LR.docx

Background

Carbon aerogels, discovered by Dr Pekala, have various chemical and physical properties that make them suitable to be used in applications such as energy storage, filtration, and catalysis (). Carbon aerogels are made from carbon and usually have low densities as a result of the lightness of the carbon as an element. For example, silica aerogels are known as the world’s lightest material with a density of 1 mg/cm3. However, carbon-based aerogels have densities below 200 μg/cm3(). That makes it easier to fabricate carbon-based aerogel to achieve an ultralight surface area. The Brunauer-Emmett-Teller (BET) surface area for carbon nanotube and graphene aerogel have an extra 500 and 100 m2/g, respectively [1]. Whereas activated carbon obtained the density values around 300 m2/g. Carbon-based aerogels have special characteristic; Sp2 hybridized carbon atoms. Which makes it capable of high electrical conductivity and mechanical strength. For example, carbon-based aerogels have better compressibility in relation to other inorganic aerogel with equal densities. Recently, more aerogel compounds are being processed. Recent products include carbon allotropes; CNT, graphene and diamond aerogels. Nowadays, carbon-based aerogel is a significant technology that has gained interests among scientists [2].

Numerous methods have been developed to produce carbon- based aerogel materials. Carbon aerogels are produced as a result of making suspensions of different carbon nanomaterials. Among the allotropes used to make suspensions that synthesise carbon aerogels include CNT, graphene or graphene oxide (GO) with highly hybridized Sp2. One of the methods used to make suspension of carbon-based aerogels is freeze drying. Also, sol gel procedure can be used to form suspensions [3-5]. In both methods, van der waals force occur to make covalently cross-linked aerogel. Hybridized carbon Sp2 and the organic precursor can be regulated in suspensions to ensure that organic particles are nucleated on the surface of sp2 hybridized carbon. The function of organic particles is to link sp2 carbon bridges after carbonization while the role of Sp2 hybridized carbon is to provide mechanical strength and conductivity. The final aerogel contains three-dimensional (3D) networks of amorphous carbon, CNTs or graphene. In a comparison to the traditional carbon aerogels, there is significant benefits due to improved properties such as transport and mechanical strength (). The difference is due to presence of carbon units in crystallite nature. Since 2009, carbon-based aerogels have become a major area of study because of phenomenal properties especially for graphene aerogel. example

Graphene- based aerogel is one of important carbon-base aerogel. It is applied (what role) in energy conversion, lithium ion batteries, sensors and supercapacitors. The fundamental properties that make it essential are electrical conductivity, high surface area and high porosity. However, it is possible for graphene aerogel to be damaged as a result of mechanical distortion. In addition, the π-π stacking assembly of graphene sheet minimizes the surface area and the application will be limited [6].

The limitation of graphene aerogel can be improved. One-dimension materials (1D) such as carbon nanotube, nanofiber and metal oxide nanorods can be used to improve its mechanical performance, surface area and high-performance. For instance, supercapacitors have been designed with reduced graphene oxide or titanium dioxide nanofiber aerogel. The role of nanofiber is to maintain the distance between the graphene sheets by guaranteeing easy access to reactant and increasing surface area [7-9].

This study focused on the exploring of the fabrication of aerogels from GNF by considering literature from known fabrication routes for aerogels synthesised from other carbon nanostructures such as graphene, carbon nanotubes. In order to ensure future sustainability in society and environment, there is an urgent need to optimize industrial processes in terms of energy, waste and overall productivity. Heterogeneous catalysis has a remarkable role to play in this [18, 19] by making chemical reactions used in industry more efficient, reducing both chemical waste and energy consumption. In this project, it will be investigated how aerogels can be used to produce new heterogeneous catalyst systems with improved properties. Aerogels are sponge-like, highly porous materials, consisting of an inter-connected 3D particle network where the continuous phase is a gas. This project will specifically focus on the use of aerogels made from graphitic nanofibers (GNF) in catalysis. It is hypothesised that GNF aerogels can act as highly efficient, multifunctional supports for catalytic nanoparticles. Benefits provided by the GNF aerogel support are expected in terms of NP-catalyst stability and improved mass transfer/kinetics during the catalytic reaction. Other advantages might include new confinement effects with impact on reaction selectivity or the electrical conductivity of the interconnected GNF aerogel network, which could be exploited in electrochemical synthetic reactions.

Chapter 2

Literature Review

&

Research Objectives

2.1. Literature review

This chapter will introduce the background of the information relevant to the carbonous materials e.g. graphene, CNT and aerogel nanocomposites. The first part of this chapter will present the nanomaterials and their structure. Where the second part will sum up what has been explored in this area represented in the previous researches and how these materials can be characterized and evaluated with different techniques and theory behind the evaluation techniques.

