a comprehensive solution for recycling...
TRANSCRIPT
A COMPREHENSIVE SOLUTION FOR
RECYCLING WASTE
(with the possibility of processing all types of solid municipal waste and industrial waste)
Processingofalltypesofmunicipalandindustrialwastes,includingoilsludgeThedescriptionoftechnologyofobtainingcommercialproducts.
2018
Tableofcontents1. Descriptionoftechnology
2. Jobdescription
3. Thedraftplantandlayout
4. Derivedproducts
5. Samplebusinessproposaloninstallationintothecapacityofupto200m3/day
6. Technicalandeconomicindicatorsoftheproject
7. Thelistincludedinthecomplexofequipment
8. Ourequipment
9. LetterfromtheMinistryofeducationandscienceoftheRussianFederation
ContactsforInternationalProjects
Worldwideprojects
PINSECTORGroup
EstoniaHarjumaa75303LagediKooli18C
Mob.+3725107070
www.pinsector.com
ThedescriptionoftechnologyofHIGH-EFFICIENCYreactor,withTURBULENTHEATINGofinertgas,RAWMATERIALS
Atthefirststageinthereactorproducedgasificationturbulentmodesolidorliquidwaste.Whenpyrolysisgas,containingcarbonmonoxide,hydrogen,hydrocarbons.Usually,pyrolysisgasrecycling,incorporatingcomplexorganiccompounds,containsinadditiontohydrogen,carbondioxideandmonoxide,etc.,spray,consistingofverysmalldropsofhydrocarbonsorresins,chemicalcompositionofwhichisdeterminedbythenatureoftheprocessedmaterial.Inourtechnology,gasisinferredfromtheGasifierattemperatures450-500°c,passesthroughtheareawithatemperatureof850°c,thenitdoesnotcontaincarbonnedogorevshegoorganicresidues,dust.Highspeedgasflowingazifikatorecausedbyfeedingthroughtheturbulentsuperchargers,heatedtoveryhightemperaturesininertgas,leadtototalabsenceofsoliddustparticlesintheoutput.Gasificationiscarriedoutatatmosphericpressure.Obtainedduringtheprocessingofpyrolysisgas,partiallycondensedinspecialcontainerswithgas-liquid-cooled,noncondensingfractionofgasburnedincellgenerator,allowingyoutowarmuptheinertgastoultra-hightemperatureandtherebyincreasethespeedoftheirfallingintothepyrolysisreactorduetotheacceleratedexpansionofthegas.Thedignityoftheproposedtechnology-highenergyefficiency.Efficiencyatthestageofgasificationreaches97%intheabsenceofexternalpowersources.Theabilitytorecyclesolidandliquidhigh-ashandhighwetwasteinotherdevicespoorlyprocessed,withtheformationofsootandotherproductsofincompletecombustion.Therelativeeaseandaffordability.Highenvironmentalcleanprocess:completenessofcombustion,theabsenceofsoot,carcinogensandothertoxicsubstances,absenceofdustinthefluegas.Easyrawmaterialpreparation.Stageoffinecrushingandgrinding.Technologyoptionsinobtaininghigh-purity,fullyobesserennojpyrolysisliquid(syntheticoil).
TheprincipleofoperationofHIGH-PERFORMANCEreactorwithTURBULENTHEATINGofRAWMATERIALSofINERTGAS
Theproposedtechnologyisheatingupwaste(hereinafterreferredtoastherawmaterial)withoutaccesstoairandfurtherdeepdestructionwhereOrganicsandrelatedvolatilesubstancespassintothegaseousstate(gasified).Theinstallationismadeofhigh-qualityheat-resistantstainlesssteel.Thistechnologyinvolvestheheatingofrawmaterialsthroughthewallofthereactor,whereitisloadedasneeded.Thereactoroperatescontinuously,theoutletofthereactorisconnectedtotheinputpipecondenser,wheregas-steammixturecomeswhenheatingreactor.Submittedbyequipment,capableofprocessingrawmaterialhumidity,whilelosseswillbeminimal.Dedicatedwaterappliedpyrolysisunitoperationaschillercondensers.Watertreatmentfacilities,allowcleanwaterintouptonormsofindustrialwaterdischargedintofishponds,no.1.Toensureuninterruptedworkcyclereactor,choppedtoacertainfaction,servedrawspecialdeviceinthehopper,wherelocalizedentersthereactor.Theequipmentconsistsofaheatgenerator,pyrolysisreactor,airandfuelfilters,capacitors,septictanks,regulatorsblockrawmaterialssupply,technicalcarbondischargeunitwithatankforcollectingheatdistributionsystems.Thecompositionandnumberofpyrolysisproductsdirectlydependonthefeedstock.Iftherawrubberprevails,therewillbemoresolidresidue-carbonthatisusedinthemanufactureofrubberproducts,bulkfilters,Foundationblocksandpelletsforcombustioninboilers.Submittedbypyrolysisliquidfractionationtechnology,allowstheuseofvacuum,inwhichfinalproductsaresubjectedtofractionation,minimalthermalloads,whichinturnimprovesthequalityofthefuel.
