 33 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

Langmuir

Figure 2. FT-IR spectra of (a) PEOS and (b) silica foams (Entry 3 in Table 1) before and (c) after calcination at 800 °C.

It is well known that the hydrolysis and condensation kinetics of silica precursors like PEOS as well as the resulting silica structure are strongly affected by pH.9,49-52,54 HIPEs can be formed in a wide pH range of the aqueous media from 1 to 11, and the structure and properties of the resulting silica foams are pH dependent. On the one hand, the foam density decreases and the corresponding porosity increases with the increase of pH, when the PEOS concentration in toluene and the volume fraction of water are kept constant (Table 1). The dried silica foam prepared at pH 7 has a density of 24 mg cm-3 and a porosity of 98.9% that are very close to the theoretical values calculated by assuming that the silica foam occupies the same volume as the initial HIPE. A bit higher density and lower porosity at lower pH therefore imply a slight shrinkage of the sample volume during the PEOS conversion. On the other hand, the mechanical integrity improves with the decrease of pH. At pH 11, instead of intact 11

ACS Paragon Plus Environment

Langmuir 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

Page 12 of 33

silica foam monoliths, small pieces of silica fragments are formed after complete solidification. At such a high pH, PEOS molecules lose their interfacial activity very fast due to the high rate of hydrolysis and condensation. Therefore, the initially formed HIPEs quickly break down before a continuous silica layer can form around the water droplets. At pH 9 the resulting foam products exhibit a clear macroporous structure derived from the water droplet templating, indicating a high stability of the HIPEs throughout the whole sol-gel reaction, although they are quite brittle and fall into big pieces when removed from the Teflon® mold. This mechanical integrity of the silica foams is greatly improved when the aqueous pH is lower than 7.

Figure 3. (a) A silica foam (diameter ~ 2.2 cm, height ~ 2.5 cm) on a leaf. (b) 228 mg of silica foam (diameter ~ 2.2 cm, height ~ 2.5 cm) supports a weight of 500 g.

Although the foams are very light (Figure 3a), they possess pretty good mechanical strength. For instance, a cylindrical foam sample (density 24 mg·cm-3 and mass 228 mg) with a diameter of 2.2 cm and a height of 2.5 cm can support a weight of 500 g (Figure 3b). The mechanical properties under compression were measured for silica 12

ACS Paragon Plus Environment

Page 13 of 33 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

Langmuir

foams prepared with aqueous media of different pH values. In contrast to traditional silica aerogels with densities lower than 100 mg cm-3, which are ductile and can be easily deformed under load,55,56 the silica foams prepared in this work appear to be hard (Figure S1). The compression modulus of the silica foam obtained at pH 7 is measured as 0.5 MPa (Figure 4a). When decreasing pH from 7 to 1 (Entry 3 - 6 in Table 1), the compression modulus continuously increases and reaches a maximum of 1.75 MPa at pH 1, while the density of the foams keeps almost unchanged. In the meantime, the compressive strength of silica foams also increases significantly from 37 kPa to 80 kPa with decreasing pH values from 7 to 1. In general, these silica foams are mechanically stronger than traditional silica aerogels. For instance, it was reported that a series of silica aerogels with an average density of 80 mg cm-3 possessed compressive modulus from 0.5 MPa to 0.8 MPa,57 and even lower modulus and strength were observed for another series of silica aerogel samples.58 Besides the high specific mechanical strength the silica foams prepared in this work also have a low thermal conductivity. The thermal conductivity of a foam sample with porosity of 98.9% is measured as 48 mW m-1 K-1 under ambient conditions, very close to the values of macroporous polymer foams with similar porosity (normally in the range of 20 - 50 mW m-1 K-1),1 which are employed extensively as thermal insulation materials. A more detailed investigation on thermal conductivity of silica foams will be performed in our future work.

13

ACS Paragon Plus Environment

Langmuir 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

Page 14 of 33

Figure 4. (a) Compressive modulus and (b) strength of silica foams prepared at different pH (Entries 3 - 6 in Table 1). The error bars represent the standard deviation.