2.1.1. Nanocarbons:

Nanocarbons materials (NCs) represents a massive nanomaterial with different nanoscale dimension [20]. Nanocarbons refer to a broad range of carbon materials with nanoscale dimension, structures, and textures [1]. Nanocarbons known for their physiochemical properties and can be synthesis via bottom up (i.e. templated deposition) or top down (i.e. structural controlled carbonization of precursor). Generally, nanocarbons have phenomenal properties either the internal and inherent properties which are related to the surface chemistry and electronic structure or the external one that is the morphology and specific surface area. To improve the chemical stabilities, reusability and increase the activity can be obtained via the decorating of the nanocarbon either with metal nanoparticle MNPs or metal oxide MO. NCs have been used in different applications such as energy storage, photocatalysis, nanomedicine and industrial catalysis (). These carbon nanostructures (CNSs) can be defines as the allotropes of carbon with a graphitic structure of sp2 graphitized carbon atoms. They vary in shapes and sizes. The morphological diversity of these graphitic structure has led to a strong drive to discover more chemical and physical properties [21]. Due to this, there has been growth of interest in materials science and engineering communities. In the last twenty years, CNSs that would include graphene, fullerene and carbon nanotubes (CNTs) were researched ().

The catalytic composites of the low dimensional nanocarbons such as CNT, graphene, ordered mesoporous carbon (OMC) and carbon nanofibers can be representive; see Figure 2.2. We focus on the mechanistic aspects of catalytic composites of several representative low-dimensional nanocarbons used for catalytic composites, including CNT, graphene, OMC, and carbon nanofibers (CNFs)

Figure 2.1. Scheme represents catalytic nanocarbon composites.

2.1.2. Catalytic nanocarbon composites

Carbon nanotube:

Carbon nanotubes were originally discovered by Iijima in 1991(). CNTs have cylindrical structure with a nanoscale diameter and consist of rolled up graphene sheets. Their characteristic one-dimensioned morphology gives rise to unique thermal, electric and mechanic properties (). This structure of walls has the same honeycomb lattice structure of sp2 hybridized carbon as graphene. Moreover, CNT have many advanced structure and properties that are fascinating and are discussed in a wide range of different research topics. The superiority of the electronic can be optical, mechanical and even thermal. On the basis of tube layers, CNTs can be divided into distinct categories: SWNTs, single-walled carbon nanotubes, and MWNTs, multi-walled carbon nanotubes, see Figure 2.3 [25-38]. CNTs employed to different catalytic reactions such as Fischer-Tropsch, hydrogenation reaction, hydrogen evolution reaction and electrocatalysis. These phenomenon properties of CNTs cause an improvement on the synergistic performance as they enable the CNT with highly conductive surface for stronger interfacial interaction between the CNT and the catalyst and improve catalyst dispersion, etc. These CNTs can be stabilize electronically the intrinsic transition state of semiconducting nanoparticles, influence activation energy and extend the absorption wavelength of the catalyst. The catalyst can be immobilized on CNT via different methods such as impegration followed by reduction/oxidation, evaporation deposition and electrochemical deposition [39].

Figure2.2. CNTs structures: single-walled carbon nanotube (SWNT) and multi-walled carbon nanotube (MWNT) [40].

Graphene:

Graphene is known for being single atom their Sp2 hybridized carbon atoms, where the graphene in the form of a hexagonal ring structure with the length of 0.124 nm. Graphite is known by 3-dimensional (3D) layered crystal lattice structure which consist of 2-dimensional (2D) graphene sheets as shown in Figure 2.4 [41]. These graphite sheets are stacked together due to van der waals forces with a calculated distance equal to 0.335 nm for each other. Graphene well known also as the main material for the different kinds of graphitic forms including carbon nanotube CNT and fullerenes, see Figure 2.5 [42].

Figure 2.3. Basis of all graphitic forms. Graphene is a 2D building material for other dimensionalities of carbon materials.

Figure 2.4 Layered structure of graphite showing the Sp2 hybridized carbon

atoms tightly bonded in hexagonal rings.

Graphitic Nanofibres (GNF)

Graphitic nanofibers (GNFs) are a CNS with a unique morphology. They are known for their cylindrical structure. The internal surface has step edges with the size of 3-4 nm which can work as a support position for guest species. The fibres are of stack orientation and are made of graphite planes. Step edges provide large inner hollow cavity (50 – 70 nm) that permit for the transfer of different molecules which have the GNFs unique and interesting for heterogeneous catalytic reactions, see Figure2.6 [43, 44].

