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. 2022 Jul 20;15(16):e202201006. doi: 10.1002/cssc.202201006

Table 6.

Variation of catalyst loading on the formation of acetates applying the reaction conditions for the simplex optimization.[a]

Entry

Catalyst loading [mol %] (μmol)

Conv. MF [%]

Product distribution [mmol]

TON acetates[c]

Sel. acetates [%]

Mass balance [%]

AcOH

AcOMe

AcOEt

MeOH

FA

DME

CO

CO2

Other[b]

1

15×10−3 (10)

89.1

9.4

13.2

0.5

3.8

3.6

3.2

14.6

2.3

1.5

2223±88

39.9

85.6

2

7.5×10−3 (5)

92.9

17.7

11.9

0.5

2.1

3.8

3.2

19.2

2.2

0.8

5509±506

49.9

92.8

3

3.75×10−3 (2.5)

88.6

14.8

11.4

0.3

2.9

5.1

3.2

19.5

1.5

0.8

11204±580

46.1

94.0

4

1.87×10−3 (1.25)

91.0

14.3

10.4

0.2

2.0

4.0

4.9

20.5

1.0

0.5

19749±187

42.2

87.8

5[d]

1.87×10−3 (1.25)

99.9

48.2

5.1

0.6

0.1

n.d.[e]

<0.1

2.2

1.3

0.2

43130

83.1

93.7

[a] Reaction conditions: P/Pd=6 : 1, NaOMe=215 μmol, NaI=2.92 mmol, MF=4.0 mL (65.0 mmol), T=173 °C, t=16 h. Quantification of the liquid phase using GC‐FID with mesitylene as internal standard. Quantification of the gas phase using ethylene as internal standard. [b] Acetaldehyde, ethanol, methane. [c] TON=mmolproduct mmolPd‐catalyst −1 as determined in at least two independent runs. [d] t=168 h. [e] n.d.=not determinable.