FE-SEM images of silica foams prepared at different pH of the aqueous phase are shown in Figure 5. It can be seen that macroporous silica foams with a closed-cell structure are formed in a wide range of pH from 1 to 9. In comparison to the size of the water droplets in the HIPE, the pore size of the corresponding silica foam is much smaller (cf. Table 1 and Figure 6). The size of the water droplets in the HIPEs and the pores in the corresponding foams shows a similar pH dependence, i.e. increase with

14

ACS Paragon Plus Environment

Page 15 of 33 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

Langmuir

the increase of pH, though the water droplets are systematically larger than the corresponding pores. Insets in Figure 5 reveal the internal morphology of the foam skeletons that appears also to be pH dependent. At lower pH (1-3) the interspace between the pore walls is practically empty (Figure 5d and Figure S3); in contrast it is filled with stacks of small silica particles in the foams prepared at higher pH values (5-9). The experimental data indicate that the pore size and the water droplet size in the HIPEs are directly related. The interfacial tension between water and organic solution containing PEOS generally increases with the increase of the aqueous pH.50 Thus, the

size of the water droplets and the resulting pore size increase when the pH arises. With further growth of pH to 11, no macroporous structure is observed according to FE-SEM data (Figure S2) due to breakdown of the HIPE during the sol-gel reaction. Smaller pore size and higher density are clearly responsible for better mechanical strength of the silica foams formed at lower pH. There can be two main reasons for the pore size to be smaller than the size of the water droplets. First, in contrast to hydrophobic PEOS, the product silica is hydrophilic and can adsorb a pretty large amount of water. Second, the oil phase consists of a W/O miniemulsion at higher pH,51 and water is consumed to convert PEOS stabilizing the W/O miniemulsion in the oil phase. At lower pH, the W/O miniemulsion is not stable due to too fast hydrolysis of PEOS.51 The formation of a W/O microemulsion in the oil phase of a HIPE was previously reported by several research groups.59-61 In our case, a W/O miniemulsion with small nanosized water droplets rather than a microemulsion 15

ACS Paragon Plus Environment

Langmuir 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

Page 16 of 33

is formed, since a high-energy emulsification process is required. Furthermore, ethanol,

which is released upon the PEOS conversion, destabilizes the

(mini)emulsions, creating water channels between the water droplets.62 It becomes clear that the formation of a W/O miniemulsion in the oil phase at higher pH accounts not only for the more significant pH dependence of the water droplet size than that of the pore size, but also for the different finestructures in the pore wall. The difference in the HIPE structure at different pH of aqueous media might also be responsible for the observed volume change during the sol-gel reaction. At high pH the solidification of the PEOS-stabilized W/O miniemulsion in the oil phase results in an additional silica network that seems to prevent shrinkage of the whole system. Besides the pH of the aqueous media, the pore size can also be reduced by more intensive homogenization. By changing the circumferential speed of the rotor-stator homogenizer from 12000 to 18000 rpm, the mean pore size is reduced from 7.2 to 4.8 µm (Entries 10 and 11 in Table 1). It can therefore be expected that the pore size can be further reduced by using high-energy homogenizers such as ultrasonic device and microfluidizer.

16

ACS Paragon Plus Environment

Page 17 of 33 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

Langmuir

Figure 5. FE-SEM images of silica foams prepared at different aqueous pH: (a) 9, (b) 7, (c) 5, and (d) 1 (Entries 2-4 and 6 in Table 1). The insets show the enlarged view of the skeletons of corresponding silica foams. FE-SEM images of silica foams prepared with different PEOS concentrations in toluene: (e) 21.8%, and (f) 59.0% (Entries 7 and 9 in Table 1).

17

ACS Paragon Plus Environment

Langmuir 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

Page 18 of 33

Figure 6. (a) Water droplet size in HIPEs and (b) pore size of silica foams prepared at different pH of the aqueous media (Entries 2 - 6 in Table 1). The error bars represent the standard deviation.

