SECTION C -INFRASTRUCTURE & OPERATION Attachment C1: Operational Information Requirements - Outline Description of the Treatment Process at Kildalkey WWTP & Agglomeration - Drawing No. 5270-2888 - Drawing No. 5270-2889 For inspection purposes only. Consent of copyright owner required for any other use. EPA Export 26-07-2013:14:15:38
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SECTION C -INFRASTRUCTURE & OPERATION
Attachment C1: Operational Information Requirements
- Outline Description of the Treatment Process at Kildalkey WWTP & Agglomeration
- Drawing No. 5270-2888
- Drawing No. 5270-2889
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OUTLINE DESCRIPTION OF THE TREATMENT PROCESS FOR KILDALKEY WASTE
WATER TREATMENT PLANT AND AGGLOMERATION
1.0 EXISTING PLANT
Kildalkey Waste Water Treatment Plant (WWTP) is located east of Kildalkey Village. The
plant was commissioned in 2000, treating municipal waste water from the village, with a
design capacity of 900 P.E. The drainage network serving Kildalkey discharges by gravity to
the sewage treatment plant.
The treatment process currently comprises extended aeration (activated sludge) secondary
treatment and clarification, followed by a tertiary (reed bed) polishing process.
Treated effluent from the works is discharged to the adjacent stream, which is a tributary of
the Tremblestown River, via two 150mm diameter gravity outfall pipes.
The existing treatment works currently consists of the following units:-
• Inlet pump sump chamber with bypass facility (for excess stormwater to bypass
treatment process)
• 'Agisac' preliminary screening
• Grit removal
• Preliminary balance tank
• Aeration (glass-lined steel) tank
• Secondary clarifier (glass-lined steel tank)
• Sludge holding (glass-lined steel) tank
• Reed bed tertiary treatment system
• Gravity outfall to the stream
• Offlce / Control building
Inlet to Works
Untreated waste water from Kildalkey Agglomeration enters the inlet lift pumping station via a
225mm diameter sewer. The pumping station consists of an underground holding
chamber/sump and is equipped with 2 Nr. submersible wet well pumps. Untreated
wastewater is then lifted to preliminary treatment, with continuous flow monitoring occurring at
Ihis stage of the works.
The inlet lift chamber is also equipped with an emergency storm water overfiow facility, such
that in extreme weather events stormwater can by-pass the treatment process and fiow
directly to the receiving waters, thus preventing inundation of the works. Excess stormwater
by-passing the works flows in a 225mm diameter pipe to the stormwater overfiow point
(SW3), terminating at the stream tributary of Tremblestown River.
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Inlet Works (Preliminary Treatment)
Preliminary treatment entails the removal of plastics, rags, grit, silt and sand from the waste
stream. Screening facilities are provided for solids removal of inorganic materials via an
'Agisac' fine screen. This screen is designed to produce washed screenings down to a
particle size of 3mm, with delivery to a nearby skip. Grit removal of the incoming screened
sewage is provided via a grit trap I classifier. The collected grit is also discharged to the
adjacent skip.
Screened sewage flows forward to an underground balance tank (capacity 32m' approx.).
The balance tank ensures that homogenous sewage is fed to the process plant. Following a
short retention time in the balance tank, partially treated waste water is then pumped (via two
submersible forward feed pumps) in a 100mm diameter rising main to the aeration unit.
Secondary Treatment
Extended aeration of the partially treated waste water is provided via a glass lined steel
aeration tank. Dissolved oxygen is supplied via a fine bubble diffusion system attached to the
base of the tank. Air is supplied to the diffusion system by means of a 7.5kW rated blower.
Dissolved oxygen is monitored continuously from a probe connected to the aeration tank,
which is linked to SCADA.
The activated sludge reactor has been constructed to the following approximate dimensions:
- diameter: gAm,
- overall depth: 4.0m
- freeboard: O.15m
- capacity: 267m'
Aerated waste water overflows a weir and is then diverted to the secondary clarifier. The
secondary clarifier comprises a glass-lined steel tank with the following approximate
dimensions:
- diameter: 5.1m,
- overall depth: 3.3m
- freeboard: O.8m
- capacity: 51 m'
The biomass generated in the aeration process tends to readily settle out during the
clarification stage. The secondary sludge collected in the clarifier is returned to the balancing
tank via the sludge return pump chamber (Return Activated Sludge line - RAS). A smaller
amount of this secondary sludge is 'wasted' and is pumped to the sludge holding tank via the
surplus sludge pump chamber (Waste Activated Sludge line - WAS).
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Currently a split-flow operation is in place at the plant, whereby treated effluent discharge, on
exiting the clarification stage, is split, with a proportion of this treated effluent discharging
directly to the receiving waters (refer to Secondary Discharge Point SW2) and the remainder
flowing forward to receive tertiary treatment in the on-site reed bed system.
Tertiary Treatment and Treated Effluent Outfall
As stated above, a portion of treated effluent also receives tertiary treatment. Effluent exiting
the secondary clarifier flows by gravity in a 150mm diameter pipe to the tertiary treatment
chambers, where it is distributed to the reed beds.
The effluent is distributed through the substrate layers of reed beds (6 nr. reed bed units on
site). The overflow from the reed beds is collected in an outflow chamber and then
discharged by gravity in 150mm diameter pipe to the adjacent stream (primary discharge
point SW1). Discharge of treated effluent is through a simple open-ended pipeline,
terminating directly over the stream, above the water level.
Sludge Handling
Settled sludge is drawn from the clarifier base via the surplus sludge pump chamber and sent
forward for temporary storage in the (glass-lined steel) sludge holding tank. As discussed
above, return activated sludge (RAS) is pumped back to the balancing tank via the sludge
return pump chamber. Waste sludge is pumped to the sludge holding tank at a rate, which is
determined by the MLSS concentration in the aeration unit. The sludge holding tank has a
capacity of approximately 34m3.
Sludge is allowed to settle in this tank and the resulting supernatant is siphoned back to the
balance tank. The sludge holding tank is emptied monthly (approximately) by tanker with the
thickened sludge being transported to the Navan Waste Water Treatment Plant for
dewatering.
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SW3 STORMWATER OVERFLOW
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J:IProjecls\5270pp Meath Discharge Licence ApplicalionsID6-Drawings\02·TOBIN DrawingsIKHdalkey\5270·2888.dwg, 2888, 1710612009 17:14:22. ray kelly
SW2 SECONDARY DISCHARGE POINT (BY-PASSING REED BEDS)
SW1 PRIMARY DISCHARGE POINT ( PASSING THROUGH REED BEDS)
o Ordnance Survey Ireland. All rights reserved. Licence number 2008/10CeMA' Meath Local Authorities
Q
NOTES
WWTPSITE BOUNDARY
PRIMARY DISCHARGE
SECONDARY DISCHARGE
STORMWATER OVERFLOW
I . FIGURED DIMENSIONS ONLY TO BE TAKEN FROM nilS DRAWING
2. ALL DRAWINGS TO BE CHECKEO BY THE CONTRACTOR ON SITE
3. ENGINEER TO BE INFORMED BY THE CONTRACTOR OF ANY DISCREPANCIES BEFORE ANY WORK COMMENCES
4. ALL LEVELS SHOWN RELATE TO ORDNANCE SURVEY DATUM AT MALIN HEAD