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. 2021 May 5;14(19):4041–4070. doi: 10.1002/cssc.202100400

Table 4.

Summary of selected metal‐based and organocatalysts reported for the hydrogenation and hydrosilylation of PET.

Cataylst

Cat. [mol %]

Solvent

T [°C]

H2 [bar]

t [h]

PET conv. [%]

Product(s)

Yield[a] [%]

Ref.

Hydrogenation

ruthenium(II)‐PNN pincer

2[b]

anisole/THF

160

54.4

24

100

1,4‐benzenedimethanol; EG

>99

[156]

RuII‐triphos complex (R=xyl)

0.2[c]

1,4‐dioxane

140

100

16

100

1,4‐benzenedimethanol; EG

>99

[157]

RuII‐sulfoxide complex

2[d]

anisole/THF

110

50

48

1,4‐benzenedimethanol; EG

73

[277]

C/MoO2

2.5

260

1.0

24

TA; EG; trace acetaldehydes

87; 87; <5

[279]

Hydrosilylation

Silane (equiv.)

B(C6F5)3

2

CH2Cl2

25

Et3SiH (4.3)

3

Si‐1,4benzenedimethanol; Si‐EG

85; 72[e]

[161]

5

CH2Cl2

25

TMDS (6.0)

16

p‐xylene; ethane

82; –[f]

[161]

7.5

CH2Cl2

25

PMHS (11.0)

16

p‐xylene; ethane

75; –[f]

[161]

Brookhart's iridium(III) catalyst

1

chlorobenzene

70

Et3SiH (6.0)

72

Si‐1,4benzenedimethanol; Si‐EG

63; 48[e]

[162]

MoO2Cl2(H2O)2

5

chlorobenzene

160

PhSiH3 (6.0)

96

p‐xylene; EG

65

[163]

[a] Product yields refer to 1H NMR analysis unless otherwise stated. [b] KOtBu employed as a co‐catalyst in a loading ratio of 50 : 1 : 2 {[ester repeat unit]/[catalyst precursor]/[KOtBu]}. [c] HNTf2 employed as a co‐catalyst in a loading ratio of 500 : 1 : 5 {[ester repeat unit]/[catalyst precursor]/[HNTf2]}. [d] KOtBu employed as a co‐catalyst in a loading ratio of 50 : 1 : 20 {[ester repeat unit]/[catalyst precursor]/[KOtBu]}. [e] Isolated yield. [f] p‐Xylene yield obtained by GC‐MS analysis. Ethane yield not determinable by 1H NMR spectroscopy owing to insolubility of PET in CH2Cl2.