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The Microalgae hub project:
how to use microalgae for agro-industrial wastewater
bioremediation and valorisation of the algal biomass
E. Ficara, M. Bellucci, F. Marazzi, V. Mezzanotte K. Parati
The project – The microalgae hub
2
Collaborations:
Partners:
Consortium
Funding:
The motivation/context
Cremona Province
• Agriculture: 15.5% of companies belong to the
agricultural sector, breeding 887,000 pigs,
288,000 cows, e 1,800 buffalos  intensive
breeding
• Anaerobic digestion: prompted by national
incentive  more than 140 biogas plants
Nitrate directive (676/91/CE)
56% of the Cremona province is
classified as vulnerable to nitrate
3
Dairy by-
products
Zootechnical
waste
Microalgae Biomass
transformation
processes
transformation
processes
Effluent
Organic material, nittrogen,
Phosphor and salts
Cosmesis
Animal feed
Biofuels
Bioplastics
Biostimulants
WP2: Implementation of the Hub
WP 3: research and
technological development
activities
WP4 4: Training and
monitoring
WP5: Services
WP 6: Dissemination
CO2
The case study
Piggery farm
(20.000 capi)
W1
Biogas
Biogas
RW
2 digesters
V = 3,000 m3
HRT ≈ 30 d
T = 40°C
330 kWel
2 digesters + 2
post digesters
V = 9,000 m3
HRT ≈ 55 d
T= 42°C
1 MWel
WWTP
W2W3 5
The case study
6
• Low optical density/turbidity
• Physiological pH
• Non –inhibiting N-NH4
• N:P=10-30
W1
piggery
W2
digestate
W3
digestate
TQ SL TQ SL TQ SL
TS g/L 5 2 73 7,5 591 53
VS (g/l) 3 0.74 51 2 37 32
pH 7.4 7.3 7.7 8.1 7.8 8.2
N-NH4 (mg/l) 152 148 1 920 1 300 2 240 2 150
P (mg/l) 25 19 142 26 239 271
Turbidity (FAU) 148 191 4 280 70 3 660 4 460
COD sol (mg/l) 1 390 1 070 4 220 1 920 4 240 5 070
COD tot (mg/l) 4 550 1 000 72 440 3 400 5 560 50 000
Ideal
Pilot scale tests
Experimental campaigns:
• 2016: diluted digestate (1:5  1:3)
• 2017: piggery wastewater
• 2018: undiluted digestate
Assessment of:
• N and P forms
• Organic contamination (COD)
• Algae growth parameters (counts, TSS, OD680,
turbidity)
Raceway
A = 3.8 m2 (V =0.9 m3),
• paddlewheel
• pH control by bubbling CO2
• CO2 sump
• feeding pump
7
0
50
100
150
200
250
300
350
400
0
5
10
15
20
25
30
35
15/4 29/4 13/5 27/5 10/6 24/6 8/7 22/7 5/8 19/8 2/9 16/9 30/9 14/10
I(W/m2)
T(°C)
data
Averagedaily Temp°C Averagedaily irradiance W/m2
Pilot scale tests - 2016: diluted digestate
 Microalgae could grow in the liquid
fraction of agro-digestate and under
sub-optimal climatic conditions for
200 d
 Average productivity: 8.2 g TSS m-2 d-1
 N apportioning: 7±3% N was
assimilated; 61 ± 24% was nitrified
8
0
25
50
75
100
125
150
10/5 4/6 29/6 24/7 18/8 12/9 7/10 1/11 26/11HRT,SRT[d]
HRT → ∞
Pilot scale tests - 2018: undiluted digestate
Liquid recirculation
QIN(m3/d)
QOUT (m3/d)
Qevap
Qalgae (kgDW/d)
VRW(m3), Calgae (kgDW/m3)
Centrifuge
SRT = VRW× Calgae/ Qalgae
HRT = VRW/ QOUT
Undiluted
W2
9
Pilot scale tests - 2018: undiluted digestate
10
𝑑(𝑋 ∗ 𝑉)
𝑑𝑡
= 𝑄𝑖𝑛 ∗ 𝑋𝑖𝑛 − 𝑄𝑎𝑙𝑔𝑎𝑒 ∗ 𝑋𝑎𝑙𝑔𝑎𝑒 − 𝑄𝑜𝑢𝑡𝑋𝑜𝑢𝑡 +𝒓
Raceway mass balances:
V = Qin  t- Qout  t-Qalgae  t+  P – E
RW
Xout
Qin
Xin
Qout
Xout
Precipitation
(meteo data)
Evaporation
(estimated, Penman’s equation)
Pilot scale tests - 2018: undiluted digestate
Productivity: 6.2 gDM/(m2∙d) (< 8.2 ± 8.5 gDM/(m2∙d)
2016)
11
Removal efficiencies:
• NH4
+-N: 95 ± 12 [%]
• N: 52 ± 13 [%]
• PO4
3--P: 80 ± 21 [%]
• CODs: 45 ± 35 [%] N-NH4
+: 0 ± 1 %  high removal
N stripped: 35 ± 7 %  poor pH
control  stripping (or denitrification)
N-NO2
-: 8 ± 4 %
N-NO3
-: 44 ± 12 %  nitrification
N-biomass: 13 ± 1 %
Pilot scale tests - 2017: piggery WW
12
TSS
(g/L)
N-NH4
(mg/L)
N-NO3
(mg/L)
OD @680
(-)
sCOD
(mg/L)
P-PO4
(mg/L)
Cond.