ENSURINGtheENVIRONMENTALPERFORMANCEofCOMPLEXonPROCESSINGofSOLIDMUNICIPALwasteandindustrialwaste.
Toensureproductionecology,thecomplexemployedthreefilteringsystemsandlinkingofharmfulsubstances:1. Three-tieredsystemoffluegascomingfromtheheater.Thefirststageofthesystemismechanical,includesdrycyclone,whichcapturedalargemechanicalparticlesandscrubberwithair-flowdripirrigation,vymyvajushhimfromthefluegasremainingaftercyclonemechanicalincorporation.Thesecondstageisliquid.Thiswetscrubber,whichcirculatesliquidabsorbentrecycledconstantlyflowaspecificgas.Thisapparatustoremoveacidicfluegasofthefragments.Thethirdstepprovidesmaximumadditionalcleaningoffluegases,equippedwithadryfilter-sinkwithbulkstructure,allowingtocompletelyabsorballharmfulsubstances.Thesefiltersareusedinairpurificationsystemsinnuclearshelters.Purifiedcarbondioxideenterstheliquefactionincarbondioxide.2. Two-steppurificationofpyrolyticgasbeforeitsreleasetothegazoporshnevujupowerstationandpyrolysisreactor.Ensuresmaximumcleaningoffuelgas,whichinturn,prolongslifeandreducestheamountofharmfulemissionsinitsexhausttreatmentfacilitiesconsistofbulkabsorberswithbytherecycledcontent.
3. Two-stagepyrolysiscleaningfluidisproducedbypumpingheatedpyrolysisliquidthroughthebulkofabsorberswithbytherecycledcontent.purificationandfiltrationsystem,completelyexcludethepossibilityofemissionsofgasesandliquidsintotheenvironmentWednesday.
Equipmentisopen24hoursadaywithoutstopping.Currentyearworkset-340days.
ThecompositionofCOMPLEXonPROCESSINGofSOLIDMUNICIPALwasteandindustrialwaste.
Partoftheproposedcomplexincludes:Screeningofwaste:theselectionofglass,metal,stone,concrete,checkingmaterialsforradioactivity;
Theplottoacertainfactiongrinding;Plotmechanismsformovementofrawmaterials;Plotofpyrolysisprocessingofrawmaterials;TransitionalParktanksunderpyrolysisoil;Stretchtubingfiltration;Carbonwarehouse;Plotpropertiesofmaterialsthatarenotsubjectto
pyrolysisprocessing;Powerplant;
Plottheseparationofpyrolysisliquidintofractions;TransitionalParktanks,underthefinishedproducts;Theplotoftheissuanceofthefinishedproduct.
The project «Complex on pyrolysis of SOLID MUNICIPAL WASTES processing and industrial waste».
Equipmentlayoutwithdimensionsoffoundations
DescriptionderivedfromprocessingofsolidMUNICIPALWASTEandINDUSTRIALWASTEproducts.Stovefuel(mazutM100)-DarktranslucentliquidwithBrownottekom,890densitykg/m3(containssuspendirovannujusoot).Withoutlimitationcanbeusedasfuelforindustrialfurnacesandboilers,airheatersequippedwithraspyljajushhimiburners.FlashtemperatureintheclosedCrucibleover22-27°c,thefreezingpointofminus15°cheatofcombustion39700kJ/kgcanbeprocessedattherefineryintolighterfractionsofpetroleumproducts-tradegasolineanddieselfuellikecokingproductsandofpyrolisisoilresiduesinthefuture,wheneconomicfeasibility,theprojectwillbeabletorecyclethisfaction(heatingoil)topetrolanddiesel,purchaseappropriateequipment;PetrolAI-92-correspondstoRUSGOST;Diesel-complieswithEuro5quality;Tarviscous(heavy)-correspondstoGOST;Gas(Butane/propane/Ethane)-usedinprocessing,butyoucanselectasthecommercialcomponent;Technicalcarbon-weightblackwithgreyshade("petroleumcokemalosernistyj")isusedforthemanufactureofabrasivesandotherproductscarboncharacteristics:totalmoisturenotmorethan3%massfractionofvolatilesubstancesmorethan11.5%,ashcontentnotmorethan0.80%sulphurcontentnotexceeding1.50%.CarbonBlackisusedinchemicalmanufacturingaswellassolidfuelcombustion29000kJ/kg.Afteradditionalheatcanbeappliedtotheelectrode.Steelcord-(scrap)ofusedtires,usedasrawmaterialsarebriquettedformetallurgicalindustry.
Samplebusinessproposal.Pyrolysisinstallationcapacityofupto200m3/dayofSOLIDMUNICIPALwasteandINDUSTRIALWASTE.
