Not only catalyst composition, but also temperature, pressure and H2/C4 ratio play important roles in vapour phase hydrogenation of maleic anhydride (MA) to gamma-butyrolactone (GBL), affecting both MA conversion and GBL yield. Pressure determines the GBL BDO equilibrium (notwithstanding the presence of excess hydrogen), the H2/C4 ratio affects catalyst activity and life, and the optimum reaction temperature depends considerably on catalyst composition. On the contrary, high temperature activation and regeneration by thermal desorption under high hydrogen flow do not show any advantages. Furthermore, by comparing the catalytic reactivity of MA, succinic anhydride (SA) and their dimethyl-esters (DMM and DMS), it was shown that MA may be con...
The gas phase hydrogenation of maleic anhydride to obtain γ-butyrolactone was studied using Ni suppo...
The gas-phase maleic anhydride hydrogenation was studied at 170 °C and 1 bar using Ni/SiO2–Al2O3 cat...
A bubble-column slurry-reactor model has been developed for the hydrogenation of aqueous maleic acid...
Not only catalyst composition, but also temperature, pressure and H2/C4 ratio play important roles i...
The catalytic reactivity of maleic anhydride (MA), succinic anhydride (SA) and their dimethyl esters...
The catalytic reactivity of maleic anhydride (MA), succinic anhydride (SA) and their dimethyl esters...
The reactivities of the main products observed in the vapour phase hydrogenation of maleic anhydride...
The reactivities of the main products observed in the vapour phase hydrogenation of maleic anhydride...
Cubic spinel-type phases containing excess copper ions may be obtained by controlled oxidation of ho...
Succinic acid (SA) is a valuable raw material obtained by hydrogenation of maleic acid (MA). The pro...
Succinic acid (SA) is a valuable raw material obtained by hydrogenation of maleic acid (MA). The pro...
Hydrogenation of maleic anhydride (MAH) with Pd/C catalysts in supercritical carbon dioxide (scCO(2)...
The proper selection of transition metals and support is pivotal to the design of active and selecti...
Design and plantwide control of an integrated plant for the hydrogenation of maleic anhydride and th...
Long-term liquid phase studies of the activity in the formic acid-mediated hydrogenation of MAc to S...
The gas phase hydrogenation of maleic anhydride to obtain γ-butyrolactone was studied using Ni suppo...
The gas-phase maleic anhydride hydrogenation was studied at 170 °C and 1 bar using Ni/SiO2–Al2O3 cat...
A bubble-column slurry-reactor model has been developed for the hydrogenation of aqueous maleic acid...
Not only catalyst composition, but also temperature, pressure and H2/C4 ratio play important roles i...
The catalytic reactivity of maleic anhydride (MA), succinic anhydride (SA) and their dimethyl esters...
The catalytic reactivity of maleic anhydride (MA), succinic anhydride (SA) and their dimethyl esters...
The reactivities of the main products observed in the vapour phase hydrogenation of maleic anhydride...
The reactivities of the main products observed in the vapour phase hydrogenation of maleic anhydride...
Cubic spinel-type phases containing excess copper ions may be obtained by controlled oxidation of ho...
Succinic acid (SA) is a valuable raw material obtained by hydrogenation of maleic acid (MA). The pro...
Succinic acid (SA) is a valuable raw material obtained by hydrogenation of maleic acid (MA). The pro...
Hydrogenation of maleic anhydride (MAH) with Pd/C catalysts in supercritical carbon dioxide (scCO(2)...
The proper selection of transition metals and support is pivotal to the design of active and selecti...
Design and plantwide control of an integrated plant for the hydrogenation of maleic anhydride and th...
Long-term liquid phase studies of the activity in the formic acid-mediated hydrogenation of MAc to S...
The gas phase hydrogenation of maleic anhydride to obtain γ-butyrolactone was studied using Ni suppo...
The gas-phase maleic anhydride hydrogenation was studied at 170 °C and 1 bar using Ni/SiO2–Al2O3 cat...
A bubble-column slurry-reactor model has been developed for the hydrogenation of aqueous maleic acid...