utah guidance for performance, application, design ... · distribution system. the distribution...
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UtahGuidanceforPerformance,Application,Design,Operation&Maintenance
PressureDistributionSystems
RevisedDraft
December2017
UtahOn-SiteWastewaterTreatmentTrainingProgramUtahWaterResearchLaboratoryUtahStateUniversityLogan,UT84322-8200
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PressureDistributionSystems–Utah,2017
TableofContents
Introduction.......................................................................................................................11.0 SystemComponents/ProcessSummary.................................................................3
Figure1:Majorcomponentsofatypicalpressuredistributionsystem......................3Table1:Majorcomponentsofatypicalpressuredistributionsystem........................4
1.1. SepticTank............................................................................................................5Figure2:Typicalseptictankandpumpchamber........................................................5Table2:Septictankrequirements...............................................................................6Table3:Materialsusedforwatertightness...............................................................7
1.2. OutletEffluentFilter.............................................................................................7Table4:Effluentfilterperformancerequirements......................................................8
1.3 PumpTanks,VaultsandBasins.............................................................................8PumpTanks........................................................................................................8Table5:Pumptankrequirements...............................................................................9
PumpVaults.....................................................................................................10Table6:Pumpvaultrequirements............................................................................11
PumpBasins.....................................................................................................11Table7:Pumpbasindesignissues............................................................................12
1.4. Pumps,DosingOptions,Controls,Fittings,andValves.......................................12Pumps..............................................................................................................12Table8:Pumprequirements.....................................................................................13
PumpPerformanceCurve................................................................................13Figure3:Examplesofpumpcurves...........................................................................14
DosingOptions.................................................................................................14DemandDosing................................................................................................14TimedDosing...................................................................................................15Controls............................................................................................................16Table9:Controlssystemrequirements.....................................................................17
Fittings..............................................................................................................17Valves...............................................................................................................17Table10:Typesofvalvesandtheiruses...................................................................19
1.5. Floats(orOtherTypesofLiquidSensors)............................................................191.6. ForceMain..........................................................................................................201.7. Manifold..............................................................................................................20
Figure4A:Pressuredistributiondrainfield(slopingground).....................................21Figure4B:Pressuredistributiondrainfield(slopingground).....................................22Figure5:Pressuredrainfieldteetotee.....................................................................22Figure6:Pressuredrainfieldcrossconstruction........................................................23Figure7A:Drainfieldcontrolbox(slopingground,manifoldbelowlaterals)...........23Figure7B:Drainfieldcontrolbox(slopingground,manifoldabovelaterals)...........24Table11:Possiblemanifoldconfigurations..............................................................26
1.8. Laterals................................................................................................................26LateralSpacing.................................................................................................26LateralOrifices.................................................................................................27Table12:Lateralorificepositions.............................................................................28
LateralOrificeDiameters.................................................................................28Table13:Lateralorificediameters...........................................................................28
ResidualPressure(Head)Requirements..........................................................29Table14:Residualpressure(head)...........................................................................29
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LateralOrificeFlowRate..................................................................................29Table15:Flowratecalculations................................................................................30
LateralOrificeShields.......................................................................................30Figure8:Orificecapsandshields..............................................................................31
CleanoutandMonitoringofLaterals................................................................31Figure9A:Cleanoutport...........................................................................................31Figure9B:Cleanoutport(example)...........................................................................32Table16:Cleanoutandmonitoringoflaterals..........................................................33
2.0 PressureDistributionDesignforSpecialConditions..............................................352.1. FreezingConditions.............................................................................................35
Table17:Recommendationsforfreezingconditions................................................362.2. SlopingSites.........................................................................................................36
3.0 PressureDistributionDesignProcess....................................................................39Table18:Designsteps...............................................................................................55Figure10:Systemandpumpperformancecurves....................................................55
4.0 PressureDistributionDesignSubmittalRequirements..........................................575.0 TestingandInspectionofPressureDistributionSystemafterInstallation.............59
Timed-dosetesting...........................................................................................60Post-inspectionfollow-up.................................................................................61
6.0 OperationandMaintenance(O&M)Criteria&Recommendations........................63Permitrequirements........................................................................................63Maintenancerequirements..............................................................................63
AppendixA:PressurizedDistributionDesignWorksheet.................................................65AbsorptionAreaDesign....................................................................................65PressureNetworkDesign.................................................................................66SystemPerformanceCurveWorksheet............................................................77
AppendixB......................................................................................................................79GraphB-1A:Minimumlateraldiameterfor1/8"orifices..........................................79GraphB-1B:Minimumlateraldiameterfor1/8"orifices..........................................80GraphB-2A:Minimumlateraldiameterfor5/32"orifices........................................81GraphB-2B:Minimumlateraldiameterfor5/32"orifices........................................82GraphB-3A:Minimumlateraldiameterfor3/16"orifices........................................83GraphB-3B:Minimumlateraldiameterfor3/16"orifices........................................84GraphB-4A:Minimumlateraldiameterfor1/4"orifices..........................................85GraphB-4B:Minimumlateraldiameterfor1/4"orifices..........................................86TableB-5:Orificeflowrates......................................................................................87TableB-6:Frictionalheadlossper100feetofsolidpipe..........................................88TableB-7:Frictionallossesthroughplasticfittings...................................................89TableB-8:Voidvolumeforvariousdiameterpipes...................................................89
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PressureDistributionSystems–Utah,2017
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Introduction
Gravityflowisafrequentlyusedmethodfordistributingeffluent.Itisalsothesimplest.Itallowswastewatertoflowbygravitythroughlargediameterpipesintoasubsurfacesoilabsorptionfield.Distributionisusuallylocalizedinafewareaswithinthefield,whichresultsinoverloadingoftheinfiltrativesurfaceinthoseareasuntilamaturebiomatdevelops.Thedisadvantageofthismethodisthatoverloadingcanleadtogroundwatercontaminationincoarsegranularsoilsduetoinsufficienttreatment,ortomorerapidclogginginfiner-texturedsoils.
Pressuredistribution,ontheotherhand,isamethodusedtoapplyeffluentuniformlyoveranentireabsorptionarea.Eachsquarefootofaninfiltrativesurfacereceivesapproximatelythesameamountperdose.Therateofdistributionislessthanthereceivingcapacityofthesoilormedia.
Theadvantagetopressuredistributionisthatinsoil-basedoralternative(mound,andpackedbed)on-sitesystems,treatmentperformanceisimprovedbymaintainingverticalunsaturatedflow.Infiner-texturedsoilsormediathedegreeofcloggingisreduced.
Researchevidenceindicatesthatwastewatertravelingverticallythrough2to4feetofsuitable,unsaturatedsoilprovidesadequatetreatmentofthewastewater.Researchalsoindicatesthatthemethodofdistributionofseptictankeffluentwithinthesoilabsorptionfield,mound,orpackedbedsystemwillaffectthetreatmentperformanceofthesystem.
Pressuredistributionisusuallyusedinlocationswhereitiseitherdesirableorrequiredto:
• Achieveuniformapplicationofwastewaterthroughoutasoilabsorptionfieldorontheinfiltrativesurfaceofpressurizedalternativesystems,includingmoundorpackedbedsystems
• Treatanddisperseeffluenthigherinthesoilprofile
• Improvethetreatmentperformanceandextendthelifeexpectancyofasoilabsorptionfield,amound,orapackedbedsystem
Apressuredistributionsystemconsistsof:
• Aseptictanktoseparatethemajorsolidmaterialsfromtherawwastewaterenteringthetank
• Ascreeningdevicetoprotectthepumpanddistributionlateralorificesfromsolids
• Ameanstodeliverspecifieddosesofeffluent,underpressure,tothedistributionsystem.Thedistributionsystemconsistsofsmall(typically1to2inchesindiameter,basedonhydrauliccalculations)lateralswithsmalldischargeorifices.Apressureheadiscreatedwithinthelaterals,usuallybymeansofapump
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AsregulatedbyUtahAdministrativeCodeR317-4,pressuredistributionisapplicabletoanysystemthatusessoilasatreatmentmediumwherepressuredistributionmayimprovelong-termperformanceofthosesystems.
Pressuredistributionisarequiredcomponentofalternativesystemsthatincludethemoundsystemandpackedbedsystems.ItisalsoappropriateforlargersoilabsorptionandpackedbedsystemsthatareregulatedbyUtahAdministrativeCodeR317-5.
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1.0 SystemComponents/ProcessSummary
Pressuredistributionsystemsrequirethefollowingbasiccomponents:
CONTROLPANEL
SEPTICTANK
PUMPCHAMBER
PRESSUREDISTRIBUTIONLATERALS
CLEANOUT/MONITORINGPORTS
FORCEMAIN
ACCESSRISER
MANIFOLDPIPE
Figure1:Majorcomponentsofatypicalpressuredistributionsystem
Component: Primaryfunction:
Septictank Solidsseparationandstorage.
Effluentfilter Protectionofpumpanddistributionnetworkorificesfromsolids.
Pumpchamber Transportofaspecificvolumeofeffluentfromthepumpchambertothedistributionnetwork.
Accumulateeffluentbetweenpumpcyclesandduringmalfunction.
Forcemain(transportpipe)
Pipelinethatconnectsthepumptothemanifold.
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Component: Primaryfunction:
Manifold Pipingnetworkconnectingtheforcemaintothevariouslaterals.
ControlPanel NEMA-ratedboxcontainingallthecontrolsforthepumpingsystem,dosecyclecounter,pumpruntimemeter,andalarmcontrols.
Laterals Smalldiameterpipeswithorificesthatdistributeeffluentovertheinfiltrativesurfaceofanabsorptionarea.
Absorptiontreatmentarea
Nativesoilorotherreceivingmediawherevariousbiologicalandphysicalprocessesprovideadditionaltreatmentofseptictankeffluent;Consistsofasoilabsorptionfieldortheinfiltrativesurfaceofamoundorpackedbedsystem.
Table1:Majorcomponentsofatypicalpressuredistributionsystem
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1.1. SepticTank
Apressuredistributionsystemmustbeprecededbyaproperlysizedseptictank:
Figure2:Typicalseptictankandpumpchamber
TheseptictankmustbedesignedincompliancewiththeguidelinesgiveninUtahAdministrativeCodeR317-4.
24” DIAMETER ACCESS RISER
FINISH GRADE
SECURED LID WITH GAS TIGHT SEAL
SEDIMENTS
FLOATING MATFROM SEWAGE SOURCE
TO PUMP CHAMBER
APPROVED EFFLUENT
FILTER
24” DIAMETER ACCESS RISER
FIGURE 2
PUMP CHAMBER (TYPICAL)
SEPTIC TANK (TYPICAL)
SEDIMENTS
WORKING VOLUME
EMERGENCY STORAGE
NORMAL TIMER OFF LEVEL
HIGH WATER ALARM LEVEL
ENCLOSED PUMP SEDIMENT SHROUD *
INDEPENDENT FLOAT STEM FOR FLOAT MOUNTING
FROM SEPTIC TANK
FINISH GRADE
SUBMERSIBLE CENTRIFUGAL
PUMP
CHECK VALVE *
ANTI SIPHON VALVE *
THREADED UNION
SERVICE VALVE *
SECURED LID WITH GAS TIGHT SEAL
TO DRAINFIELD
18”
* AS NEEDED
SLUDGE
SLUDGE SCREEN
SLUDGE
OPTIONAL
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Allseptictanksshould:
Septictankmust: Requirement:
Betestedforwatertightness
Bewatertighttoalevelaboveanypossibleseasonalgroundwater.EachtankmustbetestedforwatertightnessaccordingtotheproceduresoutlinedinUtahAdministrativeCodeR317-4.
Retainsolids Havefunctioningoutletbaffleortees.Mayincludescreeningoftheeffluentwithaneffluentfilterthatislocatedintheseptictankorinaseparatepumpchamber.Screeningaroundthepumpinapumpvaultcanalsobeusedtoprotectthepump;howeveralsousinganeffluentfilterintheseptictankcanprovideextraprotection.
Beaccessible Haveserviceaccessmanholesandmonitoringportsfortheinletandoutlet.
Havewatertightrisersthatmeetrequirements
Risersmustbeplacedtofacilitatepumpingbothsidesofthetank.Multiplerisersmaybenecessary.
Coversmustbegasketedandsecurelyfastenedbyscrewsorsomeotherlockablemeans.
Risersmustbeconstructedofdurable,structurallysoundmaterialsanddesignedtowithstandexpectedphysicalloadsandcorrosiveforces.
Ifsoilcoverismorethan24inches,risersmustextendtowithin6inchesofthesurfaceoftheground.Therisershouldpreferablybebroughtuptothefinishedgradetoencourageperiodicservicingandmaintenance.
Table2:Septictankrequirements
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Someorallofthefollowingmaterialscanbeusedtoaidinachievingwatertightnessofthetanks:
Material: Use:
Cast-in-placeflexiblerubbergaskets
Usedforinletandoutletopeningswithstainlesssteelclampstosealtherubbertothepipes.
Flexiblerubbergaskets Sealtotheinletandoutletopeningswitharatchetedexpansionsealandstainlesssteelclamps.
Expandinggroutmaterial Usedtosealtanksandrisers.Somegroutswillshrinkandcrackovertimeandthusallowtankstoleakafterthetankisbackfilled.
Bentonitebackfill Usedaroundthetankseamsandpipeentrancestohelpprovideawatertighttank.
Epoxy Anothereffectivemethodofsealingsomekindsofjoints,buttheweatherconditionsmustbeidealandthereisnocapacityforflex.
Rubbergrommets Usedaroundsmallerinletanddischargepipes,conduitandjunctionboxpenetrations,canbeeffectiveincontrollingleaks.
Table3:Materialsusedforwatertightness
1.2. OutletEffluentFilter
Aneffluentfilterorscreenisaremovable,cleanabledeviceinstalledontheoutletpipingofaseptictankforthepurposeofretainingsolidslargerthanaspecificsize(1/8inchorgreater)and/ormodulatingtheeffluentflowrateoutofthetank.
Theeffluentfiltershouldprovideanopenareaflowcapacityatleastequaltotheflowcapacityprovidedbya4-inchdiameterPVCpipe.However,usingtheminimumareawillverylikelyrequireahighfrequencyofcleaning.Instandardpracticeamuchlargerflowareashouldbeused.Largerflowareaswillresultinlongerintervalsbetweenservicesforthesamehydraulicandorganicstrengthloadings.
Aneffluentfilterisrequiredinallpressuredistributionsystems.
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Theeffluentfiltershouldmeetthefollowingperformancecriteria:
Function: Filtermust:
Positioning Drawliquidfromthe“clearzone”oftheseptictank.
Durability Beconstructedofdurable,non-corrodingmaterials.
Besecurelyfastenedtopreventdislodgingormisalignment.
Protection Preventdischargeorificesfrompluggingbyparticleslargerthantheorifices.
Protecttheeffluentpumpfromdamageduetoparticlesthatexceedthepump’scapacitytopass(maybeanissuewithsometypesofpumps).
Service Avoidlossofperformancebetweenroutineserviceevents.
Shouldnotrequirefrequentroutineservicing.
Bedesigned,constructedandinstalledforeasyandthoroughcleaning.
