For inspection purposes only.Westfalia UCD-345 1 500 l/hr Ultromat 2 Duty/Standby oto 1000 l/hr Seepex or equal. 2 4 m3/hr 304 Stainless Steel For inspection purposes only. Consent

ATTACHMENT C1

.w Ross \/IMITP ProcessDrawing Number NR 11- Quay Pumping Station PlanDrawing Number NR 12- Quay Pumping Station SectionDrawing Number NR 13- Rosbercon Pumping Station- Location & PlanDrawing Number NR 14- Rosbercon Pumping Station- Section A-ADrawing Number NR 15- Rosbercon Pumping Station- Section C-CDrawing Number NR 16- Rosbercon Pumping Station- Section B-BDrawing Number NR 17 - Bawnmore Terrace Pumping Station-Location PlanDrawing Number NR 18 - Bawnmore Terrace Pumping Station-Section A-ADrawing Number NR 19 - Bawnmore Terrace Pumping Station-Section B-B & Section C-C

WWDL_ApplicationForm V65.doc ANNEX - Standard Forms

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WEXFORDCOUNTYCOUNCIL

NEW ROSSWastewater Treatment Works

Design, Build, Operate Contract

PRELIMINARY TREATMENTFlow from the Quay Pumpstaion discharges into a common channel. The flow may then enter the grittank via one of two screens . The screens operate on a duty / assist basis. Actuated penstocks divert theflow to the duty screen. Moving belt screens are proposed to remove gross solids ( greater than 6 mmdiameter ) from the effluent. Screenings are washed and compacted within the screen by an integralcompactor. The screenings are compacted and discharged to a skip. The flow passes through thescreens and enters the grit tank. Here the grit in the flow settles and is collected using an air lift pumparrangement. It is transferred to a grit classifier where any organics are separated and returned to theflow, with the screenings supernatant. A bypass, with a hand raked screen, has been included to allowflow to be diverted around the grit trap to facilitate maintenance etc . The inlet works had been sized asper specification to deal with Phase 2 flows of315Us.

Fine Screens:

Number .Operation .Capacity .Make .Type .Screen Aperture .Material .

Screening Handling:

Number .Capacity .Make .Type .Material .

Grit Tank:

Number .Capacity .

Grit Classifier:

Number .Manufacturer .Type .Material .

Grit Air Blowers:

Number .Operation .Make .Type ..Duty .

2Duty/Assist157.5 UsJones & AttwoodHiFlow6mmStainless Steel

22.4 mvhr wet screeningsJones & AttwoodIntegral CompactorStainless Steel

1315 Us

IJones & Attwood.Bache ClassifierMild Steel

2Duty/StandbyHick HargreavesRootes0.42 m3/min @ 1496 mbar

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INTERSTAGE PUMPSTATIONThe flow overflows directly from the combined inlet works into the flow to treatment wet well of theinterstage pumpstation. From here the flows are pumped directly to the SBR flow split chamber . Understorm conditions the level in the wet well rises and overflows a concrete baffle wall into the storm wetwell of the interstage pumpstation and the storm flow is pumped to the storm tank. The interstagepumpstation and pumps have been sized to deal with Phase 2 flows.

Interstage Foul Pumps:

Number .Operation .Make .Type .Installation .Duty .VSD's ..

Interstage Storm Pumps:

Number .Operation .Make .Type .Installation .Duty .

3DutylDuty/StandbyABS, Flygt or equalSubmersibleWet Well82.5 Us @ Sm TDHYes.

2Duty/StandbyABS , Flygt or equalSubmersibleWet Well100 Us @4m TDH

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A CTIVATED SLUDGE TREATMENTThe activated sludge treatment system proposed is based on the use of sequencing batch reactors. It isproposed to provide 2 SBR with the possibility of adding additional units in the future to cater forincreased flows or nutrient removal. Flow to the SBR is distributed in a concrete flow sp lit chamberconstructed alongsid e the SBR. The flow split chamber has been constructed to take into account Phas e2 flows .

Flow to the SBR enters via an actuated weir penstock to a pre-react zone where it overflows andunderflows a number of barnes into a second pre-react zone before flowin g through a number of portsin a dividing concrete wall into the main aeration zone. A full process description for the CASS processcan be found at the end of this section. Both these zones and the main basin are aerated using fmebubble membrane diffusers. Two air blowers will be provided operating on a duty/standby basis .

A single decanter will be provided for each basin. The decant period control will be on a time basis .There are two decant period times , 1 hour during the standard 4 hour cycle and 45 minutes during theshorter 3 hour storm cycle . At the end of the cycle the decanter is driven to a park position above topwater level, where it operates as an emergency overflow.

Surplus sludge will be wasted using a duty submersible pump in each basin. Surplus sludge will bepumped to the picket fence thickener.

Activated Sludge Process:

Type ..Supplier .No. of Tanks ..Tank length .Tank width .Tank depth .

FBDA System:

Make .Diffuser type .No. of diffusers ..

