91Ö±²¥ engineers boost sustainable acrylic acid production using next‑generation membrane reactor
Acrylic acid is essential for everyday products – from paints and coatings to absorbent polymers – yet almost all of it is currently made from propylene, a petrochemical. As global biodiesel production rises, so does the supply of low‑value glycerol by‑product, creating an opportunity for cleaner, renewable chemical manufacturing.
In the new study, 91Ö±²¥ engineers, including Dr , compared a conventional packed‑bed reactor with an intensified membrane‑assisted system. By feeding oxygen gradually through a porous ceramic membrane, the team achieved better control of the reaction and suppressed unwanted combustion pathways.
Under optimised conditions, the membrane reactor delivered up to 58.7% acrylic‑acid selectivity – a 10‑percent improvement over standard reactor technology. It also helped regulate temperature, reducing hot‑spots and improving reaction stability.
Our membrane reactor concept shows clear advantages for selective oxidation systems. By distributing oxygen gradually along the reactor, we avoid the formation of hot spots and suppress over‑oxidation pathways, which ultimately boosts acrylic‑acid selectivity. This is a promising step toward a scalable, lower‑emissions alternative to the fossil‑based acrylic‑acid industry.
A more sustainable route for a globally important chemical
Glycerol is produced in large quantities by the biodiesel sector as a major by-product, with global production growing rapidly over the last two decades. Its oversupply has depressed market prices and created a need for new valorisation routes. Converting this low‑value by‑product into acrylic acid offers a way to lower emissions, reduce reliance on fossil resources and increase the circularity of chemical manufacturing.
The researchers used two catalysts, one to add oxygen in the right way, and one to remove water molecules (orthorhombic Mo–V–O (Ortho‑MoVO) oxidation catalysts and HZSM‑5(200) dehydration catalysts) respectively, to enable high glycerol conversion (94–99%) across all tested conditions, while the membrane reactor design strategically minimised over‑oxidation to CO/CO₂ (COₓ).
The team applied a statistical Design of Experiments (DoE) approach to map the coupled effects of temperature, GHSV, oxygen-to-glycerol ratio and feed‑to‑membrane ratio. This enabled the identification of precise operating windows that maximise acrylic acid yield while maintaining high conversion and limiting COₓ formation.
A 44‑hour stability study highlighted that catalyst deactivation is primarily driven by coke deposition on HZSM‑5(200), suggesting future work should focus on developing more coke‑resistant materials or regeneration strategies. Ortho‑MoVO, by contrast, retained its structure and showed minimal deactivation.
Waste glycerol represents an abundant and under‑used renewable feedstock. Demonstrating that a membrane‑assisted reactor can outperform conventional designs at scale is an important milestone for making this conversion route commercially attractive.
Pathway to industrial implementation
The results demonstrate strong potential for integrating membrane‑assisted reactors into future commercial glycerol‑to‑acrylic‑acid processes. Beyond enhanced selectivity, the reactor design:
- reduces oxygen consumption,
- improves temperature control,
- may reduce downstream purification costs due to higher product yields, and
- provides a more sustainable alternative to propylene‑based production.
The researchers note that next‑generation membranes specifically engineered for selective oxygen transport could unlock even greater performance improvements, along with opportunities to optimise operating pressure and reactor compactness.
This research was published in: Chemical Engineering Journal
Full title of the paper: Direct valorisation of bio-glycerol to acrylic acid: Experimental comparison of membrane and conventional reactors
DOI: 10.1016/j.cej.2026.175331
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