64646-09-9

Upstream product

• 67-47-0 5-hydroxymethyl-2-furfuraldehyde 

Downstream Products

• 129971-50-2 <1S*,5S*>-8-methoxy-7-oxabicyclo<4.3.0>nonane-2-one 
• 129971-50-2 <1S*,5S*>-8-methoxy-7-oxabicyclo<4.3.0>nonane-2-one 
• 118237-87-9 cis-(+/-)-2-Amino-6-chloro-9-<4-(hydroxymethyl)-2-cyclopenten-1-yl>-9H-purine 

Relevant academic research and scientific papers

Highly selective ring rearrangement of 5-hydroxymethylfurfural to 3-hydroxymethylcyclopentanon catalyzed by non-noble Ni-Fe/Al2O3

3-Hydroxymethylcyclopentanone (HCPN) has been regarded as a considerable intermediate for the synthesis of polymers, pesticides and fragrances, which is mainly produced from petrochemical refinery. In recent years, the preparation of HCPN from biomass has gradually attracted attention. HCPN can be obtained through the selective ring rearrangement of biomass-based 5-hydroxymethyl furfural (5-HMF). In this paper, the Ni-Fe/Al2O3 was fabricated and used as an efficient catalyst for the production of HCPN, giving a 5-HMF complete conversion with a high HCPN selectivity (86 %) at 160 °C under 4 MPa H2 for 4 h. The optimized Ni-Fe/Al2O3 showed excellent activity towards the production of HCPN compared with monometallic catalysts, suggesting that there was a synergistic effect in Ni-Fe alloy. The introduction of Fe into Ni/Al2O3 improved the H2 adsorption capacity and also changed the acidic/basic sites, which are beneficial for the formation of HCPN. Moreover, Ni-Fe/Al2O3 exhibited superb stability and could be successively used four times without obvious loss in catalytic activity.

Reductive conversion of 5-hydroxymethylfurfural to 1,2,6-hexanetriol in water solvent using supported Pt catalysts

One-pot conversion of biomass derived 5-hydroxymethylfurfural (HMF) to 1,2,6-hexanetriol (1,2,6-HT) in water solvent was performed using Pt catalysts supported on various acid-base metal oxides. Pt catalysts supported on hydrotalcite, MgO, and CeO2 showed better yield of 1,2,6-HT and 2,5-bis(hydroxymethyl)-tetrahydrofuran (BHF), while ring-rearranged cyclopentanol derivatives were predominant products on the other Pt catalysts. The product distribution with time course on Pt/hydrotalcite revealed that HMF is at first hydrogenated to BHF, then the following parallel reactions proceed; ring-rearrangement to cyclopentanol derivatives, ring-hydrogenation to BHF, and hydrogenolysis to 1,2,6-HT. When pure hydrotalcite, MgO and CeO2 were physically mixed with Pt/SiO2, the selectivity to 1,2,6-HT was almost zero or less than 10 %. It was suggested that the formation of 1,2,6-HT proceeds at metal-support interface. The effect of metal-support interface was examined by means of IR spectra of adsorbed methanol. It was indicated that both basic property of supports and surface monodentate alkoxide formation are essential for the production of 1,2,6-HT. The maximum yield of 1,2,6-HT (42 %) was obtained using Co-promoted Pt/CeO2 catalysts pre-reduced at 200 °C.

Highly efficient hydrogenative ring-rearrangement of furanic aldehydes to cyclopentanone compounds catalyzed by noble metals/MIL-MOFs