(mS/cm)
Mean 0.2 200 3.6 0.15 658 20 3.5
Standard dev. 0.28 60 3.6 0.08 314 14 0.3
Stable growth but variable composition of algal community
Average productivity: = 10 gDM/m2/d  9 months = 27 tDM/ha/year
Pilot scale tests - 2017: piggery WW
13
• Ammonium removal Mean: 90%
• P removal: More variable Mean: 46%
• sCOD removal: Mean: 67% (O2 from algae)
N apportioning
Biomass apportioning
16%
73%
10% 1%
Nbio
Nox
NH4
Nstripp
75%
2%
15%
8%
Algae
Nitrifiers
Het
debris
Conclusions/Perspectives
PROs
- Reduced N load to the fields ( reduced
arable land demand for N disposal)
- Lower energy request for aeration
- Production of valuable algal biomass (CO2
capture, organic C and nutrients to be returned
to soils)
CONs
- Large areal request for algae treatment
- Overall efficiency largely dependent on
climatic conditions (may imply
discontinuous operation)
- Long term stability still to be proven
 Integrated schemes are to be tested for final applicability assessment
 Biomass valorization
 Optimization of culturing (respirometry+modelling)
14
Valorization
- Fertilisers,
biostimulants
- Biofuels
- Feed in aquacultures
- Biomaterials
Valorization – CH4
Biogas
Simple/straightforward
Reduces the overall N removal benefit
Low methane yield
(100-200 Nm3_CH4/ton_DM)
16
Obiettivo: Ottimizzare rapporto C/N
della miscela
++
• Pretreatments are required
(cost/benefit balance)
• Co-digestion
Valorization - PHA
17
Bioplastics/VFAs
More complex
Allows for N, P recovery
Low yield (0,08 -0,2 g_PHA/g_DM)
Fermentation
Struvite
Precipitation
PHA
accumulation
PHA
estraction
VFA
A
C
B
• Optimization of process parameters
• Co-fermentation
Thanks to
Francesca Marazzi
Valeria Mezzanotte
Micol Bellucci
Andrea Pizzera
All of you for listening
Katia Parati
Co-authors
18

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The Microalgae hub project - SaltGae Final event

  • 1. The Microalgae hub project: how to use microalgae for agro-industrial wastewater bioremediation and valorisation of the algal biomass E. Ficara, M. Bellucci, F. Marazzi, V. Mezzanotte K. Parati
  • 2. The project – The microalgae hub 2 Collaborations: Partners: Consortium Funding:
  • 3. The motivation/context Cremona Province • Agriculture: 15.5% of companies belong to the agricultural sector, breeding 887,000 pigs, 288,000 cows, e 1,800 buffalos  intensive breeding • Anaerobic digestion: prompted by national incentive  more than 140 biogas plants Nitrate directive (676/91/CE) 56% of the Cremona province is classified as vulnerable to nitrate 3
  • 4. Dairy by- products Zootechnical waste Microalgae Biomass transformation processes transformation processes Effluent Organic material, nittrogen, Phosphor and salts Cosmesis Animal feed Biofuels Bioplastics Biostimulants WP2: Implementation of the Hub WP 3: research and technological development activities WP4 4: Training and monitoring WP5: Services WP 6: Dissemination CO2
  • 5. The case study Piggery farm (20.000 capi) W1 Biogas Biogas RW 2 digesters V = 3,000 m3 HRT ≈ 30 d T = 40°C 330 kWel 2 digesters + 2 post digesters V = 9,000 m3 HRT ≈ 55 d T= 42°C 1 MWel WWTP W2W3 5
  • 6. The case study 6 • Low optical density/turbidity • Physiological pH • Non –inhibiting N-NH4 • N:P=10-30 W1 piggery W2 digestate W3 digestate TQ SL TQ SL TQ SL TS g/L 5 2 73 7,5 591 53 VS (g/l) 3 0.74 51 2 37 32 pH 7.4 7.3 7.7 8.1 7.8 8.2 N-NH4 (mg/l) 152 148 1 920 1 300 2 240 2 150 P (mg/l) 25 19 142 26 239 271 Turbidity (FAU) 148 191 4 280 70 3 660 4 460 COD sol (mg/l) 1 390 1 070 4 220 1 920 4 240 5 070 COD tot (mg/l) 4 550 1 000 72 440 3 400 5 560 50 000 Ideal
