JZ-013 used tyre refinery equipment

used tyre refinery equipmentcanpyrolysisthetires,outputfueloil,steelwiresandcarbonblackwithoutpollution. Severalcharacteristicsofthestreamlinedseriesrefiningequipment 1.Eachsetofequipmentarecomposedbytenparts: a.mainenginehorizontaltyperevolvingsplitprocessor b.Horizontal-fixeddistillationProcessor c.Feeding-insystem. d.Tappingsystem. e.Centralelectricallycontrolledsystem. f.Condensationsystem. g.Everyoilrefiningsystems... h.fuelgasheatingsystem(wastegasprocessingsystem). i.Wastewaterprocessingsystem.. j.Fluedustremovalsystem.. 2.Domesticpioneerofthistechnology a.Initskeyinstallmentdecompositionprocessordesign,hasthoroughlyovercomethedisadvantagesofthedomesticpresentverticalflatbasesplitprocessor,suchasbottompartialbeingheatednon-uniformity,easytobreak,lowoutput,shortservice-lifeisshortandsoon,themainengineuseshorizontal-type360ostructure-0.4R/M b.Fastpracticalfeed-inanddischargesystem.Thehighestfeed-inquantityevery24hourachieved5tons,Dischargetimefor300kgcarbonblackonlyneeds90minutes.Thehighestfeed-inamountoftheintegralunitequipmentevery24hoursachieves15tons. c.Highlyeffectivelygasheatingsystem.Intheprocessofrefiningoil,afterthegasisheatedupto150,itwillproducealargeamountofunliquefiedgas-CH4&C4H8,whichcantbeformedatnormaltemperature,normalpressure.Ifthosegaseshavebeenfullyburningbythespecificdesignedgasnozzle,theycanproduceagreatamountofenergyandeconomizeresources.Takethebunkercoalastheexample,whenthereisnofuelgasascombustion-supportingfortheequipment,every24hoursneed1.2tonscoals.Afterthefuelgasaidcombustion,every24hourneed0.3tonscoal,whichenhancesproductionefficiencyinthelargescaleandreducedthefuelcost? d.Fluedustcatchersystem.Itmatchesthebidirectionalwaterimpacttypetornadodustremovalroom,andtherateofthefluedustcatchisaccessthan95%. 3.CompanyCommitment: Thecompanypledgethateachkindofseriesequipmentwesellhavetheconsummationthepost-saleservice,awarrantyperiodyear,thatthoroughlysettledowncustomerextraworries. Security Themainequipmentisofhighsafety.ThephaseoftheunliquefizablewastegasproducedduringtheprocessisalkylfromC1toC4,whichisdangerouswhenburningdirectly.Inourprocess,itistransferredfirstthroughawaterclosedeviceandasafetydevice-burningairmuzzle.Beforeburning,weshouldensurethesafetyofproduction. EnvironmentalProtective Disposewastegas,liquid,andresiduaintheprocess: 1.Wastegas:Transferredthroughtwosafetydevice:waterclose&burningairnozzle.Fullyburnt,notonlyeliminatedpollutantbutalsominimizedthequantityoffuels.Forsmokedustdischarge,weapplyseriesmachinesofpatentinourcompanyDesulphurizationanddustremoverwhichcouldcontrolthesmokedustdischargeamountmeetrelativestandardsofGB-2001. 2.Wasteliquid:Producedwasteacidicwaterintheprocessofoildisposing(50kgprocessfrom1tonofoileasytoprocessforsmallquantity).counteracttheliquidbyalkalescentliquidsolution.Afterthreestageoffiltration,thelitmuslesswastewaterwasintroducedtoevaporator(usetheheatoftheflueofmainprocessorasitsheatingresource) 3.Wastesolid.Thesolidresiduawillbeleftafterthecatalystsplittingfromscrapplastic,approximatelycomposesthewasteplasticweightabout5%to10%.Itsmaincomponentisthethickblackcarbon.Itcanbetherawmaterialoftheproductionindustryofblackcarbon.Alsocouldbemixedwiththepulverizedcoalashwhichproducesfortherawmaterialthermalpowerplant,alsocouldbetherawmaterialofmanufacturepulverizedcoalashbrick(onekindofenvironmentalprotectionbuildingmaterial).