Hydrogenative ring-rearrangement reaction of biomass-derived furanic aldehydes to cyclopentanone compounds catalyzed by metal/support bifunctional catalysts suffers a low selectivity of target product and serious carbon loss because of the Br?nsted acid catalysis. Herein, a series of pure Lewis acid sites MIL-MOFs (Fe-MIL-100, Fe-MIL-101 and Cr-MIL-101) with different crystal topology structures and metals are synthesized. Then the nanoparticles of Ru, Pt, Pd and Au are uniformly dispersed on the internal surface of the MOF support. The hydrogenation rate catalyzed by the noble metals/Fe-MIL-100 is three times faster than those obtained with Fe-MIL-101 and Cr-MIL-101-based catalysts due to the higher dispersion of nanoparticles on the former to make it more accessible to reactants. Meanwhile, both of the noble metals on Fe-MIL-100 and Fe-MIL-101 have a higher selectivity of cyclopentanone compounds than that on Cr-MIL-101, since the Fe ions in the MOF host with a higher oxophilicity will promote the adsorption and hydrolysis of the intermediate furanic alcohols (furfural alcohol or 2,5-bis(hydroxymethyl)furan). Furthermore, the noble metals/MIL-MOFs catalyst can maintain a good activity and stability after recycling for five runs. The current work will present an efficient catalytic reaction system for the hydrogenative ring-rearrangement of furfural and 5-hydroxymethyl furfural to synthesize cyclopentanone compounds.

Selective conversion of 5-hydroxymethylfurfural to diketone derivatives over Beta zeolite-supported Pd catalysts in water

Conversion of 5-hydroxymethylfurfural (HMF) in water to the linear diketone derivatives 1-hydroxyhexane-2,5-dione (HHD) and 2,5-hexanedione (HXD) was investigated over a series of Beta zeolite-supported transition metal catalysts (Co, Ni, Cu, Ru, Pd). Their catalytic performance was tested in a batch stirred reactor (T = 110 °C, PH2 = 20 bar) with Pd showing the highest activity and selectivity to HHD and HXD. The effects of Pd particle size, zeolite Si/Al ratio and reaction conditions (T = 80–155 °C, PH2 = 5–60 bar) were also investigated. The incorporation of Pd into Beta zeolite by the deposition-coprecipitation method produced the most efficient catalyst, affording complete HMF conversion (T = 110 °C, PH2 = 60 bar) predominantly to HHD (68% selectivity) and HXD (8% selectivity). The combination of a bifunctional acid/redox solid catalyst and water enhances the hydrolytic ring-opening and subsequent hydrogenation of the furan ring. Catalytic activity can be partially restored by a simple regeneration treatment. This work establishes a catalytic route to produce valuable diketone derivatives from renewable furanic platform sources in water.

Catalytic selective hydrogenation and rearrangement of 5-hydroxymethylfurfural to 3-hydroxymethyl-cyclopentone over a bimetallic nickel-copper catalyst in water

The selective hydrogenation and rearrangement of 5-hydroxymethylfurfural (5-HMF) to 3-hydroxymethyl-cyclopentone (HCPN) were studied over a MOF-derived bimetallic nickel-copper catalyst in water. The combination of nickel and copper dramatically improved the efficiency in both the selective hydrogenation of the carbonyl group of 5-HMF and the hydrogenative ring-rearrangement of the C5 ring, affording 70.3% yield for HCPN and 99.8% yield for the rearrangement products. Moreover, it was indicated that water acted as a solvent, reactant, and proton donor by dissociation at an elevated temperature, which supplied slightly acidic conditions and promoted the rearrangement reaction.

Effect of Cp*Iridium(III) Complex and acid co-catalyst on conversion of furfural compounds to cyclopentanones or straight chain ketones

In this paper, Cp*Ir (III) Complex and acid co-catalyst system was developed. By using Cp*Ir and γ-Al2O3 (Lewis acid), 5-hydroxymethylfurfural (5-HMF) can be converted efficiently to 3-hydroxymethyl cyclopentanone (HCPN). Meanwhile, Cp*Ir and Br?nsted acid can promote conversion of 5-HMF to 1-Hydroxy-2,5-hexanedione (HHD). The effect of Lewis acid and Br?nsted acid on the hydrogenation of furan derivatives was studied. Mechanism of conversion of 5-HMF to HCPN was discussed in detail and mechanism proposed by our predecessors was revised. Instead of being an intermediate for the formation of HCPN, it is believed that, HHD is a product of another reaction pathway. HHD condensed via Aldol reaction to produce 3-methylcyclopenten-2-ol-1-one (MCP) instead of HCPN. Under the promotion of Lewis acid, 5-HMF firstly convert to the precursor of HHD. After that, the reaction is through 4 π-electrocyclic ring closure process and HCPN was formed ultimately. Furthermore, we found that our Cp*Ir and acid co-catalyst system is suitable for a variety of furfural compounds. By using Cp*Ir, Br?nsted acid can promote conversion of furfural compounds to straight chain ketones and Lewis acid can promote the rearrangement of furfural compounds to cyclopentanone derivatives.