  • 7. Pilot scale tests Experimental campaigns: • 2016: diluted digestate (1:5  1:3) • 2017: piggery wastewater • 2018: undiluted digestate Assessment of: • N and P forms • Organic contamination (COD) • Algae growth parameters (counts, TSS, OD680, turbidity) Raceway A = 3.8 m2 (V =0.9 m3), • paddlewheel • pH control by bubbling CO2 • CO2 sump • feeding pump 7 0 50 100 150 200 250 300 350 400 0 5 10 15 20 25 30 35 15/4 29/4 13/5 27/5 10/6 24/6 8/7 22/7 5/8 19/8 2/9 16/9 30/9 14/10 I(W/m2) T(°C) data Averagedaily Temp°C Averagedaily irradiance W/m2
  • 8. Pilot scale tests - 2016: diluted digestate  Microalgae could grow in the liquid fraction of agro-digestate and under sub-optimal climatic conditions for 200 d  Average productivity: 8.2 g TSS m-2 d-1  N apportioning: 7±3% N was assimilated; 61 ± 24% was nitrified 8
  • 9. 0 25 50 75 100 125 150 10/5 4/6 29/6 24/7 18/8 12/9 7/10 1/11 26/11HRT,SRT[d] HRT → ∞ Pilot scale tests - 2018: undiluted digestate Liquid recirculation QIN(m3/d) QOUT (m3/d) Qevap Qalgae (kgDW/d) VRW(m3), Calgae (kgDW/m3) Centrifuge SRT = VRW× Calgae/ Qalgae HRT = VRW/ QOUT Undiluted W2 9
  • 10. Pilot scale tests - 2018: undiluted digestate 10 𝑑(𝑋 ∗ 𝑉) 𝑑𝑡 = 𝑄𝑖𝑛 ∗ 𝑋𝑖𝑛 − 𝑄𝑎𝑙𝑔𝑎𝑒 ∗ 𝑋𝑎𝑙𝑔𝑎𝑒 − 𝑄𝑜𝑢𝑡𝑋𝑜𝑢𝑡 +𝒓 Raceway mass balances: V = Qin  t- Qout  t-Qalgae  t+  P – E RW Xout Qin Xin Qout Xout Precipitation (meteo data) Evaporation (estimated, Penman’s equation)
  • 11. Pilot scale tests - 2018: undiluted digestate Productivity: 6.2 gDM/(m2∙d) (< 8.2 ± 8.5 gDM/(m2∙d) 2016) 11 Removal efficiencies: • NH4 +-N: 95 ± 12 [%] • N: 52 ± 13 [%] • PO4 3--P: 80 ± 21 [%] • CODs: 45 ± 35 [%] N-NH4 +: 0 ± 1 %  high removal N stripped: 35 ± 7 %  poor pH control  stripping (or denitrification) N-NO2 -: 8 ± 4 % N-NO3 -: 44 ± 12 %  nitrification N-biomass: 13 ± 1 %
  • 12. Pilot scale tests - 2017: piggery WW 12 TSS (g/L) N-NH4 (mg/L) N-NO3 (mg/L) OD @680 (-) sCOD (mg/L) P-PO4 (mg/L) Cond. (mS/cm) Mean 0.2 200 3.6 0.15 658 20 3.5 Standard dev. 0.28 60 3.6 0.08 314 14 0.3 Stable growth but variable composition of algal community Average productivity: = 10 gDM/m2/d  9 months = 27 tDM/ha/year
  • 13. Pilot scale tests - 2017: piggery WW 13 • Ammonium removal Mean: 90% • P removal: More variable Mean: 46% • sCOD removal: Mean: 67% (O2 from algae) N apportioning Biomass apportioning 16% 73% 10% 1% Nbio Nox NH4 Nstripp 75% 2% 15% 8% Algae Nitrifiers Het debris
  • 14. Conclusions/Perspectives PROs - Reduced N load to the fields ( reduced arable land demand for N disposal) - Lower energy request for aeration - Production of valuable algal biomass (CO2 capture, organic C and nutrients to be returned to soils) CONs - Large areal request for algae treatment - Overall efficiency largely dependent on climatic conditions (may imply discontinuous operation) - Long term stability still to be proven  Integrated schemes are to be tested for final applicability assessment  Biomass valorization  Optimization of culturing (respirometry+modelling) 14
  • 15. Valorization - Fertilisers, biostimulants - Biofuels - Feed in aquacultures - Biomaterials
  • 16. Valorization – CH4 Biogas Simple/straightforward Reduces the overall N removal benefit Low methane yield (100-200 Nm3_CH4/ton_DM) 16 Obiettivo: Ottimizzare rapporto C/N della miscela ++ • Pretreatments are required (cost/benefit balance) • Co-digestion
  • 17. Valorization - PHA 17 Bioplastics/VFAs More complex Allows for N, P recovery Low yield (0,08 -0,2 g_PHA/g_DM) Fermentation Struvite Precipitation PHA accumulation PHA estraction VFA A C B • Optimization of process parameters • Co-fermentation
  • 18. Thanks to Francesca Marazzi Valeria Mezzanotte Micol Bellucci Andrea Pizzera All of you for listening Katia Parati Co-authors 18