Air Blowers:

Number .Operation .Type .Duty .Make ..Variable Speed Drives .

Return Activated Sludge:

Number ..Operation .Duty .Make ..Type ..Installation .Variable Speed Drives .

Sequencing Batch ReactorEarth Tech CASS224.5 m8m6.5 m

EDI or equalMiniPanel32 per basin

2Duty/StandbyRootes Type1434 m3/hr @ 650 mbarAerzen or equalYes

2Duty/Duty6.0 lis @ 6.0m TDHABS , Flygt or equal.Submersible CentrifugalWet WellNo

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Waste Activated Sludge Pumps:

Number .Operation .Duty ..Make .Type ..lnstallation ..Variable Speed Drives .

2DutylDuty1O.81/s @ 6.0m TDHASS, Flygt or equalSubmersible CentrifugalWet WellNo

NUTRIENT REMOVALIn accordance with the specification requirements the current system design does not incorporatenutrient removal. If required in the future the operating sequence of the SSR could be modified toprovide nitrification / denitrification. Phosphorous removal could be provided biologically and bydosing Ferric Sulphate.

UV DISINFECTIONProvision has been made hydraulically for the future installation of a UV Plant, as specified.

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STORMWATER IlANDLINGAs stated abo ve flows in exc ess of 110 lis ( 16511s - Phase 2) are diverted to the storm tank . A singlestorm tank is proposed with a tipping bucket system provided for tank cleaning. Duty / standbysubmersible pumps will be provided which will allow the storm tank to be emptied after a storm and thecontents gradually returned to the flow distribution chamber, upstream of the SBR, for furthertreatment.

Storm Tank:Number .Length .Width .Depth .Volume .

Storm Tank TippingBucket:Make .Number .Size ..Material ..

Storm Return Pumps:Number .Operation .Duty .Make .Type .Installation .Variable Speed Drives ..

I24.5 m8m5.5 m1080 rrr'

CSO Technik or equal1500 11m304 SS

2Duty/Standby /108 mvhr @ 4.5 m TDHABS , Flygt or equal.Submersible CentrifugalWet WellNo

t , . .....l _ , . ,_!'f ~ i " :'I : ' ;

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WASTE A CTIVATED SLUDGE THICKENINGWaste activated sludge thickening will be achieved using a Picket Fence Thickener. Anticipated feedsolids concentration is 0.8 %. SAS sludge from the SBR basin is pumped directly to the picket fencethickener. Final solids concentration from the picket fence thickener is approximately 3%.

Thickened sludge is transferred from the Picket Fence Thickener to the Sludge Blending Tank usingprogressive cavity pumps.

Waste Activated Sludge Thickener:No .Type .Diameter .Tank Type .

Thickened WAS Pumps:Number .Operation .Duty ..Type .Make .Variable Speed Drive ..

2 dutyPicket Fence Thickener5.0m.Reinforced Concrete

2Westfalia3 mlfhr @ 2 bar gProgressive CavityMono , Seepex or equal.Yes

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Design, Build. Operate Contract

IMPORTED SLUDGEProvision has been made to receive liquid sludge in accordance with the specification requirement.Liquid sludge is fed directly to the sludge screen via a bauer coupling. The flow is monitored using anelectromagnetic flowmeter before the screen. This provides for the screening of the imported sludgefollowed by discharge to the sludge blending tank. Screenings from the screen are compacted anddischarged to a storage skip. A dry installed submersible pump is provided to pump the sludge from thescreen to the sludge blending tank.

Imported Sludge Screen:

Number .Operation .Capacity .Make .Type .Screen Spacing ..Material .

Imported Sludge Pump:

Number .Operation .Duty .Make .Type .Installation .Variable Speed Drives ..

1Duty16 lisJones & AttwoodSludgepactor SLP 21005mm304 Stainless Steel

1Duty16 lis @ 3m TDHABS, Flygt or equalSubmersible CentrifugalDry WellNo

E A R

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SLUDGE BLENDINGTwo sludge blending tanks will be provided. Imported and thickened waste activated sludge iscombined in these tanks to provide a consistent feed to the dewatering plant. The tank is provided witha concrete roof and a submersible mixer is provided to keep the contents mixed. The tank also providesstorage capacity in the event of the dewatering plant being out of service. The blending tank has beensized to incorporate 3 days of maximum imported sludge storage as per the specification. Blendedsludge is pumped directly to the centrifuges via a set of progressive cavity pumps.

Sludge Blending Tank:

Number .Length ..Width .Depth .Storage Volume ..

Sludge Blending Mixer.

Number .Operation .Make .Type .

Decanter Feed Pumps:Number .Operation .Duty .Type .Make .Variable Speed Drive .

