Fast and accurate hydraulic design of baffled chlorine contact tanks (CCTs)
and service reservoirs is now possible with the help of new design software
known as DISINFEX. BHR Group has recently completed the development of
DISINFEX with partners Northern Ireland Water Service and Yorkshire Water.
CCTs are commonly used to provide the required contact time for chlorine
dosed upstream of their inlets. The size and internal geometry of CCTs are
critical in determining their efficiency. If contact times are too short,
microbiological failures may occur, if contact times are too long THM
formation will be promoted. THMs are potentially carcinogenic disinfection
by-products currently regulated at 100µg/l. New European regulations may
reduce the THM limit, to around 40µg/l.
CCTS are typically rectangular concrete chambers with single inlets and
outlets. The theoretical residence time (contact time), t, of the water in
the tank is simply the tank volume divided by the flow rate. If the water
moved through the CCT completely uniformly as a piston or plug (ideal plug
flow) every water molecule would remain in the tank for exactly the
theoretical residence time. However, in practice very significant
short-circuiting and dead zones occur due to non-ideal flow patterns. This
results in a residence time (contact time) distribution (RTD).
The internal geometry of CCTs frequently includes one or more horizontal
baffles to provide a serpentine flow path between inlet and outlet. Internal
baffling can reduce the extent of short circuiting and dead zones, providing
a RTD closer to ideal plug flow. Generally, the more horizontal baffles
installed the closer the RTD approaches ideal plug flow. The CCT inlet
design can also have a significant effect on the flow pattern and RTD.
Engineers designing CCTs need to compromise between volume, baffling and
inlet design. The most efficient CCTs are those with well designed inlets
and baffles resulting in the minimum volume (and hence cost) required to
achieve the desired contact time.
The minimum contact time in relation to an RTD is often defined as t10. This
is the time taken for ten per cent of a pulse of fluid injected at the inlet
to arrive at the outlet and corresponds to the first ten per cent of the are
under the RTD curve. The use of t10 is conservative as 90 per cent of the
fluid leaving the CCT has a greater contact time.
In practice, RTD curves can be determined by physical measurement or
computational techniques. Physical measurements can be carried out on
existing full scale CCTs or on scale models of existing or planned CCTs. A
tracer is injected as a pulse at the tank inlet and the tracer concentration
recorded against time at the outlet. Although tracer tests are accurate they
are very time consuming, especially when variations in interval geometry and
flow rate need to be evaluated. Several man-days are typically required for
RTD measurement on one CCT.
RTD predictions can also be made using three dimensional CFD simulations
which divide the CCT volume into a large number of cells. Once boundary
conditions are set, mass, energy and momentum equations are solved for each
cell throughout the tank. CFD simulations require specialised operator
skills and dedicated hardware and software. Again, several man-days of
effort per CCT is likely, making widespread use of CFD modelling expensive.
DISINFEX was developed to provide a quick and easy tool for water industry
users to assess baffled CCT and SR hydraulics. The software does not require
any in-depth training or fluid dynamic skills. The overall goal of the
software is to optimise the tank dimensions, number of baffles and inlet
arrangement (hence minimise capital cost) to achieve the desired contact
time and to have confidence that the chlorine residual and outlet THM levels
are within acceptable limits.
Developed using CFD modelling, DISINFEX is based on the concept of
constructing the overall tank RTD from two or more RTDs generated for
individual channels. DISINFEX supports a database of RTDs for inlet
channels, second channels, standard channels and outlet channels. For each
channel type RTDs are stored for different channel length to width (2-10)
and depth to width (1.5-0.275) rations. Six inlet types and five outlet
types (weirs, various orientation bellmouths, horizontal pipes) are covered.
Individual channel Œbuilding block’ RTDs are combined using a mathematical
procedure called convolution. The resulting RTD is then scaled to the
required flow rate between 1-100+ Ml/d.
Users enter the design characteristics, number of channels, flow rate,
required contact time in a physical data sheet. A RTD is then generated
showing the required contact time. A table containing specific time events
associated with the RTD can also be displayed. Two RTDs can be plotted
together for comparative purposes and RTD data can be exported to Excel
spreadsheets for further analysis.
Models for chlorine decay and THM formation which can be applied to
previously generated RTDs are also featured. The user enters a range of
inlet free chlorine concentrations and corresponding decay coefficients to
enable a curve showing inlet vs outlet chlorine concentration to be plotted.
THM levels can also be estimated following input of TOC, pH, UV absorption,
temperature and bromine concentration data. The resulting curves show the
range of chlorine doses required to achieve a minimum chlorine residual at
the outlet and to avoid exceeding the THM limit.
© Faversham House Ltd 2023 edie news articles may be copied or forwarded for individual use only. No other reproduction or distribution is permitted without prior written consent.
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