Haveanaccessriserforcleaningovertheseptictankopeningabovetheeffluentfilter.Thetypicalconcreteriserandlidcommonontanksthatareburiedbelowfinishedgradearenotacceptableforextendingtothesurface.Theyarenotwatertightandwillnotkeepodorsandgaseswithinthetank.Althoughconcretelidsareheavy,theyarenotnecessarilyheavyenoughtokeepchildrenoutofaseptictank.
Table4:Effluentfilterperformancerequirements
1.3. PumpTanks,Vaults,andBasins
PumpTanks
Apumptankisachamberusedtohousethepump,floats,andmiscellaneousequipmentrequiredforthepumpingsystem.Pumptanksreceivingseptictankeffluentwillaccumulatesludgeandscum.Thesludgelevelshouldnotbeallowedtoaccumulatetolevelsabovetheintakeofthepump.
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Pumptankmust: Requirement:
Bestructurallysound
Bewatertighttoalevelaboveanypossibleseasonalgroundwater.
Leaktestingisrequired.
Beequippedwithawatertightriserwithasecuredlidthatextendstothegroundsurface.
Lidsmustbeequippedwithanairtightgaskettoeliminatenuisanceodorsandbesecuredfromaccidentalorintentionalremovalbyunauthorizedpersons,especiallychildren.
Havesufficientinternalvolumeofthepumpchamber
Designmustaccommodate:
Theoperatingvolume.
Deadspacebelowthepumpinlettoprovideforfulltimepumpsubmergenceandtoensurethatthepumpintakeisaboveaccumulatedsludgelevels.
Emergencystoragevolumeforperiodsofpoweroutage,mechanicalfailure,orequipmentmalfunctions.Thismaybeachievedbyrelyingonthefullvolumeoftheseptictankandpumptank(uptothebottomofthelids),providedthattheelevationofthetopofthehighestlidisbelowthelowestfloordraininthebuildingservedbythesepticsystemtopreventbackupintothebuilding.Reductionsinemergencypumpchambervolumemaybeconsideredwhen"duplex"orredundantpumpsareused.
Time-dosedsystemsmayrequireadditionalsurgetankcapacity.
Surgevolumemaybeaconcernfortime-dosedsystemsthatmayperiodicallyexperiencehigherinfluentflowratesintothepumptankthandischargeflowratesfromthepumptank.
Failuretosizethetankforsurgeflowscouldresultinnuisancehighlevelalarms,leadingtotheneedtouseshortertimersettingstoaccommodateperiodsofhighflow.
Usingshortertimesettingsduringsurgeflowconditionssimulatesademanddosingconfigurationandlimitsthebenefitsofatimed-dosingsystem.
Table5:Pumptankrequirements
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PumpVaults
Pumpvaultsmaybeusedtohousethepumpingequipmentwithinaseptictank,apumptankorapumpbasin.Apumpvaultusuallyconsistsofeitherone(Simplex)ortwo(Duplex)pumps,dischargeassembly(ies),filterorscreensaroundthepump(s),afloatswitchassembly,andafloatstembracket.
Pumpvaultmust: Requirement:
Beaccessible Thepumpvaultmustbedesignedandconstructedtofacilitateremovalandmaintenanceofthevaultscreen,pumps,andfloats.
Haveadequatevolume
Theminimumstorageandpumpworkingvolumesintheseptictankmustbeequivalenttothevolumerequiredinaseptictank.Theminimumvolumesinclude:
• Sufficientvolumetohandlethefunctionsofaseptictankandtokeepthepumpsubmerged,whenrequired
• Additionalreservestorageforemergencysituationsasappropriateforprotectionofpublichealthandtheenvironment.
Notinterferewiththeseptictank
Ifapumpvaultisinstalledwithinaseptictankthevaultmustnotinterferewiththemainfunctionoftheseptictank,whichistoprovidefortheseparationofscumandsettleablesolids.
Theuseoftwocompartmentseptictanksisrecommendedalthoughnotrequiredwhenapumpvaultisused.
Topreventinterference,thepumpvaultshouldbeinstalledsuchthat:
• Theentrypointofthewastewaterintothepumpvaultisattheleveloftheclarifiedeffluentinthemiddleofthetank.Theelevationofthepumpvaultisbasedonthetankdimensionsandthemaximumallowablelevelsofscumandsludgebeforethetankrequirespumping
• Theliquidlevelchangescausedbyoperationofthepumpsystemareminimizedtoreducethedisturbanceofthescumlayer.Thischangewillgenerallybelessthantwoinches,butmayvarydependingonthespecifictankdimensions
• Theamountofwastewaterpumpedoutofthetankduringeachdosingeventisequaltotherequireddosevolume.Whentheinfluentflowratetemporarilyexceedstheeffluentflowrateduringa24hourperiod,surgevolumeisrequiredtoaccommodatethesetemporaryhighflowperiods
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Pumpvaultmust: Requirement:• Timer-basedpumpcontrolsystemsmayalsorequiresurgevolume
capacityinthetank
• Thepumpingrateshouldalwaysbelessthan30gallonsperminute,andpreferablylessthan20gallonsperminute.Ifhigherpumpingratesarerequired,thepumpingsystemshouldbeinstalledinaseparatepumptankaftertheseptictankandnotinapumpvaultintheseptictank
• Reservevolumemustbeprovidedwithintheseptictankforemergencystorageintheeventofapoweroutageormechanicalfailure.Thereservevolumemaybeachievedbyrelyingonthefullvolumeoftheseptictank(uptothebottomofthelid),providedthattheelevationofthetopofthelidisbelowthelowestfloordraininthebuildingservedbytheseptictank,toensurethatbackupintothebuildingdoesnotoccurduringemergencyevents
• Thepumpvaultmustnotinterferewiththepumpingofsolidsfromthetank.Ifthepumpingvaultaccessriseristhesameaccessriserusedforpumpingofsolidsandscumfromthetank,thepumpvaultandtheassociatedpumpingequipmentshouldbeinstalledsothattheycanbeeasilyremovedwhenthetankisbeingpumped.Preferablytheseptictankshouldhaveotheraccessopeningsforsolidsremoval.
Table6:Pumpvaultrequirements
PumpBasins
Apumpbasinisaseparatepumpingchamberlocatedwithinapackedbedsystemorafterapackedbedsystem.Becausewastewateristime-dosedintoapackedbedsystem,demanddosingfromthepumpbasinafterthepackedbedsystemcanbeusedbecausetheamountofflowforpumpingwillbecontrolledbythetimed-dosingoftheeffluenttothepackedbedsystem.
Apumpbasinmayalsobeusedtolifteffluentfromaseptictanktoagravity-flowabsorptionfieldortoanat-gradesystem.Demanddosingmayalsobeusedinothersituations,ifthedesignisapprovedbytheregulatoryauthority.
Pumpbasinissues: Considerations:
Volume Apumpbasinhaslittletonostoragevolumeandmustbeusedonlyindemanddosing.
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Pumpbasinissues: Considerations:
Off-lineprovisions Thedesignermustaccountforperiodswhenthepumpisoff-linebyconsideringcorrectiveactionresponsetimesandactivities.
Iftherewillbeabackuporoverflowconditioncreatedduringapoweroutageoramechanicalfailure,andiftheflowscannotbestoppedorminimizeduntiltheproblemiscorrected,apumpbasinwithmorestoragevolumeshouldbeused.
However,ifthefacilitygeneratingtheflowscanbeclosedorothertemporaryarrangementsmadetoreducewastewaterflow,orifadrinkingwaterpumpcanalsonotbeusedduringapoweroutage,thenapumpbasinwithlittleemergencystoragevolumecanbeused.
Table7:Pumpbasindesignissues
1.4. Pumps,DosingOptions,Controls,Fittings,andValves
Pumps
Theeffluentpumpsusedforpressurizingthedistributionnetworksareeithercentrifugaleffluentpumpsorturbineeffluentpumps,whichareslightlymodifiedwellpumps.Thecentrifugalpumpisahighercapacity/lowerheadpumpwitharelativelyflatperformancecurveandtheturbinepumpisalowercapacity/higherheadpumpwitharelativelysteepperformancecurve.Turbinepumpsprobablyhavealongerlife.Theymaybethepreferredchoicefortimedosingbecauseoftheirlongevityrelativetostop/starts.
Pumpsandpumpinstallationsmustmeetthefollowingrequirements:
Requirement: Pumpmust:
Pumpeffectively Beabletopumpeffluentscontainingsolidsupto1/8inchindiameterwhenfollowinganeffluentfilter,andsolidsupto1/2inchindiameterwhenaneffluentfilterisnotused.
Becapableofmeetingtheminimumdesignhydraulicflowandheadrequirementsoftheproposedpressuredistributionsystem.
Pumpsmustbeabletowithstandthewet,corrosiveenvironmentfoundwithinthepumpchamber,vault,orbasin.Onlypumpsthatarespecifiedforuseinwastewatershouldbeused.
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Requirement: Pumpmust:
Beaccessible Pumpsmustbeinstalledsothattheycanbeeasilyremovedand/orreplacedfromthegroundsurface.
Undernocircumstancesshouldpumpreplacementand/orrepairrequireservicepersonneltoenterthepumptank.
Pumpsmustbefittedwithunions,valves,andelectricalconnectionsnecessaryforeasypumpremoval,servicing,andrepair.
Haveaprotectivefilter
Pumpsmustbeprotectedbyanapprovedoutleteffluentfilterinthechamberprecedingthepumpchamberorbypumpscreens,asdescribedinprevioussections.
Complywithelectricalrequirements
Pumpsandassociatedcontrolsshouldhavegas-tightjunctionboxesorsplicesandhaveelectricaldisconnects(asperNationalElectricCode)appropriatefortheinstallation.
Theboxesshouldbeplacedsothattheydonotinterferewiththeservicingand/orremovalofothercomponentsinstalledinthesystem.
Pumpsandelectricalhook-upsmustconformtoallstateandlocalelectricalcodes.
Dependingonthesizeofthesystemand/orlocationofthepumpingequipment,specializedequipmentforexplosionmayberequiredbyfirecodes.Theappropriateregulatoryauthoritywilldeterminewhetherspecializedequipmentisrequired.
Table8:Pumprequirements
PumpPerformanceCurve
Apumpperformancecurveisagraphicalrepresentationthatdescribestherelationshipbetweenflowrateandheadforaspecificmodelofpump(Figure3).Thebottomaxisislabeled“gallonsperminute”,andtheleftsideislabeled“totaldynamichead”.ThesevaluesarecalculatedinthePressureDistributionDesignProcess(section3.0ofthismanual).Theflowrateandtotaldynamicheadneededtooperateaspecificpressurizeddistributionsystemisnotedbyapointonaspecificpumpperformancecurvethatrepresentsthecombinationofflowrateandheadatwhichthesystemmustperform.Thispointshouldbeonthepumpperformancecurveorjustbelowthecurve.Ifthepointisaboutthecurve,adifferentpumpmustbeselected.
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Figure3:Examplesofpumpcurves
DosingOptions
Therearetwodifferentoptionsfordeliveringdosesofeffluenttothereceivingcomponentofapressurizeddistributionsystem:demanddosingandtimed-dosing.
DemandDosing
Indemanddosing,thedoseisdeliveredtothereceivingcomponentwheneveradosevolumeaccumulatesinthepumpchamber.Theeffluentisnotmeteredoutuniformlyovera24-hourperiod.
Demanddosingistheleastcomplexmethodofdosingandthereforeleastcostlytoinstallandeasiesttounderstand.
Demanddosingisnotsensitivetoheavyusedaysandthereforewillnotactivatethealarmcircuitwithweekendguests,largelaundrydaysorparties.
Additionally,demanddosingdoesnotprotectthesoilabsorptionfield,moundorpackedbedsystemfromhydraulicsurgesandoverload.
Effluentdistributionisbasedonthepatternofwateruseintheparticularsystem.Forexample,inresidentialsystems,mostoftheeffluentisdistributedduringtheperiodsofhouseholdwateruse,thatis,usuallyinmorning,eveningandweekendsurges.
Whendemanddosingisused,thedosevolumesshouldbeminimizedtoprovidesmallerandmorefrequentdosestothesystem,withlargedosesavoidedasmuchaspossible.
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TimedDosing
Intimeddosing,theeffluentismeteredtothereceivingcomponentindiscrete,evenlyspaceddoses.
Thismethodofdosingallowsmorefrequent,smallerdosestobepumpedtothereceivingcomponent,therebypromotingunsaturatedflowthroughthesoilorfiltermediawhileprotectingthereceivingcomponentfromhydraulicoverload.
Timeddosingisstronglyrecommendedonallpressuredistributionsystems,forthistypeofsystemenhancesperformanceandreliability.
Timeddosingmeansthatboththelengthofeachdose(whichdeterminesthegallonsperdose)andtheintervalbetweendoses(whichdeterminesthenumberofdosesperday)iscontrolledbyatimingdevicewheneveradosevolumeisinthepumpchamber.
Thenumberofpumpcyclesshouldbeadjustableandinsufficientnumbertomeetthedesignneedsofthesystem.
However,timeddosingissensitivetoheavyusedaysandthereforethehighwateralarmmaybeactivatedwhenthevolumeofwastewaterexceedsthedesignflow.Somecausesofexcessiveflowareweekendguests,largelaundrydays,parties,leakingfixtures,andgroundwaterleakingintotheseptictankorpumpchamber.
Withtimeddosing,dosevolumespumpedtothereceivingcomponentareoftensmallerandmorefrequent,withinterveningrestingandaerationperiods,therebyassuringunsaturatedflowthroughthesoilorfiltermedia.Thesesmallerdosesmayrequiresmallerorifices,smallertransportandlateralpipes,checkvalves,andorificesinthe12o'clockpositiontomaintainthesystemfullofeffluentbetweendoses.
Whentimed-dosingisused,thetimersettingsshouldbesetsuchthatthesystemdosesequalamountsofeffluentevenlyduringthedaybydelivering12to24dosesperday.Somesystemsmayevenbedosed100to200timesina24-hourperiod,resultinginimprovedtreatmentperformance.Thetimersettingsshouldbesetsothatnomorethanthedailydesignflowisdeliveredtotheinfiltrativeserviceduringa24-hourperiod.
Surgeanalysisisespeciallyimportantwhentimed-dosingisused,thatis,whenmanysmalldosesarebeingappliedovertime.Enoughsurgevolumeisrequiredtoavoidhighlevelalarmsduringtheshortduration,higherflowsthatarecommonlyobservedinthemorningsandeveningsinresidentialapplications.
Timeddosingisnotrequiredforpressuredistributionsoilabsorptionfieldsfollowingtreatmentcomponentsthataretimed-dosed.Theflowisalreadytime-dosedtothetreatmentcomponent,andthereforethepumpchamberafterthetreatmentcomponentmaybedemand-dosed.
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Controls
Forallpumpingsystems,theappropriatecontrolssystemmustbespecified.Thecontrolssystemmusthavetheproperfunctionalityfortheproposeddesign.
Requirement: Controlssystemmust:
MeetCodeandsafetyrequirements
Meettheapplicablecoderequirementsfortheinstalledlocation.ThismayincludeNEMA4,orNEMA4X,orotherstandardsdependingonwherethecontrolsaremounted.
