PROJECT-SPECIFIC THERMAL SYSTEM

Do not treat a reactor name or daily capacity as a complete project specification.

Materia prima, preparation, operating continuity, condensation, gas safety, product handling, kontrolnan ambiental, utilities and local delivery scope must be configured together.

UN

Approved small-scale reference

YSX-F1 to YSX-F5 denote 1, 2, 3, 4 i 5 t/day skid or modular planning references for tire, plastic or oily-sludge trials.

B

Material balance

Oil, gas, solids and metal-bearing outputs require representative feedstock, stable-run data and an agreed sampling boundary.

C

Commercial boundary

Prices, operating costs, product value and return require dated quotations and local market evidence.

Source control: approved YOTO group product register. Final parameters are issued on the project-specific technical agreement.

The HTP-1000 name is retained as a project reference. Stable throughput, dryer duty, reactor configuration, gas treatment, controls and price require representative sludge analysis and a written quotation.

  • E sistema tin un kapasidat di produkshon anual di mas o ménos 2,000 ton di karbon pirolítiko, ku ta kontené un balor signifikante riba merkado. Ademas, pa medio di rekuperashon di energia i proseso di fihamentu di karbon, e ta redusí dióksido di karbon emishonnan pa mas o ménos 1,500 ton anualmente, ku ta logra e meta di kordinashon ekológiko i ekonómiko.

  • 1000 Liña di Produkshon di Pirolisis di Lodo di kgh

    Kiko ta e diferensianan den efisiensia entre sistemanan di pirolisis kontinuo i intermitente?

    Den solushonnan di pirolisis pa proyektonan di tratamentu di lodo di munisipio, diferente ruta di proseso di pirolisis ta impaktá efisiensia operashonal i kalidat di produkto direktamente. Entre esakinan, sistemanan di pirolisis kontinuo i di lote ta representá dos moda di operashon típiko, kada un ku karakterístika tékniko úniko i senarionan aplikabel.

    Komparashon di Sistemanan di Pirolisis Kontinuo i di Lote

    Sistemanan di pirolisis intermitente ta operá prinsipalmente den lotenan. Despues di kompletá kada lote di prosesamentu, ta nesesario pa kita residuonan, alimentá material nobo, i restart e siguiente siklo. Su bentahanan ta inkluí struktura simpel, invershon abou den ekipo, i enkargo fásil, ku ta adekuá pa prosesamentu na eskala chikí.

    Na kontraste, sistemanan di pirolisis kontinuo ta utilisá transportadónan di skru pa alimentashon di lodo kontinuo, di manera ku e reakshon di pirolisis ta sigui bou di kondishonnan konstante. Miéntras ku e diseño di e sistema ta mas kompleho, e ta mehorá kapasidat di prosesamentu i stabilidat operashonal signifikantemente, ku ta adekuá pa proyektonan di tratamentu di lodo na eskala mediano pa grandi.

    Sistemanan di pirolisis kontinuo ta ofresé bentahanan signifikante den uso di energia. Tin ménos pèrdida di kalor pasobra e temperatura di reakshon por keda denter di un rango relativamente stabil. Na mes momento, e kalor residual di pirolisis por mantené e temperatura di reakshon, pa asina realisá outosufisiensia di energia.

    Miéntras ku den e sistema intermitente, kada siklo di keintamentu i friamentu ta kousa fluktuashonnan signifikante di energia, resultando den pèrdida di kalor opvio. P'esei, si no tin un mekanismo di rekuperashon di kalor di desperdisio amplio, e konsumo di energia pa trata un unidat di lodo lo ta mas haltu.

    Sistemanan di pirolisis kontinuo ta permití kontrol stabil di parameternan manera temperatura, ora di residensia, i atmósfera, pues e kalidat di produktonan di pirolisis lo ta mas konsistente. Fluktuashonnan di temperatura i atmósfera den sistemanan di lote ta relativamente skèrpi, pues ta difísil pa logra un kòntròl presis. Esaki por trese insertidumbre pa e prosesonan di rekuperashon di rekurso siguiente. Di otro banda, sistemanan intermitente ta ofresé operashon fleksibel, i fasilitá optimalisashon di parameternan di proseso, ku ta adekuá pa prosesamentu eksperimental di diferente materia prima.

    Nos no solamente ta enfoká riba tratamentu di pirolisis di lodo pero tambe ta poseé eksperensia amplio den rekuperashon di rekurso di desperdisio sólido, manera sistema di pirolisis di taira di desperdisio i planta di pirolisis di plèstik di desperdisio. Tuma kontakto ku nos mesora pa personalisá bo mes sistema di maneho di desperdisio elektróniko.

    YUSHUNXIN
    YUSHUNXIN THERMAL CONVERSION

    Drilling waste, tank-bottom sludge, refinery sludge and marine oily residues differ in water, sólidonan, hydrocarbons, salt, sulfur and metals. They should not share an assumed standard configuration.

