Continuous
catalytic supercritical water gasification (CSCWG; 400
°C, 28 MPa) of microalgal biomass (Chlorella vulgaris) was carried out at the microalgae production site of ZHAW in Wädenswil
(Switzerland) nonstop over a period of 100 h. Microalgae slurries
(3–15 wt %) were successfully gasified to a methane-rich gas
for 55 h. The low total organic carbon of the reactor effluent (<400
mg L–1) recorded during that period demonstrated
the high catalytic activity of the Ru/C catalyst for converting microalgae
to the gaseous products. The addition of a sulfur removal step with
a commercial zinc oxide adsorbent was essential for protecting the
catalyst against sulfur poisoning. A brine effluent rich in nutrients
(N, K, S, P, Na) was withdrawn continuously from a salt separator.
In summary, the use of a zinc oxide adsorbent upstream of the catalyst
bed, together with a higher ruthenium loading of the catalyst, improved
the long-term performance of the CSCWG process significantly.