ODOURsim®
This is a revolutionary odour emission modelling software package
that predicts formation and emission of H2S from sewage treatment
works. The software is unique in producing dynamic predictions
that demonstrate variation of emission rate over time. It can
help generate accurate and meaningful odour contour plots in
dispersion modelling packages.
The product was launched at IWEX last October and is now being
proactively marketed to all utilities and consultants along
with a process modelling service providing specialist in-house
expertise.
Positive feedback is being received from the marketplace
and Water Innovate is currently in the final stages of negotiating
a number of significant contracts. The Company has employed
an
additional process modeller to handle the growing workload.
ODOURsim® is an essential design tool aiding the development
of defensible odour management plans and abatement strategies
for existing and planned installations. Because the product
is compatible with existing dispersion models its adoption
is relatively
simple.
The use of dispersion models to predict odour concentrations
from sewage treatment works is commonplace. The resulting
odour contour plots are often used in support of planning
applications.
The models can also be used to make decisions about site
specific odour control technologies.
However, it is critical to regard each element in the odour
annoyance pathway (see right) with equal importance.
An over-emphasis
on dispersion modelling can give inaccurate predictions.
ODOURsim® was
developed because of this over-emphasis on dispersion
modelling and the lack of attention given to inputs to
dispersion models.
The software allows the dynamic impact of flow, quality
and meteorological variables on emission rates to be
examined, avoiding the inaccuracies
inherent in using a constant H2S dispersion rate, through
mechanistic modelling of variable H2S formation and
emission. ODOURsim® employs
a liquid-phase H2S model and uses mass-transfer calculations
for various process components.
Variations in wastewater flow and quality at a treatment
works inlet can lead to significant differences in
influent odorant
concentrations and emissions from downstream processes.
To illustrate these effects, ODOURsim® has been
used to model a sewer feeding a set of primary sedimentation
tanks. The software
reveals emission
peaks at high flow conditions because the sewer flows
full, allowing H2S to form under anaerobic conditions,
and because
high flows
enhance emissions from the sedimentation tank weirs
(Figure 2).

Figure 2: Emission peaks for the sewer
and sedimentation tank system
These large variations have implications for when
odour measurements are taken. If spot measurements
were being
inputted into
dispersion models, the time of measurement would
be crucial. But because
ODOURsim® is dynamic, the impact over time of variables
on emission rates can be predicted. It is essential for emission
variations to be included in odour modelling exercise because
when significant variations in emission rate exist, deviations
can radically alter odour footprint.
N-Tox®
The patented N-Tox® nitrification toxicity monitor provides
early warning of wastewater treatment works breakdown and helps
prevent ammonia pollution of the aqueous environment. The monitor
avoids problems associated with probe fouling because it relies
upon gas-phase detection of dinitrogen oxide (N2O) rather than
detection of a chemical in the aqueous phase.
A final pre-production prototype is now under
test at Cranfield University’s Pilot Hall facility. Water Innovate has
advanced orders for units from major industrial customers under
long term
service contracts. The innovative design now comprises an integral
sample pump, gas conditioning device, non-dispersive IR gas
analyser, auto-calibration system and data logging unit, housed
within
an IP65 enclosure.
Prior research at Cranfield demonstrated
that N2O is rapidly detected when nitrification
starts to
fail.
The rate of
N2O production is linked to oxygen depletion
and ammonia shock
loading. Increases
in dinitrogen oxide levels are directly
related to nitrification failure. Hence, measurement
of the
N2O off-gas level
allows the monitoring of nitrification
performance to prevent
release of
ammonia.
Using N-Tox® to detect an increase of N2O above the start
of an activated sludge aeration lane means that at least one
hydraulic retention time of the final clarifier would pass
before nitrification failure. Figure 3 demonstrates that the
time lag
between detection of increased N2O, and the appearance of ammonia
provides typically seven hours warning of nitrification failure.

Figure 3: This graph shows what happens when
a short aeration failure occurs in an activated sludge plant.
The N-Tox® alarm allows time for remedial action to be taken.
Once a failure is detected, a number
of process options can be followed
to restore
nitrification
including
increasing aeration
rates, bypassing influent to storm
tanks, or returning high
ammonia liquors to the works inlet.
The key markets for N-Tox® are municipal sewage and industrial
effluent treatment. Many treatment works that discharge direct
to the aqueous environment are consented for ammonia at < 5
mg/l. These plants rely on ammonia removal through bacterial
conversion to nitrate.