BeUnderwritersLaboratories(UL)listedorotheracceptedequivalent.
Functionality Deliverprescribeddosesuniformlytotheorificesinthedistributionnetwork.
Havecontrolslocatedwithinsightofthepumpingsystem.Wherethisisnotpossible,itmaybenecessarytoprovideelectricaldisconnects.Thelocalelectricalcodesshouldbeconsultedforspecificrequirements.
Havedefaultsettingsfortimed-dosecontrolstoassurethattheflowsdonotexceedthemaximumdesigncapacitywithoutenteringalarmcondition.
Recordandstorepumpruntimesandnumberofpumpingeventsusingbuiltincyclecountersandelapsedtimemeters.Awatermetermayalsobeusedtotrackandrecordsystemflows.
Shouldnotbeinstalleddirectlytotheoutsidewallofthehouseorstructurewherethesystemmaycreatenuisancecomplaints.Thecontactmotorswitchingsoundmaytransferthroughthewallandcreatenuisancecomplaints.Noisecanbereducedbymountingthecontrolsonapostnexttothewallofthestructureorbyinstallingthecontrolsonthegarageornon-bedroomwalls.
Alarms Provideanaudiblealarm.Theaudiblealarmmayhaveasilencingswitch.
Provideavisiblealarm.Thismustcontinuetoshowuntiltheconditioniscorrected.
Providearemotealarminaconspicuousplaceforsystemswherethealarmconditionmaygoundetected.
Thealarmcircuitmustbeindependentofthepumpcircuit,
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Requirement: Controlssystemmust:includingaseparatebreakerfromthehousesupply.Thisistoensurethatanalarmsoundsifthepumpbreakerorthebreakersupplyingpowertothecontrolpanelistripped.Thedesignermustclearlyspecifythisrequirementinthedesigndocumentationandtheinspectorsmustcheckforthisseparatealarmcircuit.
Table9:Controlssystemrequirements
Fittings
Pipefittingsincludetherangeofcomponentsthatareusedtoconnectpipeendsforin-line,multi-port,offsetandmountingconfigurations.
Pipefittingcrosssectionsaremostly,butnotalways,circularinshapetomatchwiththepipesectionwithwhichtheyareconnected.
Pipefittingsareusedforvariouspurposes.Theycanbeusedtoextendorterminatepiperuns,changeapipe'sdirection,toconnecttwoormorepipesandtochangethepipesize.
Theamountoffrictionlossassociatedwithfittingsmustbeaccountedforinthedesignofthepressuredistributionsystem.
Adischargeassemblyiscomposedofallofthepipingandfittingsbetweenthepointofpumpdischargetothepointatwhichtheforcemainexitsthetank.Thefrictionlossassociatedwiththedischargeassemblyisacriticalcomponentofsystemdesignandmustbeaccountedforinsystemdesign.
Valves
Valvesaremechanicaldevicesusedtocloseoff,regulate,ordiverttheflowoffluids,includingliquidsandgases.
Valvetype: Uses:
Checkvalve Acheckallowsflowinonlyonedirectionbyclosingwhentheflowdirectionreverses.
Commonusesofcheckvalvesinonsitesystemsaretokeeptheforcemainpipefromdrainingbetweendoses,andinduplexpumpingapplications.
Whentheforcemainpipeisnotallowedtodrain,acheckvalveshouldbeinstalledjustabovethepumpinthedischargepiping.Thiswillincreasethepumpingefficiency,asalltheeffluentpumpedwillbedischargedtothepumpingchamberwithoutreturningaportionattheendofeachcycle.
Incoldweatherinstallationstheforcemainpipewithacheckvalvemustbeinstalledbelowthefrostdepthorinsulatedtopreventfreezing.
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Valvetype: Uses:Duplexpumpingsystemsareoftenusedorrequiredonlargerornon-residentialapplicationstoprovidepumpredundancy.Duplexpumpsareusuallyconnectedintoasinglesupplyorforcemainpipe.Eachpumpmusthaveacheckvalveinstalledsothatwhenapumpisoperational,theeffluentdoesnotdischargeintothetankthroughtheotherpump.Thecheckvalveshouldbelocatedasclosetothepumpaspossible.
Whenaduplexpumpsystemisinstalledinacoldweatherapplicationwithdrainback,thedrainbackorificemustbelocatedabovethecheckvalvesothatthepipecandrainbetweendosecycles.
Acheckvalvewillrequiremaintenanceandthereforeshouldbeinstalledsothatitcanberemovedforservicingorreplacement.
Unionsplacedatthecheckvalveareacommonmeanstoallowservicingofthecheckvalveswhileavoidingdestroyingofthevalve.Somecheckvalvescanbedisassembledwithoutremovingthemfromtheline.Ifpossible,checkvalvesshouldbeinstalledsuchthattheyareaccessiblefromthesurface.
Thelocationofcheckvalvesmustbewelldocumentedandmarked.Preferablycheckvalvesshouldbelocatedinastructurethatisaccessiblefromthesurface.
Air/vacuumvalve
Air/vacuumvalvesreleaseairbuildupwithinthepipeaswellasletairintothepipetopreventasiphonorvacuumcondition.
Theyareneededwhenpipesareinstalledtopumpoverahillandbackdowntheothersidetoanopendischargepoint.
Therearemultipleoptionsforlocationoftheair/vacuumvalve.Itisofteninstalledatthehighpointofthesystem.However,insmallerresidentialsystems,itcanbeinstalledinthedischargeassemblywithinthepumpaccessriser.Theair/vacuumvalvewillopenandallowairtoenterthesystemunderavacuumconditioncreatedwhentheeffluentdrainsdownthebacksideofthehill,releasingthevacuumwithinthepipe.Theopeningofthevalvewillalsostopthevacuumfromsiphoningeffluentfromthepumptank.
Forlargersystems,theair/vacuumvalveshouldbeinstalledatthehighpointofthepipesystem.Forinstallationswheretheelevationdropfromthehighpointtothelowpointissignificant,thevacuumwithinthepipecouldresultincollapseofthepipewithoutanair/vacuumvalve.Whenthisisaconcern,thedesignershouldspecifythatthevalvemustbelocatedatthehighpointandnotinthedischargetank.
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Valvetype: Uses:
Airreleasevalve
Airreleasevalvesonlyletairbuildupoutofthepipe.
Theyareusedwherethereisahighpointinthepipingthatcanaccumulateairandgasbuildup.
Theairreleasevalveisasimplervalvethantheair/vacuumcombinationvalve.Whenthedownhillsideofthepipingsystemwillremainfullandthereisnoriskofdrainingthatwouldcreateavacuumwithinthepipe,anairreleasevalveisadequatetoreleaseanybuildupofairwithinthepipe.
Vacuumreleasevalve
Vacuumreleasevalvesonlyallowairintothepipe,andwhileunderpressuretheyareclosed.Theyareusedmostoftenindripdispersalsystemstoimmediatelyreleasethevacuumafterthepumpshutsoff.
Theyareinstalledatthehighpointofthesystem.Vacuumreleasevalvesopenwhenthepumpshutoffs,releasingvacuumanddecreasingpotentialforpullingsoilintothetubing.
Table10:Typesofvalvesandtheiruses
1.5. Floats(orOtherTypesofLiquidSensors)
Afloatisasensorinstalledinapumpvault,chamber,orbasinthatopensorclosesanelectricalcircuitinresponsetochangingliquidlevels,therebycontrollingequipmentoperation.
Floatsinstalledinapumpingsystemshouldnotbeinstalledonthepumpdischargepiping.Theyshouldbeinstalledonaseparatepipeormechanism(forexample,afloattree,whichisaremovabledevicelocatedwithinapumpvaultorpumptanktowhichfloatsareattached)sothattheycanbeeasilyremovedforservicing,adjustment,andmaintenancewithoutremovingthepump.
Theminimumrequirementsfortimedpumpcyclecontrolsareatimeractuatorfloatforthepumpandahighliquidlevelalarm.
Inaddition,alowliquidlevelofffloatishighlyrecommended.
Forpumpchambersservingsingle-familyresidences,thenecessaryfloatsorliquidlevelsensorsaretoactuateandturnoffthepumpcontrolsystem,andahighwateralarmfloat.
Redundant“off”controlsareoptional,butarehighlyrecommendedandmayberequiredbytheregulatoryauthority.
Commercialandmulti-familyapplicationsmayrequireredundant“off”andspecialratingsoninstalledmotorsandequipment.
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1.6. ForceMain
Theforcemain(maintransportpipe)mustbesizedbasedonhydrauliccalculationsforflow(gallonsperminute)andtotalhead(infeet)fortheproposedlayout.
Wherepotentialforfreezingexists,thelinemustbeburiedbelowthefrostdepth,insulated,orinstalledwithdrainbackorificessuchthatthewaterdoesnotremaininthepipebetweendoses.
Whenthedrainbackoptionisused,thesmallestacceptablediameterofpipeshouldbeselectedtoincreasethepumpingefficiencyandminimizeunnecessarypumpingofeffluent.
Wheneverapumpisusedtopumpeffluenttoanelevationlowerthanthepump,pumpfittings,orforcemain,anair/vacuumreleaseorsimilaranti-siphondevicemustbeinstalledtopreventsiphoning.
1.7. Manifold
Theprimaryfunctionofthemanifoldistodeliverequalflowtoalllateralswhileminimizingsystemfrictionlosses.
Themostcommonconfigurationsarethecenterandtheendmanifolds.
Endmanifoldsmaybeusedwhenthesystemutilizesshortlaterals,butcentermanifoldsallowforuseofsmallerlateralpipesizes.
Thelateralsmaybeconnectedtothemanifoldinseveralways.Manifoldtolateralconnectionmustbeappropriateforthesiteconditionsandthespecificuse.
Manifolddesignsforslopingsitesareparticularlycritical.Lateralsatdifferentelevationswillhavedifferentresidualpressures,withthelowestlateralhavingthehighestresidual.Inaddition,ifthemanifoldisnotdesignedcorrectly,thelowestlateralwillreceivepressurebeforethetoplateralandsystembackflowwillcontinuetothelowerlateralsafterthepumpingcyclehasended.Inthisinstance,thelowesttrenchwillreceivemoreflowthantheothers,withthepotentialforoverload.Whiletheremaybeseveralsolutionstotheseproblems,Figures4Aand4Billustratetwomethodsforresolvingthem.ThecheckvalvesandflowcontrolvalvesshowninFigures7Aand7Bareassumedtobeanintegralpartofthemanifold.
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LEGEND
LOCATEVALVECONTROLBOXATELEVATIONBELOWLOWEST
LATERALSERVED
FEATURES:
1. FLOWISCONTROLLEDTOEACHLATERALBYFLOWCONTROLVALVE
2. BACKFLOWISPREVENTEDBYCHECKVALVEONEACHLATERALFEEDERPIPE
3. PIPINGABOVECHECKVALVESISALWAYSFLOODED.LENGTHANDVOLUMEOFLATERALSORLATERALFEEDERPIPESDOESNOTIMPACTSIZEOFDOSE.
CHECKVALVE FLOWCONTROL VALVE
FORCEMAINFROMPUMPCHAMBER
LATERALFEEDERPIPES
HEADERMANIFOLDPIPE
PRESSUREDISTRIBUTIONLATERALS
DOWNSLOPEGRADIENT
Figure4A:Pressuredistributiondrainfield(slopingground)
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HEADERMANIFOLDPIPE
FORCEMAINFROMPUMPCHAMBER
LATERALFEEDERPIPES
DOWNSLOPE
GRADIENT
PRESSUREDISTRIBUTIONLATERALS
LEGEND
CHECKVALVE FLOWCONTROL VALVE
FEATURES:
1. FLOWISCONTROLLEDTOEACHLATERALBYFLOWCONTROLVALVE
2. BACKFLOWISPREVENTEDBYMANIFOLDPOSITIONABOVELATERALS
3. ACCEPTABLEVARIANCEOFDOSETOEACHLATERALMAYBEIMPOSSIBLEDUETODIFFERINGVOLUMESWITHINEACHOFTHELATERALFEEDERPIPES,ALLOFWHICHDRAINAFTERPUMPCYCLE
Figure4B:Pressuredistributiondrainfield(slopingground)
ORIFICES
FROMPUMP
CHECKVALVE(OPTIONAL)
MANIFOLDINSTALLEDBELOWFREEZINGDEPTHFLOWCONTROLVALVE
THREADEDPLUGORCAP
LEGEND
CHECKVALVE FLOWCONTROL VALVE
Figure5:Pressuredrainfieldteetotee
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ORIFICES
FROMPUMP
CHECKVALVE(OPTIONAL)
THREADEDCAPORPLUG
FLOWCONTROLVALVE
LEGEND
CHECKVALVE FLOWCONTROL VALVE
Figure6:Pressuredrainfieldcrossconstruction
TODRAINFIELDPRESSURELATERALS
A A
RISERWITHLOCKINGLID
FLAPCHECKVALVE
FLOWCONTROLVALVE
LONGSWEEP90DEGREEELBOW
FORCEMAINFROMPUMPCHAMBER
WASHEDROCKDRAINSUMP
SECTIONA-A
SLOTSASREQUIRED
Figure7A:Drainfieldcontrolbox(slopingground,manifoldbelowlaterals)
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A A
TODRAINFIELDPRESSURELATERALS
RISERWITHLOCKINGLID
FLOWCONTROLVALVE
LONGSWEEP90DEGREEELBOW
FORCEMAINFROMPUMPCHAMBER
WASHEDROCKDRAINSUMP
SECTIONA-A
SLOTSASREQUIRED
Figure7B:Drainfieldcontrolbox(slopingground,manifoldabovelaterals)
Examplesofpossiblemanifoldconfigurationsaregivenbelow.Otherconfigurationsthanthosedescribedmayalsobeused.
Configuration: Uses:
Headermanifoldwithcheckvalves
Aheadermanifoldispositionedatanelevationbelowthelaterals(Figure4A),withcheckvalves,flowcontrolvalvesandfeederlinestoeachlateral.
Thisconfigurationwillmaintainthemanifold,feederlinesandlateralsfullbetweendoses,willnotallowdrainback,andcanbeadjustedatonelocationtoequalizeresidualheadinalllaterals.
Thisarrangementcandeliversmallvolumesperdose,allowingmanydosesperday,ifdesired.
Cautionshouldbetakentominimizethepotentialforeffluentfreezinginthelateralsandmanifold.
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Configuration: Uses:
Headermanifoldwithoutcheckvalves
Aheadermanifoldisplacedatanelevationabovethelaterals(Figure4B)withoutcheckvalves,withflowcontrolvalvesandfeederlinestoeachlateral.
Themeasuredflowsfromanorificeineachlateralarenearlyequalwithouttheuseofcheckvalvesandwithoutmaintainingthesystemfullbetweendoses.
Tee-to-teewithmanifoldbelow
Tee-to-Teewithmanifoldbelow(Figure5)-Whenfreezingandslopingsiteconditionsarenotaconcern,thismethodofconstructioncanbeusedtoallowaveryrapidpressurizationofthesystem,especiallyifthetransportlineremainsfullbetweendoses.
