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www.jacobs.com | worldwide
Nitrogen Shortcut, Carbon Redirection and
Enhanced Oxygen Transfer: Elements of a Roadmap
to Sustainable Energy Independence Julian Sandino, PE, PhD, BCEE, WEF & IWA Fellow
MWEA Sustainable Energy & Process Joint Seminar
Battle Creek, MI
October 17, 2018
What is driving projects?
Addressing today’s issues…
– Aging infrastructure
– Service area changes
– Water stress
– Increased regulations
– Mitigating community and
environmental impacts
– Improve O&M efficiencies
While positioning for the
future...
Energy optimization: essential for
sustainable wastewater management
• Energy consumption has
significant environmental &
social impacts
• Energy is 2nd to labour in cost
of “used” water management
• Energy requirements limit
recovery of some resources
• Energy optimization =
f(reducing consumption;
increasing recovery)
Sustainable Energy
Management
A multi-pronged approach
to energy management
– Energy Use
Optimization
– Energy Recovery
Balancing carbon in the wastewater holds
the key to energy optimization
• Effective primary treatment reduces carbon load
to subsequent processes reducing energy
consumption
• Redirected carbon offers potential of significant
energy recovery
• Conventional BNR relies on carbon for nitrogen
and phosphorus removal.
• Mainstream deammonification: alternative to
current energy intensive carbon driven
processes
Deammonification: requires less energy
and allows for carbon redirection
1 mol Ammonia
(NH3/ NH4 +)
1 mol Nitrite(NO2
- )
1 mol Nitrate(NO3
- )
38% O2
1 mol Nitrite(NO2
- )
½ mol Nitrogen Gas(N2 )
25% O2
60% Carbon
NITRIFICATIONAerobic , Autotrophic
40% Carbon
Anammox
bacteria
DENITRIFICATIONAnoxic, Heterotrophic
VandCenter Syd (VCS)
• Established in 1853 as first modern waterworks in
Denmark
• 3rd largest water and wastewater company in
Denmark. Headquartered in Odense.
• Adopted in 2010 goal of achieving energy and CO2
neutrality in 5 years
• Ejby Mølle WWTP: 410,000 PE BNR facility; energy
self-sufficient in 2014
• Beyond Energy Neutrality Program: Jacobs
developed approach and assisted in the
implementation of multiple projects that by 2016
resulted in 115% electrical power and 160% heat self-
sufficiency. Excess heat is being sold to District
Heating grid, with locations as far as 20 kms away.
• Awards: 2013 Water and Energy Exchange (WEX)
Global Innovation Award (Madrid); International
Water Association’s 2018 Project Innovation Award
Ejby Mølle WWTP
DEMONTM selected for sidestream N removal
Sidestream
deammonification
reactors at the EMWWTP
Operational 2014
Mainstream deammonification was enabled by
adding hydrocyclones to the WAS flow
Dewatering
Centrate
Influent Primary
Clarifiers
WAS
Bioreactor (aerobic/anoxic)
Effluent
DEMON
Reactors
AOB Seed
Anammox
Seed
CEPT
Mainstream
hydrocyclones
Nitrogen shortcut allows further carbon redirection
• Improving primary clarification removal
– Historically 65-70% TSS removal w/o chemicals
– How much more will CEPT remove?
• Optimizing the trickling filter process
– Kept alive for wet weather flow conditions (~ 20% PE)
– Maximize PE feed to meet minimum wetting rates
• Reduces carbon and ammonia to bioreactors (lower O2 demand = lower energy)
• Nitrified effluent fed to bioreactors; sufficient carbon
• Increases biogas production11
Deammonification has contributed to net positive energy
status
12
0
5000000
10000000
15000000
20000000
25000000
2011 2012 2013 2014 2015 2016
En
erg
y,
kW
h
Electric Power Generated Heat Generated Electric Power Consumed Heat Consumed
En
erg
yO
pti
miz
ati
on
Stu
dy
Sid
es
tre
am
De
am
mo
nif
ica
tio
n
Co
ge
ne
rati
on
Ca
pa
cit
y E
xp
an
sio
n
Ele
ctr
ica
l P
ow
er
Su
rplu
s
Ma
ins
tre
am
De
am
mo
nif
icati
on
Ele
ctr
ical P
ow
er
Ne
utr
ali
ty
Carbon redirection reduces energy consumption from
secondary processes and recovers energy from sludge
• Conventional primary
treatment
• Chemically enhanced primary
treatment
• “A” stage of A/B Process (high
rate biological contact)
“A” Stage Dissolved Air Flotation
• Combines grit and FOG removal, biological contact, primary
treatment, P removal and sludge co-thickening
• Small footprint
Agua Nueva WRF, Pima Co., AZ
Solids Processing is Key to Energy Recovery
Opportunities
Brands Sands,
UK
Minworth, UK
DCWater, DC
Tuas WRP, SGP
Jurong WRP,
SGP
Bonnybrook WWTP,
AB