Figure 2.6 GNF and their unique step-edges [45].

Inorganic Aerogels

Inorganic aerogels are one of the most exciting materials of the 21st century, based on their remarkable properties such as extremely high porosity and low densities, excessive dialectical strengths and large active surface areas [46, 47]. Due to these properties, inorganic aerogels have been used in numerous applications such as aerospace, energy generation and storage, biomedical devices and implants, sensors and coating [48]. The first inorganic aerogel was reported by Kistler who introduced silica-based aerogels. Since then, aerogels have been produced from many other inorganic materials, such as metal oxides, chalcogenides, and carbons. More recently, aerogels have also been fabricated from carbon nanostructures such as carbon nanotubes and graphene, see Figure2.7 [49, 50].

Figure2.7 Types and evolution timeline of aerogels [51].

Aerogels can be very generally classified into two categories: single-component aerogels and aerogel composites as shown in Figure2.8 [52]. This project will introduce a new class of single-component aerogels, specifically GNF aerogels, and study their synthesis and properties. Subsequently the synthesis of new aerogel composites will be explored, namely metal-NP/GNF aerogels, followed by the study of important structure-function relationships in context of heterogeneous catalysis.

In general, aerogel can be prepared using sol gel method, either using supercritical fluid drying or freeze drying

3 Introduction

Over the last decade significant advancement in noble metal nanoparticles supported carbon-based materials for applications in catalysis has been made. This is a result of important progress in synthesis, characterization and materials leading to better understanding of the fundamental properties of these materials allowing transfer into industrial applications.

3.1 Supported MNPs for heterogeneous catalysis

Noble metal nanoparticles (MNPs) such as Ru, Rh, Pd, Ag, Au, and Pt are known to exhibit exciting chemical and optical properties [51-53]. As MNPs have low coordinate metal atoms on their surface area and a colossal surface to volume ratio they typically display high catalytic performance. However, since they are intrinsically metastable, they tend to leach or irreversibly aggregate atoms of metal under standard chemical process conditions. Therefore, MNPs/CNTs nanohybrids have an interesting application in numerous sectors, see Figure3.1. They have limited practical application in catalysis reactions, as process conditions result in rapid loss of intrinsic catalytic performance due to aggregation or agglomeration. Support materials, however, can be utilized to stabilise them, for example nanocarbon materials [54].

Figure3.1 Brief summary of preparation and application of noble metal NPs/CNTs nanohybrids. (Reproduced from Wu et al. [54] with permission from Elsevier Science.)

Graphene have phenomenal properties due to its thermal, mechanical stability and its extreme mobility with an ideal atomic lactic. Graphene is also ideal for supported system in heterogeneous catalysis reactions due to the synergy between its sp2 hybridised surface and organic molecules [55].

Active catalysts have been reported in which graphene-based nanomaterials act as stabilising supports, reducing the size the particulates and simultaneously enhancing both the stability and solubility [56-57]. Wang, P. et al. [58] reported enhanced catalytic activity in the Heck carbon-carbon coupling reaction using palladium supported graphene. The material was prepared by first intercalation of M+ ions between layers of a graphene oxide support, prepared using the Hummer’s method [59]. Chemical reduction was then used for Pd NPs in the graphene oxide using H2O and hydrazine hydrate. The catalytic activity of the resultant materials was investigated, and the performance compared to that of various supported palladium-based catalysts in the coupling reaction of iodo-benzene and styrene, see Table3.1.

Table3.1 Performance of numerous supported Pd based catalysts in coupling reaction of iodo-benzene and styrene.

Entry

Catalysis

Solvent

Base

Amount (mol %)

T ( ͦ C)

t (h)

Yields (%)

Ref.

1

Pd/graphene oxide

Toluene

NEt3

0.54

Reflux

5

62

60

2

Pd@PRGO

H2O: EtOH = 1:1

K2CO3

0.5

180a

1/6

95

61

3

PdNs-PAMAM-g-MWNTs

NMP

K2CO3

0.3

100

2.5

95

62

4

Pd/HCN

DMF

K2CO3

0.255

120

1

100

63

5

Pd/graphene

NMP

K2CO3

0.05

100

2.5

98

64

a The temperature was obtained by microwave irradiation.