Selective conversion of 5-hydroxymethylfurfural to cyclopentanone derivatives over Cu-Al2O3 and Co-Al2O3 catalysts in water

The production of cyclopentanone derivatives from 5-hydroxymethylfurfural (HMF) using non-noble metal based catalysts is reported for the first time. Five different mixed oxides containing Ni, Cu, Co, Zn and Mg phases on an Al-rich amorphous support were prepared and characterised (XRD, ICP, SEM, TEM, H2-TPR, NH3/CO2-TPD and N2 sorption). The synthesised materials resulted in well-dispersed high metal loadings in a mesoporous network, exhibiting acid/base properties. The catalytic performance was tested in a batch stirred reactor under H2 pressure (20-50 bar) in the range T = 140-180 °C. The Cu-Al2O3 and the Co-Al2O3 catalysts showed a highly selective production of 3-hydroxymethylcyclopentanone (HCPN, 86%) and 3-hydroxymethylcyclopentanol (HCPL, 94%), respectively. A plausible reaction mechanism is proposed, clarifying the role of the reduced metal phases and the acid/basic sites on the main conversion pathways. Both Cu-Al2O3 and Co-Al2O3 catalysts showed a loss of activity after the first run, which can be reversed by a regeneration treatment. The results establish an efficient catalytic route for the production of the diol HCPL (reported for the first time) and the ketone HCPN from bio-derived HMF over 3d transition metals based catalysts in an environmental friendly medium such as water.

Catalytic Response and Stability of Nickel/Alumina for the Hydrogenation of 5-Hydroxymethylfurfural in Water

The catalytic response of Ni on Al2O3 obtained from Ni-Al layered double hydroxides was studied for the liquid-phase hydrogenation of hydroxymethyl furfural to tetrahydrofuran-2,5-diyldimethanol (THFDM) in water. The successive calcination and reduction of the precursors caused the removal of interlayer hydroxyl and carbonate groups and the reduction of Ni2+ to Ni0. Four reduced mixed oxide catalysts were obtained, consisting of different amount of Ni metal contents (47-68 wt %) on an Al-rich amorphous component. The catalytic activity was linked to Ni content whereas selectivity was mainly affected by reaction temperature. THFDM was formed in a stepwise manner at low temperature (353 K) whereas 3-hydroxymethyl cyclopentanone was generated at higher temperature. Coke formation caused deactivation; however, the catalytic activity can be regenerated using heat treatment. The results establish Ni on Al2O3 as a promising catalyst for the production of THFDM in water.

The effect of heterogeneous acid-base catalysis on conversion of 5-hydroxymethylfurfural into a cyclopentanone derivative

The effect of heterogeneous acid-base catalysis on conversion of 5-hydroxymethylfurfural (HMF) to 3-hydroxymethylcyclopentanone (HCPN) was investigated. It was demonstrated that acidic metal oxides, in particular Ta2O5, significantly enhanced the yield of HCPN due to their moderate Lewis acidity.

Conversion of 5-hydroxymethylfurfural to a cyclopentanone derivative by ring rearrangement over supported Au nanoparticles

Supported Au nanoparticles showed efficient catalytic performance for the ring rearrangement of 5-hydroxymethylfurfural (HMF) to a cyclopentanone derivative, 3-hydroxymethylcyclopentanone (HCPN), by taking advantage of the selective hydrogenation on Au nanoparticles and the Lewis acid catalysis of metal oxide supports. Among various metal oxide supported Au catalysts, the highest yield of HCPN was obtained by using Au/Nb2O5 (86% yield). the Partner Organisations 2014.