Whencheckvalvesareusedinthemanifoldjustdownstreamofeachlateral,themanifold(andlateralstoo,whenorificesareinthe12o'clockposition)staysfullofeffluentbetweendoses.
Withthislayout:
• Thereisnodrainbackfromtheupperlateralsandmanifoldintothelowerlateral
• Thesystemiscompletelychargedwithinjustasecondortwoafterthepumpisturnedon
• Thesystemcanbedosedwithverysmallvolumesperdose.
Crossconstruction Crossconstruction(Figure6)-Ifthelateralorificesaredrilledinthe6o'clockposition,thisdesignwillallowthelateralsandaportionofthemanifoldtodrainbetweendoses,assumingthetransportlineremainsfullbetweendoses.
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Configuration: Uses:
Tee-to-teewithmanifoldabove
Ifthelateralorificesaredrilledinthe6o'clockposition,theentiredistributionnetworkwilldrainaftereachdose.
Thismaybedesirableonaslopingsite(wherecheckvalvesarenotinstalledinthemanifold),topreventupperlateralsfromdrainingbackthroughthemanifoldtothelowermostlaterals,therebyoverloadingthem.
Iftheorificesaredrilledinthe12o'clockposition,thelateralswillremainfullbetweendoses.Thismaybedesirablewhentheobjectiveistopressurizethedistributionnetworkquicklywithouttheuseofcheckvalves.
Cautionshouldbetakentominimizethepotentialforeffluentfreezinginthelaterals.
Table11:Possiblemanifoldconfigurations
1.8. Laterals
Lateralsareperforatedpipesusedtodelivereffluentequallyovertheinfiltrativesurfaceofthepressuredistributionsystem.
LateralSpacing
Uniformdistributionofeffluentisaccomplishedthroughlateralspacingandorificespacing.Thefollowingminimumspacingoforificesandlateralsisrecommended:
1orifice/6sq.ft.-Mounds
1orifice/4sq.ft.-Intermittentsandfilter
1orifice/4sq.ft.orless-Recirculatingsandfilter,Recirculatinggravelfilter,Textilefilter
Closerorificespacingshouldbeconsideredforusewhensmalldosesarespecifiedandwheretheinfiltrativesurfaceisinhighlystructuredsoilsorhaslargemacropores.
Forpressurizeddrainfields,eachtrenchwillusuallyhaveasinglelateral.Inthiscase,itisrecommendedthattheorificesbeasclosetoeachotherasispractical,preferablyoneorificeevery2to4feet,oncenter.
Orificespacingisalsousedtodeterminethemaximumspacingbetweentheoutsidelateralsandtheedgeofthetrenchorbed,whichis1/2oftheselectedorificespacing,±0.5feet.
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LateralOrifices
Orifices(holesinthelateralsofaspecifieddiameter)areacriticalelementofasuccessfulpressurizeddistributionsystem.Theyareusedtodeliverequalamountsofeffluentoveragivenarea.
Caremustbegiventohowtheorificesaredrilledinthepipe.Evenwithagooddesign,useofadulldrillbitandasloppyprocessfordrillingtheholescanleadtoafailedinspectionbytheregulatoryauthorityorunequaldistributionofeffluentthroughthesystem.
Orificesshouldbedrilledinamanufacturingsettingsothattheholesarelinedupcorrectlyandarecleanandfreefromdebris.Additionally,theorificesmustbedrilledwithaproperlysized,sharpdrillbit.Accurateholediametersmayalsorequiretheuseofjigsorotherdrillstabilizingtoolstopreventwobbleandtodrilltheholeperpendiculartothepipe.Properlayoutandcontrolwillensurethatthecorrectnumbersoforificesareactuallydrilledineachlateral.
Orificescanbedrilledinthetopofthepipe(12o'clockposition)orinthebottomofthepipe(6o’clockposition).
Orificeposition: Considerations:
12o’clockupposition Orificesdrilledinthe12o’clockpositionwillmaintainthelateralsfullorpartiallyfullandthereforereducetheamountofeffluentneededtopressurizethesystem.
Maintainingeffluentinthelineswillpromotebiologicalgrowth,whichmayacceleratecloggingoftheorificesandbuildupofsludgeandslimeinthelines.Italsomakesthelateralssubjecttofreezinginareaswherethisisaconcern.
Thelateralsmaybedrainedbyputtingafeworificesinthe6o’clockposition,orbydesigningthesystemssuchthattheforcemainandlateralsdrainbacktothesurgetank.However,thesepracticeswillincreasethedosevolumerequired.
Whenusinggravellesschamberswithpressuredistribution,theorificesmustbeorientedinthe12o’clockposition.Ifoneortwoorificesareplacedinthe6o’clockpositiontofacilitatedrainingaftereachpumpcycle(topreventfreezinginareasofthestatewherethatmayoccurortopreventbuild-upofmicrobialgrowthinsidethelaterals),theymusthavesomemechanismtobreaktheflow(anorificeshieldthatdrains,apadofgravel,etc.).
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Orificeposition: Considerations:
6o’clockdownposition
Whensomeoralloftheorificesareinthe6o’clock,or"down"position,thelateralswilldrainbetweendosecycles,thusretardingbiologicalgrowthandreducingfreezeuppotential.
Althoughsystemswithsomeoralloftheorificesinthe“down”positionmaybelesspronetoclogging,theyalsowillrequirealargerdosevolumetopressurizethesystem,duetolateralsdrainingbetweenpumpcycles.
Table12:Lateralorificepositions
LateralOrificeDiameters
Ingeneral,smallerorificesarepreferredforonsitesystems.
Theminimumorificediameteris1/8inch.Largerorificesmaybeused,butcautionshouldbeusedwhendesigningsystemswithlargerorifices.Theywillincreaseflowrates,thusrequiringtheuseoflargerpipesandlargerpumps.Largerpipesandpumpsincreasetheinitialcostofthesystemandresultinsystemsthataremoreexpensivetooperate.
Thefollowingorificediametersaresuggested:
Orificediameter: Uses:
1/8inch Usedinallalternativesystems&pressurizedtrenches
5/32inch Typicallyusedinpressurizedtrenches
3/16inch Usedinmoundsorpressurizedtrenches
1/4inch Canbeusedinmounds(butgenerallynotrecommendedforuse)
Table13:Lateralorificediameters
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ResidualPressure(Head)Requirements
Residualpressuresaredeterminedbymeasuringsquirtheight,thatis,theheightachievedbytheliquidinapressurizedlateralwhenanorificeispositionedsuchthatthedischargeisverticalintotheatmosphere,typicallyexpressedinfeetofheight.
Thefollowingresidualpressuresarerecommended,basedonorificediameters:
Orificediameter: Residualpressure:
1/8inch 3to5ft
5/32inch 2to4ft
3/16inch 2to3.5ft
1/4inch 2to2.5ft
Table14:Residualpressure(head)
LateralOrificeFlowRate
Theactualflowratefromeachorificeisrepresentedbytheequation:
Qo=11.79d2h0.5
where:
Qo istheorificeflowingallonsperminute
d istheorificediameterininches
h isthedischargeheadinfeet(alsocalledresidualpressureorhead)
Thereareotherfactorsthataffectaccuratecalculationoftheorificeflowrate,suchasaccuratedrillingofholes,classofpipe,sizeofpipe,andslightvariationsinthefrictioncoefficientsusedforfittings.
Thechoiceofcoefficienttouseinadesigncanvary,dependingontheexperienceofthedesignerinbeingabletopredictaccuratelyandcontrolforthefrictionlossesandothervariablesofconstructionandmanufacture.Thetwomostcommoncoefficientsusedare11.79and12.38.
Formanydesigns,experiencehasshownthatuseofaslightlyhighercoefficientintheequationmoreaccuratelypredictstheactualflow.
Forwhichevercoefficientisselected,itiscriticallyimportantthatthesamecoefficientbeusedthroughoutthedesign.
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Examplesoforificeflowratesingallonsperminute(gpm),using11.79asthecoefficient,include:
Orificediameter: Squirt: Flowrate:
1/8inch 5ft 0.41gpm
5/32inch 3.5ft 0.54gpm
3/16inch 3.5ft 0.78gpm
1/4inch 2.5ft 1.17gpm
Table15:Flowratecalculations
LateralOrificeShields
Orificeshieldsaredevicesusedtoprotectorificesfromexternalblockagesandtodeflectthesquirtoverawidersurfacearea,thusspreadingtheeffluentovermoreoftheinfiltrativesurface.
Theuseofshieldsisrecommended,evenwhenthesystemisinstalledingravel,andespeciallywhenorificesareorientedinthe12o-clockposition.Theshieldsmustbestrongenoughtowithstandtheweightofthebackfillandlargeenoughtoprotecttheorificefrombeingpluggedbypiecesofgravel.
Orificeshieldsmaybethehalfpipedesign,thelocalcaptype,oranotherdesignthataccomplishesthesameendresult(Figure8).
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Pressure line in 6" PVC 1/2 shell braced to prevent line shifting.
Cover Soil
Lateral Gravel
6" PVC cut in half
Pressure line suspended per manufacturer specifications. Orifices must be oriented in the 12:00 position
Chamber Lateral
Cover Soil
Pressure line to be cross braced to prevent line shifting. Orifices must be oriented in the 12:00 position
Lateral
Cover Soil
Chamber
Orifice covered by 2”- 6" PVC pipe cut in 1/2
Cover Soil
Gravel
Orifice with Cap Trench Detail
Orifice capLateral
Cover Soil
Gravel
Orifice with Cap Trench Detail
Orifice with Cap Trench Detail
Original Ground Surface
Original Ground Surface
Original Ground Surface
Original Ground Surface Original Ground Surface
Gravelless Trench Detail Gravelless Trench Detail
Lateral Orifice shield
Figure8:Orificecapsandshields
CleanoutandMonitoringofLaterals
Alllateralsmusthaveaccessforcleanoutsandmonitoringportstothelateralendsfromthegroundsurface,suchasthroughasmalllandscapingbox(Figures9Aand9B).Designsmustincludedetailsofmonitoringandcleanoutportsandexplainhowtheyaccomplishtherespectivetasks.
METERBOXOROTHERENCLOSURE
BACKFILL
MEDIA
ORIFICESHIELD
THREADEDCAP
LATERAL
Figure9A:Cleanoutport
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THREADEDCAPORPLUG
PLUGINSLEEVE 6"PVC
LASTORIFICE;WITHORIFICESHIELDSIFORIFICEORIENTATIONISUPWARD
PRESSURELATERALASSPECIFIED
DRAINROCK;6"MIN.BELOWPIPE
6"PVCWITHDRAINHOLES;EXTENDTOBOTTOMOFGRAVELTOMONITORPONDING
UNDISTURBEDSOIL
PVCHOSEORLONGSWEEPELBOW
BACKFILLMATERIAL
INFILTRATIVESURFACE
VALVE(OPTIONAL)
Figure9B:Cleanoutport(example)
Components: Considerationsforcleanoutandmonitoring:
Lateralaccess Somelocalhealthdepartmentshavespecificrequirementsforlateralaccess.Thedesignershouldconsultwiththelocalpermittingauthorityandspecifytheappropriatefittingsinthedesign.Theaccessboxshouldbelargeenoughtoallowaccesstocaps,plugs,orvalveswithhands,tools,etc.
Wideswingfittings Lateralsmusthavewideswingfittingstowardsthesurfacefortheinstallationsofapipebrushorothermaintenancetools.
Theuseoftwo45-degreeelbowsorwidesweeping90-degreeelbowsatthelateralendsisrecommended.
Plugorcap Theendsmusthaveaplugorcapthatiseasilyremovedformaintenanceandformonitoringlateralresidualpressure(squirtheight).
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Components: Considerationsforcleanoutandmonitoring:
Monitoringports Monitoringportsshouldbeopenandslottedatthebottomandbevoidofgraveltotheinfiltrativesurfacetoallowvisualmonitoringofpossiblestandingwaterontheinfiltrativesurface.
Shutoffvalve Ashutoffvalveisofteninstalledatthelateralends.
Insomecases,theremayalsobeashutoffvalvelocatedatthebeginningofthelaterals.Thismaybedoneintheindividualtrenchorinavalvebox.
Thebenefitofinstallingthevalvesontheinletsideofthelateralsistofacilitatemaintenanceandtroubleshootingandtoassistincontrollingflowsonslopingsites.Theydoincreasetheoverallcostofthesystemandarenotmandatory.
Table16:Cleanoutandmonitoringoflaterals
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2.0 PressureDistributionDesignforSpecialConditions
Specialcaremustbetakenwhendesigningpressuredistributionsystemsforuseunderfreezingconditionsoronslopingsites.
2.1. FreezingConditions
ManylocationsinUtahhavefreezingconditionsduringthewintermonths.Dependingonthespecificlocation,thefrostdepthcanrangefromafewinchestoseveralfeet.Trafficareasandareasthatareclearofsnowwillhavedeeperfrostdepthsthanareaswithgoodsnowcover.
Alldesignsinstalledinfreezingconditionsrequireproperdesignandengineeringtoensurethatthesystemdoesnotfreeze.Thefollowingrecommendationsareprovidedasaguidetoassistthedesigner.
Recommendation: Considerations:
Avoidstandingwater
Oneofthebestprotectionsagainstfreezingisdesigningthesystemsothatitdoesnotholdstandingwaterforprolongedperiodsoftime.Thisisusuallyaccomplishedwithdrainbackholesinpipeinthepumpingtank.Thepipingsystemshouldbeinstalledwiththeappropriateslopebacktothepumptankandadequatebeddingtopreventsaggingofthepipe,whichcouldresultineffluentaccumulatingandfreezingintheareaofsagging.
Theorificesinthelateralsshouldalsobeinstalledfordrainageaftereachdose.Forsystemswiththeorificesinstalledpointingdownward,drainageshouldoccurnaturally.Orificeshieldsshouldbeusedtokeeptheorificesclearandfreetodrainaftereachdoseevent.
Lateralsmaybeinstalledwithorificespointingupward(12o’clockposition)providedthatthereareseveralorificespointingdownward(6o’clockposition).Dependingonthesizeofthesystem,adequatedrainagemaybeaccomplishedwiththefirst,middleandlastorificepointeddownward.Longerlateralsmayrequiremoredownwardpointingorificestoensuredrainageaftereachcycle.
Installbelowfrostdepth
Deeperburialisespeciallyrecommendedforsystemsthathavealongforcemainorforsystemswithlargerpipediametersthatrequiremorevolumeofwatertofillthesystem.
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Recommendation: Considerations:
Insulate Pipingthatisinstalledwithinthefrostdepthandthatmayretainwatermustbeinsulated.
Insulationmustbeadequatefortheappropriatefrostdepth.
Whererigidinsulationboardistobeusedaboveaninstalledpipe,itmustextendbeyondeachsidetoprotectthepipefromfreezing.
Manifoldposition Installingthemanifoldatthehighpointinthesystemmayalsobehelpfulincoldweatherinstallations.
Thisconfigurationwillalloweffluentinthetransportpipeandsomeoftheeffluentinthemanifoldtodrainbacktothepumptank.Theremainingwaterinthemanifoldandthelateralswouldthendrainintothereceivingsystem.