In a separate study B. Cornelio, et al. [65] investigated how the preparation method as described by Zhi et al. [66] and the structure of a range of catalytic nanoreactors, based on nanoparticles located in hollow encapsulated graphitized nanofibers, effected the catalytic performance. In this study, the optimum catalytic material was observed to have small (2-5 nm) palladium nanoparticles located at the graphitic step-edges within the GNFs, see Table3.2, scheme 3.1 and scheme 3.2. The materials exhibited impressive catalytic properties in Suzuki Miyaura cross coupling reactions. The results reveal that the addition of the oxidative agents to the Pd NPs in the Suzuki Miyaura reaction happens at the step-edge of the nanofibers with the confinement at the nanoscale playing a sensitive role in the mechanism and kinetics of the reactions. Hence, the extent of the confinement imposed by the carbon nanoreactors can be controlled through careful selection of the aryl iodide reactant. To explore this the Suzuki Miyaura reaction was performed with variety of confinement in the cross-coupling reaction, see Table3 and scheme 3.1 and scheme 3.2.

Schem3.1 The palladium catalysed reactions of aryl iodides 1 and phenylboronic acids 2 leading to the products of Suzuki Miyaura cross coupling 3, dehalogenation 4 and Ullmann coupling 5.

Scheme3.2 The competitive Suzuki Miyaura reactions of (a) two aromatic boronic acids with a common aryl iodide and (b) two aryl iodides with a common aromatic boronic acid.

Table3.2 Comparison of the selectivity and activity of catalytic nanoreactors in the Suzuki Miyaura cross coupling of 1-iodo-4-nitrobenzene 1a and phenylboronic acid 2aa.

Entry

Catalyst

t/h

Conversion b/%

Selectivity for 3aa

(4: 5a) b/%

1

PdNP@GNF

24

83

87 (10: 3)

2

PdNP@GNF-I

24

98

95 (0: 5)

3

PdNP@GNF-II

24

82

96 (0: 4)

4

PdNP@GNF-III

24

36

93 (2: 5)

5

PdNP@GNF-IV

144

40

0 (100: 0)

a Standard conditions: 1-iodo-4-nitrobenzene 1a (0.056 mmol), phenylboronic acid 2a (0.075 mmol), sodium acetate (0.13 mmol), catalyst (2 mol%), methanol (5 mL), 700C, 24 h.

b Conversion and selectivity for 4-nitrobiphenyl (3aa), nitrobenzene (4) and 4,4̀-dinitrobiphenyl (5a), the products of cross-coupling, dehalogenation and Ullmann coupling respectively, were determined by 1H NMR spectroscopy of the crude mixture.

Table3.3 Comparison of the activity and selectivity of PdNP@GNF and PdNP/GNF catalysts in the Suzuki Miyaura cross-coupling reaction of aryl iodides 1a–e and phenylboronic acids 2a–ea.

Entry

Catalyst

R1

R2

Conversion b/%

Selectivity for 3 (4:5a-b) b/%

1

PdNP@GNF

1a

4-NO2

2a

H

83

2aa

87 (10: 3)

2

PdNP/GNF

1a

4-NO2

2a

H

78

2aa

80 (17: 3)

3

PdNP@GNF

1a

4-NO2

2b

4-Me

77

3ab

94 (3: 3)

4

PdNP/GNF

1a

4-NO2

2b

4-Me

65

3ab

92 (4: 4)

5

PdNP@GNF

1a

4-NO2

2c

3-Me

74

3ac

97 (1: 2)

6

PdNP/GNF

1a

4-NO2

2c

3-Me

74

3ac

97 (1: 2)

7

PdNP@GNF

1a

4-NO2

2d

2-Me

58

3ad

68 (32: 0)

8

PdNP/GNF

1a

4-NO2

2d

2-Me

58

3ad

67 (33: 0)

9

PdNP@GNF

1a

4-NO2

2e

3-OMe

83

3ae

96 (2: 2)

10

PdNP/GNF

1a

4-NO2

2e

3-OMe

81

3ae

95 (3: 2)

11

PdNP@GNF

1b

3-NO2

2a

H

99

3ba

71 (28: 1)

12

PdNP/GNF

1b

3-NO2

2a

H

98

3ba

79 (19: 2)

13

PdNP@GNF

1c

2-NO2

2a

H

80

3ca

64 (36: 0)

14

PdNP/GNF

1c

2-NO2

2a

H

87

3ca

99 (1: 0)

15

PdNP@GNF

1d

H

2b

4-Me

42

3db

100 (0: 0)

16

PdNP/GNF

1d

H

2b

4-Me

44

3db

100 (0: 0)

17

PdNP@GNF

1e

4-NO2

2b

4-Me

23

3eb

100 (0: 0)

18

PdNP/GNF

1e

4-NO2

2b

4-Me

24

3eb

100 (0: 0)

a Standard conditions: aryl iodides 1a–e (0.041–0.056 mmoll) boronic acids 2a–e (0.053–0.075 mmol), sodium acetate (0.094–0.13 mmol), catalyst (2 mol%), methanol (5 mL), 70 ͦ C, 24 h. b Conversion and selectivity for biphenyls 3aa–eb, nitrobenzene 4 and 4,4̀- and 3,3̀-dinitrobiphenyls 5a and 5b, respectively, the products of cross-coupling, dehalogenation and llmann coupling respectively were determined by 1HNMR spectroscopy of the crude mixture.