In this work PEOS acts as not only the HIPE stabilizer but also the silica precursor. Its concentration in the oil phase can influence both the HIPE formation and the density of the resulting silica foams. The density of the silica foams decreases linearly with the decrease of the PEOS concentration in toluene under the same reaction conditions (Table 1). Meanwhile, the dilution of the PEOS solution causes an increase in pore size (Figure 5 and S4) due to the reduction of the concentration of the effective emulsifier (partially hydrolyzed PEOS) as well as interfacial dilational modulus ε. FE-SEM images in Figure 5 show clearly that the pore walls of the silica foams are porous. It is well known that silica obtained from a sol-gel process without high-temperature densification is mesoporous with a large specific surface area.63 To prove the mesoporous nature of the silica foams nitrogen sorption measurements were performed. The size of macropores templated by HIPEs generally ranges from 3 to 11 18

ACS Paragon Plus Environment

Page 19 of 33 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

Langmuir

µm, so they contribute barely to the specific surface area. All silica foams prepared at different pH exhibit type IV nitrogen adsorption and desorption isotherms with H3 or H4 hysteresis loops (Figure 7a), which are characteristic for mesoporous materials.64 The pore size distribution determined from the adsorption branch of the isotherm using the BJH model is depicted in the inset of Figure 7a.

Figure 7. (a) Nitrogen adsorption-desorption isotherms and pore size distribution curves calculated with the BJH method (inset) for silica foams prepared at different pH (Table 1, Entries 2-6). (b) Surface area of silica foams versus pH.

19

ACS Paragon Plus Environment

Langmuir 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

Page 20 of 33

In all samples, the pore size distribution is broad and both micropores (< 2 nm) and mesopores (2 - 50 nm) are present.65 The specific surface areas were calculated using the BET equation, and their pH dependence is shown in Figure 7b. The highest surface area of 755 m2 g-1 is observed in the foam prepared at pH 3. By reducing the pH from 3 to 1, the surface area of the silica foams is slightly lowered. At pH higher than 3 the surface area declines with increase of pH. This can be explained by the different mechanisms of silica growth at different pH during the conversion of PEOS. Neutral and basic conditions can be expected to result in compact silica structures as a consequence of reaction-limited monomer-cluster growth, meanwhile loose, more porous structures are formed under acidic conditions due to reaction-limited cluster-cluster aggregation.9

CONCLUSION Silica macro/mesoporous foams with ultrahigh porosity (99.5%) and high specific surface area (755 m2 g-1) have been prepared via W/O HIPE templating. The HIPEs are formed by emulsifying water in a toluene solution containing a silica precursor polymer PEOS, which becomes amphiphilic by hydrolysis at the oil-water interface, under high-speed homogenization. After the conversion of PEOS to silica, the emulsions solidify, and silica foam monoliths with macropore sizes in the range of 1 20 µm are obtained after removing the solvent. These foams are mechanically stronger than traditional silica aerogels due to their closed-cell structure. According to nitrogen sorption data, the resulting silica foams exhibit a high specific surface area 20

ACS Paragon Plus Environment

Page 21 of 33 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

Langmuir

and the foam skeletons are micro- and mesoporous. pH has a strong influence on the structure of the foams due to the pH dependence of hydrolysis and condensation of PEOS. The increase of pH results in an increase of porosity and pore size as well as a decrease of surface area. The pore size can further be controlled by PEOS concentration and homogenization intensity. Thermal insulating and mechanical properties are expected to be improved by further reducing the pore size to submicron range. This work opens a new avenue for manufacture of formable ultralight porous inorganic materials and such kind of ultralight silica foams may replace expensive aerogels in a number of application fields.

METHODS Materials. Tetraethoxysilane (TEOS, reagent grade, 98%, Sigma-Aldrich), acetic anhydride (ACS reagent, ≥98.0%, Sigma-Aldrich), Toluene (≥99.5%, Sinopharm Chemical Reagent Co., Ltd), hydrochloric acid (36.0 - 38.0%, Sinopharm Chemical Reagent Co., Ltd), ammonium hydroxide (25.0%, Jiangsu Tongsheng Chemical Reagent Co., Ltd) and titanium trimethylsiloxide (ABCR) were used as received. Deionized

water

was

used

throughout

the

experiments.