Thisdesigncanbeaccomplishedwiththeuseofverticallymountedteesinthemanifoldandlateralpiping.
Withsystemsthatareveryshallow,withinthefrostdepth,suchasashallowdripdispersalsystem,themanifoldshouldbeinstalledbelowthedriptubingatadeeperdepthtoprotectagainstfreezing.
Heating Althoughaheatingsystem(heattape,lightbulbs,etc.)maybedesignedtomaintaintemperaturealongthepipes,thisdesignisusuallynotrecommended.
Table17:Recommendationsforfreezingconditions
2.2. SlopingSites
Slopingsitescanbechallengingforbothgravityandpressurizeddistributionsystems.Oneofthemainconcernsismakingsurethattheslopingsitereceivesequalamountsofeffluentthroughouttheabsorptionarea.Specifically,lowerareasshouldnotreceivemoreeffluentthantheupperareas,resultinginoverloadingorsurfacingofeffluent.
Oneofthemostcommonmethodsfordosingmultipletrenchesonslopingsitesisthedropboxmethodofserialdistribution.Withserialdistribution,theuppertrenchreachesasaturatedconditionbeforeoverflowingtothelowertrenches.Withpumpingtothehighpointofthesystem,asimplemanifoldorsplittermechanismcanbeinstalledthatwillequallysplittheflowintoequalvolumesthatcanbedirectedtotheindividualtrenches.
Ifapumpisrequiredtolifttheeffluenttothehigherelevationoftheabsorptiontrenches,thepumpingsystemcouldalsobeusedtopressurizetheentiredistributionsystemoflaterals.Researchhasshownthatequaldistributionovertheentireinfiltrativearea
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promotesimprovedperformanceofthesystem,alongerlifeofthesystem,andbettertreatmentoftheeffluent.
Wherepressurizedtrenchesareinstalledonaslopingsite,thesystemmustbesizedtolifttheeffluenttothehighestpointandmeettherequiredsquirtheight.Whenlateralsareinstalledatvaryingelevations,thelowertrenchesmaydischargeeffluentathigherflowrates,anddependingonthedifferenceinelevation,thelowertrenchescanbeeasilyoverloaded.
Thereareseveralmethodsforadjustingdistributionofeffluenttothedifferentelevationsoflaterals.
• Valvesatthebeginningofthelateralsmaybeused,withgatevalveslesslikelytochangeduetosystemcycling
• Pipediametersmaybeadjustedtoequalizeflowsatthedifferentelevations
• Flowcontroldiscsmayalsobeused.However,itmaybedifficulttocalculatethecorrectsizeoforificesforthediscstoensurethatequaldistributionbetweentrenchesoccurs.Additionally,constructionchangesinelevationwillrequirerecalculationoftheflowcontroldiscorificesizes
• Deliveringtheeffluenttothehighpointofthesystem(Figure4B)willminimizeoverloadingofthetrenchesbecausetheeffluentfromtheuppertrenchescannotdraintothelowertrenches.
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3.0 PressureDistributionDesignProcess
Thepressurizeddistributionsystemmustbesizedappropriatelyforthedesignflowsofthesystem.
Criticaldesignflowsthatwillaffecttheappropriatedesignforaparticularsystemincludethedailydesignflowandtheoperationaldesignflow.Operationaldesignflowsareafunctionoftheproposeddistributionsystem.Therearemanycorrectdesignapproachesforaparticularsituation,providedthatsomesimpledesignstepsarefollowed.
Overall,thedesignflowandthetotaldynamicheadarecalculatedandusedtodesignthecriticalcomponentsofapressurizeddistributionsystem.Thedesignflowistheestimatedvolumeofwastewaterperunitoftimeforwhichthesystemisdesigned,andthetotaldynamicheadisthemeasureofthecumulativeenergythatapumpmustimparttoaliquidtomoveitfromonepointtoanother,consistingofthesumoffrictionhead(asbaseduponpipingdiameter,systemconfiguration,andflowrate)andthestatichead(thesumofelevationheadandoperatingpressure).
ManypumpandonsitesystemmanufacturersoffersoftwarethatwillperformthedesigncalculationsforthedesignerusingthehydraulicequationsandthehydraulicperformancesoftheirparticularsystemcomponentsthataregivenintheDesignWorksheet.
Tofacilitatetheappropriatedesignapproach,thePressurizedDistributionDesignWorksheetinAppendixAmaybeused.AsummaryoftheWorksheetdesignprocessisincludedinthissection,withsupplementalexplanationsforeachstep.
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Designstep: Discussion:
Step1:
Determinethedailyflowrate
Thedailyflowrateisthemaximumflowofwastewaterthatthesystemwillreceiveina24-hourperiod.
Onsitewastewatersystemsforsingle-familyresidencesusingconventionalabsorptionsystemsaresizedbasedonthenumberofbedroomsinthehome.Inpressurizedsystems,thedailydesignflowisdefinedasgallonsperdaydistributedthroughthesystem.
Additionally,thedesignflowratemustalsobedetermined.Thedesignflowrateisnotthesameasthedailydesignflowbutistheflowrateofthepumpingsystemwhileinoperation.
Thedailydesignflowforpackedbedsystems,accordingtoUtahAdministrativeCodeR317-4,isestimatedas300gallonsperday(gpd)forthefirsttwobedrooms,plusanadditional100gpdforeachadditionalbedroom.Absorptionsystemsandmoundsystemsaredesignedusing150gpd/bedroom.
Forsystemsotherthansingle-familyresidences,thedailyflowrateisdeterminedusingtheproceduresoutlinedinUtahAdministrativeCodeR317-4.
Forpressurizedsystems,flowpatternsthroughoutthedayandparticularlythroughouttheweekcanbeanimportantconsiderationinsystemdesign.Theuseofasurgeorequalizationtankmayberequiredtohandlepeakflows.
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Designstep: Discussion:
Step2:
Determinethemaximumloadingrate
Theloadingrateisdefinedastherateatwhichthewastewaterisappliedontotheabsorptiontreatmentarea.
Forpressurizedtrenchesforresidentialandnon-residentialsystems,selecttheloadingrateusingguidancefromR317-4.
ForthealternativewastewatertreatmentsystemsdefinedinUtahAdministrativeCodeR317-4,themaximumloadingrateisbasedontheparticulartreatmenttechnology:
• Moundsystems=1.0gal/sq.ft./day
• Intermittentsandfilter:Sandmedia=1.0gal/sq.ft./day;Sandfill=1.2gal/sq.ft./day
• Recirculatingsandfilter=5.0gal/sq.ft./day
• Recirculatinggravelfilter=15.0gal/sq.ft./day
• Textilefilter=30gal/sq.ft./day
• Peatfilter=5.0gal/sq.ft./day
• Syntheticpolystyrenemediafilter=21gal/sq.ft./day
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Designstep: Discussion:
Step3:
Determinetherequiredabsorptiontreatmentarea
Therequiredabsorptiontreatmentareaisspecifictothetreatmentmediumthatreceivesthewastewater.
1)Forpressurizedtrenchesinsystemswithoutpretreatmentofeffluentsinpackedbedsystems,therequiredsizeoftheabsorptiontreatmentareaisdeterminedusingthesizingtableinR317-4.
2)Whenpressurizedtrenchsystemsareusedtodisperseeffluentfrompackedbedsystems,theymaybereducedinsizeaccordingtotheguidelinesgiveninR317-4.
3)Inmoundsystems,theabsorptiontreatmentareaisthegravelbedinwhichthedistributionpipesareplaced.
FormoundsystemstherequiredtreatmentareaisdefinedasAxB,whereA=absorptionareawidthandB=absorptionarealength.
4)Forapackedbedsystem,thetreatmentareaisthesurfaceareaofthesystem.Thetreatmentareamayconsistofsand,gravel,textile,orpeat,dependingonthetypeofpackedbedsystem.
Thedailydesignflowisusedtodeterminetherequiredareaformounds,packedbedsystems,andpressurizedtrenchesfornon-residentialsystems.Theminimumrequiredsurfaceareaiscalculatedusingthefollowingequation:
MinimumRequiredSurfaceArea=DailyFlowRate,gpd(Step1)/MaximumLoadingRate,gpd/sq.ft(Step2)
Step4:
Sketchthedimensionsofthetreatmentareafromsite-specificinformationobtainedfromthesiteevaluationprocess
Theconfigurationandsizeofthesoiltreatment/infiltrativesurfaceisdependentonthesoilandsitecriteriaandlimitationsofthespecificsite.Oncethedimensionshavebeenestablished,thedistributionnetworkcanbedesigned.
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Designstep: Discussion:
Step5:
Selecttheorificediameter
Theorificediameterwilldirectlyimpactthedesignflowrate.Largerorificeswillresultinlargerflowratesperorifice,evenwithalowersquirtheight.
Historically,largerorificeswererecommendedasaresultofconcernsthatwastewaterwouldeitherplugorificeswithsolids,and/orgrowthontheinsideofthepipewouldplugtheorifices.Pressurizeddesignsthatuselowheadpumpswillnotbeabletodeliverthenecessarypressureevenifonlyminimalpluggingoccurs.However,routinemaintenanceofthesystempreventscloggingproblems.Additionally,usingsmallerorificesoftenoffsetstheconcernofpluggingoforificesbecausesmallerorificesallowsmallerdoses,whichimprovesthelifeandperformanceofthesystem.
Guidelinesfortheselectionoforificediametersinclude:
• 1/8inchorificesareacceptableforanyoftheapprovedalternativewastewatersystems.
• 5/32inchorificesaretypicallyusedforpressurizeddrainfieldtrenches.
• 3/16inchorificescanbeusedinmounds,especiallywhenlowheadpumpsareinstalled.
• 1/4inchorlargerorificesarenotrecommendedformostonsitesystems.
Step6:
Selectthesquirtheight
Thesquirtheightrecommendationsweredevelopedtoensurethatthesystemwilldosethecorrectamounteachcycleandtominimizecleaningoftheorifices.
Thefollowingsquirtheightsarerecommendedbasedonorificediameter:
• 1/8inchorifice=3ft.to5ft.
• 5/32inchorifice=2ft.to4ft.
• 3/16inch=2ft.to3.5ft.
• ¼inch=2.5ft.
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Designstep: Discussion:
Step7:
Determinetheorificeflowrate
Theorificeflowratecancalculatedusingthefollowingequation:
Q=11.79*d2*(h)½
Where:
Q=Orificeflowrate,gpm
d=Orificediameter,inches
h=Squirtheight,ft.
Anothercommonlyusedcoefficientusedinsteadof11.79is12.38.
Usingtheaboveequationwith11.79asthecoefficient,thefollowingflowratescorrespondtotheorificediametersasfollows:
1/8inchorificewith5ft.squirt=0.41gpm
5/32inchorificewith3.5ft.squirt=0.54gpm
3/16inchorificewith3.5ft.squirt=0.78gpm
1/4inchorificewith2.5ft.squirt=1.17gpm
AdditionalflowratesfororificediametersandsquirtheightsaregiveninAppendixB,TableB-5:Orificeflowrates.
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Designstep: Discussion:
Step8:
Selecttheorificespacing
Orificespacingdeterminestheapplicationrateoveragivensurfacearea.
Fortrenches,theorificespacingwilllikelybegreaterthanformoundsandpackedbedsystems.However,thedesignershouldspacetheorificesasclosetogetheraspracticaltoprovideequalloadingthroughouttheentiresystem.Mosttrenchdesignswillhaveanorificeevery2feetto4feetalongthepressurizedlateral.
Formoundsandpackedbedsystems,theorificespacingshouldbesettoprovideforequaldistributionwithintheareaofinfluenceofeachorifice.Theproperapplicationofthisprinciplewillresultinsquareareasofinfluence,thatis,equalorclosetoequalspacingbetweentheorificesandthelaterals.
Theserecommendationsareprovidedasaguideforsettingthespacingforeachtypeofalternativesystem:
1orifice/6sq.ftformoundsystems
1orifice/4sq.ftforintermittentsandfiltersystems
1orifice/4sq.ft.orlessforrecirculatingsandfiltersystems
1orifice/4sq.ft.orlessforrecirculatinggravelfiltersystems
1orifice/2sq.ft.fortextilesystems
Forpressurizedtrenches,orificesaretypicallyplacedevery2to4feetalongeachpressurizedlateral.
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Designstep: Discussion:
Step9:
Determinethenumberandlengthoflaterals
Thenumberandlengthoflateralsaredependentonthespaceavailableforthesystemandaresite-specific.UsingthesketchofthesystemcreatedinStep4andtheorificespacing,thedesignershouldselectlateralplacementthatpromotesequaldistribution.
Whenmultiplelateralsareusedwithinthesameinfiltrativesurface,thelateralsandorificesshouldbeplacedtoprovideequilateraldistribution(equalspacingofthelateralsandorifices)oftheeffluent.
Thenumberoflateralsisallofthelateralsinthesystem.Thenumberoflateralsdosedbypumpisthenumberoflateralsdosedwhenthepumpruns.Itisthesameasallofthelateralswhenzonesarenotused.Itisthenumberoflateralswithinthezonewhenzonesareused.ThisnumberisusedfordeterminingthedesignflowrateofthepumpinStep14.
Lateralsshouldextendtowithin6inchesto1footoftheendoftheabsorptionarea.
Thedistancefromthelateralstotheedgeoftheinfiltrativeareashouldbe6inchesto1footforbedareasand1footto1.5feetfortrenches.
Step10:
Determinethenumberoforificesineachlateral
Thenumberoforificesineachlateralisafunctionoftheorificespacingandthelaterallength.
Thefollowingequationshouldbeusedtodeterminethenumberoforificesineachlateral.
Numberoforifices=(laterallength/orificespacing)+1
Afractionremainingasaresultofthecalculationisaccountedforbydisregardingthefractionandaddinganadditionalorifice.
Step11:
Determinethelateralflowrate
Theorificeflowrateismultipliedbythetotalnumberoforificesinalateraltodeterminethelateralflowrate.Thefollowingequationisused:
(Orificeflowrate)x(Numberoforifices)=Lateralflowrate(gpm)
Thelateralflowrateistheamountofwaterneededtoprovideeachorificewiththeflownecessarytoprovidethedesignsquirtheight.
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Designstep: Discussion:
Step12:
Determinethelateralpipediameter
Lateralsizingisacriticalstepinthedesignprocess.Failuretosizethelateralcorrectlycanresultinunevendistribution.
Thelateralsmustbesizedlargeenoughtoprovideflowsthatareequalthroughoutthelengthofthelateral.
Theorificesatthebeginningofapressurizedlateralwilldischargeatahigherratethanattheendofthesamelateral.Theproperlysizedlateralwillminimizethisdifferencetopromoteequaldistribution.
Themaximumdifferencebetweenthefirstandlastlateralorificeshouldbelessthan10%oftheorificeflowrate,or21%ofthesquirtheight.