    Reference three-dimensional layout of a continuous thermal conversion line
    01 / CONNECTED PROCESS

    Follow the material, vapor, líkido, gas and solid paths

    The reactor is one part of the line. Commercial operability depends on how each stream is prepared, transferred, controlled and discharged.

    1. 01Material characterization
    2. 02Feed preparation and sealed transfer
    3. 03Controlled thermal conversion
    4. 04Vapor separation and staged condensation
    5. 05Non-condensable gas safety and reuse
    6. 06Solid cooling, discharge and product handling
    02 / MATERIAL-SPECIFIC DESIGN

    Configuration questions that change the proposal

    The following points should be resolved before selecting a capacity or preparing a commercial quotation.

    Conditioning and dewatering

    High water content changes feeding stability and energy demand; pumping, mixing, dewatering or screw feeding may be required.

    Fouling and corrosion

    Salt, fine solids and heavy fractions influence reactor cleaning, metallurgy and condensation-system maintenance.

    Recovered phases

    Separate the project basis for recovered oil, water and treated solids, including sampling and permitted downstream use.

    Hazardous-waste boundary

    Licensing, residue classification, worker protection and emissions monitoring must be defined for the project jurisdiction.

    03 / OPERATING MODEL

    Make utilities and product outlets visible before investment

    A useful feasibility review connects the mass balance, energy balance, operating schedule and local product route.

    Operating schedule

    Define planned hours per day, shutdown windows, cleaning strategy, labor model and feedstock storage capacity.

    Energy integration

    Evaluate non-condensable gas reuse, startup fuel, electrical loads, cooling demand and optional downstream energy use as one balance.

    Quality control

    Set sampling points for incoming material, condensate fractions, recovered solids, wastewater and exhaust gas.

    Commercial boundary

    Budgetary results remain conditional until the feedstock, lugá, product route and local compliance requirements are confirmed.

    KONFIGURASHON DI REFERENSIA

    Tradusí echonan di proyekto den un lista di ekipo.

    E matris di referensia aki ta mustra e lógika di desishon. Kantidatnan final, modelonan i interfasenan ta pertenesé na e proposishon di proyekto aprobá.

    Blòki di sistemaAlkanse típikoBase di konfigurashon
    Receiving and conditioningSampling, mixing, screening, dewatering or pumpable-feed preparationWater, sólidonan, salts and viscosity
    Controlled feedingAgitated buffer, pumps or screws, seals and isolationPhase stability and hazardous-waste controls
    Tratamentu termalReactor, heating, fouling management and cleanout accessHydrocarbon range, solids and corrosion basis
    Phase recoveryVapor separation, oil-water handling and treated-solid coolingSampling and permitted downstream routes
    Environmental and residueGas treatment, wastewater, residue containment and monitoringLocal licensing and acceptance tests
    TRAINO DI DECISION CU STAGE-GATED

    Adelantá e proyekto solamente ora e evidensia nesesario ta disponibel.

    Kada porta ta kombertí informashon di kliente den un output tékniko òf komersial definí pa e siguiente desishon.

    01

    Waste characterization

    Sample water, zeta, sólidonan, salts, sulfur, metals and hazardous properties.

    SalidaRepresentative waste profile
    02

    Conditioning trial

    Verify mixing, dewatering, pumping or screw-feeding requirements.

    SalidaStable feed-preparation route
    03

    Output controls

    Define recovered phases, treated residue, wastewater and sampling methods.

    SalidaPermitted output-management plan
    04

    Facility integration

    Confirm licensing, containment, utilidatnan, monitoring and acceptance.

    SalidaSite-specific technical boundary
    FAQ DI PROYEKTO

    Preguntanan pa resolvé promé ku konfigurashon.

    Kontesta ta definí e frontera di ingenieria; nan no ta remplasá prueba di material representativo òf revishon di kumplimentu lokal.

    What determines the continuous pyrolysis equipment list?

    Feedstock form, komposishon, humedat, contamination, planned operating schedule, recovered-product route, site utilities and permit requirements determine the configuration.

    Can tires, plastics and oily sludge use exactly the same line?

    No. They may share thermal-conversion principles, but their preparation, feeding, corrosion, condensation, solid handling and environmental controls differ materially.

    Can recovered oil performance be guaranteed from a general material description?

    No. Representative analysis and an agreed sampling method are required before recovered-liquid quantity, quality or downstream use can be evaluated.

    What should be included in acceptance testing?

    Define feedstock, run duration, mass balance, operating stability, sampled outputs, utilidatnan, safety interlocks and the applicable emissions or residue tests.

    REVISHON DI INGENIERIA DI PROYEKTO

    Definí e material promé ku selektá e ekipo.

    Kompartí un deskripshon di material representativo, volúmen disponibel, status di e sitio i salidanan di meta. YUSHUNXIN lo usa e echonan ei pa prepará e frontera di proseso relevante i e diskushon di konfigurashon.

    Kuminsá Repasá Proyekto