|
|
L/min |
Volumetric flow rate |
|
μ(T) |
Pa s |
Temperature‐dependent viscosity |
| ‐B |
|
Backflushing |
|
C
|
g/L |
Concentration (Indices: 0: Start, f: final, x: biomass) |
|
C. vulgaris
|
|
Chlorella vulgaris
|
| CF |
Critical flux |
|
| DW |
|
Dry weight |
|
E
|
kJ/kWh |
Energy (indices: v: per m3 permeate, w: per kg algae biomass) |
| EOM |
|
Extracellular organic matter |
| FC
|
– |
Concentration factor |
| FS |
|
Flux‐stepping |
|
g
|
kg m/s2
|
Gravity acceleration |
|
H
|
m |
Pumping height |
| HDPE |
|
High‐density polyethylene |
| IFM |
|
Improved flux‐step method |
|
J
|
L/m2/h |
Permeate flux |
|
J
c
|
L/m2/h |
Critical flux |
| MF |
|
Microfiltration |
| MWCO |
|
molecular weight cut‐off |
| OD |
|
Optical density |
|
P
|
– |
Power (indices: th: theoretical, s: pump specific, a: aeration) |
|
p
|
bar |
Pressure (index hydro: hydrostatic) |
| PES‐PVD |
|
Polyethersulfone polyvinylpyrrolidone |
| PVDF |
|
Polyvinylidene fluorid |
| ‐R |
|
Relaxation |
| Rm
|
m−1
|
Membrane resistance |
|
S. cerevisiae
|
|
Saccharomyces cerevisiae
|
| TMP |
mbar |
Transmembrane pressure |
| TSS |
|
Total suspended solids |
| UF |
|
Ultrafiltration |
| VRF |
– |
Volumetric reduction factor |
|
η
|
– |
Efficiency factor |
|
ρ
|
kg/m3
|
Density |