Ohtaka A. et al. [67] reported that palladium and bimetallic Pd–Ni NPs can be prepared by reduction using a solvent method of the oxidized material deposited on multiwalled carbon nanotubes (MWNTs) . The catalytic activity was explored using materials with 0.1 mol% Pd loading, at 120°C for 1 h and water as a solvent under ligand-free conditions. The reaction took place quantitatively for the cross coupling of 4-bromoanisole with phenylboronic acid for all materials, see Table3.4. Interestingly, the reactivity was observed to decrease in the presence of potassium phenyltrifluoroborate, see Table3.5. Moreover, the analogous 4-methoxytolane was quantitatively obtained allowing the recycling of the catalyst during 3 cycles, as illustrated in Table3.6. Finally, for the cross coupling reaction of 4-iodoanisole and phenyl acetylene with pyrrolidine as base at 120 ͦ C in water, see Table3.7.

Table3.4 Catalytic activity of Pd and bimetallic Pd–Ni NPs in the Suzuki Miyaura reaction using phenylboronic acid in water[a] showing better results with MWNT supported Pd NPs coated with PVP.

Entry

Catalyst

Yield [%] [b]

1

Pd/MWNTs

54

2

Pd70Ni30/MWNTs

48

3

Pd50Ni50/MWNTs

47

4

Pd30Ni70/MWNTs

63

5[c]

PVP–Pd

30

[a] Reaction conditions: 4-bromoanisole (0.5 mmol), phenylboronic acid (0.75 mmol), catalyst (0.1 mol %Pd), K2CO3 (1.5 mmol) in H2O (0.3 mL).[b] Determined by GC analysis based on 4-bromoanisole consumption. [c] In 0.5 mL of H2O.

Table3.5 Reaction data for the Suzuki Miyaura reaction with phenylboronic acid in water[a] catalysed by various Pd and Ni catalyst showing optimization of the reaction conditions by using the bimetallic Pd30Ni70/MWNTs as a precatalyst.

Entry

Catalyst [(mol% Pd)]

Base

Additive

T [⁰C]

t [h]

Yield [%][B]

1

Pd30Ni70/MWNTs (0.1)

KOH

-

100

1

41

2

Pd30Ni70/MWNTs (0.1)

K2CO3

-

100

1

63

3

Pd30Ni70/MWNTs (0.2)

K2CO3

-

100

1

53

4

Pd30Ni70/MWNTs (0.3)

K2CO3

-

100

1

75

5

Pd30Ni70/MWNTs (0.1)

K2CO3

-

100

2

61

6

Pd30Ni70/MWNTs (0.1)

K2CO3

-

100

3

72

7

Pd30Ni70/MWNTs (0.1)

K2CO3

-

120

1

83

8

Pd30Ni70/MWNTs (0.1)

K2CO3

PEG300[c]

120

1

92

9

Pd30Ni70/MWNTs (0.1)

K2CO3

TBAB[e]

120

1

95

10[d]

Pd/MWNTs (0.1)

K2CO3

TBAB[e]

120

1

96

11[d]

Pd30Ni70/MWNTs (0.1)

K2CO3

TBAB[e]

120

1

94

12[d]

Pd50Ni50/MWNTs (0.1)

K2CO3

TBAB[e]

120

1

˃ 99

13[d]

Pd10Ni90/MWNTs (0.1)

K2CO3

TBAB[e]

120

1

95

[a] Reaction conditions: 4-bromoanisole (0.5 mmol), phenylboronic acid (0.75 mmol), catalyst, base (1.5 mmol) in H2O (0.3 mL). [b] Determined by GC analysis based on 4-bromoanisole consumption. [c] PEG300/H2O (1:5) in 0.5 mL volume was used as a solvent. [d] 1.2 equiv. of phenylboronic acid were used. [e] TBAB (0.5 mmol).

Table3.6 Reaction conditions studies for the Hiyama reaction using Pd NPs/MWNTs

in water[a] showing variation of the yield due the amount of the Ph Si(OMe)3.