Inhibition by aeration failure, toxic
chemicals or high ammonia concentrations
can result
in a wastewater
treatment
works
not meeting its required ammonia
consent. Some industrial effluents,
such as landfill leachate or pharmaceutical
wastewaters, have high ammonia
levels. The requirement for
an N-Tox® alarm
here is critical as the consequences of nitrification failure
are more serious.
The N-Tox® monitoring system provides an effective alternative
to other methods of nitrification failure detection (such as
ammonia probes or on-line respirometry) by providing an earlier
warning. Plant operators are alerted to problems early so that
remedial action can be taken.
ZR-Coag®
Special zirconium compounds have
been used to develop ZR-Coag®,
a product that enables high efficiency coagulation of potable
supplies and waste treatment effluents.
DWI approval for use in drinking
water treatment has been
applied for, as
well as international
patents, and Water
Innovate has
put in place a secure and
robust supply chain to
bring ZR-Coag® into
the UK market during 2006.
Any water or wastewater
treatment process that
currently uses
iron or aluminium
based coagulants
is a potential
application for ZR-Coag®. These coagulants characteristically dissociate
into strongly charged ions and their charge density is a significant
factor in determining coagulation and particle removal efficiency.
Zirconium ions are more effective as coagulants because they
have a 4+ charge, which
is more charge per mole than the 3+ charge of iron and aluminium.
Also, they exhibit a lower tendency
to
dissociate into lower
charged intermediates, or complete hydrolysis species, over a
broader pH range than either iron or aluminium.
The higher charge density
of ZR-Coag® significantly
improves the charge neutralisation
coagulation mechanism,
resulting
in enhanced organic and
suspended particle removal.
This can be
achieved at lower dose
rates, with less pH adjustment
and sludge production.
Larger flocs are produced
that are easier to separate,
allowing subsequent separation
systems to be operated
at higher
flow rates.
ZR-Coag® was originally developed with a specific focus on
NOM removal from upland waters, but it is equally applicable
to removal of other pollutants including turbidity, DOC and colour.
Applications include industrial processes that treat effluents
or process liquids by using coagulants to aid the removal of
organics and suspended or colloidal negatively charged particles,
and ZR-Coag® can
be effectively employed
in membrane pre-filtration
applications utilising
enhanced coagulation
techniques.
Coagulants are increasingly
used in municipal
sewage treatment
works either
to improve
the performance
of sedimentation
processes for suspended
solids removal,
or to reduce phosphate
concentrations
to satisfy the
requirements of
the Urban Wastewater
Treatment Directive.
To further demonstrate
the effectiveness
of ZR-Coag®, trials
with two water companies are ongoing. The first trial is examining
the use of ZR-Coag® as
a seasonal substitute
for ferric sulphate during
periods of very high
colour in upland raw
water
supplies.
The second trial is investigating
suitability of the product
for phosphate removal
in wastewater treatment.
Current Developments
Three advanced
tertiary
treatment technologies
are currently
being developed.
The Membrane
Chemical
Reactor MC-R™
is an innovation
combining
UV
and titanium
dioxide
to remove
pollutants
from high
COD and coloured
effluents.
Water Innovate
has
been successful
in
obtaining
a DTI Technology
Programme
grant
for
development
of the technology
under the
Waste Management
and Minimisation
initiative.
This
is part of
a large collaborative
project
to develop
a solution
to treating
waste
cutting oil
from
the metal
finishing
industry.
The second
technology
is the
Odour Extraction
Membrane
Reactor
OEM-R™.
It is a
new process that
will
remove
odour causing molecules,
with
applications
in sewage,
waste management,
and
oil and
gas sectors.
Finally,
the
Nitrification-Denitrification
Reactor
ND-R™is a novel
technology
for
removing
nitrogen
from wastewater,
avoiding
the
need for
chemical
additives.
The initial
focus
has been on
commercialising
ODOURsim®,
N-Tox® and ZR-Coag® and
taking them to market
either directly or through
licensing deals. During
2006 the Company
will be investing significant
resources in further
development of the remaining
technologies, as well
as in evaluating opportunities
to acquire additional
portfolios of water related
technology
to commercialise.
Authors’ Note
Steve
Callister
is
Managing Director
at
Water Innovate
Ltd.
Visit
www.waterinnovate.co.uk
or
telephone 01234
756014
for
further
details.
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