2lO.Om5.0m2.0m200 m)

2DutylDutyABS, Flygt or equalSubmersible Mixer

2Duty/Standby5 - 15 mvhr @ 2 bar gProgressive CavityMono, Seepex or equal.Yes

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SLUDGE DEWATERINGSludge dewatering will be carried out using a decanter. Sludge would be pumped directly from thepicket fence thickeners to the centrifuge. Anticipated feed solids concentration is 3%. The decanter willachieve final solids concentration of 18 %. A poly preparations system and poly dosing pumps wouldbe provided for use with the centrifuge. The sludge cake would be transferred to the skip using a screwconveyor.

Centrifuge:Number .Operation ..Solids Loading .Hydraulic Loading .Make .Model .

Polyelectrolyte Preparation Unit:Number .Capacity .Make .

Polyelectrolyte Dosing Pumps:Number .Operation .Duty .Make .

Sludge Conveyor:Number .Capacity .Material .

2Duty/Standb y450 kg/hr12 mvhr @ 3%DSWestfaliaUCD-345

1500 l/hrUltromat

2Duty/Standbyoto 1000 l/hrSeepex or equal.

24 m3/hr304 Stainless Steel

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CASSTM PROCESS DESCRIPTION

CASS ™ (Cyclic Activated Sludge System)u.s. Patents 4663044 , 4693821, 4891128, 5013441 and Canad ian Patent 524910

BRIEF HISTORY OF SEQUENCING BATCH REACTORSActivated sludge is the most widely used biological wastewater treatment process in thedeveloped world, treating both sewage and a variety of industrial wastewater. Batch operation ofthe activated sludge process is nothing new. During the early development of the activatedsludge process in the United Kingdom by Ardern and Lockett around 1914, plants were operatedusing fill-and-draw or batch feed methods. These researchers firmly established the concept ofoperating a single reactor basin using repetitive cycles of aeration, settlement and discharge oftreated effluent. Around 1956, during the development of oxidation ditch technology, Pasveerincorporated interrupted and cont inuously fed batch treatment principles. Further advancementsto the oxidation ditch fed-batch treatment then took place by incorporating a rectangular basinconfiguration. By the late 1970s, the sequencing batch reactor (SBR) was well established andmany small plants were in operation. A major development took place in 1978 with theincorporation of a pre-react selector zone within the SBR to control filamentous sludge bulking .Further refinements of SBR processes took place mainly in Australia and the United States andhas led to the wide scale application of the technology worldwide. The shortfalls of the originaldesign have led to the present state-of-the-art CASS ™ Sequencing Batch Reactor . While SBRshave generally been classified by the water industry for small or medium scale app,lications,CASS TMhas found applicat ion in large scale municipalities (50 MGD 1200,000 mid or 400,000+population equivalent) and the modular expans ion, retrofit or upgrading of existing wastewatertreatment facilities .

Yannawa Multi-Storey CASS TM SBR WWTP, Thailand

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CASS ™ PROCESS COMPONENTSThe CASSTMSBR is a combination of a biological selector and variable volume process reactor.The process operates with a single sludge in a single reactor basin to accomplish both biologicaltreatment and solids-liquid separation. CASS ™ is by design and operation with municipalwastewaters, a biological nutr ient removal process, configured to function with filamentous sludgebulking control. A simple repeated sequence of aeration and non-aeration is used to provideaerobic, anoxic and anaerobic process conditions, which in combination with the aerationintensity , favor nitrification, denitrification and biological phosphorus removal.The essent ial features of the CASS ™ SBR are the plug-flow initial reaction conditions andcomplete-mix reactor basin. Each CASS ™ reactor basin is divided by baffle walls into threesections (Zone 1: Selector, Zone 2: Secondary Aeration, Zone 3: Main Aeration). For typicaldomestic wastewater treatment applications, these sections are in the approximate proportions of5%, 10%, and 85%. Sludge biomass is continuously recycled from Zone 3 to the Zone 1 selectorto remove the readily degradable soluble substrate and favor the growth of the floc-formingmicroorganisms. System design is such that the sludge return rate causes an approximate dailycycling of biomass in the main aeration zone through the selector zone. The mechanisms of Zone1 and the internal sludge recycle elim inate the requirement for separate fill- ratio selectiv ity,anoxic, and anaerobic mixing periods. The selector is self-regulating for any load condition andoperates under anoxic condit ions during aerobic periods and anaerobic reaction conditions duringnon-aerated periods. Polishing denitrification and enzymatic transfer of available substrate duringenhanced biological phosphorus removal is also achieved in the selector zone . The complete-m ixnature of the main reactor provides flow and load balancing and a tolerance to shock or toxicloading, and the process prevents solids washout during peak or wet weather hydraulic surges.

.. ~;~~)~.Typical Two Basin CASS™ SBR Layout

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PROCESS CYCLE OPERATIONCASS TMutilizes a simple repeated time-based sequence, which incorporates:

• FILL - AERATION (for biological reactions)• FILL - SETTLE (for solids-liqu id separation)• DECANT (to remove treated effluent)

Completion of these three operations in the sequence described above constitute a cycle which isthen repeated . The sequence above can also include a FILL, FILL - MIX, FILL - REACT, andREACT if required.