Entry

Catalyst [(mol% Pd)]

PhSi(OMe)3

[equiv.]

t [h]

Yield

[%][b]

1

Pd/MWNTs (0.1)

1.5

3

95

2

Pd70Ni30/MWNTs (0.1)

1.5

3

96

3

Pd/MWNTs (0.1)

1.5

1

95

4

Pd70Ni30/MWNTs (0.1)

1.5

1

92

5

Pd/MWNTs (0.1)

1.2

1

85

6

Pd70Ni30/MWNTs (0.1)

1.2

1

77

7

Pd50Ni50/MWNTs (0.1)

1.2

1

76

8

Pd70Ni30/MWNTs (0.1)

1.2

1

82

[a] Reaction conditions: 4-iodoanisole (0.5 mmol), trimethoxyphenylsilane, catalyst

(0.1 mol% Pd),50% aqueousNaOH (2.5 mmol). b] Determined by GC analysis based on

4-iodoanisole consumption.

Table3.7 Reaction conditions studies for the Sonogashira Hagihara reaction in water[a] showing variation of the yield due the amount of the phenyl acetylene.

Entry

Catalyst

Additive

t [h]

Yield [%][B]

1

Pd/MWNTs

-

5

74

2

Pd/MWNTs

PEG300[c]

5

73

3[d]

Pd/MWNTs

-

5

92

4[d]

Pd/MWNTs

-

1

92

5[e]

Pd/MWNTs

-

1

99

6[e]

Pd70Ni30/MWNTs

-

1

74

7[e]

Pd50Ni50/MWNTs (0.1)

-

1

69

8[e]

Pd30Ni70/MWNTs (0.1)

-

1

68

9[e]

Pd10Ni90/MWNTs (0.1)

-

1

60

[a] Reaction conditions: 4-iodoanisole (0.5 mmol), phenyl acetylene (0.6 mmol), catalyst (0.1 mol% Pd), pyrrolidine (1 mmol). [b] Determined by GC analysis based on 4-iodoanisole consumption. [c] PEG300/H2O (1:1) in 0.5 mL volume was used as a solvent. [d] 1.5 equiv. of phenyl acetylene were used. [e] 2 equiv. of phenyl acetylene were used.

The results show palladium particles were recorded to yield maximum activity and show stability, with high recyclability while retaining high activity from cycle to cycle. Further, a microscopic investigation of the nanoscale morphology discovered an increase in NPs size after catalysis. However, the extent of growth is highly dependent on the type of nanocarbon support. In summation, the overall performance found the process to be functional in term of catalytic properties and stable in several cross-coupling reactions.

Aygün M. et al, [68] investigated the catalytic performance of Pt and Pd NPs encapsulated in magnetically fabricated GNF and tested the reduction of nitrobenzene with both materials that exhibited high activity and selectivity, particularly PdNPs@GNF. Magnetic nanoreactor allows the confinement of the activity and recyclability. where, see Table3.8. The reduction of nitrobenzene has been done in the presence of catalysts that are of high glass pressure and molecular H2. It has to be quantified by 1H NMR. PdNP@GNF becomes the lower catalytic activity that cannot be compared to PdNPs@GNF-2 which is considered to be in large NPs size. As a result, this brings a surface area to the Pd NPs in PdNPs@GNF-1. On the other hand, there are no spotted reactions on the smaller PtNPs in PtNPs@GNF-2, this was a different case in the larger PtNPs@GNF-1, in this case the observation confirmed that it was likely to be active. The lack of reactivity was due to the fact that small Pt NPs in PtNPs@GNF-2 needed more investigation, as a result we thought out that the small nanoparticles would probably be amorphous to some point and so they had a poorly defined site for catalysis. On the other hand, they could be having residual dibenzylideneacetone (dba) ligands blocking the surface.

Table3.8 Reaction data for the reduction of nitrobenzene using PdNP@ GNF and PtNP@GNF catalytic nanoreactors using a high pressure H2 glass reactor showing the activity and selectivity of nitrobenzene due the NPs size.

Catalyst

Time

Conversion of Ph-NO2 [%]

Selectivity [%]

Ph-NHOH Ph-NH2

-

24 h

0

0

0

GNFa)

24 h

0

0

0

PdNPs@GNF-1

30 min

3.5

71

29

PdNPs@GNF-2

30 min

77

15

85

PdNPs@GNF-2

50min

100

0

100

PtNPs@GNF-1

30 min

24

36

64

PtNPs@GNF-1

200 min

100

0

100

PtNPs@GNF-2

30 min

0

0

0

PtNPs@GNF-2b)

24 h

0

0

0

Reaction conditions: Nitrobenzene (0.78 mmol); ethanol (0.5 mL); catalyst (0.00047 mmol of metal); H2 (8 bar); room temperature. All reactions were performed in duplicate and nitrobenzene conversion was determined by 1H NMR with an error of ±2%. a) GNF were annealed at 450 °C for 1 h prior to use; b) PtNPs@GNF-2 was annealed under H2 flow for 5 h at 150 °C prior to the reaction to get rid of any impurities on the surface of Pt which can cause deactivation of the catalyst.