San Francisco
PUC, CA
Thermal Hydrolysis Process
HaarslevTM HCHS 2 operating facilities
Semi-continuous process
Lower complexity
17-22% TS pre-dewatering
Compact vacuum condenser
- overall smaller footprint
Lower heat requirements
Lower O&M costs
KC-based service center
ExelysTM
2 operating facilities
Continuous process
Lower complexity
18-24% TS pre-dewatering
Smaller systems
Dynamic steam mixer
Lower heat requirements
Lower O&M costs
Class A not proven
Cambi© THP >90% of all operating facilities
Batch process
Higher complexity
17% TS pre-dewatering
Oversized systems
Higher heat requirements
Higher O&M costs
Cooling footprint can be
significant
Modular- easy to install
Summary of Energy/Mass Balances and Costs - EMWWTP
Scenario
Electricit
y Sold
(MWh/d)
Heat
Sold
(MWh/d
)
Total
Energy
Sold
(MWh/d)
Biosolids
to
Disposal
(Wet
ton/d)
Simple
Payback
(Years)
Baseline 23.7 16.4 40.1 53 -Full THP 29.1 22.9 52.0 32 9WAS Only THP 29.4 30.7 60.1 38 10
Post-Digestion THP 26.7 15.3 42.0 23 16
Intermediate THP 23.4 4.3 27.7 30 28
Full THP +
Incineration29.1 37.6 66.7 6 55
Co-digestion maximizes use of existing assets –
potential for net positive energy condition!
• Fats, oil & grease (FOG)
• Food industry wastes
• Organic fraction of municipal
solid waste (OFMSW)
• Animal Manures
Energy recovery/generation: The key to neutrality and
beyond
19
F. Wayne Hill Water
Resources Center
Solids processing Point Loma WWTP -1.35 MW
San Diego, CA (90 ft)
Hydropower
Effluent Heat Recovery Wind Turbines
ACUA WWTP, NJ - 7.5 MW
Solar Panels
Rogers Rd. WWTP, AZ – 1.1 MW
MABR = Membrane Aerated Biofilm Reactor
• Bundles of hollow fibre gas permeable
membranes through which air (or oxygen) is
passed
• “Bubbleless” aeration – biomass directly
grows on membrane surface
• Technology that can be easily installed in
existing bioreactors to:
– Improve oxygen transfer efficiency and
reduce energy(3-4 times diffused aeration)
– Increase secondary treatment capacity
– Improve biological treatment performance
(e.g. ammonia removal)
Desktop evaluation suggests significant
benefits of a MABR retrofit at Ejby Mølle
• 40% reduction in energy consumption in BNR process
• 45% increase in achievable peak flow secondary clarifier
capacity
• 20% reduction in annual nitrogen mass discharged
• 5% increase in biogas production due to lower SRT
operation
Demonstration testing with full-scale units aimed at answering
several key questions for full scale implementation
• Biofilm management
– Is stuff going to get stuck?
– Is screening material an issue?
– What impact does mixing intensity and
scour have on performance?
• Taking advantage of the unique biofilm
– Shortcut nitrogen removal?
– Impacts on N2O emissions
• Response to dynamic flows and loads
In and out of basin configuration allows testing
MABR for different goals
Effluent
RAS
Primary Effluent
MABR module
Zone 1 RAS Fermentation
Zone 2
Zone 3
Zone 4
Effluent
RAS
Primary Effluent
Zone 1 RAS Fermentation
Zone 2
Zone 3
MABR Zone
In-basin MABR testing
• One of each manufacturer
in Zone 4
• Testing goals: biomass
accumulation, material
clogging (if any), O2
transfer rate
• Removal every 4 to 6
months for inspection
Parallel MABR testing out of basins
• Specific rate testing
• Diurnal variation
impacts
• Flow fed at ~1% of total
influent flow
• N2O emissions
• Removal every 4 to 6
months for inspection
MABR Demonstration Study – Collaborative
effort from key partners
Some summary thoughts …
• Energy is only 2nd to labor in the cost of treatment/ reclamation of water
• After water, energy is the most cost-effective and environmentally beneficial
resource to be recovered in a C-constraint world
• Energy self-sufficiency (even net positive status) is possible with typical
“used” water
• Balancing nutrient removal, carbon management, energy conservation, and
energy production is key
• Carbon management through redirection is key in energy optimization
• Recent developments such as mainstream deammonification and MABRs
are now increasingly being considered to help utilities achieve external
energy independence
www.jacobs.com | worldwide
Nitrogen Shortcut, Carbon Redirection and
Enhanced Oxygen Transfer: Elements of a Roadmap
to Sustainable Energy Independence
Julian Sandino, PE, PhD, BCEE, WEF & IWA Fellow
MWEA Joint Sustainable Energy & Process Seminar
Battle Creek, MI
October 17, 2018
Q & A