During the period of a cycle, the liquid level inside the reactor basin rises from a set bottom waterlevel in response to a varying influent wastewater flow rate. Aeration ceases at a predeterm inedperiod of the cycle to allow the biomass to flocculate and settle under quiescent conditions. Aftera specific settling period, the treated effluent supernatant is removed (decanted), using a movingweir decanter. This operation returns the liquid level in the reactor basin to the bottom water level.Surplus solids are wasted as required to maintain the biomass MLSS at the required level. Solidswasting after settling enables waste sludge concentrations in excess of 10,000 mg/L to beremoved .

FILL - AERATIONThe FILL - AERATION (react) operation refers to the air-on time of the process cycle. During thisperiod, influent is received into the basin through the selector zone where it contacts with thesludge biomass recycled from the main aeration zone.Complete-mix reaction conditions occur in Zone 3 during this variable volume operational period.

FILL - SETTLEThis refers to the first part of the air-off time period when quiescent settling cond itions are createdin Zone 3 for solids-liqu id separation . The activated sludge solids form a sludge-level interface ,which progressively falls , towards the floor of the basin. The floes adhere together and the masssettles as a blanket leaving a clear supernatant.At the end of the aeration period, the sludge is at a uniform concentration . During the initialsettling period, the sludge undergoes internal flocculation due to the residual mixing energy withinthe basin. As this energy dissipates the sludge interface forms and settles as a blanket. Densesolids fall through the formed mass to settle on the basin floor. There is an initial slow settling

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velocity , which increases and then gradually falls off due to the compressive accumulation ofsolids on the basin floor. Zone settling velocity is a function of the initial solids concentration,basin depth , total area of the basin and nature of the biological solids. A top water level solidsconcentration of 3,500 mg/L will typically settle to form a layer of sludge having a meanconcentration of approximately 10,000 mg/L.GASS™ SBR facilities are sized and configured to operate with inflow into the basin during thesettle phase of cycle. Biomass is returned from the main aeration zone to the selector zone topromote selectiv ity and create anoxic/anaerobic conditions .

DECANT (EFFLUENT REMOVAL)Inflow to the GASS™ basin undergoing decanting(effluent withdrawal) is interrupted and directed to analternate basin in a multi-basin facility or stored in apump well in a single basin facility. The weir trough ofthe decanter is situated above top water level for bothaeration and settling phases to prevent the accidentaldischarge of mixed liquor suspended solids . Whenoperated during the decant phase of the cycle , thedecanter travels down at an initial fast speed .Interaction with the liquid level is detected by a levelindicator float switch which then causes the decanterto proceed at its design rate of travel producing aconstant rate of discharge of treated effluent from thebasin. On reach ing designated bottom water level, thedecanter is reversed to travel back to its rest positionat the initial fast speed.

IDLEIn practice, decanting will always be less than the allocated time available. This residual time isdesignated as IDLE and can be used as a period of inflow without aeration or reaction. The IDLEsequence beg ins 4 minutes after the decanter has traveled in the reverse up direct ion andfinishes at the end of the designated decant period . Biomass is recycled from Zone 3 to theselector zone to promote selectivity and create anoxic/anaerobic conditions .

RESPIRATION RATE CONTROL (RRCTM)Dissolved oxygen is a necessary requirement for the biological oxidation reactions, which takeplace with the CAS3™ SBR process. Residual dissolved oxygen occurs as a result of oxygen ,which is not used by the microorganisms in the biomass. Too much dissolved oxygen in theCASS ™ process is wasteful of energy and may inhibit biological nutrient removal mechanisms. Asimple control method to ensure optimum biological reaction conditions take place and valuableenergy is not wasted . Advantage is taken of the fact that the GASS™ SBR conforms to acomplete-mix reaction model. This also means that GASS™ provides a very stable reactionenvironment when compared to other conventional plug-flow activated sludge , extended aeration ,contact stab ilization, or sequencing batch reactor systems. A dissolved oxygen sensor is used tomeasure changes in biomass oxygen demand. For example , a reduction in the oxygen loaddemand to a CASS™ basin will automatically cause a lowering of the aeration intensity (airsupply) so that excessive dissolved oxygen concentrations are prevented.

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Conversely, an increase in load demand will cause an increase in aeration intensity so that themetabolic activity of the biomass, as registered by its propensity to use oxygen, is matched withthe corresponding aeration intensity rate of air feed into the reaction basin.RRCTM directly interacts with the best sensor, which is available for the control of air into theprocess . The system is an in-basin respirometer. Simply stated, low oxygen demand caused bylow loadings through diurnal, or other variations can now be directly matched to energy use. Thebiomass senses the oxygen requirements , which are needed for the process. The dissolvedoxygen sensor interprets that message and causes interaction with the rate of introduction of airinto the reaction basin.The CASS TMRRCTM is simple and direct. RRCTM has direct benefits:

• Saves operating energy costs.• Reduction of waste activated sludge.• Improved nutrient removal performance.

