biological struvite crystal formation in sludge …...options for p recovery primary sed. second....
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Dr Ana Soares, Lecturer Biological Engineering Copyrighted
Biological struvite crystal formation in sludge dewatering liquors
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Phosphorus: a pollutant or a resource?
Guideline
UWTD
(91/271/EEC)
2 mg/L (10k-100k p.e.)
1 mg/L (>100k p.e.)
New targets 0.01-0.1 mg/L P
Rock Phosphate Monthly Price -
US Dollars per Metric Ton
http://www.indexmundi.com/commodities
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World P resources
Gilbert N: The disappearing nutrient. Nature 2009 461: 16–718
Stopped exporting in 1997
Planned bans
on exportation
In gigatonnes
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Recovery of phosphorus from wastewater enough?
Municipal
wastewater
treatment
pant P
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Options for P recovery
Primary sed. Second. sed. Tertiary treatment
Treated
effluent
Sludge
Sludge
Large
items
Grit
Screens Grit
chamber
Activated sludge
or trickling filter
Sludge
Biogas Anaerobic digester
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P recovery from sludge liquors
Struvite chemical precipitation
+ Well known process installed at full-scale with a market
+/- Recovery of 90% of phosphorus (10% left in the wastewater)
- Needs high phosphorus streams >100 mg/L
- Crystallisation through chemical process with chemical addition
Le Corre KS, Valsami-Jones EB, Hobbs PC, Parsons SA: Phosphorus recovery from wastewater by struvite crystallization: A review. Crit Rev
Environ Sci Technol 2009, 39: 433–477.
Pratt C, Parsons SA, Soares A, Martin BD: Biologically and Chemically Mediated Adsorption and Precipitation of Phosphorus from Wastewater.
Trends in Biotechnology
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Sludge liquors have high P – other ways to recover P?
Sustainable
(no chemicals)
Versatile
(range of [P] )
High quality effluent
Usable for wastewater
mixed matrix
High yield, good product
quality
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Investigate the suitability of selected bacteria to produce struvite in wastewater and dewatering liquors
Bio-mineralization: biological formation of inorganic materials
Over 60 different minerals have been identified, including struvite and CaP
Widespread property in environment/nature
Well studied in biomedical sciences (e.g.: kidney stones)
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Bio-mineralization: Known mechanisms
Nucleus Crystal Vacuole Nucleus Crystal Vacuole
Nucleus
Crystal
Extracellular microenvironment
Crystal
Intracellular crystal production
Extracellular crystal production
Bacteria
Bacteria
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Bio-mineralization bacteria selection: Literature information
Myxococcus xanthus: soil bacteria, EXTRACELLULAR crystal production observed after 2 days in synthetic media
Bacillus pumilus: soil bacteria, EXTRACELLULAR crystal production observed after 6-20 days in synthetic media
Halobacterium salinarum: Aquatic halophilic bacteria, INTRACELLULAR crystal production observed after 3-4 days in synthetic media
Brevibacterium antiquum: permafrost soil bacteria, INTRACELLULAR crystal production observed after 2-3 days in synthetic media
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Bio-mineralization bacteria selection: Cultivation in synthetic media
Strains Growth rate
(1/h)
Dry weight
(mg/L)
Myxococcus xanthus 0.013 2160
Bacillus pumilus 0.039 720
Halobacterium salinarium 0.042 63
Brevibacterium antiquum 0.027 980
Negative control: media without bacteria – no crystal
production
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Bio-mineralization bacteria selection: Cultivation in wastewater
Primary sed. Second. sed.
Treated
effluent
Sludge
Sludge
Large
items
Grit
Screens Grit
chamber
Activated sludge
Sludge
Biogas Anaerobic digester Sludge liquors:
PO4-P: 30 mg/L
NH4-N: 629 mg/L
Mg: 39 mg/L
WW
PO4-P: 2.3 mg/L
NH4-N: 70 mg/L
Mg: 17.8 mg/L
Full-scale wastewater treatment plant (UK)
PE 570,000.
Thick./dewatering
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Bio-mineralization bacteria selection: Cultivation in wastewater
Typical µmax:
Denitrifiers= 0.1 1/h; Methanogens= 0.02 - 0.002 1/h;
Anammox = 0.001 - 0.004 1/h
Wastewater M.
xanthus
B.
pumilus
H.
salinarium
B.