Hyperbranched

polyethoxysiloxane (PEOS) was synthesized according to the method published elsewhere.48 The resulting PEOS had the following characteristics: degree of branching 0.54, SiO2 content 49.2%, Mn 1740 and Mw/Mn 1.9 (measured by gel permeation chromatography in chloroform with evaporative light scattering detector calibrated using polystyrene standards). 21

ACS Paragon Plus Environment

Langmuir 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

Page 22 of 33

Preparation of HIPEs. pH of water was delicately adjusted by adding hydrochloric acid or aqueous ammonium solution. The aqueous solution of different pH was added to the toluene solution of PEOS. The resulting mixture was gently shaken for 2 min, and then emulsified for 3 min with a rotor-stator homogenizer (T18 digital Ultra-Turrax®, IKA). The compositions of the emulsions are summarized in Table 1. The volume fraction of internal aqueous phase was kept to be 80%.

Preparation of silica foams. The obtained HIPE was transferred to a Teflon® form, which was then sealed in a metallic container. The whole system was placed in an oven and heated at 60 °C for 12 h. The content of the form was then washed in a Soxhlet extractor with acetone. Finally, the product was dried in an oven at 100 °C for 2 h.

Characterization. Optical microscopic observation of emulsions was conducted on a fluorescent microscope (Axiovert 200, Zeiss, Germany) mounted with a charge coupled device (CCD, AxioCam HRC, Zeiss, Germany). For these measurements a small amount of sodium fluorescein was dissolved in the aqueous phase. The pore structure of silica foams was investigated using a Zeiss Ultra 55 field-emission scanning electron microscope (FE-SEM). All samples were placed onto lacy carbon-coated substrates and sputtered with gold before observation. The mean pore size of silica foams was obtained by averaging the size of at least 1000 pores from FE-SEM images. Fourier transform infrared (FT-IR) spectra were recorded on a Thermofisher Nicolet 6700 FT-IR spectrometer using KBr pellet technique. 22

ACS Paragon Plus Environment

Page 23 of 33 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

Langmuir

Nitrogen adsorption−desorption isotherms were recorded on a Quadrasorb evo surface area and porosity analyzer (Quantachrome Instruments, USA) by static adsorption procedures at 77 K. The specific surface areas of the samples were calculated by applying the Brunauer−Emmett−Teller (BET) equation. The pore size and volume were determined from the adsorption branch of the isotherm using the Barrett−Joyner−Halenda (BJH) model. The mechanical properties of silica foams were studied on a SANS CMT-6503 table-top universal testing machine (MTS Systems Co., Ltd, China) equipped with a 100 N load cell. For the compression tests, the cylindrical samples were placed between the self-leveling plates and compressed at a rate of 1 mm/min. The environmental temperature was 25 °C and relative humidity (RH) was 50%. Thermal conductivity λ of a monolith sample was measured on a thermal constants analyzer (TPS 3500, Hot Disk Sweden) equipped with a 5465 Kapton-insulated heat flow sensor using transient plane heat source (hot disc) method. The environmental temperature was 25 °C and RH was 50%.

23

ACS Paragon Plus Environment

Langmuir 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

Page 24 of 33

ASSOCIATED CONTENT Supporting Information This material is available free of charge via the Internet at http://pubs.acs.org. Additional experimental procedure and data, including strain-stress curve and FE-SEM images are presented. (PDF)

AUTHOR INFORMATION Corresponding Authors * Dr. Xiaomin Zhu, e-mail: [email protected] * Prof. Dr. Haitao Wang, e-mail: [email protected]

Author Contributions The manuscript was written through contributions of all authors. All authors have given approval to the final version of the manuscript.

Notes The authors declare no competing financial interests.