SUPERVISORY CONTROL AND DATA ACQUISITION· (S.C.A.D .A.)S.C.A.D.A. will allow the treatment plant operating personnel to monitor, print and log daily eventswhich occur within the wastewater treatment process funct ions, as well as the Automated ControlOperat ing functions. This feature allows the operating personnel to randomly extract current andpast data information pertinent to the system functionality. The system will graphically display allaspects of the Process Control Equipment and the operating parameters , including set points .Several screen selections including process flow diagrams will enable the operating personnel toview the plant System Monitoring .The S.C.A.D .A. feature also allows the process equipment supplier, contractor, engineer or ownerto remotely mon itor, edit, and trouble shoot and repair, if necessary , most aspects of thefunctionality of the Process Control Center.

•..- .. _A350,000 PE CAS Sw SBR Facility in China

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EPA Export 26-07-2013:17:02:36

STORM

DATE

91600mm RISING MAINTO WASTEWATERTREATMENT PLANT-.

AYENDMENT DETAlIS

STORM

HIGH LEVEL PLAN

STORM PUMPCHAMBER

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NO PART OF THIS DOCUMENT MAY BE RE-PRODUCEO OR TRANSMITTED IN ANY FORM DR STORED IN ANY RETRIEVALSYSTEM OF ANY NATURE WITHOUT THE WRITTEN PERMISSION OF THE CONSULTING ENGINEER AS COPYRIGHTHOLDEREXCEPTAS AGREEDFOR USE ON THE PROJECTFORWHICH THE DOCUMENTWASaRlGINALLY ISSUED.

T.J.O'CONNOR & ASSOCIATESCONSULTING ENGINEERS

CORRIG BOUSE. CORRIG ROAD, SANDYFORD, DUBUN 18.Tel: 295 2321 Fax: 295 4541

'RoBeT:NEW ROSS EPA DISCHARGE LICENSE APPLICATION

WEXFORD COUNTY COUNCIL

e ATTACHMENT C.1

SCALE: 1:100

QUAY PUMPING STATION PLANJOB NO: I DRAWING NO:

DATE:oor09 I DRAWN BY: JH 2778 NR11

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EPA Export 26-07-2013:17:02:36

te

GROUND LEVEL,

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AMENDMENT DETAJIS DATE

NO PARTOF THISDOCUMENTMAY BE RE..pROOUCED ORTRANSMITTEDINANY FORMOR STOREDINANY RETRIEVALSYSTEMOF ANY NATUREWITHOUT THE WRITTENPERMISSIONOFTHECONSULTING ENGINEERASCOPYRIGHTHOLDEREXCEPTAS AGREEDFOR USE ON THE PROJECTFORWHICHTHE DOCUMENTWAS ORIGINALl.Y ISSUED.


CORRIG BOUSE. CORRIG ROAD. SANDYFORD. DUBLIN 18.Tel: 295 2321 Fill[: 295 4541

,aCT:NEW ROSS EPA DISCHARGE LICENSE APPLICATION

WEXFORD COUN1Y COUNCIL

e ATTACHMENT C.1

SCALE: 1:100

QUAY PUMPING STATION SECTIONJOB NO: I DRAWING NO:

DATE:ocrOl I DRAWN BY: JH 2778 NR12

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EPA Export 26-07-2013:17:02:36

DATE

NR13

DRAlJING NO:

N

2778

JOB NO:

AMENDMENT DETAlIS

~.~-_._--

NEW ROSS EPA DISCHARGE LICENCE APPLICATION

T.J.O'CONNOR Be ASSOCIATESCONSULTING ENGINEERS

CORRIG BOUSE, CORRIG ROAD, SANDYFORD, DUBIJN 18.Tel: 295 2321 Fax: 295 4541

'ROJiCT:

SCALE: 1:50; 1: 1000 (» A3

DATE:__.. IDRAWN BY: D.D

ATTACHMENT Cl-ROSBERCON PUMPING STATION-LOCATION AND PlAN

WEXFORD COUNlY COUNCIL

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EPA Export 26-07-2013:17:02:37

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AMENDMENT DETAIlS DATE

NOPARTOF THISDOCUMENTMAYBE RE-PRODUCEO OR TRANSMITTEDN AN( FORMOR STOREDINMY RETRIEVALSYSTEMOF MY NATUREWITHOUTTHE WRITTEN PERMISSIONOf THE CONSUl.TlNGENGWEERASCOPYRIGHTHOLDEREXCEPTAS AGREEDFORUSEONTHEPROJECTFORWHICHTHEDOCUMENTWASORIGINALLY ISSUED.


CORRIG HOUSE. CORRIG ROAD. SANDYFORD. DUBLIN lB.

