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. 2024 Jun 13;14(13):9678-9686.
doi: 10.1021/acscatal.4c02028. eCollection 2024 Jul 5.

Deconvoluting Substrates, Support, and Temperature Effects on Leaching and Deactivation of Pd Catalysts: An In Situ Study in Flow

Affiliations

Deconvoluting Substrates, Support, and Temperature Effects on Leaching and Deactivation of Pd Catalysts: An In Situ Study in Flow

Oliver J Newton et al. ACS Catal. .

Abstract

Leaching behavior of three different Pd heterogeneous catalysts (PdEnCat 30, FibreCat FC1001, and Pd/Al2O3) during the Heck reaction of iodobenzene and methyl acrylate, in the presence of triethylamine, was compared using a tandem flow reactor. While leaching was observed in all three cases, Pd/Al2O3 appeared to be the most robust, showing little/no leaching at ambient temperature. The leached Pd species also appear to display different catalytic activities. With a slight modification of the reactor, the leaching caused by individual components of the reaction mixture can be assessed separately. For the polymer-supported catalysts, triethylamine caused the largest amount of leaching, even at 30 °C. In contrast, the leaching from Pd/Al2O3 was observed only in the presence of iodobenzene at 90 °C. Variations in leaching behavior were ascribed to differences in Pd species and immobilization methods.

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Conflict of interest statement

The authors declare no competing financial interest.

Figures

Figure 1
Figure 1
Original configuration of the tandem flow reactor (configuration 1).
Scheme 1
Scheme 1. Heck Coupling between Iodobenzene and Methyl Acrylate to Form Methyl Cinnamate
Figure 2
Figure 2
Three heterogeneous Pd catalysts were selected for this study.
Figure 3
Figure 3
Reaction profiles of Heck coupling obtained using PdEnCat 30, FC-1001, and Pd/Al2O3 in toluene, dioxane, and DMF in batch reactors. Reaction conditions: Pd catalyst (1 mol %), PhI (3.84 mmol), methyl acrylate (7.40 mmol), NEt3 (7.40 mmol), solvent (50 mL), 90 °C. % Conversions to product were determined by HPLC (see S1.1, Supporting Information).
Figure 4
Figure 4
Evaluation of leaching of PdEnCat 30 in different solvents in the tandem flow reactor (configuration 1, Figure 1): (A) DMF (T1 = 90 °C, T2 = 110 °C); (B) DMF (T1 = 30 °C, T2 = 110 °C); (C) dioxane (T1 = 90 °C, T2 = 110 °C); and (D) toluene (T1 = 90 °C, T2 = 110 °C). Red = S1 conversions; blue = S2 conversions.
Figure 5
Figure 5
Assessing leaching of FC-1001 and Pd/Al2O3 at 90 °C (A and C, respectively) and 30 °C (B and D, respectively) in DMF, using a tandem reactor (configuration 1, Figure 1). T2 = 110 °C in all these experiments. Red = S1 conversions; blue = S2 conversions.
Figure 6
Figure 6
Modified tandem reactor (configuration 2) for monitoring leaching caused by individual reaction components.
Figure 7
Figure 7
Leaching experiments were conducted with PdEnCat30 using the modified reactor (configuration 2, Figure 6). Each experiment started with PBR (T1) at 30 °C (blue), then increased to 90 °C (red).
Scheme 2
Scheme 2. Reaction of Pd(OAc)2 with Triethylamine to Form Pd(0) via a Dehydrogenative Mechanism
Figure 8
Figure 8
Pd leaching from FC-1001 by PhI (A) and NEt3 (B). Each experiment started with PBR (T1) at 30 °C (blue), then increased to 90 °C (red).
Figure 9
Figure 9
Stability of Pd/Al2O3 in iodobenzene (A) and triethylamine (B). Each experiment started with PBR (T1) at 30 °C (blue), then increased to 90 °C (red).

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