Priceofasetofequipmentwillbe12726215USD(721850000RussianRublesratesJan.2018)
Thepriceincludesthefollowingequipmentandservices:1. InstallationonprocessingMSWbundled–10754300USD.2. REFINERYcompletewithcapacitiveParkon7daysofwork–1685428USD.3. Complexforgrindingandfinishingoftechnicalcarbonplant(drymatter)withthe
systemofaspiration,separationandpackingcost-286487USD.4. Chefmontage(1-2)isincludedinthepriceoftheequipment.Fortheoperationofalltheequipmentyouneedforkliftg/nisnotlessthan2.5tonnes.
Electricity,gasandwaterisnotrequired.
Backgroundinformation:Theinstallationallowstoprocessanykindofoilsludges,TKO,RUBBER,plastics,organicchemistry,medicalwaste,wastefromagriculturalandotherinadditiontoglassandmetal.Theresultisthefollowing:liquidpyrolysisproducts-37-58%,carbonbalance-20-30%-5-7%,metalcord.Inthecompletesetequipmentcanrecycleacidtarswithaconcentrationofacidto30%moreacidictarsarerecycledtoinstallmoreexpensiveequipment.
TECHNICALANDECONOMICINDICATORS.PROJECT200(200-70-h).TECHNICALANDECONOMICINDICATORS.PROJECT200(200-70-h).Thereactorisdesignedforprocessingvolume:200m3ofwastesperday,wegetthefollowingindicatorsfromthecalculationofthemass1m3/kg=600120tons/day.At20%moisturewastewegetthefollowingresult:Liquidpyrolysis-upto55%,Carbonfuelresidue(carbon):10-15%,synthesisgas:16.2-30%,Technicalwater-upto5%.Consumptionofpyrolysisreactoronsynthesis-gas=600m3/hour.ThefluegasesarecleanedupandcometotheCo2liquefaction,thatallowsyoutogetanextracommercialproduct-liquidcarbonicacid.
Thevolumeandcostofliquidcarbondioxideperhour/day/30days:CO2-600kg/14400kg/345600kgx0.18$=108$/2592$/62208$.2x720kWpowerplantconsumptionforsynthesisgas=400m3/h.
Pyrolysisproductsfor1day/30days:Pyrolysisliquid(density1liter=0.89kg)=58.74/762.21ton.Carbon-12/360tons,whichisimplementedbyprice:$14/1ton=$168/$5040Syngas-38880M3=19.44tons.Elaborationofsynthesis-gasperhour-1620M3.Wateris6/180tons,usedintheproductionprocess.
Fractionationpyrolysisliquids,wehavethefollowingresult:PetrolAI-92-25-30%.DENSITYat20°c,g/cm3=0.71-0.76Eurodiesel-5-45-50%.DENSITYat20°c,g/cm3=0.80-0.85Mazutm-100-12-15%.DENSITYat20°c,g/cm3=0.92-0.99Propane-butaneGasis10%.Fullyusedinproduction.Tar-heavy5-8%oftheDENSITYat20°c,g/cm3=1.2-1.5Calculationoftheamountoffuelbeingproducedatminimum%valuesandlowestprices.
Lightanddarkfactions,volume+pricefor1day/30daysMarkedasbluepricesmustbelocal.PetrolAI-92=10.426/312.78tonsx440$/t=4587.44$/137623.20$Diesel5euro=21.146/634.38tonsx440$/t=9304.24$/279127.20$MazutM-100=6.484/194.52tonsx211$/t=1368.12$/41043.72$.Tarheavy=3.524/105.73tonsx141$/t=496.88$/14907.93$TOTALAMOUNT(withoutcostofShoot)for1day/30days:15756.68$./472702$.ThecostoftheSHOOT-1day/30days:1763$/52890$
Equipmentincludedinthecomplexof200PROJECT(200-70-h).
Twinshaftshredder(producedinAustriaorGermany);VVU50m3of;Pyrolysisreactor200m3/14*1220*60;Blockcoolingandcondensation;Scrubbersforcleaningoffluegas;Co2liquefactionstation;Storagetankofliquidpyrolysis100m3;Obessernivanijastationanddegassing;Transitionaltank20m³;Pyrolysisoilpurificationstation;EquipmentforstoragedepotsandPETROLFILLINGSTATIONS-100(fortheupperfillfueltankers);GPJeS-720kW/400VMITSUDIESELAG-720p-t400-1R29;DSU-500kW/380VAD500-T400;Synthesisgascompressionstation;Liquefactionofpropanestation;Stationfiltersynthesisgas;Capacityofhighpressurecompressedgassynthesis2000l(CNG);Cryo-gastankforliquefiedpropaneground48M3(LNG);Fuelpump170l1561BladeMaster/min;Pressformetal;Petrolstoragetank80M3;Storagetank/t80M3;Fueloilstoragetank50M3;Bitumenheatedcapacity30m3;Fuelcleaningequipment;Hotoilpumpstation1*8PCs.;Pumpingstationabsorbentnaja1*6PCs.;Pipecommunication,electriccommunications,switchboards.
ContactsforInternationalProjects
Worldwideprojects
PINSECTORGroup
EstoniaHarjumaa75303LagediKooli18C
Mob.+3725107070
www.pinsector.com