ACKNOWLEDGMENTS This work was financially supported by the National Natural Science Foundation of China (no. 51373038) and Shanghai Pujiang Talent Program (no. 18PJ1432900). The support by Senior Scholar Foundation of Key Laboratory in Fudan University is also gratefully acknowledged. 24

ACS Paragon Plus Environment

Page 25 of 33 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

Langmuir

REFERENCES (1) Gibson, L. J.; Ashby, M. F. Cellular Solids: Structure and Properties. 2nd ed. Cambridge University Press: Cambridge, 1997. (2) Liu, P.; Chen, G.-F. Porous Materials: Processing and Applications. Elsevier: Oxford, 2014. (3) Eaves, D. Handbook of Polymer Foams. Rapra Technology Limited: Shropshire, 2004. (4) Klempner, D.; Sendijarevic, V. Handbook of Polymeric Foams and Foam Technology. 2nd ed. Klempner, D.; Sendijarevic, V.; Eds. Hanser: Munich, 2004. (5) Zhang, T.; Kong, L. Y.; Dai, Y. T.; Yue, X. J.; Rong, J.; Qiu, F. X.; Pan, J. M. Enhanced Oils and Organic Solvents Absorption by Polyurethane Foams Composites Modified with MnO2 Nanowires. Chem. Eng. J. 2017, 309, 7-14. (6) Abraham, A. M.; Kumar, S. V.; Alhassan, S. M. Porous Sulphur Copolymer for Gas-phase Mercury Removal and Thermal Insulation. Chem. Eng. J. 2018, 332, 1-7. (7) Banhart, J. Manufacture, Characterisation and Application of Cellular Metals and Metal Foams. Prog. Mater. Sci. 2001, 46, 559-553. (8) Scheffler, M.; Colombo, P. Cellular Ceramics: Structure, Manufacturing, Properties and Applications. Wiley-VCH: Weinheim, 2005. (9) Brinker, C. J.; Scherer, G. W. Sol-gel Science: the Physics and Chemistry of Sol-gel Processing. Academic Press: San Diego, 1990. (10) Feinle, A.; Elsaesser, M. S.; Hüsing, N. Sol-gel Synthesis of Monolithic Materials with Hierarchical Porosity, Chem. Soc. Rev. 2016, 45, 3377-3399.

25

ACS Paragon Plus Environment

Langmuir 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

Page 26 of 33

(11) Cundy, C. S.; Cox, P. A. The Hydrothermal Synthesis of Zeolites: History and Development from the Earliest Days to the Present Time. Chem. Rev. 2003, 103, 663-701. (12) Wan, Y.; Zhao, D. Y. On the Controllable Soft-templating Approach to Mesoporous Silicates. Chem. Rev. 2007, 107, 2821-2860. (13) Studart, A. R.; Gonzenbach, U. T.; Tervoort, E. L.; Gauckler, J. Processing Routes to Macroporous Ceramics: a Review. J. Am. Ceram. Soc. 2006, 89, 1771-1789. (14) Yang, T.; Hu, Y.; Wang, C. Y.; Binks, B. P. Fabrication of Hierarchical Macroporous Biocompatible Scaffolds by Combining Pickering High Internal Phase Emulsion Templates with Three-dimensional Printing. ACS Appl. Mater. Interfaces

2017, 9, 22950-22958. (15) Petkovich, N.; Stein, D. A. Controlling Macro- and Mesostructures with Hierarchical Porosity Through Combined Hard and Soft Templating. Chem. Soc. Rev.