Tel: 295 2321 Fax: 295 4541

,&a:NEW ROSS EPA DISCHARGE LICENSE APPLICATION


WWTP OUTFALL SECTIONe ATIACHMENT C.2

SCALE: N.T.S. JOB NO: DRAWING NO:

DATE:llCT"OIl I DRAWN BY: JH 2778 NR21

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EPA Export 26-07-2013:17:02:37

ATTACHMENT E2

Drawing Number NR23- Location of Monitoring &Sampling PointsDrawing Number NR24- Location of Monitoring &Sampling Points

WWDL_ApplicationForm V65.doc ANNEX- Standard Forms

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EPA Export 26-07-2013:17:02:37

~\'o'IIl'- ,00,-,-0- ..-----

aSW1d~~(STROKESTOWN POINT

i SAMPLING POINT)QjE: 270076

N: 124443

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NO PARTOF T'HISDOCUMENTMAYBE RE-PRODUCEDORTRANSMITTEDIN ANY FORM ORSTOREDIN ANY RETRIEVALSYSTEM OF ANY NATUREWITHOUTTHE WRITTEN PERMISSIONOFTHE CONSULTINGENGINEERASCOPYRIGHTHOlDER EXCEPTAS AGREEOFORUSEON THE PROJECTFORWHICHTHE OOCUMENTWASORtGiNALLY ISSUED.

T.J.O'CONNOR & ASSOCIATESCONSULTING ENGUNEERS

CORRIG ROUSE. CORRIG ROAD. SANDYFOBD. DUBLIN 18.

Tel: 29S 2321 Po:: 295 4114.1iOJiCT:

NEW ROSS EPA DISCHARGE LICENSE APPLICATION


NR232778

1:10000

ATTACHMENT E.2 - LOCATION OF MONITORING &: SAMPUNG POINTS

i lOB NO: i DRAWING NO:SCALI::

DATI::_'OI I DRAWN BY: J H

MAP REPRODUCED BY PERMISSION OFORDNANCE SURVEY IRELAND

(WEXFORD CCMA 9802)

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EPA Export 26-07-2013:17:02:37

DATE

NR222778

lOB NO: I DRA1JING NO:

- LOCATION OF MONITORING POINTS


AJlENDMEl'lT DETAWI

MAP REPRODUCED BY PERMISSION OFORDNANCE SURVEY IRELAND

(WEXFORD CCMA 9802)

N

NEW ROSS EPA DISCHARGE LICENSE APPLICATION


CORRIG HOUSE. CORRIG ROAD. SANDYFORD. DUBLIN 18.Tel: 295 2321 Fu:: 295 .54.1

MJEM:

SCALE: 1:1000

NO PART OF THIS DOCUMENT MAY BE RE-PROOUCEO OR TRANSMrrTeO IN ANY FORM OR STORED IN ANY RETRIEVALSYSTEM OF ANY NATURE WlTHOUTTHE WRITTEN PERMISSION Of THE CONSULTING ENGINEER AS COPYRIGHTHOLDER eXCEPT AS AGREED FOR USE ON THE PROJECT FOR INHICH THE DOCUMENT WAS ORIGINALLY ISSUED

DATE:_.... I DRAWN BY: J H

SW1PRIMARY DISCHARGEMONITORING LOCATIONE:270819N: 125972

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PROPOSED PRIMARYDISCHARGE POINT

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EPA Export 26-07-2013:17:02:37

WWDL_ApplicationForm V65.doc

TABLE 02

Tabular data on Discharge points

ANNEX- Standard Forms

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EPA Export 26-07-2013:17:02:37

e e e ePT CD PT TYPE LA NAME RWB TYPE RWB NAME DESIGNATION EASTING NORTHING VERIFIED

SW1 Primary Discharge Wexford County Council Kilkenn River (Tidal) River Barrow SAC 270724 126016 NoCountv Council

SW2 Secondary Discharge Wexford County Council Kilkenn River (Tidal) River Barrow SAC 270831 125927 NoCountv Council

SW3 Secondary Discharge Wexford County Council Kilkenn River (Tidal) River Barrow SAC 271731 127787 NoCountv Council

SW4 Secondary Discharge Wexford County Council Kilkenn River Unnamed SAC 273491 128072 NoCountv Council

SW5 Storm water overflow Wexford County Council Kilkenny River (Tidal) River Barrow SAC 271519 127226 NoCountv Council

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EPA Export 26-07-2013:17:02:37

WWDL_ApplicatianFarm V65.dac

TABLE E3

Record of each Monitoring Point

ANNEX - Standard Farms

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EPA Export 26-07-2013:17:02:37

e e e e

PT CD PT TYPE MaN TYPE EASTING NORTHING VERIFIEDSW1 (rn) primary (effluent) M&S 270819 125972 noaSW1u All river) S 271720 121656 noaSW1d All river) S 270076 124443 no

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EPA Export 26-07-2013:17:02:37

---------------_ ... -

WWDL _ApplicationForm V65.doc

TABLES 01

ANNEX - Standard Forms

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EPA Export 26-07-2013:17:02:37

WWD Licence Application Annex I

e Table D.1(i)(a): EMISSIONS TO SURFACE/GROUND WATERS (Primary Discharge Point)

Discharge Point Code: SW-1

Local Authority Ref No:Source of Emission: treated effluentLocation: outfall adiacent to WWTPGrid Ref (12 diaits 6E 6N) 270724 / 126016Name of Receivina waters: River BarrowWater Body: Transitional BodyRiver Basin District South Eastern RBDDesianation of Receivina Waters: SACFlow Rate in Receiving Waters: 9 rrr.sec' Dry Weather Flow

om3.sec·1 95% Weather FlowAdditional Comments (e.g. The contruction of the New Ross WWTP is currently incommentary on zero flow or other the commissioning phase. Flow data will be availableinformation deemed of value) shortly. Where data is unknown a zero figure has been

inserted.

