中华人民共和国国家标准----次氯酸钠发生器（people's republic of china national standard -- sodium hypochlorite generator）

中华人民共和国国家标准次氯酸钠发生器（PEOPLESREPUBLICOFCHINANATIONALSTANDARDSODIUMHYPOCHLORITEGENERATOR）PEOPLESREPUBLICOFCHINANATIONALSTANDARDSODIUMHYPOCHLORITEGENERATORSODIUMHYPOCHLORITEGENERATORGB12176901THEMECONTENTANDSCOPEOFAPPLICATIONTHISSTANDARDSPECIFIESTHEPRODUCTCLASSIFICATION,TECHNICALREQUIREMENTS,TESTMETHODSANDINSPECTIONRULESOFSODIUMHYPOCHLORITEGENERATORFORELECTROLYSISOFLOWCONCENTRATIONSALTWATERTHISSTANDARDISSUITABLEFORDRINKINGWATERDISINFECTION,WASTEWATERTREATMENT,SANITATIONANDEPIDEMICPREVENTIONANDTHEUSEOFSODIUMHYPOCHLORITEGENERATORININDUSTRIALPRODUCTIONDEPARTMENT2CITATIONCRITERIAGB3859SEMICONDUCTORPOWERCONVERTERGB5461EDIBLESALTHYGIENICSTANDARDOFDRINKINGWATERFORGB5749GB5750STANDARDTESTMETHODFORDRINKINGWATERJB1043CHEMICALCORROSIONPROTECTIONLOWVOLTAGEAPPARATUSTESTMETHODFORCHEMICALGASCORROSIONOFJB1045ELECTRICALPRODUCTSGENERALTECHNICALREQUIREMENTSFORPACKAGINGOFJB2759MECHANICALANDELECTRICALPRODUCTS3TERMSANDTERMS31ELECTROLYZERELECTROLYTICCELLINTHESODIUMHYPOCHLORITEGENERATORFORELECTROLYSISOFLOWCONCENTRATIONSALTWATER,THEELECTROLYTICREACTIONANDSOLUTIONREACTIONARECALLEDELECTROLYTICCELLSDIFFERENTCELLSTRUCTUREANDELECTRODESHAPECANBEADOPTEDINTHEELECTROLYZERACCORDINGTODIFFERENTOPERATIONMODESANDREQUIREMENTS32EFFECTIVECHLORINECONCENTRATIONCCONCETRATIONOFAVAILABLECHLORINETHEOXIDATIONCAPACITYOFSODIUMHYPOCHLORITESOLUTIONISQUANTITATIVELYEXPRESSEDBYEFFECTIVECHLORINECONCENTRATIONTHEOXIDATIONCAPACITYOFEACHLITERSOLUTIONISEQUIVALENTTOTHEOXIDATIONCAPACITYOFSEVERALGRAMMASSCHLORINEINWATERUNITG/LTHEEFFECTIVECHLORINECONCENTRATIONIS2TIMESOFTHECONCENTRATIONOFTHEPOSITIVEVALENCECHLORINEINTHESOLUTIONTHESOLUTIONCONTAINS1GOFSODIUMHYPOCHLORITEANDCONTAINSEFFECTIVECHLORINE0953G33EFFECTIVECHLORINEYIELDGPRODUCTIONOFAVAILABLECHLORINETHEOUTPUTOFSODIUMHYPOCHLORITEGENERATORISEXPRESSEDBYEFFECTIVECHLORINEYIELD,WHICHISEQUALTOGUNITG/HOFEFFECTIVECHLORINEPERHOURWHENTHEEQUIPMENTISWORKINGINRATEDSTATETHEEFFECTIVECHLORINEYIELDWASCALCULATEDACCORDINGTOFORMULA1GCXQ1FORMULAQHOURLYSODIUMHYPOCHLORITESOLUTIONFLOWRATE,L/H34CURRENTEFFICIENCYNCURRENTEFFICIENCYTHERATIOOFTHEACTUALQUANTITYOFTHEEFFECTIVECHLORINETOTHETHEORETICALAMOUNTOFPRODUCTIONISCALLEDTHECURRENTEFFICIENCYOFTHEELECTROLYTICCELLAFTERFLOWINGTHROUGHACERTAINAMOUNTOFELECTRICITYINTHEELECTROLYTICCELLACCORDINGTOTHEELECTROLYSISLAWOFFALASBROTHER,THETHEORETICALYIELDOFEFFECTIVECHLORINEIS1323GWHENTHEELECTRICQUANTITYOF1A/HPASSESTHROUGHTHEELECTROLYZERTHECURRENTEFFICIENCYISCALCULATEDACCORDINGTOTHEFORMULA2NG/IXNX1323X1002TYPEIELECTROLYTICCURRENT,ANSERIESSERIESOFELECTRODES1323THEORETICALGENERATIONOFEFFECTIVECHLORINEPERAMPEREHOUR,G/AH35ELECTROLYTICVOLTAGEVELECTROLYTICVOLTAGEWHENTHESODIUMHYPOCHLORITEGENERATOROPERATESINRATEDSTATE,THEDIRECTVOLTAGEAPPLIEDBETWEENTHEANODEANDCATHODEOFTHEELECTROLYTICCELLISCALLEDELECTROLYTICVOLTAGE,UNITVTHEELECTROLYTICVOLTAGEISEXPRESSEDBYMULTIPLYINGTHEELECTROLYTICVOLTAGEOFEACHPAIROFANODEANDCATHODEBETWEENTHECATHODEANDANODEINSERIESSUCHAS4V336RATEDELECTROLYTICCURRENTINOMINALELECTROLYTICCURRENTINORDERTOMAINTAINTHENOMINALYIELDOFSODIUMHYPOCHLORITEGENERATOR,THEELECTROLYTICCURRENTFLOWINGTHROUGHTHEELECTROLYTICCELLISCALLEDRATEDELECTROLYTICCURRENT,UNITAWHENTHEEQUIPMENTELECTROLYZERISPOWEREDBYMANYPAIRSOFANODEANDCATHODE,THERATEDELECTROLYTICCURRENTCANBEEXPRESSEDBYMULTIPLYINGTHECURRENTBETWEENEACHPAIROFELECTRODESANDTHENUMBEROFPARALLELPOLES,SUCHAS50A237ELECTROLYTECONCENTRATIONSCONCENTRATIONOFELECTROLYTESOLUTIONSODIUMHYPOCHLORITEGENERATORADOPTSLOWCONCENTRATIONSALTWATERASELECTROLYTETHECONCENTRATIONOFELECTROLYTEISEXPRESSEDINGRAMSPERLITEROFSOLUTIONCONTAININGNACI,UNITG/L38DCPOWERCONSUMPTIONPDCDCPOWERCONSUMPTIONTHESODIUMHYPOCHLORITEGENERATOROPERATESUNDERRATEDCONDITION,THEDCENERGYCONSUMEDBYEACHEFFECTIVECHLORINEGENERATEDINTHEELECTROLYTICCELLISCALLEDTHEDIRECTCURRENTPOWERCONSUMPTIONTHEUNITISKWH/KG,ANDTHEFORMULAISCALCULATEDACCORDINGTOTHEFORMULA31KGPDCUXI/GUXI/QXC3TYPEUVDCIELECTROLYTICCURRENTADCGEFFECTIVECHLORINEYIELDG/HQSODIUMCHLORIDESOLUTIONYIELDL/HCTHEEFFECTIVECHLORINECONCENTRATIONG/LOFSODIUMHYPOCHLORITE39ALTERNATINGCURRENTCONSUMPTIONPACACPOWERCONSUMPTIONWHENTHESODIUMHYPOCHLORITEGENERATORWORKSUNDERRATEDCONDITION,THEEFFECTIVECHLORINEPRODUCEDBYTHEWHOLEMACHINECANBECALLEDACPOWERCONSUMPTIONTHEUNITISKWH/KG,ANDTHEFORMULAISCALCULATEDACCORDINGTOTHEFORMULA41KGPACP1X1000/G4TYPEP1THEINPUTACTIVEPOWEROFTHEWHOLEMACHINE,KW310SALTCONSUMPTIONUSSALTCONSUMPTIONWHENTHESODIUMHYPOCHLORITEGENERATOROPERATESUNDERRATEDCONDITION,THEQUALITYOFNACICONSUMEDBYPRODUCING1KGEFFECTIVECHLORINEISCALLEDITSSALTCONSUMPTION,THEUNITISKG/KG,ANDTHEFORMULAISCALCULATEDACCORDINGTOTHEFORMULA5USS/C5FORMULASELECTROLYTECONCENTRATION,G/LCEFFECTIVECHLORINECONCENTRATION,G/L4,PRODUCTCLASSIFICATION41CLASSIFICATIONPRINCIPLE,SODIUMHYPOCHLORITEGENERATORACCORDINGTOTHEUSE,OPERATIONMODE,SPECIFICATIONSANDQUALITYLEVELCLASSIFICATION411SODIUMHYPOCHLORITEGENERATORISDIVIDEDINTOTWOCATEGORIESSANITARYDISINFECTIONANDENVIRONMENTALPROTECTIONACCORDINGTOITSUSESANITARYDISINFECTIONCANBEUSEDFORENVIRONMENTALPROTECTION,ANDENVIRONMENTALPROTECTIONSHALLNOTBEUSEDFORSANITARYDISINFECTIONSANITARYDISINFECTIONREFERSTOTHESODIUMHYPOCHLORITEGENERATORWHICHISDIRECTLYRELATEDTOTHEHEALTHOFHUMANBODYFORDISINFECTION,SANITATIONANDTABLEWAREDISINFECTION,VEGETABLES,FRUITS,FOODDISINFECTIONANDSOONENVIRONMENTALPROTECTIONREFERSTOTHESODIUMHYPOCHLORITEGENERATORWHICHISNOTDIRECTLYRELATEDTOHUMANHEALTH,SUCHASINDUSTRIALWASTEWATERTREATMENT,HOSPITALSEWAGETREATMENTANDOTHERINDUSTRIALSECTORSTHATUSESODIUMHYPOCHLORITESOLUTIONTHEOPERATIONMODEOF412SODIUMHYPOCHLORITEGENERATORISDIVIDEDINTOTWOTYPESCONTINUOUSOPERATIONANDINTERMITTENTOPERATION413SODIUMHYPOCHLORITEGENERATORSPECIFICATIONSACCORDINGTOTHEEFFECTIVECHLORINEYIELDEQUIPMENTISDIVIDEDINTO5,10,25,50,75,100,150,200,250,300,400,500,750,1000,1500,2000,3000,5000,G/H,MORETHAN5000G/HSPECIFICATIONSAREDETERMINEDACCORDINGTOTHEACTUALNEEDS414SODIUMHYPOCHLORITEGENERATORISDIVIDEDINTOHIGHQUALITYPRODUCTSA,FIRSTGRADEPRODUCTSBANDQUALIFIEDPRODUCTSCACCORDINGTOQUALITYGRADE42PRODUCTLABELINGTHEPRODUCTMARKOF421SODIUMHYPOCHLORITEGENERATORCONSISTSOF3PARTSANDISARRANGEDINTHEFOLLOWINGORDERPRODUCTNAMETECHNICALCHARACTERISTICSSTANDARDNUMBER422PRODUCTNAMEIS“SODIUMHYPOCHLORITEGENERATOR“THETECHNICALFEATURESOF423CONSISTOFTHEUSEOFTHEEQUIPMENT,THEMODEOFOPERATION,THESPECIFICATIONS,THELETTERSANDNUMBERSOFTHEQUALITYGRADETHEFIRSTCHINESEPHONETICALPHABETOFTHEFEATUREPARTOF4231TECHNOLOGYINDICATESTHEUSEOFTHEEQUIPMENTTHELETTER“W“ISUSEDFORSANITARYDISINFECTION,ANDTHELETTER“H“ISUSEDFORENVIRONMENTALPROTECTIONTHESECONDCHINESEPHONETICALPHABETSINTHEFEATUREPARTOFTHE4232TECHNOLOGYREPRESENTTHEOPERATIONMODEOFTHEEQUIPMENT,CODELCONTINUOUSELECTROLYTICMODE,JBATCHTYPEELECTROLYTICPROTECTIONTHETHIRDARABIAFIGURESOFTHE4233TECHNOLOGYFEATUREREPRESENTTHESPECIFICATIONSOFTHEEQUIPMENT,ANDTHENUMERICALVALUEISTHERATEDOUTPUTOFTHEEQUIPMENTTHEFOURTHLETTERSOFTHE4234TECHNOLOGYFEATUREINDICATETHEQUALITYLEVELOFTHEPRODUCTLETTERAQUALITYPRODUCTS,BGRADEA,CQUALIFIEDPRODUCTSTHESTANDARDPARTOFTHE424PRODUCTLABELINDICATESTHATTHEPRODUCTCONFORMSTOTHENATIONALSTANDARDANDISEXPRESSEDINGB1217643PRODUCTLABELINGEXAMPLESFOREXAMPLEFORDISINFECTION,CONTINUOUSOPERATION,THERATEDYIELDOF100G/H,QUALITYGRADEREACHEDTHEFIRSTCLASSOFSODIUMHYPOCHLORITEGENERATOR,ITSPRODUCTSMARKEDASSODIUMHYPOCHLORITEGENERATORWL100BGB1217690FOUR4THEQUALITYGRADEMARKUSEDINPRODUCTMARKANDTHEMARKCONFORMINGTOTHEREQUIREMENTSOFTHISNATIONALSTANDARDMUSTBEAPPROVEDBYTHESTATESPECIALIZEDAGENCYORDESIGNATEDQUALITYMONITORINGUNIT45THESPECIFICMODELOFTHEPRODUCTALLOWSTHEPRODUCTIONPLANTTODETERMINEACCORDINGTOTHEREQUIREMENTSOFTHISSTANDARD5TECHNICALREQUIREMENTS51THEUSEOFENVIRONMENTALCONDITIONSSODIUMHYPOCHLORITEGENERATORSHOULDBEABLETOWORKINTHEFOLLOWINGENVIRONMENT511AMBIENTTEMPERATURE040OC512AMBIENTHUMIDITYTHEMAXIMUMRELATIVEHUMIDITYINAIRISNOTMORETHAN90EQUIVALENTTOAIR205OC513INTHEQUALITYGRADEFORTHEQUALITYOFSODIUMHYPOCHLORITEGENERATORONTHESELECTIONOFLOWVOLTAGEELECTRICALAPPLIANCESINADDITIONTOMEETTHEIRRESPECTIVEPRODUCTTECHNICALREQUIREMENTS,SHOULDALSOCOMPLYWITHTHEPROVISIONSOFJB104352BASICTECHNICALREQUIREMENTS521SODIUMHYPOCHLORITEGENERATORSHALLBEMANUFACTUREDACCORDINGTOTHEDRAWINGSANDTECHNICALDOCUMENTSAPPROVEDBYTHEPRESCRIBEDPROCEDURESTHESPECIFICATIONSOF522SODIUMHYPOCHLORITEGENERATORSHALLCOMPLYWITHTHEREQUIREMENTSOFTHISSTANDARD413523SODIUMHYPOCHLORITEGENERATORACCORDINGTOTHEPROVISIONSOFTHISSTANDARD54QUALITYCLASSIFICATION,TOACERTAINQUALITYLEVELOFPRODUCTS,SHOULDMEETTHEREQUIREMENTSOFTHEINDICATORSINTHISCLASS524SODIUMHYPOCHLORITEGENERATORMUSTBEEQUIPPEDWITHSHELLGROUNDINGBOLT,EACHPARTOFTHESHELLANDPOWERSUPPLYPART,METALSTRUCTUREANDGROUNDINGBOLTHASRELIABLEELECTRICALCONNECTION,THEMEASUREDVALUEOFRESISTANCEISLESSTHAN01EARTHINGBOLTSHALLBEMARKEDWITHGROUNDINGMARKTHEELECTROLYTICCELLANDTHELIQUIDSTORAGETANKUSEDINTHEEQUIPMENTWITH525YIELDGREATERTHAN25G/HMUSTADOPTACLOSEDSTRUCTUREANDSETUPASTANDARDINTERFACECONNECTEDTOTHEOUTDOOREXHAUSTPIPETHESTANDARDINTERFACEOF526INTERCONNECTYIELDMORETHAN25G/HEQUIPMENTSHOULDHAVEAFFILIATEDWITHTHESALINEDEPLOYMENTDEVICECONNECTEDANDFILLINGDEVICETHEELECTROLYTICCURRENTANDELECTROLYTICVOLTAGEMONITORINGINSTRUMENTMUSTBESETUPWHENTHEOUTPUTOF527ISGREATERTHAN25G/H,ANDTHEACCURACYISNOTLOWERTHAN25CONTINUOUSOPERATIONOFTHEEQUIPMENTMUSTBEEQUIPPEDWITHELECTROLYTEFLOWMETERINGINSTRUMENT,INTERMITTENTOPERATIONOFTHEEQUIPMENTMUSTBEINTHEELECTROLYTICTANKORCIRCULATINGTANKEQUIPMENTLEVELGAUGEPHYSICALANDCHEMICALPROPERTIESOFSODIUMHYPOCHLORITESOLUTIONPRODUCEDBY528EQUIPMENT5281SODIUMHYPOCHLORITESOLUTIONSHOULDBECLEARANDTRANSPARENTWITHNOVISIBLEIMPURITIESTHECONTENTOFCHROMIUMANDLEADINTHESODIUMHYPOCHLORITESOLUTIONPRODUCEDBYTHESODIUMHYPOCHLORITEGENERATORUSEDFORSANITARYDISINFECTIONOF5282SHALLCOMPLYWITHTHERELEVANTPROVISIONSOFTHEWATERQUALITYSTANDARDSANDHYGIENICREQUIREMENTSOFGB5749SECONDCHAPTERTHEGRAPHITEGENERATORELECTRODEANDTWOLEADOXIDECOATINGANODEARENOTALLOWEDFORTHESODIUMHYPOCHLORITEGENERATORUSEDINSANITARYDISINFECTIONOF5283OPERATINGPARAMETERSANDSERVICEPERFORMANCEOF53SODIUMHYPOCHLORITEGENERATOR531POWERSUPPLYTHEINPUTPOWEROFSODIUMHYPOCHLORITEGENERATORSHOULDBEAC220V/380V1050HZ5THERANGEOF532ELECTROLYTICCURRENTSHOULDBEMORETHAN10OFTHERATEDELECTROLYTICCURRENT533SODIUMHYPOCHLORITEGENERATORSHOULDGUARANTEETHERATEDYIELDOFEQUIPMENTUNDERLONGTERMWORKINGCONDITION,ANDCANEXCEEDTHEYIELDOF10,SAFETYWORK1HTHERECOMMENDEDCONCENTRATIONRANGEOFELECTROLYTEFOR534EQUIPMENTIS3050G/LTHEFIXEDCONCENTRATIONELECTROLYTESELECTEDINTHISRANGESHOULDBEUSEDINTHEWHOLEPROCESSOFEQUIPMENTPERFORMANCETESTTHEELECTROLYTECONSUMPTIONOF535ISEXPRESSEDINTHEELECTROLYTICCELLOFCONTINUOUSOPERATION,INTHEAMOUNTOFELECTROLYTEPERHOUR,EXPRESSEDINUNITL/HINBATCHELECTROLYTICCELL,THEAMOUNTOFBRINEANDTHEPERIODOFELECTROLYSISHINELECTROLYSISPERIODAREEXPRESSEDASUNITL/H,SUCHAS50L/15H536PRODUCTSSHALLSPECIFYTHEDIMENSIONS,WEIGHTANDMOUNTINGDIMENSIONSOFEQUIPMENTANDACCESSORIESFORDRINKINGWATERDISINFECTIONANDSEWAGETREATMENTSHOULDBEPROVIDEDWITHTHEINSTALLATIONOFEQUIPMENTSCHEMATIC537EQUIPMENTSHOULDENSURETHATTHEELECTROLYTETEMPERATUREISLESSTHAN40OCDURINGTHEELECTROLYSISPROCESS,ANDIFNECESSARY,THECORRESPONDINGCOOLINGMEASURESSHOULDBETAKEN54TECHNICALANDECONOMICINDICATORSANDQUALITYCLASSIFICATIONTABLE1TABLE1TECHNICALANDECONOMICINDICATORSANDQUALITYANALYSISTECHNICALANDECONOMICINDICATORSPERUNITQUALITYGRADEABC63VISUALINSPECTIONINTHISSTANDARD,52BASICTECHNICALREQUIREMENTSOF521527BARSAND55APPEARANCEREQUIREMENTS,THEUSEOFVISUALINSPECTIONMETHODSIXTHETESTMETHODOFVOLTAGEWITHSTANDTESTANDINSULATIONRESISTANCEMEASUREMENTFOR4ELECTROLYTICPOWERSHALLCOMPLYWITHTHERELEVANTPROVISIONSINGB3859THETEMPERATURERISETESTMETHODOF65ELECTROLYTICPOWERSUPPLYCANBECARRIEDOUTACCORDINGTOTHERELEVANTPROVISIONSOFGB3859,ANDTHETEMPERATURERISETESTCANBECARRIEDOUTSIMULTANEOUSLYWITHCONTINUOUSOPERATIONTHEOPERATIONTESTOF66SODIUMHYPOCHLORITEGENERATORISCARRIEDOUTTOCHECKTHEWORKINGSTATEOFTHEEQUIPMENTANDADJUSTTHERANGEOFELECTROLYTICCURRENTBEFORETHE661TEST,CHECKTHEASSEMBLYOFTHECIRCUITANDPIPINGACCORDINGTOTHEREQUIREMENTSOFTHEDRAWINGAFTERCHECKINGTHENORMALCONDITION,CONNECTTHEBRINEPIPELINE,ADDTHEELECTROLYTEACCORDINGTOTHERATEDSTATEOFTHEEQUIPMENT,ANDEACHPARTSHOULDWORKNORMALLYWITHOUTLEAKAGETHE662ISCONNECTEDWITHTHEPOWERCIRCUITOFTHEEQUIPMENT,ANDTHEELECTROLYTICCURRENTISADJUSTEDTOTHERATEDVALUETHEOPERATIONOFTHEELECTROLYTIC30MINEQUIPMENTSHOULDBENORMAL663REGULATESTHEELECTROLYTICCURRENTCONTROLDEVICEFORTHEVALUEOFTHE10INTHERATEDSUPPLYVOLTAGE,ELECTROLYTICCURRENTOUTPUTCANBEADJUSTEDTOTHERATEDVALUEOF10,THEPOWERSUPPLYOFTHEELECTRICPRESSURERATINGOF10,THEELECTROLYSISCURRENTCANBEADJUSTEDTOTHERATEDVALUEAT10INTHETEST,THEINPUTVOLTAGEISALLOWEDTOBECHANGEDBYTHEAUTOTRANSFORMER,ANDTHETESTRESULTSSHOULDMEETTHEREQUIREMENTSOFTHESTANDARD532AND5611AFTERTHE664TEST,THEELECTROLYTICTANKANDTHELIQUIDSTORAGETANKAREEMPTIED,ANDTHEVENTINGTIMEISRECORDEDTHEEMISSIONTIMESHOULDCOMPLYWITHTHEREQUIREMENTSOF573AND5104OFTHISSTANDARD67CONTINUOUSRUNNINGTESTELECTROLYTICVOLTAGE,RATEDPRODUCTIONRATE,CURRENTEFFICIENCY,DCPOWERCONSUMPTION,ACPOWERCONSUMPTION,SALTCONSUMPTION,TOTALPOWERINPUT,ELECTROLYTETEMPERATURERISEANDTEMPERATURERISEOFELECTROLYTICPOWERSUPPLY671TESTMETHODSTHESUBJECTSOFSODIUMHYPOCHLORITEGENERATORWORKINGINCONTINUOUSRATEDWORKINGSTATEUNDERTHEPROVISIONSOFARTICLE672,SUCHASTHE674RECORDSHOWNINVARIOUSOPERATINGPARAMETERSINTHEPROCESSOFOPERATION,ANDCALCULATETHEPARAMETERSACCORDINGTOTHEPROVISIONSOFTHEFORMULARATEDWORKINGSTATEOF672CONTINUOUSOPERATIONTESTTHEELECTROLYTEUSEDINTHE6721TESTSHOULDMEETTHEFOLLOWINGREQUIREMENTSAELECTROLYTEISPREPAREDWITHREFINEDSALTANDTAPWATERREFINEDSALTSHOULDMEETTHEREQUIREMENTSOFREFINEDSALTINGB5461TAPWATERQUALITYSHOULDBEINLINEWITHGB5749DRINKINGWATERSTANDARDTHEVARIATIONRANGEOFELECTROLYTECONCENTRATIONANDCONCENTRATIONINBTESTSHOULDCOMPLYWITHTHEPROVISIONSOFTHISSTANDARD593INCTEST,THEELECTROLYTETEMPERATUREOFTHEINPUTELECTROLYZERSHOULDBE205OCELECTROLYTEFLOWSHOULDBEMAINTAINEDATRATEDVALUEINDTESTFORCONTINUOUSOPERATION,THEFLOWRATESHOULDBELESSTHANTHERATEDVALUE5FORBATCHOPERATION,THEELECTROLYTEINJECTIONRATEANDELECTROLYSISTIMESHOULDBEMAINTAINEDATRATEDVALUETHEELECTROLYTICCURRENTSHOULDBEMAINTAINEDATRATEDVALUEIN6722TEST,ANDTHEDEVIATIONSHOULDBELESSTHAN25AVOLTAGEREGULATORORAVOLTAGEREGULATORISALLOWEDTOBEADDEDTOTHEPOWERINPUTTERMINALTHERUNNINGTIMEOF673CONTINUOUSELECTROLYZERISSTABLEAFTERTHEEQUIPMENTSTARTUP4HBATCHELECTROLYZERSHOULDWORK4ELECTROLYSISCYCLES674OPERATIONDATARECORDINGCONTINUOUSELECTROLYSISINTHEOPERATIONOFEACH05H,EACHBATCHSTARTANDENDOFTHEELECTROLYTICELECTROLYSISCYCLE,SUCHASOPERATIONSHOULDFAITHFULLYRECORDTHEDATATHEELECTROLYSISTIME,INPUTVOLTAGE,INPUTSUPPLYCURRENT,ELECTROLYTICVOLTAGE,ELECTROLYTICCURRENT,ELECTROLYTEFLOWELECTROLYTECAPACITY,ELECTROLYTECONCENTRATION,FLOWRATE,SODIUMHYPOCHLORITESOLUTIONSODIUMHYPOCHLORITESOLUTIONEFFECTIVECHLORINECONTENT,ELECTRICALCONTACTTEMPERATURE,ELECTROLYTETEMPERATURE,SODIUMHYPOCHLORITESOLUTIONTEMPERATURE,AMBIENTTEMPERATURE,EXPERIMENTALPERSONNELSIGNATUREETCWHENRECORDINGTHEINSTRUMENTDISPLAYDATA,THELABORATORYINSTRUMENTDISPLAYDATASHOULDBERECORDEDATTHESAMETIME675TESTINSTRUMENTTHEACCURACYOFTHELABORATORYINSTRUMENTUSEDINTHETESTSHOULDBENOLESSTHAN05,ANDTHERESOLUTIONOFTHETHERMOMETERIS02OCTHEEXPERIMENTOF676CONTINUOUSELECTROLYSISOFSODIUMHYPOCHLORITESOLUTIONFLOWQ,ANDUSINGASTOPWATCH,CALCULATEDBYMETHODOFVOLUMEDIVIDEDBYTHETIME,EACHFLOWPARAMETERSAMPLINGSHOULDBEMORETHAN3TIMES,EACHSAMPLINGTIMEOFNOTLESSTHAN1MIN,CALCULATEDTHEAVERAGEVALUEOFSEVERALMEASUREMENTSCALCULATIONOFTHEEFFECTIVECHLORINEYIELDOF677FORTHECONTINUOUSOPERATIONOFTHESODIUMHYPOCHLORITEGENERATOR,CALCULATIONOFEFFECTIVECHLORINEYIELDACCORDINGTOARTICLE33OFTHISSTANDARDFORMULA1ISCALCULATED,THEAVERAGEVALUEOFSODIUMHYPOCHLORITESOLUTIONFLOWCALCULATIONOFSODIUMHYPOCHLORITESOLUTIONFLOWQTAKENFROMTHERECORDSOFTHERUNNINGTESTINTHE,ANDTHEEFFECTIVECHLORINECONCENTRATIONC,ALSOTAKETHEAVERAGEVALUEOFTHEEFFECTIVECHLORINECONCENTRATIONRECORDEDFORTHESODIUMHYPOCHLORITEGENERATORINTERMITTENTOPERATION,EACHCYCLEOFCONSUMPTIONBYELECTROLYTICBRINEELECTROLYTEVOLUMEDIVIDEDBYTHEELECTROLYSISTIMETOEXPRESS,ANDACCORDINGTOTHEFORMULA1CHLORINEYIELDWASCALCULATEDFOREACHCYCLE,TESTPRODUCTIONOFAVAILABLECHLORINEEQUIPMENTSHALLBETAKINGTHEAVERAGEOFSEVERALEFFECTIVECHLORINEELECTROLYSISCYCLEMEASUREDYIELDCALCULATIONOF678CURRENTEFFICIENCYNACCORDINGTOTHEACTUALPRODUCTIONRATEGANDTHEAVERAGEVALUEOFTHEELECTROLYTICCURRENTINTHECONTINUOUSRUNNINGTEST,THEFORMULAISCALCULATEDACCORDINGTOTHE34FORMULA2OFTHISSTANDARDCALCULATIONOFDCPOWERCONSUMPTIONFOR679ACCORDINGTOTHECONTINUOUSOPERATIONEXPERIMENT,THEAVERAGEVALUEOFELECTROLYTICVOLTAGE,ELECTROLYTICCURRENTANDEFFECTIVECHLORINEYIELDISCALCULATEDACCORDINGTOTHEFORMULA3IN38CALCULATIONOFACPOWERCONSUMPTIONTESTRESULTSOF6710ACCORDINGTOTHEAVERAGEVALUEOFTHEACINPUTPOWERANDTHEAVERAGEVALUEOFTHERATEDOUTPUTOBTAINEDFROMTHECONTINUOUSRUNNINGTEST,THEFORMULAISCALCULATEDACCORDINGTO39FORMULAS46711INPUTPOWERPIINTHETEST,THEMETERINGVALUEOFTHEKILOWATTHOURMETERINSTALLEDINTHEPOWERSUPPLYLINEOFACERTAINPERIODOFTIMEINTHERATEDOPERATINGSTATECANBECALCULATEDBYDIVIDINGTHEELECTROLYSISTIME,ANDCANBEDIRECTLYMEASUREDBYWATTMETER,UNITKWTEMPERATURERISEOF6712ELECTROLYTEFORTHECONTINUOUSOPERATIONOFTHEELECTROLYTICCELL,THETEMPERATURERISEOFTHEELECTROLYTEISMEASUREDBYTHETEMPERATUREOFTHESODIUMHYPOCHLORITESOLUTIONATTHEENDOFTHECONTINUOUSRUNNINGTEST,ANDTHEINLETTEMPERATUREOFTHEELECTROLYTEISREDUCEDTOOCFORBATCHOPERATIONELECTROLYZER,THETEMPERATUREOFSODIUMHYPOCHLORITESOLUTIONATTHEENDOFELECTROLYSISCYCLEMINUSTHEELECTROLYTETEMPERATUREATTHEBEGINNINGOFELECTROLYSISISOCTEMPERATURERISEOF6713ELECTRICALCONTACTTHEEQUIPMENTINSTEADYSTATEOPERATION,WHENTHETEMPERATUREISLESSTHAN1OC/HCHANGEPOINTISDETECTED,THEJUNCTIONTEMPERATUREANDAMBIENTTEMPERATUREDIFFERENCEOFTHETEMPERATURERISE,THETEMPERATUREMEASUREMENTOFELECTRICALCONTACTWITHSEMICONDUCTORPOINTTHERMOMETER,THEAMBIENTTEMPERATUREISMEASUREDBYMORETHANTWOPIECESOFGLASSTHERMOMETER,INSTALLEDINTHE1MEQUIPMENTFROMFAR,HEIGHT1MPOSITIONINTHETEMPERATURERISETEST,THEAMBIENTTEMPERATUREISWITHINTHERANGEOF1040OC,ANDTHERESHOULDBENOLIGHT,HEATRADIATIONANDAIRFLOWINVASIONTHATAFFECTTHETEMPERATURERISETESTINTHE6714TEST,THEDISPLAYVALUEOFTHEINSTRUMENTONTHEINSTRUMENTANDTHEERROROFTHEDISPLAYVALUEOFTHE05METERSHOULDBELESSTHAN2568OVERLOADINGTESTAFTERCONTINUOUSWORKOVERLOADTESTTESTTESTSHOULDMAKETHEELECTROLYTICCURRENT,ELECTROLYTEFLOWRESPECTIVELYTOMAINTAINTHEIRRATINGS110,OVERLOADTESTTIMEOF1HEQUIPMENTSHOULDWORKNORMALLY,NODAMAGETOCOMPONENTS,COMPLYWITHTHERELEVANTPROVISIONSOFARTICLE533OFTHISSTANDARDTESTONCUMULATIVEWORKINGTIMEOF