2013, 42, 3721-3739. (16) Vuong, G.-T.; Kaliaguine, S.; Do, T.-O. A Strategy towards Macroporous Sponge-like Networks of Metal Oxide-surfactant Mesophases and Bulk Metal Oxides, J. Porous Mater. 2008, 15, 679-683. (17) Timusk, M.; Kuus, A.; Utt, K.; Kangur, T.; Sutka, A.; Jarvekulg, M.; Knite, M. Thick Silica Foam Films through Combined Catalytic Decomposition of H2O2 and Sol-gel Processes. Mater. Design 2016, 111, 80-87. (18) Gesser, H. D.; Goswami, P. C. Aerogels and Related Porous Materials. Chem. Rev. 1989, 89, 765-788. 26

ACS Paragon Plus Environment

Page 27 of 33 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

Langmuir

(19) Hüsing, N.; Schubert, U. Aerogels Airy Materials: Chemistry, Structure, and Properties. Angew. Chem. Int. Ed. 1998, 37, 23-45. (20) Pierre, A. C.; Pajonk, G. M. Chemistry of Aerogels and Their Applications. Chem. Rev. 2002, 102, 4243-4265. (21) Aegerter, M. A.; Leventis, N.; Koebel, M. M. Aerogels Handbook. Springer, 2011. (22) Aleman, J.; Chadwick, A. V.; He, J.; Hess, M.; Horie, K.; Jones, R. G.; Kratochvil, P.; Meisel, I.; Mita, I.; Moad, G. et al. Definitions of Terms Relating to the Structure and Processing of Sols, Gels, Networks, and Inorganic-organic Hybrid Materials. Pure Appl. Chem. 2007, 79, 1801-1827. (23) Kistler, S. S. Coherent Expanded Aerogels. J. Phys. Chem. 1932, 36, 52-64. (24) Hrubesh, L. W. Aerogel Applications. J. Non-Cryst. Solids 1998, 225, 335-342. (25) Baetens, R.; Jelle, B. P.; Gustavsen, A. Aerogel Insulation for Building Applications: a State-of-the-art Review. Energ. Buildings 2011, 43, 761-769. (26) Venkataraman, M.; Mishra, R.; Kotresh, T. M.; Militky, J.; Jamshaid, H. Aerogels for Thermal Insulation in High-Performance Textiles. Text. Prog. 2016, 48, 55-118. (27) Cameron, N. R.; Sherrington, D. C. High Internal Phase Emulsions (HIPEs) Structure, Properties and Use in Polymer Preparation. Adv. Polym. Sci. 1996, 126, 163-214. (28) Solans, C.; Esquena, J.; Azemar, N. Highly Concentrated (Gel) Emulsions, Versatile Reaction Media. Curr. Opin. Colloid Interface Sci. 2003, 8, 156-163.

27

ACS Paragon Plus Environment

Langmuir 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

Page 28 of 33

(29) Cameron, N. R. High Internal Phase Emulsion Templating as a Route to Well-defined Porous Polymers. Polymer 2005, 46, 1439-1449. (30) Zhang, H. F.; Cooper, A. I. Synthesis and Applications of Emulsion-Templated Porous Materials. Soft Matter 2005, 1, 107-113. (31) Zhu, Y.; Zhang, R. R.; Zhang, S. M.; Chu, Y. Q.; Chen, J. D. Macroporous Polymers with Aligned Microporous Walls from Pickering High Internal Phase Emulsions. Langmuir 2016, 32, 6083-6088. (32) Stubenrauch, C.; Menner, A.; Bismarck, A.; Drenckhan, W. Emulsion & Foam Templating – Promising Routes to Tailor-Made Porous Polymers. Angew. Chem. Int. Ed. 2018, DOI: 10.1002/anie.201801466. (33) Andrieux, S.; Quell, A.; Stubenrauch, C.; Drenckhan, W. Liquid Foam Templating – A Route to Tailor-Made Polymer Foams, Adv. Colloid Interface Sci.

2018, DOI: 10.1016/j.cis.2018.03.010. (34) Lissant, K. J. Geometry of High-internal-phase-ratio Emulsions. J. Colloid Interface Sci. 1966, 22, 462-466. (35) Williams, J. M. High Internal Phase Water-in-oil Emulsions - Influence of Surfactants and Cosurfactants on Emulsion Stability and Foam Quality. Langmuir

1991, 7, 1370-1377. (36) Barbetta, A.; Cameron, N. R. Morphology and Surface Area of Emulsion-derived (PolyHIPE) Solid Foams Prepared with Oil-phase Soluble Porogenic Solvents: Three-component Surfactant System. Macromolecules 2004, 37, 3202-3213.