Thefollowingtablegivestheactualsquirtheightdistancescorrespondingtoa10%flowdifferenceforselectedsquirtheights:
ResidualSquirtHeight 10%FlowDifference 2feet 5inches 2.5feet 6.3inches 3feet 7.6inches 3.5feet 8.8inches 4feet 10inches 5feet 12.6inchesGraphsB-1toB-8inAppendixBareusedtoselecttheappropriatelateralpipediametersize.Selectionoftheappropriategraphisdependentontheorificesizing:
1/8inchorifices UseGraphB-1orB-2
5/32inchorifices UseGraphB-3orB-4
3/16inchorifices UseGraphB-5orB-6
1/4inchorifices UseGraphB-7orB-8
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Designstep: Discussion:
Step13:
Determinethelateralheadloss
Therearemultiplemethodsfordeterminingtheheadlosswithineachlateral.Simplifiedmethodsproduceresultsaccurateenoughforonsitesystems.
Thetwomethodsdescribedbelowallowanapproximatesolutionwithouttheuseofmorecomplexhydrauliccalculations.Othermethodsmaybeacceptableprovidedthatadequateinformationisprovidedforthereviewingauthoritytoverifythedesign.
Method1:Use1/3ofthesquirtheight(inft.)selectedinStep6.Thiswillusuallybeaconservativeapproach,providedthattheotherstepsareeachfollowedcorrectly.
Method2:Calculatetheheadlossbasedonasolidpipe1/3ofthelengthoftheperforatedlateralpipedeterminedinStep9usingAppendixBTableB-6:Frictionalheadlossper100feetofsolidpipe.Thisapproachisconservativewhencomparedtotheactualheadlosseswithintheperforatedpipe.
Step14:
Determinethedesignflowrate
Thedesignflowrateingallonsperminute(gpm)isthecombinedlateralflowforallofthelateralsthataredosedatagiventime.
Forthetypicalsingle-familysystem,thedesignflowratewillusuallybetheflowfromallofthelateralsinthesystem.Forlargersystemsthataredividedintozones,thedesignflowrateincludesallofthelateralsinazone.
NumberoflateralsxLateralflowrate=Designflowrate
Thedesignflowrateisusedinpumpselection.
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Designstep: Discussion:
Step15:
Determinethediameterofthemanifold
Themanifolddiametershouldbelargeenoughtosupplyflowtoallofthelaterals.
Forsmallsystems,suchasatypicalsingle-familyresidentialsystem,themanifoldmaybethesamediameterasthelaterals,oritmaybethesamesizeastheforcemainpipe.Whenthemanifoldpipelengthsarerelativelyshortcomparedtotheoverallpipelengthsusedfortheforcemain,itmaybeacceptabletosimplifythemanifoldpipesizingtospecifythatthemanifoldbethesamepipediameterastheforcemainpipe.
Forsomesystems,themanifolddiametermaybebetweenthesizeoftheforcemainandlateralpipes.
Twoacceptablesimplemethodsfordeterminingthemanifoldpipediameterare:
Method1:Usethesamediameterofpipeusedfortheforcemain.
Method2:UsetheheadlosscalculatedforthemanifoldinStep16todeterminethebestpipesizediametertobeusedforthemanifold.Becausetheflowisbeingdispersedintoeachlateralacrossthelengthofthemanifold,itisacceptabletouseaflowrateequalto½ofthedesignflowratewhencalculatingthemanifoldheadloss.Thetotalmanifoldheadlossesshouldalwaysbelessthan40%ofthetotaldynamichead(TDH),andthediametershouldbeassmallaspossible.Wherethisisnotthecase,alargerpipesizeshouldbeused.
Step16:
Determinethemanifoldpipeheadloss
Theheadlossinamanifoldpipeisthesameasforasolidpipe,suchasaforcemain.Theheadlossisafunctionoftheflowrate,thepipesizediameter,andthepipesmoothnesscoefficient(c-value).
TheHazen-Williamsequationforwatermaybeusedtodeterminethisfrictionalloss.
Tosimplifythisprocess,AppendixBTableB-6:Frictionalheadlossper100feetofsolidpipemaybeused.
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Designstep: Discussion:
Step17:
Determinetheforcemainlength
Theforcemainlengthisthetotalpipelengthfromthepumpdischargetothebeginningofthemanifold.
Thislengthisnotthesameasthehorizontaldistancefromthepumpvaulttothedischargepoint.Thislengthissite-specificandisdeterminedforeachproposedsystemaspartoftheoverallsystemlayout.
Step18:
Determinetheforcemaindiameter
Thediameteroftheforcemainisafunctionofthedesignflowrateandtheforcemainlength.
Thedesignershouldselectthesmallestacceptablepipesizediameter,forsmallerpipediameterswillprovidehighervelocitiesduringadose.Smallerpipediameterswillalsoreducetheamountofpumpingforsystemswithdrainbackorificesthatprotectagainstfreezing.Additionally,thesmallerpipeswillfillwithwaterquickerduringadoseandwillcometopressurequicker,whichleadstofasterequaldistributionthroughoutasystem.
Thelimitingfactorinselectingsmallpipediametersistheheadlossthroughtheforcemain.
Forsmallsystemsthathaveshortforcemainlengths,thehigherheadlossperlinealfootofpipeismoreacceptablethanforasystemthathasaverylongpipelengthatthesameheadlossperlinealfoot.
Thedesignershouldalsobeawareoftheavailableheadlossthatatypicalpumphascapacitytodeliver.Forsomedesignsthisavailableheadlosswillbecritical.Otherdesignsmaybeabletoexperiencehighheadlosswithminimalimpactonpumpselection.
Oncethedesignflowrateisknownandthelengthoftheforcemainisdetermined,AppendixBTableB-6:Frictionalheadlossper100feetofsolidpipeisusedtoselectthesmallestpipesizediameterthatwillstillmaintainanacceptableoverallheadloss.
Step19:
Determinetheforcemainheadloss
TheHazen-Williamsequationforwatermaybeusedtodeterminethisfrictionalloss.
Tosimplifythisprocess,AppendixBTableB-6:Frictionalheadlossper100feetofsolidpipemaybeused.
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Designstep: Discussion:
Step20:
Determinemiscellaneousheadlosses
Everysystemhasanumberoffittingsandvalvesthatincreasetheheadlosstothesystemasawhole.Thesefittingsandvalvesmustbeincludedinthemiscellaneousheadlosstotal.Therearetwomethodsthatcanbeusedtodeterminetheselosses:
Method1:Add50%oftheforcemainheadlosstoaccountforfittings.
Thisisaconservativeapproachformosttypical,single-familyresidentialsystems.Cautionshouldbeemployedinusingthisapproachforlargersystemsorforsystemsthathavealargenumberoffittings.Whenconcernsariseregardingtheapplicabilityofthisapproach,itisrecommendedthatMethod2beused.
Method2:Determinethe“equivalent”pipelengthsforeachofthefittingsinthedesignanduseAppendixBTableB-7:Frictionallossesthroughplasticfittingstodeterminetheheadlossassociatedwiththefittings.
Frictionalheadlossesassociatedwithaparticularfittingcanberepresentedasanequivalentpipelength.Thismethodassignsalengthofstraightpipeofthesamediameterthatequalstheheadlossthatoccursthroughthefitting.Manufactureroffittingscanprovidethisinformation.Additionally,therearetablesthatcontainthisinformationforthetypicalfittingsusedinanonsitesystem.AppendixBTableB-7:Frictionallossesthroughplasticfittingsprovidesheadlossesforsomeofthemostcommonlyusedfittings.
Thetwoexamplespresentedbelowcanbeusedasaguidefordetermininghowtobestaccountformiscellaneousheadlosses:
Example1:Asmallerforcemainpipediameterresultsingreaterheadloss.Iftheforcemainpipelengthislongandthediameterissmall,thehigherheadlossforthepipeandthelonglengthwillbothincreasetheheadlosscalculatedfortheforcemainpipe.Whenusingthe50%methodabove,itispossiblethattheheadlosscalculatedinMethod1willbemuchhigherthandesired.
Example2:Somesystemswillhaveseveralfittingsduetothesite-specificconditions.Forasystemwithmanyfittings,theuseofMethod1or2maynotaccuratelyaccountforthefittingsinthedesign.Changesmadebyacontractorduringinstallationmayalsoincreasethenumberoffittingsinaparticulardesign.Wheneitheroftheseconditionsoccurs,andifthefittingscreateheadlossabovewhatisestimated,thesystemmaynotperformasdesigned.
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Designstep: Discussion:Amanufactured,pre-assembleddischargeassembly,whichconsistsofallpipingandpartsbetweenthepointofpumpdischargetothepointatwhichthesupplylineexitsthetankandusedtoconveyeffluentfromapumptotheexteriorofariserorpumpbasinorchamber,maybeusedinapressurizedsystem.
Whenusingamanufactureddischargeassembly,informationonheadlossthroughthedischargeassemblycanbeobtainedfromthemanufacturer.Usingthisinformationwillprovideamoreaccurateheadlossmeasurementthanusingeitherofthetwosimplifiedmethodsdescribedabove.
Step21:
Determineheadlossassociatedwithazonevalve
Iftheproposedsystemwillusemultiplezones,thenthesystemwilllikelyrequiretheuseofoneormorezonevalves.Dividingthedistributionareaintozonesisusedtomaintainareasonablysmallpumpsizewhenmanyorificesaretobedosed.Dividingthedistributionsystemintozoneswillalsodistributethehydraulicloadovertimeaswellasspace,allowingforlongerrestingtimes.
Azonevalvemaybeamechanicalrotatingvalve,asolenoidvalve,orothermechanismforcontrollingtheflowfromonezonetoanother.Thisvalvewillhaveaheadlossassociatedwiththeflowpassingthroughthevalve.
TheheadlossthroughthevalvewillbemorethantheamountaccountedforinthemiscellaneousheadlossesstepdiscussedinStep21.Therefore,whenasystemutilizesoneormorezonevalves,theheadlossforthevalve(s)mustbecalculatedandaddedtothetotalheadloss.
Themanufacturerofaspecificvalvewillhaveanequationand/orachartfordeterminingtheheadloss.Theheadlosswillbeafunctionofthevalvesizeandthedesignflowratethatwillpassthroughthevalveeachtimethesystemdoses.
Step22:
Determinetheelevationheaddifference
Theelevationheaddifferenceisthedifference(inft.)inelevationfromthelowwaterlevelinthepumptanktothedischargepoint.
Thisisusuallyapositivevalue,butforsystemswithadischargepointbelowthepump,itmaybeanegativevalue.Ifthedischargeisbelowthepump,theuseofananti-siphoningdeviceisnecessary.
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Designstep: Discussion:
Step23:
DeterminetheTotalDynamicHead(TDH)
Thetotaldynamichead(TDH)(inft.),whichisusedtosizeandselectthepump,isthesumofthefollowingheadlosses:
Squirtheight (Step6)
Lateralheadloss (Step13)
Manifoldheadloss (Step16)
Forcemainheadloss (Step19)
Miscellaneousheadloss (Step20)
Zonevalveheadloss (Step21)
Elevationheaddifference (Step22)
Step24:
Selecttheappropriatepumpsizingcriteria
ThepumpspecifiedandinstalledinthesystemmustbesizedbasedonthedesignflowrateandthecalculatedTDHforthesystem.
Ifchangestothedesignaremadeduringinstallation,theywilllikelychangethesystemcalculationsforflowand/orTDH.Therefore,thedesignershouldclearlydocumentthedesignbasisandallcalculations.
Thedesignflowrate(ingpm)determinedinStep14isusedforpumpselection.TheTDH(inft.)requiredforthepumpisdeterminedinStep23.
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Designstep: Discussion:
Step25:
Determinetheapplicabledosevolume
Thesystemdosevolumeistheamountofeffluentthatthepumpwilldeliverduringasinglecycleevent.Thisvolumewillincludethedoseappliedtotheabsorptionareaaswellasanyvolumerequiredtofillthepipenetwork.
Themaximumdosevolumeforanypumpeventshouldbenogreaterthan10%ofthedailydesignflow.Smallerdosevolumesarepreferred.Thiswillresultisabout5dosesperdayforthetypicalaveragedailyflow.AppendixBTableB-8:Voidvolumeforvariousdiameterpipesisusedtocalculatepipevolumesbasedonpipediameter.
Whentimed-dosingisused,itwouldbeappropriatetohavemorefrequentdosesappliedduringtheday.Smallerdoseswillprovidemoredosesduringa24-hourperiodandmayresultinbetterperformanceoftheonsitewastewatersystem,whichmayleadtoalongerdesignlife.Therefore,thesystemshouldbeabletoprovidedosesthataresmallenoughtoprovidemultipledosingevents,spreadevenlyovertime,duringtheday.Formostsystems,thiswillbeadosevolumeof5%orlessforeachdosingevent.
Oncethetargeteddosevolumehasbeenchosen,theactualpumpingdosevolumemustbedetermined.Forsystemsinstalledincoldweatherconditions,withdrainbackorifices,theforcemainpipingandmanifoldnetworkwillneedtobefilledduringeachpumpcycle.Thevolumeofthesepipesshouldbeaddedtothedosevolume.PipevolumesareprovidedinAppendixBTableB-8:Voidvolumeforvariousdiameterpipes.
Forademand-controlledsystem,thefloatsaresetinthedosetankwiththeappropriatespacingbetweenthepumponpositionandthepumpoffpositiontodelivertheselecteddosevolume.
Fortimer-controlledsystems,thepumprateneedstobedeterminedbymeansofadrawdowntestormeter.Usingthepumpflowrateoftheinstalledsystem,thetimer“on”settingcanbedeterminedtodelivertheselecteddosevolumeforeachpumpingevent.
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Designstep: Discussion:
Step26:
Developasystemperformancecurve
Thesystemperformancecurvepredictshowthedistributionsystemwillperformundervariousflowratesandheads.
Theflowrateisaresultofthetotalheadthatthepumpworksagainst.Astheheadincreases,theflowratedecreases.Theflowratedeterminesthenetworkpressureandthustherelativeuniformityofdischargethroughoutthedistributionnetwork.
Thebestwaytoselectthepumpistoevaluatethesystemperformancecurvevs.thepumpperformancecurve.Wherethetwocurvescrossiswherethesystemwilloperaterelativetoflowrateandhead.
SystemevaluationinvolvescalculationsthatareexplainedstepbystepinAppendixA.Pumpperformancecurvesaresuppliedbypumpmanufacturers.
Plotthesystemheadcurveandpumpcurvetogethertodetermine:
1. Wherethepumpwilloperateonitscurve
2. Whatchangeswilloccurifthesystemheadcurveorthepumpperformancecurvechanges
Table18:Designsteps
Figure10:Systemandpumpperformancecurves
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4.0 PressureDistributionDesignSubmittalRequirements
Suggestedinformationthatshouldbeprovidedinthesystemdesignplansincludes:
• Allpumpcalculationandresultsnecessarytodocumentthatthesystemisdesignedandsizedfortheappropriateflowsmustsubmitted.Informationonhowthedailyflowratewasestimatedshouldalsobeincluded.
• Thedesignshouldclearlyshowtheplacementoftheequipmenttobeinstalled.
• Componentsthatarecriticaltotheoperationofthesystem,suchaspumps,floats,controlpanels,effluentfilters,etc.,shouldbeclearlyspecifiedinthedesigntoensurethattheproperequipmentisinstalled.Adequateinformationshouldbeprovidedforthecontractortounderstandwhatistobeinstalledaswellastheinspectortoverify.