Emission Details:

I(j) Volume emittedNormal/dav 2880 m3 Maximum/day 8640 rn'Maximum om3 Period of emission 60 min/hr 24 hr/day 365 day/yrrate/hour I(avo)Drv Weather Flow om3/sec

WWD Licence Application - New Ross Town & Environs - Page: 2

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EPA Export 26-07-2013:17:02:37


e Table D.1(ii)(a): EMISSIONS TO SURFACE/GROUND WATERS (Secondary Discharge Point)


Local Authoritv Ref No:Source of Emission: storm water overflow at WWTPLocation: WWTP outfall pipeGrid Ref (12 dlqlts 6E 6N) 270831 / 125927Name of Receivinq waters: River BarrowWater Body: Transitional BodyRiver Basin District South Eastern RBDDesianation of Receivina Waters: SACFlow Rate in Receiving Waters: 9 rrr.sec-' Dry Weather Flow

o m3.sec·1 95% Weather FlowAdditional Comments (e.g. The construction of the New Ross WWTP is currently incommentary on zero flow or other the commissioning phase. Flow data for overflow to theinformation deemed of value) river via storm overflow will be available shortly.

Emission Details:

(i) Volume emittedNormal/dav om3 Maximum/dav om3

Maximum om3 Period of emission omin/hr ohr/day oday/yrrate/hour lravc)Dry Weather Flow om3/sec


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EPA Export 26-07-2013:17:02:37


e Table D.1(ii)(a): EMISSIONS TO SURFACE/GROUND WATERS (Secondary Discharge Point)


Local Authority Ref No:Source of Emission: Erneruencv overflow from PSLocation: stream at MaudlinsGrid Ref (12 diaits, 6E 6N) 271731/127787Name of Receivina waters: UnknownWater Body: Transitional BodyRiver Basin District South Eastern RBDDesianation of Receivina Waters: SACFlow Rate in Receiving Waters: 9 m3.sec·1 Dry Weather Flow

o m3.sec·1 95% Weather FlowAdditional Comments (e.g. No data is available on the quantity or quality of thecommentary on zero flow or other emergency overflow from Bawnmore PS. A zero figure isinformation deemed of value) inputed where data is unknown

Emission Details:

I(i) Volume emittedNormal/dav om3 Maximum/day om3

Maximum om3 Period of emission omin/hr ohr/day oday/yrrate/hour I(avo)Drv Weather Flow om3/sec

WWD Licence Application - New Ross Town &Environs - Page: 8

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EPA Export 26-07-2013:17:02:37


e Table 0.1 (ii)(a): EMISSIONS TO SURFACE/GROUND WATERS (Secondary Discharge Point)


Local Authoritv Ref No:Source of Emission: Ernerqencv overflow from PSLocation: Rosbercon New RossGrid Ref (12 diqits 6E 6N) 273491 / 128072Name of Receivinq waters: unknownWater Bodv: River Water BodyRiver Basin District South Eastern RBDDesianation of Receivinq Waters: SACFlow Rate in Receiving Waters: 9 m3.sec·1 Dry Weather Flow

o rn-.sec' 95% Weather FlowAdditional Comments (e.g. No data is available on the quality or quantity of thecommentary on zero flow or other emergncy overflow from Rosbercon PS. A zero figure isinformation deemed of value) inserted where data is unknown

Emission Details:

1m Volume emittedNormal/dav om3 Maximum/day om3

Maximum om3 Period of emission omin/hr ohr/day oday/yrrate/hour have)Dry Weather Flow om3/sec

WWD Licence Application - New Ross Town &Environs - Page: 11

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EPA Export 26-07-2013:17:02:37


e Table 0.1 (iii)(a): EMISSIONS TO SURFACE/GROUND WATERS (Storm Overflow)


Local Authoritv Ref No:Source of Emission: Emerqencv overflow from PSLocation: Quay at New RossGrid Ref (12 dlcits 6E 6N) 271519/127226Name of Receivina waters: River BarrowWater Bodv: Transitional BodyRiver Basin District South Eastern RBDDesianation of Receivina Waters: SACFlow Rate in Receiving Waters: 9 m3.sec-1 Dry Weather Flow

o m3.sec-1 95% Weather FlowAdditional Comments (e.g. The Quay pumping station has recently beencommentary on zero flow or other commissioned. No data is available on the quality orinformation deemed of value) Iauantitv of the emeraency overflow

