Abstract:An overview on the developments of zirconium phosphate (ZrP) and its organic derivatives in heterogeneous catalysis in recent years is reported in the present review. Two basic aspects have been emphasized: first, the catalytic properties of zirconium phosphates were discussed, with particular attention to the effect of surface acidity and hydrophobic/hydrophilic character, textural properties, and particle morphology on the catalytic performances. Then, the use of zirconium phosphates as support for catalytic… Show more
“…Among the recent literature, it is worth mentioning a short review highlighting the application of zirconium phosphate and its derivatives in the field of heterogeneous catalysis, especially in acid-catalyzed reactions such as dehydration, isomerization, and ester hydrolysis reactions [20]. By tuning the surface area and acidic properties, the material porosity and the functional groups anchored at the surface, it is possible to design and synthesize tailored catalysts with optimized properties for specific catalytic process.…”
In the present work, zirconium phosphates and mixed zirconium phosphate–sulphate acid catalysts have been investigated in the acetylation of glycerol in order to obtain acetins as fuel additives. The following catalysts with chemical composition, Zr3(PO4)4, Zr(SO4)2, Zr2(PO4)2SO4, Zr3(PO4)2(SO4)3 and Zr4(PO4)2(SO4)5 have been prepared and characterized by acid capacity measurements, BET, XRD, FT-IR, XPS. The surface chemical composition in terms of P/Zr and S/Zr atomic ratios was monitored in the fresh and used catalysts. Zr3(PO4)2(SO4)3 and Zr4(PO4)2(SO4)5 showed the highest acidity associated with the synergic effect of two main crystalline phases, Zr2(PO4)2SO4 and Zr(SO4)2·4H2O. The reactions of glycerol acetylation were carried out by using a mass ratio of catalyst/glycerol equal to 5 wt% and molar ratio acetic acid/glycerol equal to 3:1. The glycerol conversion versus time was investigated over all the prepared samples in order to identify the best performing catalysts. Over Zr3(PO4)2(SO4)3 and Zr4(PO4)2(SO4)5 full glycerol conversion was achieved in 1 h only. Slightly lower conversion values were registered for Zr3(PO4)4 and Zr2(PO4)2SO4, while Zr(SO4)2 was the worst catalyst. Zr4(PO4)2(SO4)5 was the most selective catalyst and was used for recycling experiments up to five cycles. Despite a modest loss of activity, a drastic decrease of selectivity to tri- and diacetin was observed already after the first cycle. This finding was attributed to the leaching of sulphate groups as detected by XPS analysis of the spent catalyst.
“…Among the recent literature, it is worth mentioning a short review highlighting the application of zirconium phosphate and its derivatives in the field of heterogeneous catalysis, especially in acid-catalyzed reactions such as dehydration, isomerization, and ester hydrolysis reactions [20]. By tuning the surface area and acidic properties, the material porosity and the functional groups anchored at the surface, it is possible to design and synthesize tailored catalysts with optimized properties for specific catalytic process.…”
In the present work, zirconium phosphates and mixed zirconium phosphate–sulphate acid catalysts have been investigated in the acetylation of glycerol in order to obtain acetins as fuel additives. The following catalysts with chemical composition, Zr3(PO4)4, Zr(SO4)2, Zr2(PO4)2SO4, Zr3(PO4)2(SO4)3 and Zr4(PO4)2(SO4)5 have been prepared and characterized by acid capacity measurements, BET, XRD, FT-IR, XPS. The surface chemical composition in terms of P/Zr and S/Zr atomic ratios was monitored in the fresh and used catalysts. Zr3(PO4)2(SO4)3 and Zr4(PO4)2(SO4)5 showed the highest acidity associated with the synergic effect of two main crystalline phases, Zr2(PO4)2SO4 and Zr(SO4)2·4H2O. The reactions of glycerol acetylation were carried out by using a mass ratio of catalyst/glycerol equal to 5 wt% and molar ratio acetic acid/glycerol equal to 3:1. The glycerol conversion versus time was investigated over all the prepared samples in order to identify the best performing catalysts. Over Zr3(PO4)2(SO4)3 and Zr4(PO4)2(SO4)5 full glycerol conversion was achieved in 1 h only. Slightly lower conversion values were registered for Zr3(PO4)4 and Zr2(PO4)2SO4, while Zr(SO4)2 was the worst catalyst. Zr4(PO4)2(SO4)5 was the most selective catalyst and was used for recycling experiments up to five cycles. Despite a modest loss of activity, a drastic decrease of selectivity to tri- and diacetin was observed already after the first cycle. This finding was attributed to the leaching of sulphate groups as detected by XPS analysis of the spent catalyst.