• Pumpingsystemsrequireaccessfromthefinishedgroundsurface.Knowledgeofappropriateequipmentneededforasafeinstallationthatprotectstheenvironmentandpublichealthmaybeunfamiliartothecontractorandtheinspector.Thedesignershouldincludedetailsanddrawingsinthedesignthataddresshowtheaccesstogroundsurfaceistobeachievedinasafemannertopreventunauthorizedaccess,especiallybychildren.
• Electricalrequirementsfortheinstalledequipmentshouldalsobespecifiedinthedesign.
• Manyofthesiteswherepressurizedsystemsoralternativesystemswillbeusedhavesiteconditionsthatlimittheinstallationofaconventionalsystem.Inmanycasestheremayonlybeoneacceptablesolutionforthesite;thereforethedesignplansmustbefollowed.Detailsregardingthelocationofthesystemshouldbecleartoallwhoreviewtheplans.
• Whenpumpingassembliesareinstalledinatank,thedimensionsofthetankwilldictatethelocationofthepumpand/orthefloats.Therefore,thedesignermustprovidethesizeanddimensionsofthepumpchamber,basin,orvault,designatespecificcomponentstobeused,andspecifythespacingsthataretobeusedforpumpandfloatplacement.Ifalternativecomponentsareproposedforuse,thedesignerandregulatoryauthoritymustbeconsultedtoensureproperinstallationoftheequipment.Thisrequirementshouldbeclearlynotedontheplans.
• Ataminimum,thepumpspecificationsshouldalsoincludethefollowinginformation:
– Pumpmanufacturer– Modelnumber– Horsepower– Voltageandphase– Amperage(runamps,startingamps,fullloadamps)– Capacity:NumberofgpmatthespecifiedfeetofTDH– Pumpcurvewithsystemcurve
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• Ifalternativeequipmentisused,documentationoftheapprovedchange,includingwhoapprovedthechange,mustbeprovidedtothepropertyownerandincludedintherecordfileattheregulatoryoffice.
• Detailsofsystemdesignthatwerecalculatedusingthedesignspreadsheet(ordesignsoftware)shouldalsobeprovided,including:
– Septictanksize,locationandoutletinvertelevation– Pumpelevationandlocation– Forcemainlength,location,highestelevation,anddiameter– Allvalves,othercomponentsandfittingsinthesystem– Manifolddiameter,location,length,andorientation– Lateraldiameter,location,length,orientation,andelevations– Orificediameter,spacing,andorientation– Dosevolumeandfrequency– Locationanddetailofaccessportsonthelaterals.
• Auser'smanualforthepressuredistributionsystemshouldbeprovidedtothehomeowner/systemuserandthelocalhealthdepartment.Thisdocumentmaybedevelopedinconjunctionwiththeinstallerandsubmittedwiththeas-builtinformation,butthedesignerisresponsibleforpreparationofthemanual.Thecontentsoftheuser’smanualshouldinclude,ataminimum:
– Diagramsofthesystemcomponents.– Explanationofgeneralsystemfunction,operationalexpectations,owner
responsibilities,etc.– Specificationsofallelectricalandmechanicalcomponentsinstalled
(occasionallycomponentsotherthanthosespecifiedontheplansareused).– Namesandtelephonenumbersofthesystemdesigner,localhealth
department,componentmanufacturers,supplier/installer,and/orthemanagemententityorserviceprovidertobecontactedintheeventofafailure.
– Informationontheperiodicmaintenancerequirementsofthevariouscomponentsoftheonsitesystem.
– Informationontroubleshootingcommonoperationalproblemsthatmightoccur.Thisinformationshouldbeasdetailedandcompleteasneededtoassistthesystemownerorusertomakeaccuratedecisionsaboutwhenandhowtoattemptcorrectionsofoperationalproblemsandwhentocallforprofessionalassistance.
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5.0 TestingandInspectionofPressureDistributionSystemafterInstallation
Testingandinspectionofapressuredistributionsystemshouldbeconductedtoverifythatdistributionisuniformwiththerequiredminimumresidualpressure,thatthesystemisdosedatthepropervolumeandfrequency,andthatthealarmsarefunctioningproperly.
Ifproblemsareencounteredduringtesting,theinstallershouldnotifythedesignerorengineer.
Specifically,thefollowingcomponentsofapressuredistributionsystemshouldbeinspectedandverified,priortobackfill,bytheregulatoryauthority,thecontractorand/orthedesigner.
Inpreparationforinspection,thepumpchamber,vault,orbasinshouldbefilledwithwater.
• Watertighttanksmustbeinspectedandverifiedaswatertightafterinstallation,asthisisacriticalcomponentinpressurizedsystems.Ifthetankallowsinfiltrationofwaterintothetank,excessivequantitiesofgroundwaterwillbepumpedontothereceiverinfiltrativesurfaceandwilloverloadthesystem,leadingtoanearlyfailure.Infiltrationcanalsocausehighwaterusealarms.Theseproblemscanbeexacerbatedduringwetperiodsofseasonallyhighgroundwater,snowmelt,orheavyrainfall.Ex-filtrationofeffluentoutofthetankcancauselowwateralarmsunderlowornoflowconditions.
• Thepumpmustdeliverthecorrectdosetotheabsorptionarea.Fordemand-dosesystems,verificationthat"dry"floatsettingswillsendthecorrectdosetothedispersalareawhenfloatsareinwatermustbemade.Minoradjustmentsoffloatplacementmayberequired.Thedrawdownperdosemeasurementsshouldberecorded.
• Allfloatsmustbeinspectedforproperoperation.Commoninstallationerrorsincludeincorrectwiringoffloats.Careshouldbetakentoensurethatwhenthefloatismovedfromtheupordownpositionthatthecorrectsignaloccursatthecontrolpanel.
• Thefloatsshouldturnonandoffatthecorrectwaterelevationsforthehighwateralarm,“on”level,“off”level,and“redundantoff”levelasidentifiedonthedesignplan.Forsimplicityandaccuracy,theseadjustmentsshouldbemadewiththefloattreeoutofthewater(“dry”floatsettings).
• Theaudibleandvisualalarmfunctionsofthecontrolpanelshouldbeconfirmed.
• Insomeregulatoryjurisdictions,asystemmustbedesignedsuchthatthehighwateralarmdoesnotturnthepumpon.Ifthehighwateralarmturnsthepumpon,thesystemwillnotbeapproved.Highwaterlevelsthatsetoffalarmsshouldbeinvestigatedastothecauseofthecondition.Ifthecauseisduetotemporaryperiodsofhighwateruse,theexcesswaterwillbepumpedoutthroughthe
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system.Ifthehighwaterlevelsareduetoon-goingconditions,suchasleakyfixturesortoilets,thoseproblemsshouldbecorrected.
• Theinstalledpipingshouldbepressurizedtoverifythatitdoesnotleakpriortobackfill.
• Drainbacksystemsrequirereverseslopebacktothedosetankinordertoensureproperdrainagebetweenpumpevents.Beddingaroundthepipemustbeadequatetopreventsaggingofpipes,whichmayretainwaterandfreezeduringlowornoflowconditions.Anydipinthepipingmustbeleveledpriortobackfill.
• Thesquirtheightmustmeetdesignspecifications.Theuniformityofsquirtheightalongthelengthofthelateralsshouldbeevaluated.Theactualsquirtheightsatbothendsofeachlateralatthetimeofinspectionshouldberecordedifpossible.Ifthesquirtheightvariesfrominlettooutletendofthelateral,theheightdifferencemustbeevaluatedtoensurethattheflowfromtheorificesiswithin10%fromthefirstorificetotheendorifice.
SquirtheightcanbemeasuredbyattachingaclearPVCstandpipetotheendofthelateral.TheinitialsquirtheightattimeofinstallationwillbeusedduringperiodicinspectionsoverthelifeofthesystembytheO&Mserviceprovider.Theresidualheadismeasuredfromthetopofthelateralpipetothetopofthewatercolumn.
• Allaccessrisers,includinglidsandlidboltsmustbeinspectedtoverifythattheyaresecureandsafe.
• Allinstalledvalvesshouldbeinspectedandverifiedtobeworkingasdesigned.
• Otherstandardinspectionrequirementsmustalsobeconfirmed,suchascomponentsizing,locations,elevations,etc.
Timed-dosetesting
Fortimed-dosesystems,thetimerruntimesprovidedbydesignersmustbefield-testedtoseeiftheseruntimeswillsendafulldosetothereceivingcomponent.Thisdeterminationcanbeaccomplishedbyrunningthesysteminmanualandmeasuringthetimeintervalrequiredforafulldosetobepumped.Theremustbesufficientwaterinthepumpchambertorunthesetests.
• Usingthetimerequiredtopumpafulldose,itmustbeverifiedthatwhenthesystemrunsautomatically,thatitrunsforthetimerequiredtosendtheproperdosetothereceivingcomponent.Timerscanbedifficulttoset,i.e.,settingatimerto2.2minutesmaynotensurearuntimeof2.2minutes.
• Thetimer“off“timeshouldbethesameasthatspecifiedintheplanorshouldbeabletodosethesystemthecorrectnumberoftimesperday.Forinstance,ifthereceivingcomponentistoreceive4dosesperday,the“off”timeshouldbeapproximately6hours.
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Post-inspectionfollow-up
Problemsencounteredduringaninspectionmustberesolvedbythecertifieddesignerandtheregulatoryauthority.
Wiringproblemsshouldbereferredtotheelectricianwhoinstalledtheelectricalcomponents.
Anyapprovedchangestothedesignsubmittaldocumentshouldberecorded.
Informationfromthefinalinspectionshouldberecordedinanas-builtconstructiondocument.Thisinformationshouldbeprovidedtotheregulatoryauthority,thesystemowner,andtotheoperationandmaintenance(O&M)serviceprovider.
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6.0 OperationandMaintenance(O&M)Criteria&Recommendations
Permitrequirements
MostofthepermittedsystemsthatutilizepressurizeddistributionrequireanoperatingpermitfromeithertheStateofUtahDivisionofWaterQualityorfromalocalhealthdepartment.
SpecificO&Mrequirementsforaparticularsystemshouldbeidentifiedduringthepermittingandapprovalprocess.
Maintenancerequirements
Thetypicalpressurizedsystemmustbemaintainedonaregularbasis.AlternativetreatmentsystemsusingpressurizeddistributionsystemsasdefinedinR317-4requireasemi-annualinspection.
Duringthesemi-annualinspection,maintenanceobservationsandactivitiesshouldbeloggedandreviewed.Oftensmallchangesinsystemperformance,ifobservedanddocumented,canbeusedtoinitiatepreventativemaintenancethatcanreduceoreliminatefutureproblemsandexpenses.
O&Mactivitiesmayincludethefollowing:
• Conductawalkthroughoftheareawherethesystemisinstalled.Lookforanyindicationofsurfacingeffluentandalsolookforchangestothesitefromthepreviousvisittoensurethatthesystemintegrityremainsintact.
• Checkalltanksandmeasureandrecordsludgeandscumlevels.
Pumptankswhennecessary.GuidelinesforwhentopumpatankarefoundinR317-4.
Checkforsignsofleakingintanksandrisers.Lidsofrisersmustbesecure.
• Checktheinletandoutletofthetanks,includingthebafflesortees,toensurethattheyarenotdamaged,broken,clogged,ormissing.
• Removeandcleantheeffluentfilterifnecessary.Re-installafterinspectionandcleaning.
• Inspectandverifyvalvestoensurethattheyareworkingasdesigned.
• Inspectfloatsforproperoperation.Floatfailureisacommoncauseofsystemfailures.Movementofthefloatsshouldnotberestricted,andthefloatsshouldbepositionedcorrectlyandprovidepositiveinstrumentationsignals.
• Measurepumpruntimepercycleanddrawdown.Comparethesevalueswiththoserecordedintheconstructionrecordandpreviousinspectionrecords.Ifthevaluesaredifferent,evaluatethesystemforimproperlysettimercontrolsorfloatsettings,cloggedlaterals,orpluggedorifices.
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• Checkandverifyconnectionsinspliceorjunctionboxestoensurethatwhenthefloatismovedfromtheupordownposition,thecorrectsignaloccursatthecontrolpanel.Testalarmsforproperfunctioningathighandlowliquidlevels.
• Checkandverifythecontrolpanelfunctionsaccordingtotheapproveddesign.
• Measureandrecordsquirtheightandcomparetopreviousrecordingsandinitialmeasurements.Increasingsquirtheightsindicatetheneedtoflushorcleanalateralpipe.Lowersquirtheightsusuallyindicateaproblemwiththepipenetworkbutmayalsobearesultofaproblemwiththepumpsystem.
SquirtheightcanbemeasurebyattachingaclearPVCstandpipetotheendofthelateral.Thetrueresidualheadismeasuredfromthetopofthelateralpipetothetopofthewatercolumn.
• Confirmthattheaudibleandvisualalarmfunctionsofthecontrolpanelareoperational.
Allfindingsandrepairsmadeduringthesemi-annualO&MinspectionsshouldberecordedandfiledforeasyaccessandreportssenttothelocalhealthdepartmentortheUtahDivisionofWaterQuality,asrequired.
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AppendixA:PressurizedDistributionDesignWorksheet
Pleaseentertheresultsofyourcalculationsforeachstep.
AbsorptionAreaDesign
AbsorptionAreaDesignNotes: Step:
Forresidentialsystems,determinethenumberofbedroomsfordesign.Fornon-residentialsystems,determinethenumberofgallonsperdayusingguidancefromR317-4.
Forabsorptionsystemsandmoundsystems,use150gallonsperdayperbedroom.
Forpackedbedsystems,use:
Aminimumof300gallonsperdayfortwobedrooms100gallonsperdayforeachadditionalbedroom.
1. Dailyflowrate
Numberofbedrooms: ______
Totalgallonsperday: ______
Forpressurizedtrenchesforresidentialandnon-residentialsystems,selecttheloadingrateusingguidancefromR317-4
Formoundsystems,use1.0gal/sq.ft./day
Forpackedbedsystems,selectfrom:
Intermittentsandfilter:Sandmedia=1.0gal/sq.ft./day;Sandfill=1.2gal./sq.ft./day
Recirculatingsandfilter:5.0gal/sq.ft./day
Recirculatinggravelfilter:15.0gal/sq.ft./day
Textilefilter:30.0gal/sq.ft./day
Peatfilter:5.0gal/sq.ft./day
Syntheticpolystyrenemediafilter:21gal/sq.ft./day
2. Maximumloadingrate______gal/sq.ft./day
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AbsorptionAreaDesignNotes: Step:
Forpressurizedtrenches,useabsorptionareasizingtablesfromR317-4
Forpressurizedtrenchesafterpackedbedsystems,useabsorptionareasizingtablesfromR317-4andallowablereductionfactors.
Formoundsystems,usevaluesofA(absorptionareawidth)andB(absorptionarealength)fromMoundDesignWorksheet
Forpackedbedsystems,use:
Dailyflowrate(fromStep1)/maximumloadingrate(fromStep2)=requiredtreatmentabsorptionarea.