Emission Details:

I(j) Volume emittedNormal/dav om3 Maximum/day om3

Maximum orn- Period of emission omin/hr ohr/day oday/yrrate/hour I(avq)Dry Weather Flow om3/sec


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EPA Export 26-07-2013:17:02:37

WWDL_ApplicationForm V65.doc

TABLES E1

ANNEX- Standard Forms

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EPA Export 26-07-2013:17:02:37


TABLE E.1(i): WASTE WATER FREQUENCY AND QUANTITY OF DISCHARGE - Primary and

Secondary Discharge Points

Identification Code for Discharge point Frequency of discharge (days/annum) Quantity of Waste Water Discharged!(~/annum)

SW-1 365 1051200

SW-4 0 0

SW-2 0 0

SW-3 0 0


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EPA Export 26-07-2013:17:02:37


TABLE E.1(ii): WASTE WATER FREQUENCY AND QUANTITY OF DISCHARGE - Storm Water

Overflows

I~tilIcation Code for Discharge ,rcrequency of discharge Quantity of Waste Water Compiles withDefinition of Stormnt daYsiannum) Dischaiaed (rna/annum) Water Overflow

SW-5 0 0 No


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EPA Export 26-07-2013:17:02:37

WWDL _ApplicationForm V65.doc

TABLES F1

ANNEX - Standard Forms

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EPA Export 26-07-2013:17:02:37


e TABLE F.1(i)(a): SURFACE/GROUND WATER MONITORING

Primary Discharge Point

Discharae Point Code: SW-1MONITORING POINT CODE: aSW-1dGrid Ref (12 diaits 6E 6N) 270076 / 124443

Parameter Results (mgll) Sampling Limit of Analysismethod Quantitation methodI

technlaue01/01/01 12/08/09

pH = 8.1 Grab 0 0

Temperature = 17.5 Grab 0 0

Electrical Conductivity (@ =0 Grab 0 025°C)

Suspended Solids =0 Grab 0 0

Ammonia (as Nl = 0.08 Grab 0 0

Biochemical Oxvaen Demand = 1.7 Grab 0 0

Chemical Oxvaen Demand =0 Grab 0 0

Dissolved OXVQen =0 Grab 0 0

Hardness (as CaCO,) =0 Grab 0 0

Total Nitroaen (as N) =0 Grab 0 0

Nitrite (as N) =0 Grab 0 0

Nitrate (as N) = 3.6 Grab 0 0

Total Phosphorous (as P) =0 Grab 0 0

OrthoPhosphate (as P) = 0.083 Grab 0 0

Sulphate (SO.) =0 Grab 0 0

Phenols (Sum) =0 Grab 0 0

For Orthophosphate: this monitoring should be undertaken on a sample filtered on 0.451..1m filter paper

For Phenols: USEPA Method 604, AWWA Standard Method 6240, or equivalent.

Additional Comments: zero inserted where information is not available at time of application

Data obtained from EPA Regional Laboratory, Kilkenny

Zero inserted where information is not available at time of application


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EPA Export 26-07-2013:17:02:37


e TABLE F.1(i)(a): SURFACE/GROUND WATER MONITORING

Primary Discharge Point

Discharae Point Code: SW-1MONITORING POINT CODE: aSW-1uGrid Ref (12 diaits 6E 6N) 271720 /127656

Parameter Results (rngII) sampling Limit of Analysismethod Quantltation method I

techniaue

01/01/01 12/08/09

IpH =8 Grab 0 0

Temperature =17.4 Grab 0 0

Electrical Conductivity (@ =0 Grab 0 025°C)

Susoended Solids =0 Grab 0 0

Ammonia (as N) - 0.083 Grab 0 0

Biochemical Oxvaen Demand = 1.1 Grab 0 0

Chemical Oxvaen Demand =0 Grab 0 0

Dissolved Oxvaen =0 Grab 0 0

Hardness (as CaCO,) =0 Grab 0 0

Total Nitrogen (as N) =0 Grab 0 0

Nitrite (as N) =0 Grab 0 0

Nitrate (as N) = 3.8 Grab 0 0

Total Phosphorous (as P) =0 Grab 0 0

OrthoPhosphate (as P) = 0.08 Grab 0 0

Sulohate (SO,) =0 Grab 0 0

Phenols (Sum) =0 Grab 0 0

For Orthophosphate: this monitoring should be undertaken on a sample filtered on 0.451.lm filter paper

For Phenols: USEPA Method 604, AWWA Standard Method 6240, or equivalent.

Additional Comments: zero inserted where information not available at time of application

data from EPA Regional Laboratory Kilkenny

Zero inserted where information is not available at time of aohcation


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EPA Export 26-07-2013:17:02:37

Documents

For inspection purposes only.Westfalia UCD-345 1 500 l/hr Ultromat 2 Duty/Standby oto 1000 l/hr Seepex or equal. 2 4 m3/hr 304 Stainless Steel For inspection purposes only. Consent