“…Solid supports for active species in heterogeneous catalysis include alumina, silica, titania, zeolites, metal oxides, activated carbons, and polymers. These have been extensively studied [3], together with layered Zr(IV) phosphates and phosphonates [4].…”
Section: Introductionmentioning
confidence: 99%
“…Zirconium monohydrogenphosphate of α-type (α-Zr(HPO 4 ) 2 ·H 2 O, α-ZrP) is a layered material with each layer consisting of ZrO 6 octahedra sharing oxygens with six HPO 4 tetrahedra through vertices. The POH groups point in the interlayer region and form hydrogen bonds with the water molecules [4][5][6]. It is a cation exchanger and has been used as a solid acid catalyst for several organic reactions.…”
Section: Introductionmentioning
confidence: 99%
“…It is a cation exchanger and has been used as a solid acid catalyst for several organic reactions. α-ZrP has been also used as solid support for catalytic species such as metal cations, noble metal nanoparticles and metal complexes [4,7]. In 2015, composite photocatalysts made of α-ZrP and AgCl particles were tested in the photo-assisted degradation of Rhodamine B [8].…”
A composite heterogeneous photocatalyst based on silver bromide was prepared by a reaction of silver exchanged zirconium phosphate (ZrP) and HBr. The ZrP/AgBr composite containing 53 wt% AgBr was tested in the photocatalytic degradation of Rhodamine B (RhB) and exhibited higher catalytic activity with respect to pure AgBr. As a matter of fact, the time needed to achieve a percentage of chromophore cleavage of about 90% was 3 min for the composite versus the 30 min needed for pure AgBr. The ZrP/AgBr composite turned out to be stable for at least three consecutive cycles. The UV-Vis spectra of the RhB solution, recorded at different irradiation times, were also decomposed and the concentration of the species formed by de-ethylation and cleavage processes during photocatalysis were calculated; the data obtained for the AgBr-based catalysis were also compared with those for the AgCl-based catalysis, and the degradation mechanism was suggested for both catalytic systems.
“…Finally, the desorption peak at 450-650°C shows the strong acidic sites on the surface of α-ZrP. [46][47][48] This indicates that the acidity of the α-ZrP is in the moderate range (1.65 mmol NH 3 g −1 ) which is attributed to the presence of P-OH groups on the surface of α-ZrP.…”
A facile synthesis of uracil‐Cu2+ nanoparticles immobilized on alpha‐zirconium hydrogen phosphate (α‐ZrP), abbreviated as α‐ZrP/Uracil/Cu2+, was presented. This compound was synthesized by the thermal method and used as a reusable catalyst for the Morita‐Baylis‐Hillman reaction without any additives. First, (3‐ iodopropyl) trimethoxysilane as a linker is reacted with α‐ZrP support to give the α‐ZrP/IPTMOS. Addition of uracil and then the addition of copper (II) acetate to α‐ZrP/IPTMOS results in the production of selected catalyst. The Morita‐Baylis‐Hillman reaction catalyzed by α‐ZrP/Uracil/Cu2+ demonstrated high product yield, short reaction time and a straightforward work‐up. The catalyst with enough outside surface was easily recovered using centrifugation and reused five times without a significant reduction in its activity.
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