28

ACS Paragon Plus Environment

Page 29 of 33 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

Langmuir

(37) Ikem, V. O.; Menner, A.; Bismarck, A. High Internal Phase Emulsions Stabilized Solely by Functionalized Silica Particles. Angew. Chem. Int. Ed. 2008, 47, 8277-8279. (38) Li, Z. F.; Ming, T.; Wang, J. F.; Ngai, T. High Internal Phase Emulsions Stabilized Solely by Microgel Particles. Angew. Chem. Int. Ed. 2009, 48, 8490-8493. (39) Zheng, Z.; Zheng, X. H.; Wang, H. T.; Du, Q. G. Macroporous Graphene Oxide-polymer Composite Prepared through Pickering High Internal Phase Emulsions. ACS Appl. Mater. Interfaces 2013, 5, 7974-7982. (40) Zheng, X. H.; Zhang, Y.; Wang, H. T.; Du, Q. G. Interconnected Macroporous Polymers Synthesized from Silica Particle Stabilized High Internal Phase Emulsions. Macromolecules 2014, 47, 6847-6855. (41) Zhang, B. X.; Zhang, J. L.; Liu, C. C.; Peng, L.; Sang, X. X.; Han, B. X.; Ma, X.; Luo, T.; Tan, X. N.; Yang, G. Y. High-internal-phase Emulsions Stabilized by Metal-Organic Frameworks and Derivation of Ultralight Metal-organic Aerogels. Sci. Rep. 2016, 6, 1-9. (42) Wang, Z.; Qiu, T.; Guo, L.; Ye, J.; He, L.; Li, X. Polymerization Induced Shaping of Pickering Emulsion Droplets: from Simple Hollow Microspheres to Molecularly Imprinted Multicore Microrattles. Chem. Eng. J. 2018, 332, 409-418. (43) Imhof, A.; Pine, D. J. Ordered Macroporous Materials by Emulsion Templating. Nature 1997, 389, 948-951. (44) Yi, G. R.; Yang, S. M. Microstructures of Porous Silica Prepared in Aqueous and Nonaqueous Emulsion Templates. Chem. Mater. 1999, 11, 2322-2325. (45) Maekawa, H.; Esquena, J.; Bishop, S.; Solans, C.; Chmelka, B. F. 29

ACS Paragon Plus Environment

Langmuir 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

Page 30 of 33

Meso/macroporous Inorganic Oxide Monoliths from Polymer Foams. Adv. Mater.

2003, 15, 591-596. (46) Carn, F.; Colin, A.; Achard, M.-F.; Deleuze, H.; Sellier, E.; Birot, M.; Backov, R. Inorganic Monoliths Hierarchically Textured via Concentrated Direct Emulsion and Micellar Templates. J. Mater. Chem. 2004, 14, 1370–1376. (47) Binks, B. P. Macroporous Silica from Solid-stabilized Emulsion Templates. Adv. Mater. 2002, 14, 1824-1827. (48) Zhu, X.; Jaumann, M.; Peter, K.; Möller, M.; Melian, C.; Adams-Buda, A.; Demco,

D.

E.;

Blumich,

B.

One-pot

Synthesis

of

Hyperbranched

Polyethoxysiloxanes. Macromolecules 2006, 39, 1701-1708. (49) Zhao, Y.; Chen, Z.; Zhu, X.; Möller, M. Silica Nanoparticles Catalyse the Formation of Silica Nanocapsules in a Surfactant-free Emulsion System. J. Mater. Chem. A 2015, 3, 24428-24436. (50) Zhao, Y.; Chen, Z.; Zhu, X.; Möller, M. A Facile One-step Approach toward Polymer@SiO2 Core–shell Nanoparticles via a Surfactant-free Miniemulsion Polymerization Technique. Macromolecules 2016, 49, 1552-1562. (51) Zhao, Y. L.; Liu, J. L.; Chen, Z.; Zhu, X.; Möller, M. Hybrid Nanostructured Particles via Surfactant-free Double Miniemulsion Polymerization. Nat. Commun.