Finally, Liu S. et al, [69] reported that single-wall carbon nanotubes (SWNTs) provide support to palladium catalysts that have been prepared through various methods. The influence in these preparatory methods on the structure and performances of the catalysts can be seen in Table3.9. Where (-1, -2,-3,-4,-5 and -6) represent these methods; Methanol pregnation method, water pregnation method, two-step water pregnation method, ion exchange method, methanol reduction method and KBH4 reduction method. Furthermore, the effect of the reduction temperatures has been studied in the hydrogenation of nitrocyclohexane to cyclohexanone oxime. Pd/SWNTs-2 prepared through water pregnation and reduced through hydrogen that showed the best result at 723 K and gives selective cyclohexanone oxime formation with nitro cyclohexanone conversion of 96 % in mild conditions of 0.3 MPA and 323 K, see Table3.10.

Table3.9 Nitro cyclohexane hydrogenation catalyzed by different catalystsa showing the effect of different preparation methods on the selectivity.

Catalyst

Conversion

of NCH (%)

Selectivity (%)

CHO CHA

Pd/SWNTs-1

99.7

70.5

2.8

Pd/SWNTs-2

98.9

85.9

6.3

Pd/SWNTs-3

99.6

79.7

2.0

Pd/SWNTs-4

99.4

65.5

5.0

Pd/SWNTs-5

79.7

85.4

0.2

Pd/SWNTs-6

99.8

76.9

3.6

a Reaction conditions: nitro cyclohexane 0.6 g; temperature 323 K; time 6 h; pressure 0.3 MPa; ethylenediamine 5 mL; NCH ¼ nitro cyclohexane; CHO ¼ cyclohexanone oxime; CHA ¼ cyclohexylamine.

Table3.10 Effect of reduction temperatures with catalysts on nitrocyclohexane Hydrogenation a.

Catalyst

Reduction temp.

(K)

Conversion

of NCH (%)

Selectivity (%)

CHO CHA

Pd/SWNTs-1

523

99.7

70.5

2.8

623

99.7

69.1

5.0

723

99.1

85.5

4.2

Pd/SWNTs-2

523

98.9

85.9

6.3

623

98.5

93.5

4.2

723

96.0

96.4

3.2

Pd/SWNTs-3

523

99.6

79.7

2.0

623

99.5

86.2

1.9

723

99.8

86.3

1.6

Pd/SWNTs-4

523

99.4

65.5

5.0

623

99.5

65.5

4.6

723

99.8

67.7

4.7

a Reaction conditions: nitrocyclohexane 0.6 g; temperature 323 K; time 6 h; pressure 0.3 MPa ethylenediamine 5 mL; NCH ¼ nitrocyclohexane; CHO ¼ cyclohexanone oxime; CHA ¼ cyclohexylamine.

There are few reported examples of routs to decorate nanocarbon aerogels with metal NPs to introduce the metal nanoparticles nanocarbon with aerogel. Here, I will review some examples regarding the graphene/CNT aerogel decorated pallidum and their performance in catalytic reactions.

Zhong W. et al, [70] reported a three-dimensional Pd/graphen aerogel hybrid that was used successfully. The preparation process of the Pd/graphene was in a systematic way. Graphene oxide was produced through the use of Hammer and Offeman’s procedure [71]. Pd NPs were formulated as reported in previous works [72]. The results showed that this type of 3D Pd/ graphene aerogel hybrid has a very excellent catalytic activity in the ammonia borane hydrolysis releasing the hydrogen with a frequency turnover of 9.70 molH2molmetal-1min-1 with an activation energy value equal to 30.82 kj/mol, see Table3.11. This is considered to be higher than that of 2D Pd/RGO and the original Pd nanoparticles. Moreover, the defects in the graphene aerogel are as a result of electron transfer of Pd nanoparticles to the graphene aerogel via metal support interactions. This is due to the benefits arising from the ammonia borane hydrolysis reaction. Besides, the pore rich 3D Pd/ graphene aerogel has provided a very big surface area for the ammonia borane hydrolysis. This is important for reutilization. The use of PTHF (Polytetrahydrofuran) makes Pd/graphene aerogel to have more structural pores. This offers graphene aerogels large specific areas and structures that are considered durable and help to recycle a catalyst.