3. Requiredabsorptiontreatmentarea______sq.ft.
Forpressurizedtrenchesandpackedbedsystems,use:
Lengthxwidth=absorptiontreatmentarea
Thelayoutwillbedependentonthecharacteristicsofthespecificsite.
Formoundsystems,usethevaluesofAandBfromtheMoundDesignWorksheet(availablefromtheUtahOn-SiteWastewaterTreatmentTrainingProgram).
4. Sketchaproposedabsorptiontreatmentareaforthesystembeingdesigned,usingtherequiredabsorptionarea
PressureNetworkDesign
PressureNetworkDesignNotes: Step:
1/8inch–canbeusedonallalternativesystems&pressurizedtrenches
5/32inch–typicallyusedinpressurizedtrenches
3/16inch–canbeusedinmoundsorpressurizedtrenches
1/4inch–canbeusedinmounds(butgenerallynotrecommendedforuseinpressurizedsystemdesign).
5. Orificediameter
______inch
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PressureNetworkDesignNotes: Step:
Selectthesquirtheightusingorificediameter(Step5)
1/8inch: 3-5ft
5/32inch: 2-4ft
3/16inch: 2-3.5ft
1/4inch: 2-2.5ft
6. Minimumsquirtheight
______ft.
Determinetheorificeflowrate(SeeAppendixBTableB-5:Orificeflowrates)usingtheorificediameter(Step5)
Examplesoforificeflowratesinclude:
1/8inchwith5ftsquirt=0.41gpm
5/32inchwith3.5ftsquirt=0.54gpm
3/16inchwith3.5squirt=0.78gpm
1/4inchwith2.5ftsquirt=1.17gpm
7. Orificeflowrateingallonsperminute(GPM)______
Selecttheorificespacing:
1orifice/6ft2–mounds
1orifice/4ft2-intermittentsandfilter
1orifice/4ft2orless-recirculatingsandfilter,recirculatinggravelfilter,textilefilter
Forpressurizedtrenches,orificesaretypicallyplacedevery2to4feetalongeachpressurizedlateral.
8. Orificespacing______ft.
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PressureNetworkDesignNotes: Step:
Basedonorificespacingandshapeofdistributionarea(fromStep4sketch),determinenumberandlengthoflaterals:
Numberoflateralsisalllateralsinthesystem
Numberoflateralsdosedbypumpisthenumberoflateralsdosedwhenthepumpruns.Itisthesameasabovewhenzonesarenotused.Itisthenumberoflateralswithinthezonewhenzonesareused.ThisnumberisusedfordeterminingthedesignflowrateofthepumpinStep14
Forendfeed:laterallength=
absorptionlengthminus0.5to1foot
Forcenterfeed:laterallength=
absorptionlengthdividedby2minus0.5to1foot
Lateralsshouldextendtowithin6inchesto1footoftheendoftheabsorptionarea.
Thedistancefromthelateralstotheedgeoftheinfiltrativeareashouldbe6inchesto1footforbedareasand1footto1.5feetfortrenches.
9. Numberandlengthoflaterals
Numberoflaterals:
______
Numberoflateralsdosedbypump
______
Lengthoflaterals
______ft.
AddthelateralstothesketchinStep4
FromStep8andStep9:
Numberoforifices=(laterallength/orificespacing)+1
Ifthecalculationresultsinafraction,dropthedecimalthenaddtheadditionalorifice.
10. Numberoforificesineachlateral
______
FromStep7andStep10:
(Orificeflowrate)x(Numberoforifices)
11. Lateralflowrate
______GPM
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PressureNetworkDesignNotes: Step:
Sizethelateraldiametertoensureflowwithinthelateraliswithin10%.
UseorificediameterfromStep5.
UseGraphsB1throughB8inAppendixBtodetermineminimumlateraldiameters:
UseGraphB-1orB-2for1/8inchorifice
UseGraphB-3orB-4for5/32inchorifice
UseGraphB-5orB-6for3/16inchorifice
UseGraphB-7orB-8for1/4inchorifice
12. Lateralsizing______in.
DeterminelateralheadlossusingMethod1or2:
Method1:use1/3ofthesquirtheightfromStep6:
(squirtheight)x(0.33)
Method2:calculatetheheadlossbasedonsolidpipe1/3thelengthoftheperforatedlateralfromStep9,usingthelateralflowratefromStep11andthediameterofthelateralfromStep12.SeeAppendixBTableB-6,FrictionalHeadLossper100feetofSolidPipe.
13. Lateralheadloss______ft.
Calculateflowratefromalllateralsdosedatonetime.Thiswillbethetotalflowrateforalllateralsoralllateralswithinazone:
(No.oflateralsfromStep9)x(LateralflowratefromStep11)=DesignFlowRate.
14. Designflowrate______GPM
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PressureNetworkDesignNotes: Step:
DeterminethesizeofthemanifoldusingMethod1or2:
Method1:usethesamesizepipeusedfortheforcemaininStep18.
Method2:calculatetheheadlosswithinthemanifoldusingvarioussizesofpipeandusing1/2ofthetotaldesignflowfromStep14.
UseAppendixBTableB-6:FrictionalHeadLossper100feetofSolidPipe.
Selectan“acceptable”headloss-usuallyselectthesmallestpossiblepipe.
Manifoldheadlossshouldbe<40%oftotaldynamichead(TDH)fromStep23.
15. Manifoldsizing______in.
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PressureNetworkDesignNotes: Step:
DeterminemanifoldheadlossusingAppendixBTableB-6:FrictionalHeadLossper100feetofSolidPipe
16. Manifoldheadloss______ft.
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PressureNetworkDesignNotes: Step:
Lengthofpipefromthepumpdischargetothebeginningofthemanifold(site-specific).
17. Forcemainlength______ft.
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PressureNetworkDesignNotes: Step:
UseAppendixBTableB-6:FrictionalHeadLossper100feetofSolidPipetodeterminethepipediameter.
Pickapipediameterwithanacceptablerangeofheadloss.
Maybeaniterativeprocess.
18. Forcemaindiameter______in.
DeterminetheforcemainheadlossfromAppendixBTableB-6:FrictionalHeadLossper100feetofSolidPipeusingtheforcemainpipesizediameterfromStep18.
19. Headlossinforcemain______ft.
Estimateadditionalheadlossforfittings,valves,etc.UseMethod1or2
Method1:add50%oftheforcemainheadlossfromStep19toaccountforfittings,valves,etc.
Method2:Determinethe“equivalent”pipelengthsforfittings,valves,etc.anddeterminetheheadlossfromAppendixBTableB-7:Frictionallossesthroughplasticfittings.
20. Miscellaneousheadloss______ft.
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PressureNetworkDesignNotes: Step:
Determinetheheadlossthroughautomaticdistributingvalve.Thisinformationisusuallysuppliedbythemanufacturer.
21. Headlossforsystemswithmultiplezones(ifused)______ft.
Theverticaldistance(elevationdifference)fromthewaterlevelinthepumptanktothewaterlevelatthedischargepoint(site-specific).
22. Elevationheaddifference______ft.
TodeterminetheTDH,addtogether:
SquirtHeight(Step6) __________
LateralHeadLoss(Step13) __________
ManifoldHeadLoss(Step16) __________
ForceMainHeadLoss(Step19) __________
MiscellaneousHeadLoss(Step20) __________
ZoneValveHeadLoss(Step21) __________
Elevationheaddifference(Step22) __________
Resultinfeet=TDH __________
23. TotalDynamicHead(TDH)______ft.
DesignFlowRate(Step14) gpm__________
TotalDynamicHead(Step23) ft.__________
24. PumpSelection
USEPUMPCURVESTOSELECTTHECORRECTPUMP
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PressureNetworkDesignNotes: Step:
Thesystemdosevolumeshouldnotexceed10%ofthedailydesignflow.Smallerdosevolumesarepreferred.
Forsystemsthatdrainbacktothepumptankaftereachcycle,thevolumeoftheforcemainshouldbeaddedtothedosevolume.
PipevolumesarecalculatedusingAppendixBTableB-8:Voidvolumeforvariousdiameterpipes.
Totaldosevolumeisthesumofthedosevolumeandpipevolume.
25.SystemDoseVolume
______gal
PipeVolume______gal.
TotalDoseVolume
______gal
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PressureNetworkDesignNotes: Step:
Calculateasystemperformancecurvebycompletingtheworksheetonthefollowingpage:
a) InColumn1RowC,entertheDesignFlowRatefromStep14.ThenselecttwoflowratesabovetheDesignFlowRateandtwobelowandenterinrowsA,B,DandE.Column1shouldnowbecompleted.
b) InColumn2,calculatetheOrificeFlowbydividingtheTotalFlowRatefromColumn1bythenumberoforificesinthenetworkfromStep10.
c) InColumn3,entertheElevationHeadDifferencefromStep22.
d) InColumn4,useTableB-6:Frictionalheadlossper100feetofsolidpipetocalculatetheForceMainHeadLoss.
e) InColumn5,calculatetheNetworkHeadusing:H=1.3(Q/(11.79d2))2Hisforheadinft.Qisfororificeflowratefromcolumn2disorificediameterininchesfromStep5The1.3isanadjustmentfactorforfrictionlossinlaterals.Example:Theequationfora3/16”orificeisH=1.3(Q/0.4145))2
f) InColumn6,calculatetheTotalHead.AddtheElevation,ForceMainandNetworkheads.
g) Todevelopthesystemperformancecurve,plottheTotalFlowfromColumn1vs.theTotalHeadfromColumn6.
h) Usingmanufacturers’PumpPerformanceCurves,selectonethatintersectstheSystemPerformanceCurveabovetheTotalSystemFlowRate.
Step26:SystemPerformanceCurveandPumpSelection
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SystemPerformanceCurveWorksheet
1.TotalFlow(gpm)
2.OrificeFlow
(gpm)
3.ElevationHead
Difference(ft)
4.ForceMainHeadLoss
(ft)
5.NetworkHead(ft)
6.TotalHead
(ft)
A
B
C
D
E
DesignFlowRatefromStep14inRowC.SelecthigherandlowerratesinrowsA,B,D,E
DividetheTotalFlowRatefromColumn1bythenumberoforificesinthenetworkfromStep10
ElevationHeadDifferencefromStep22
UseTableB-6:Frictionalheadlossper100feetofsolidpipe
SeeStep26e)
AddtheElevation,ForceMainandNetworkheads
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AppendixB
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OrificeFlowRatesinGallonsPerMinute(GPM
PressureinFeet
OrificeDiameter1/8” 5/32” 3/16” 1/4”
2.0 0.26 0.41 0.59 1.042.5 0.29 0.46 0.66 1.173.0 0.32 0.50 0.72 1.283.5 0.34 0.54 0.78 1.384.0 0.37 0.58 0.83 1.474.5 0.39 0.61 0.88 1.565.0 0.41 0.64 0.93 1.655.5 0.43 0.68 0.97 1.736.0 0.45 0.71 1.02 1.806.5 0.47 0.73 1.06 1.887.0 0.49 0.76 1.10 1.957.5 0.50 0.79 1.14 2.028.0 0.52 0.81 1.17 2.088.5 0.54 0.84 1.21 2.159.0 0.55 0.86 1.24 2.219.5 0.57 0.89 1.28 2.2710.0 0.58 0.91 1.31 2.33
TableB-5:Orificeflowrates
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FrictionalHeadLossper100feetofSolidPipe
GallonsPerMinute
NominalPipeSize3/4” 1” 1¼” 1½” 2” 3” 4”
3 3.24 0.80 0.27 0.11 0.03 0.00 0.00
4 5.51 1.36 0.46 0.19 0.05 0.01 0.00
5 8.34 2.05 0.69 0.28 0.07 0.01 0.00
6 11.68 2.88 0.97 0.40 0.10 0.01 0.00
7 15.55 3.83 1.29 0.53 0.13 0.02 0.00
8 19.91 4.90 1.65 0.68 0.17 0.02 0.01
9 24.76 6.10 2.06 0.85 0.21 0.03 0.01
10 30.09 7.41 2.50 1.03 0.25 0.04 0.01
11 35.90 8.84 2.98 1.23 0.30 0.04 0.01
12 42.18 10.39 3.50 1.44 0.36 0.05 0.01
13 48.92 12.05 4.06 1.67 0.41 0.06 0.01
14 56.12 13.82 4.66 1.92 0.47 0.07 0.02
15 63.77 15.71 5.30 2.18 0.54 0.07 0.02
16 71.87 17.70 5.97 2.46 0.60 0.08 0.02
17 80.40 19.80 6.68 2.75 0.68 0.09 0.02
18 89.38 22.01 7.42 3.06 0.75 0.10 0.03
19 98.80 24.33 8.21 3.38 0.83 0.12 0.03
20 108.64 26.76 9.02 3.71 0.91 0.13 0.03
25 164.24 40.45 13.64 5.61 1.38 0.19 0.05
30 230.21 56.70 19.12 7.87 1.94 0.27 0.07
35 306.27 75.43 25.44 10.47 2.58 0.36 0.09
40 392.20 96.60 32.58 13.40 3.30 0.46 0.11
45 120.14 40.52 16.67 4.11 0.57 0.14
50 146.03 49.25 20.26 4.99 0.69 0.17
60 204.68 69.03 28.40 7.00 0.97 0.24
70 272.31 91.84 37.79 9.31 1.29 0.32
80 348.71 117.61 48.39 11.92 1.65 0.41
90 146.28 60.19 14.82 2.06 0.51
100 177.80 73.16 18.02 2.50 0.62
125 268.78 110.59 27.24 3.78 0.93
150 155.01 38.18 5.30 1.30
175 206.23 50.79 7.05 1.74
TableB-6:Frictionalheadlossper100feetofsolidpipeBasedonHazen-WilliamsequationhL=L*(Q/(0.285*C*d^2.63))^1.852whereC=~145,L=100,Q=GPMHeadlossintablemustbecorrectedforpipelength:
(headLossfromtable)x(pipelength/100)=headlossinpipe
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FrictionalLossesthroughPlasticFittingsintermsofEquivalentLengthofSolidPipe
NominalPipeDiameterTypeofFitting 1/2" 3/4" 1" 1¼” 1½” 2" 3" 4"90oSTDElbow 2 2 3 4 4 6 8 12
45oElbow 1 1 2 2 2 3 4 5
STDTee 4 5 6 8 9 12 16 22CheckValve 4 6 7 9 11 14 19 25
QuickDisconnect 1 1 1 1 1 1 2 3AngleValve 8 12 15 19 22 28 40 55GlobeValve 15 22 27 35 45 60 80 110
GateValve-Open 1 1 1 1 1 1 2 31/4Closed 2 3 4 5 6 7 10 141/2Closed 10 14 17 22 25 35 50 703/4Closed 40 55 70 90 105 140 200 300
TableB-7:Frictionallossesthroughplasticfittings
PipeVolumes
NominalPipeDiameter Volume(gal./LF)1/2" 0.0103/4" 0.0231" 0.041
1-1/4" 0.0641-1/2" 0.092
2" 0.1633" 0.3674" 0.652
TableB-8:Voidvolumeforvariousdiameterpipes
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