2018, 9, 1918. (52) Wang, H.; Zhu, X.; Tsarkova, L.; Pich, A.; Möller, M. All-silica Colloidosomes with a Particle-bilayer Shell. ACS Nano 2011, 5, 3937-3942.

30

ACS Paragon Plus Environment

Page 31 of 33 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

Langmuir

(53) Iler, R. K. The Chemistry of Silica: Solubility, Polymerization, Colloid and Surface Properties, and Biochemistry. Wiley: New York, 1979. (54) Zhao, Y.; Li, Y.; Demco, D. E.; Zhu, X.; Möeller, M. Microencapsulation of Hydrophobic Liquids in Closed all-silica Colloidosomes. Langmuir 2014, 30, 4253-4261. (55) Kucheyev, S. O.; Stadermann, M.; Shin, S. J.; Satcher, J. H.; Gammon, S. A.; Letts, S. A.; van Buuren, T.; Hamza, A. V. Super-compressibility of Ultralow-density Nanoporous Silica. Adv. Mater. 2012, 24, 776-780. (56) Wong, J. C. H.; Kaymak, H.; Brunner, S.; Koebel, M. M. Mechanical Properties of Monolithic Silica Aerogels Made from Polyethoxydisiloxanes. Micropor. Mesopor. Mater. 2014, 183, 23-29. (57) Miner, M. R.; Hosticka, B.; Norris, P. M. The Effects of Ambient Humidity on the Mechanical Properties and Surface Chemistry of Hygroscopic Silica Aerogel. J. Non-Cryst. Solids 2004, 350, 285-289. (58) Omranpour, H.; Motahari, S. Effects of Processing Conditions on Silica Aerogel during Aging: Role of Solvent, Time and Temperature. J. Non-Cryst. Solids 2013, 379, 7-11. (59) Solans, C.; Dominguez, J. G.; Parra, J. L.; Heuser, J.; Friberg, S. E. Gelled Emulsions with a High Water-Content. Colloid Polym. Sci. 1988, 266, 570-574. (60) Ravey, J. C.; Stebe, M. J. Small-angle Neutron-scattering Studies of Aqueous Gels with Fluorinated Nonionic Surfactants. Phys. B 1989, 156, 394-397.

31

ACS Paragon Plus Environment

Langmuir 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

Page 32 of 33

(61) Quell, A.; Sottmann, T.; Stubenrauch, C. Diving into the Finestructure of Macroporous Polymer Foams Synthesised via Emulsion Templating: a Phase Diagram Study. Langmuir 2017, 33, 537-542. (62) Venditti, F.; Angelico, R.; Palazzo, G.; Colafemmina, G.; Ceglie, A.; Lopez, F.; Preparation of Nanosize Silica in Reverse Micelles: Ethanol Produced During TEOS Hydrolysis Affects the Microemulsion Structure. Langmuir 2007, 23, 10063-10068. (63) Hench, L. L.; West, J. K. The Sol-gel Process. Chem. Rev. 1990, 90, 33-72. (64) Sing, K. S. W.; Everett, D. H.; Haul, R. A. W.; Moscou, L.; Pierotti, R. A.; Rouquerol, J.; Siemieniewska, T. Reporting Physisorption Data for Gas Solid Systems with Special Reference to the Determination of Surface-area and Porosity. Pure Appl. Chem. 1985, 57, 603-619. (65) Rouquerol, J.; Avnir, D.; Fairbridge, C. W.; Everett, D. H.; Haynes, J. H.; Pernicone, N.; Ramsay, J. D. F.; Sing, K. S. W.; Unger, K. K. Recommendations for the Characterization of Porous Solids. Pure Appl. Chem. 1994, 66, 1739-1758.

32

ACS Paragon Plus Environment

Page 33 of 33 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

Langmuir

Table of Contents Graphic and Synopsis

33

ACS Paragon Plus Environment