Table3.11 H2 generation from hydrolysis of AB catalyzed by Pd-based catalysts and graphene-based composites that affect of metal-support interaction between graphene and Pd NPs in the hydrolysis of AB.

Catalyst

Metal/AB ratio

(mol/mol)

Maximum H2/AB

ratio (mol/mol)

Completion

time (min)

TOF

(molH2molmetal-1min-1)

Activation energy

(Ea, kJmol-1)

Ref.

Zeolite confined

Pd nanocluster

0.02

3.0

25

6.0

56

73

PSSA-co-MA-Pd

0.05

3.0

12

5.0

44

74

PdCl2

0.02

3.0

100

1.5

75

Pd/C

0.02

3.0

80

1.9

76

Pd/g-Al2O3

0.018

3.0

120

1.39

77

Pd black

0.018

3.0

250

0.67

78

Pd/CDG

15.55

79

Pd/RGO

0.04

3.0

12.5

6.25

51

80

Pd/graphene

aerogel

0.056

3.0

5.5

9.70

30.82

81

Cu/RGO

3.61

82

Cu@Co/RGO

8.36

51.3

83

Co/RGO

13.9

32.75

84

Ni/SiO2

13.2

34

85

In another study, Huang Y. et al, [86] reported a 3D amine terminated ionic liquid functionalized graphene through a covalent bond. There is successful fabrication of composite aerogel through a green reduction that induces self-assembly method. While ensuring there is no combination of particles on the graphene surface, Pd NPs are spread on graphene surface equally. The edifice of 3D IL rGO/Pd is composed of a structure that is permeable and with an extensive surface area which is strong. It provides a favourable environment for Suzuki cross coupling catalyst reactions.

Also, the catalyst can be recycled for more than 10 times without losing its effectiveness. Some the characteristics of 3D IL rGO/Pd catalyst that makes it necessary include; ability to be easily separated, recyclable, cost effective and being eco-friendly. Conclusively, the potential of 3D IL rGO/Pd composite aerogels in industrial catalysis cannot be exhausted, see Table3.12.

Table3.12 Optimization of the reaction conditions for Suzuki cross-coupling reactions of iodobenzene and phenylboronic acid catalyzed by catalyst-4a shown the effect of the solvents which mixed on the Suzuki cross coupling reactions.

Entry

Solvent

Base

Time (h)

Yield (%)

1

Acetone

K2CO3

1/4

11

2

DMF

K2CO3

1/4

20

3

MeOH

K2CO3

1/4

55

4

Isopropanol

K2CO3

1/4

34

5

H2O

K2CO3

1/4

46

6

EtOH

K2CO3

1/4

74

7

EtOH-H2O (v/v ¼ 1: 1)

K2CO3

1/4

93

8

EtOH-H2O (v/v ¼ 4: 1)

K2CO3

1/4

100

9

EtOH-H2O (v/v ¼ 4: 1)

KOH

1/4

87

10

EtOH-H2O (v/v ¼ 4: 1)

Na2CO3

1/4

62

a Reaction conditions: iodobenzene (1 mmol), phenylboronic acid (1.5 mmol),base (2 mmol), catalyst-4 (Pd 5 wt%, 0.5 mol%), and solvent (25 mL) at 80 _C, 15 min under air, b GC yield, c The polar aprotic Solvent. d The polar protic solvent.

However, to date research has focussed on CNT aerogels. To our knowledge, there has been no research that has investigated GNF aerogel yet, either in their pure form or functionalised with nanoparticle for catalytic reactions. Thus, the development of a synthetic route for GNF aerogels and their decoration with catalyst nanoparticles is a very topical issue that my PhD project will provide an insight on.

Summary:

Until now researcher’s efforts have been focused on the using MNPs and bimetallic NPs which are supported with CNTs either SWNT or MWNT using different methods. There are disadvantages in using these supports which can be notice in the efficiency of the catalytic properties. While using the GNF aerogel will increase the efficiency due the unique step edges that improve the NPs movement during the applied reactions. Since GNF aerogel with its high porosity, well-controlled pores and its high surface area () can offer the best quality for the NPs to be deposited on/in the nanostructure material. The material has not been explored or used in the catalytic application. My project will discuss the affect of GNF aerogel; and their different routes, that can improve the catalytic products and their applications. Furthermore, the GNF aerogel/rGNF areogel - either route A or route B- will be an excellent assistant in the process of the reactions regardless the where .

That is like critical thinking about what the others do, and what I will do in my research.

1931: First invention of Silica Aerogel

1970s: SiO

2

,

Metal Oxide

Aerogels

1990s: Organic/Polymer and Carbon Aerogels 2010s: CNT /Graphene Aerogels