Hydrogenolysis of glycerol to propanediols over Ni supported on MgO catalyst


Citation

Shakur, Maryam and Irshad, Maryum and Haider, Muhammad Sajjad (2025) Hydrogenolysis of glycerol to propanediols over Ni supported on MgO catalyst. Pertanika Journal of Science & Technology (Malaysia), 33 (2). pp. 1007-1030. ISSN 2231-8526

Abstract

A Ni/MgO catalyst was used to undergo hydrogenolysis of glycerol, a byproduct of biodiesel synthesis, in the aqueous phase at different nickel loadings (10–40% by weight). The wet impregnation-prepared catalysts were characterized by XRD, SEM, TPR, and BET methods and showed strong metal-support interaction, good Ni dispersion, and high surface area, respectively. The catalytic activity in a batch reactor was measured at 220°C, 3 MPa hydrogen pressure, and 20 hours of reaction time. Glycerol conversion exhibited an increasing trend with Ni loading in the following sequence: 10%Ni/MgO < 20%Ni/MgO < 30%Ni/MgO < 40%Ni/MgO. The 20%Ni/MgO catalyst yielded the highest 1,2-propanediol (1,2-PDO) production, with a subsequent decrease observed at higher Ni loadings. In particular, the 20%Ni/MgO catalyst produced a 74% total glycerol conversion and a 76% selectivity toward 1,2-PDO. The optimal reaction conditions were then ascertained by examining the effects of temperature (200–240°C), glycerol content (5%–30% by weight), hydrogen pressure (3–5 MPa), and reaction time (6–25 hours) on the activity of the 20%Ni/MgO catalyst.


Download File

[img] Text (PJST Vol. 33 (2) Mar. 2025)
21 JST-5490-2024.pdf.crdownload
Restricted to Repository staff only

Download (1MB)

Abstract

A Ni/MgO catalyst was used to undergo hydrogenolysis of glycerol, a byproduct of biodiesel synthesis, in the aqueous phase at different nickel loadings (10–40% by weight). The wet impregnation-prepared catalysts were characterized by XRD, SEM, TPR, and BET methods and showed strong metal-support interaction, good Ni dispersion, and high surface area, respectively. The catalytic activity in a batch reactor was measured at 220°C, 3 MPa hydrogen pressure, and 20 hours of reaction time. Glycerol conversion exhibited an increasing trend with Ni loading in the following sequence: 10%Ni/MgO < 20%Ni/MgO < 30%Ni/MgO < 40%Ni/MgO. The 20%Ni/MgO catalyst yielded the highest 1,2-propanediol (1,2-PDO) production, with a subsequent decrease observed at higher Ni loadings. In particular, the 20%Ni/MgO catalyst produced a 74% total glycerol conversion and a 76% selectivity toward 1,2-PDO. The optimal reaction conditions were then ascertained by examining the effects of temperature (200–240°C), glycerol content (5%–30% by weight), hydrogen pressure (3–5 MPa), and reaction time (6–25 hours) on the activity of the 20%Ni/MgO catalyst.

Additional Metadata

[error in script]
Item Type: Article
AGROVOC Term: glycerol
AGROVOC Term: biodiesel
AGROVOC Term: catalysis
AGROVOC Term: nickel
AGROVOC Term: catalysts
AGROVOC Term: research
AGROVOC Term: propylene glycol
AGROVOC Term: chemicophysical properties
AGROVOC Term: efficiency
Geographical Term: Pakistan
Uncontrolled Keywords: Biomass; catalysis; glycerol; green economy; hydrogenolysis; Ni/MgO
Depositing User: Ms. Azariah Hashim
Date Deposited: 17 Aug 2026 04:01
Last Modified: 17 Aug 2026 04:01
URI: http://webagris.upm.edu.my/id/eprint/4796

Actions (login required)

View Item View Item