antiquum
Settled
wastewater
Growth rate
(1/h)
Negligible 0.001 Negligible
0.004
Crystal dry
weight
(mg/L)
- 137 - 113
Sludge
dewatering
centrifuge
liquors
Growth rate
(1/h)
Negligible
0.001 0.002 0.002
Crystal dry
weight
(mg/L)
- 213 - 226
Negative control: Wastewater not inoculated – no crystal production
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Crystal characterisation
Crystals formed by B.antiquum in centrifuge sludge liquor were
approximately 250 µm
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Crystal characterisation
SEM images in sludge dewatering
centrifuge liquors
struvite
struvite
Scanning electron microscope with energy
dispersive x-ray spectroscopy (SEM-EDX)
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Effluent quality
Sludge dewatering centrifuge liquors
Settled wastewater
PO4-P
(mg/L)
NH4-N
(mg/L)
Mg
(mg/L)
PO4-P
(mg/L)
NH4-N
(mg/L)
Mg
(mg/L)
Initial concentration
30.5 629.0 38.9 Initial concentration
7.5 70.0 22.6
After cultivation
with B.
pimulus
2.1 122.5 18.7 After cultivation
with B.
pimulus
2.0 30.0 9.0
After
cultivation
with B. antiquum
1.5 117.5 21.4 After
cultivation
with B. antiquum
2.1 31.0 9.5
B. pimulus
removal
93% 81% 52% B. pimulus
removal
73% 57% 60%
B. antiquum
removal
95% 81% 45% B. antiquum
removal
72% 56% 58%
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Bio-struvite vs. chemical struvite (10,000 m3/day wastewater treatment plant producing 500 m3/day of sludge liquors)
* Costs used in chemical precipitation are from 2001 (Jaffer et al.,); struvite price $1500/ton
http://biomassmagazine.com/articles/1838/from-problem-to-profit
Parameter Biological struvite Chemical struvite
Production Kg/day 120 100
Capital costs
£ Fermentation
reactor (10 days HRT)
630,000 Precipitation
reactor
425,000
Blowers and
diffusers
Not
known
Blowers and
diffusers
825,000
Filtration unit 100,000 Desludge pump 75,000
Total capital
costs
£ total 730,000 total
1,325,000
Operating costs £/year Electricity
10,000
Electricity 3,500
Chemical costs 13,000
Total operating
costs
£/year total
10,000
total
16,500
Post treatment Likely not to be required Needs recirculation to the head of
the works
Income = £40,734
Total Opex = £10,000
Income = £33,945
Total Opex = £16,500
http://biomassmagazine.com/articles/1838/from-problem-to-profithttp://biomassmagazine.com/articles/1838/from-problem-to-profithttp://biomassmagazine.com/articles/1838/from-problem-to-profithttp://biomassmagazine.com/articles/1838/from-problem-to-profithttp://biomassmagazine.com/articles/1838/from-problem-to-profithttp://biomassmagazine.com/articles/1838/from-problem-to-profithttp://biomassmagazine.com/articles/1838/from-problem-to-profit
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Bio-struvite producing bacteria can be the “anammox” for phosphorus?
Microbial characterization
(μ, Ks, temp, nutrients, pH,
etc.)
Reactor
design
Struvite separation
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Conclusions
Bacteria can produce struvite crystals in wastewater in simple way (no optimisation yet!)
Microscope analysis showed presence of crystals as early as 3 days and visible crystals were seen in cultures after 10 days reaching up to 250 µm.
Crystals can be separated by filtration/centrifugation
The final concentration of phosphate in sludge centrifuge liquors reached 1.5 mg/L, indicating a 95% P and 55-86% ammonia removal
The process can potentially be economically attractive
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New flowsheets for wastewater treatment
Screen
Primary
Sedimentation
Raw
wastewater
anMBR
1 ry
/ 2 ry
sludge
Thickener
Sludge supernatant ( Return liquor )
Stabilised sludge to land
Anaerobic digester
Sludge recirculation
loop to heat exchanger
Gas
engine
Imported grid
electricity Digested sludge pump
Primary
sludge
pump
Thickened
Primary
sludge
pump
Disposal of gross
solids
Produced biogas
Treated
effluent
Nutrient rich
eluent
N - C
o n
t a c t o
r
P - C
o n
t a c
t o r
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Phosphorus removal media
HCO3-
SO42-
SO42-
SO42-
HCO3-
HCO3-
NO3-
Cl-
Cl-
Cl-
Cl-
Cl- PO43-
PO43-
PO43-
PO43- PO4
3-
PO43-
PO43-
Capacity 2 g P/ kg media
Regeneration 5% NaOH
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Compare technologies R
eso
urc
e r
eco
ve
ry p
ote
nti
al
Sludge to land Chemical
struvite Adsorption
processes
Phosphorus recovery technology
Bio-struvite
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Thank you for your attention
www.cranfield.ac.uk/SAS
Thank you to: Yorkshire Water and Severn Trent
Further reading:
Soares A, Veesam M, Simoes F, Wood E, Parsons SA, Stephenson T. 2013. Bio-struvite: A new route to recover phosphorus from wastewater. CLEAN - Soil, Air, Water. In Press.
mailto:[email protected]://www.cranfield.ac.uk/SAS