| Literature DB >> 27226699 |
Peter R Mooij1, Lisanne D de Jongh1, Mark C M van Loosdrecht1, Robbert Kleerebezem1.
Abstract
Microalgae have the potential to supply a biobased society with essential feedstocks like sugar and lipids. Besides being productive, strains used for this purpose should grow fast, be resistant to predators, and have good harvestability properties. Diatoms, a class of siliceous algae, have these and other preferred characteristics. In this paper, we describe the enrichment of microalgae in sequencing batch reactors with and without supply of silicate. Both reactors were operated with a light-dark cycle. To maximize storage compound production, carbon fixation and nitrogen uptake were uncoupled by limiting the availability of nitrate to the dark phase. After ten cycles, a stable culture was established in both reactors. The diatom Nitzschia sp. dominated the silicate-rich reactor, and the green algae Chlamydomonas sp. dominated the silicate-depleted reactor. Over the remaining 27 cycles of the experiment, the microalgal community structure did not change, indicating a highly stable system. Although the dominant microalga was highly dependent on the presence of silicate, the performance of both microalgal enrichments was similar. Polymers of glucose were stored during the nitrogen-limited light period. On organic matter dry weight basis, the sugar content of the biomass increased during the light period from 17 ± 4 to 53 ± 4 % for the silicate-limited culture, and from 14 ± 4 to 43 ± 4 % (w w-1) for the silicate excess culture. These results show that storage compound production can be achieved under various conditions, as long as a selective environment is maintained.Entities:
Keywords: Diatoms; Green algae; Mixed cultures; Selective environment; Storage compounds
Year: 2015 PMID: 27226699 PMCID: PMC4851980 DOI: 10.1007/s10811-015-0678-2
Source DB: PubMed Journal: J Appl Phycol ISSN: 0921-8971 Impact factor: 3.215
Operational parameters
| Parameter | Unit | Value |
|---|---|---|
| Light period | h | 16 |
| Dark period | h | 8 |
| Cycle length | h | 24 |
| Solid retention time | h | 41 |
| Liquid volume | L | 1.2 |
| Temperature | °C | 28 |
| Stirrer speed | rpm | 200 |
| Gas flow reactor in and out | NmL min−1 | 50 |
| Gas recycle over reactor | NmL min−1 | 1200 |
| Gas composition | % CO2 in air | 5 |
| Average light intensity at inner reactor surface | μmol m−2 s−1 | 650 |
| Light source | – | HPS lamps |
| pH setpoint | – | 7.5 |
| Base | – | 1.0 M NaOH |
| Acid | – | 0.5 M HCl |
Medium composition
| Compound | Unit | Value |
|---|---|---|
| NaNO3 − | mM | 1.43 |
| H3BO3 | mM | 1.66 |
| CaCl2 · 2H2O | mM | 1.07 |
| MgSO4 · 6H2O | mM | 0.64 |
| K2HPO4 | mM | 0.23 |
| FeCl3 · 6H2O | mM | 0.11 |
| Na2EDTA · 2H2O | mM | 0.11 |
| MnCl2 · 4H2O | μM | 7.71 |
| CuSO4 · 5H2O | μM | 0.03 |
| ZnSO4 · 7H2O | μM | 0.69 |
| CoCl2 · 6H2O | μM | 0.43 |
| Na2MoO4 · 2H2O | μM | 0.77 |
| NaHSeO3 | μM | 0.10 |
| NaVO3 | μM | 0.01 |
| Allylthiourea | mg L−1 | 10 |
Fig. 1Operational cycle for reactors with effluent removal (E) and medium supply (M) at the start of the dark period. Numbers indicate the cumulative time in minutes from the start of the cycle
Identity of species according to microscopic observation and PCR-DGGE analysis
| Reactor | Species determined by microscope | Species determined by PCR-DGGE | RNA gene used | Identity (%) |
|---|---|---|---|---|
| Silicate excess |
|
| 18S | 100 |
|
|
| 18S | 96 | |
|
| 16S | 99 | ||
|
|
| 16S | 100 | |
| Silicate deplete |
|
| 18S | 99 |
|
|
| 18S | 98 | |
|
| 16S | 99 | ||
|
|
| 16S | 99 |
Only the main species present are depicted
Fig. 2Community structure (black lines, left y-axis) and nitrate left over after the dark phase (black open squares, right y-axis) in time for the silicate-depleted (top) and silicate-excess (bottom) reactors
Fig. 3Fraction of glucose polymers on organic dry weight basis at the start (gray squares) and at the end (black circles) of the light period in time for the silicate-depleted (top) and silicate-excess (bottom) reactors