Loading…
A highly porous MgAl2O4 spinel-supported Mn3O4 as a reusable catalyst for glycolysis of postconsumer PET waste
[Display omitted] •Porous MgAl2O4 spinel-supported Mn3O4 catalyst was successfully synthesized from MgAl-LDH via thermal and chemical treatment, followed by Mn oxide loading.•High surface area and medium acid-base properties of the catalyst enhanced the PET conversion and BHET yield.•The catalyst wa...
Saved in:
Published in: | Journal of industrial and engineering chemistry (Seoul, Korea) Korea), 2022-11, Vol.115, p.251-262 |
---|---|
Main Authors: | , , , , , |
Format: | Article |
Language: | English |
Subjects: | |
Citations: | Items that this one cites Items that cite this one |
Online Access: | Get full text |
Tags: |
Add Tag
No Tags, Be the first to tag this record!
|
Summary: | [Display omitted]
•Porous MgAl2O4 spinel-supported Mn3O4 catalyst was successfully synthesized from MgAl-LDH via thermal and chemical treatment, followed by Mn oxide loading.•High surface area and medium acid-base properties of the catalyst enhanced the PET conversion and BHET yield.•The catalyst was highly recyclable without significant deactivation and regenerable with complete recovery of the initial activity.
A porous MgAl2O4 spinel-supported Mn3O4 catalyst, which is an efficient and robust catalyst for polyethylene terephthalate (PET) glycolysis, was synthesized from MgAl-layered double hydroxide (LDH) as a template via thermal and chemical treatment, followed by Mn oxide loading. A mesoporous structure in the MgAl2O4 spinel provided a high surface area (278 m2/g) and defects in which Mn3O4 was highly dispersed and strongly stabilized by the substitution of Al3+ and incorporation of Mn cation into the defects. The strong interaction of Mn oxide and the porous MgAl2O4 spinel support led to a dramatic increase of moderate acidic and basic properties, and to high resistance for Mn leaching during glycolysis. Using the Mn3O4/p-spMgAl800 catalyst, a yield of bis(2-hydroxyethyl) terephthalate > 95% was achieved within 3 h at 190 ℃. Despite eleven recycling times with regeneration, the catalytic activity remained without significant deactivation and was completely recovered after thermal regeneration at 500 ℃. |
---|---|
ISSN: | 1226-086X |
DOI: | 10.1016/j.jiec.2022.08.006 |