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. 2023 May 24;62(22):8635-8643.
doi: 10.1021/acs.iecr.2c04568. eCollection 2023 Jun 7.

Zeolite Supported Pt for Depolymerization of Polyethylene by Induction Heating

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Zeolite Supported Pt for Depolymerization of Polyethylene by Induction Heating

Bernard Whajah et al. Ind Eng Chem Res. .

Abstract

We demonstrate that for polyethylene depolymerization with induction heating (IH), using a bifunctional (Pt- or Pt-Sn-containing zeolite) hydrocracking catalyst, we can obtain high hydrocarbon product yields (up to 95 wt % in 2 h) at a relatively low surface temperature (375 °C) and with a tunable product distribution ranging from light gas products to gasoline- to diesel-range hydrocarbons. Four zeolite types [MFI, LTL, CHA(SSZ-13), and TON] were chosen as the supports due to their varying pore sizes and structures. These depolymerization results are obtained at atmospheric pressure and without the use of H2 and result in an alkane/alkene mixture with virtually no methane, aromatics, or coke formation. We also demonstrate how IH helps overcome diffusional resistances associated with conventional thermal heating and thereby shortens reaction times.

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Conflict of interest statement

The authors declare no competing financial interest.

Figures

Figure 1
Figure 1
(a) Desorption of 1-PA from LTL zeolites. Samples saturated with 1-PA at 50 °C prior to TPD. XPS spectra of: (b) Pt/Ba-K-L, Pt 4f5/2,7/2; (c) PtSn/K-L, Pt 4f5/2,7/2; and (d) PtSn/K-L, Sn 3d5/2.
Figure 2
Figure 2
LDPE depolymerization with IH, 54 mT (500 A, 375 °C) input for 2 h at autogenous pressure. Liquid, gas, and coke conversions are on a weight basis.
Figure 3
Figure 3
Product distributions on carbon mol % basis for LDPE depolymerization at 500 A, 2 h.
Figure 4
Figure 4
(a) Alkene-to-alkane ratio of the product distributions. (b) Activation energy for IH depolymerization of LDPE with Fe3O4 and Pt-based LTL and MFI catalysts. The activation energy Ea was calculated at temperatures of 285 °C and higher. The R2 values of these fits were 1, 0.99, 0.97, and 0.99 for PtSn/K-L, Fe3O4, Pt/K-MFI, and PtSn/K-MFI, respectively.
Figure 5
Figure 5
HRTEM images of: (a) fresh PtSn/K-L catalyst; (b) spent PtSn/K-L catalyst after depolymerization of LDPE at 375 °C for 2 h.
Figure 6
Figure 6
(a) Pt LIII XANES spectra for Pt–Sn/K-L catalysts (b) Fourier transformed XAFS spectra for fresh and used PtSn/K-L. Green and red dotted lines represent fits to bulk Pt and Pt3Sn, respectively.

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