PROJEKTA SPECIFIKA TERMĀLĀ SISTĒMA

Neuzskatiet reaktora nosaukumu vai dienas jaudu kā pilnīgu projekta specifikāciju.

Izejvielas, sagatavošana, darbības nepārtrauktība, kondensāts, gāzes drošība, produktu apstrāde, vides kontrole, utilītas un vietējā piegādes joma ir jākonfigurē kopā.

A

Apstiprināta maza mēroga atsauce

YSX-F1 līdz YSX-F5 apzīmē 1, 2, 3, 4 un 5 t/dienā sānslīdes vai moduļu plānošanas atsauces riepām, plastmasas vai eļļainu dūņu izmēģinājumi.

B

Materiālu līdzsvars

Eļļa, gāze, cietām vielām un metālu saturošām izlaidēm ir vajadzīgas reprezentatīvas izejvielas, stabili izpildīti dati un saskaņota izlases robeža.

C

Tirdzniecības robeža

Cenas, ekspluatācijas izmaksas, produkta vērtībai un atdevei ir nepieciešamas datētas kotācijas un vietējā tirgus pierādījumi.

Avota kontrole: apstiprināts YOTO grupas produktu reģistrs. Galīgie parametri tiek izsniegti uz projekta specifiskā tehniskā līguma.

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

  • The system has an annual production capacity of approximately 2,000 tons of pyrolytic charcoal, which holds significant market value. Turklāt, through energy recovery and carbon fixing process, it reduces carbon dioxide emissions by about 1,500 tons annually, which achieves the goal of ecological and economic coordination.

    • 1000 kgh Sludge Pyrolysis Production Line

    What are the differences in efficiency between continuous and intermittent pyrolysis systems?

    In pyrolysis solutions for municipal sludge treatment projects, different pyrolysis process routes directly impact operational efficiency and product quality. Among these, continuous and batch pyrolysis systems represent two typical operating modes, each with unique technical characteristics and applicable scenarios.

    Comparison of Continuous and Batch Pyrolysis Systems

    Intermittent pyrolysis systems primarily operate in batches. After completing each batch of processing, it is necessary to remove residues, feed new material, and restart the next cycle. Its advantages include simple structure, low equipment investment, and easy commissioning, which is suitable for small-scale processing.

    Turpretī, continuous pyrolysis systems utilize screw conveyors for continuous sludge feeding, so that the pyrolysis reaction proceeds under constant conditions. While the system design is more complex, it significantly enhances processing capacity and operational stability, which is suitable for medium to large-scale sludge treatment projects.

    Continuous pyrolysis systems offer significant advantages in energy utilization. There is less heat loss because the reaction temperature can remain within a relatively stable range. Tajā pašā laikā, the residual heat from pyrolysis can maintain the reaction temperature, so as to realize energy self-sufficiency.

    While in the intermittent system, each heating and cooling cycle causes significant energy fluctuations, resulting in obvious heat loss. Tāpēc, if there is no comprehensive waste heat recovery mechanism, the energy consumption for treating a unit of sludge will be higher.

    Continuous pyrolysis systems enable stable control of parameters such as temperature, residence time, and atmosphere, so the quality of pyrolysis products will be more consistent. Temperature and atmosphere fluctuations in batch systems are relatively sharp, so it is difficult to achieve precise control. This may bring uncertainty to subsequent resource recovery processes. On the other hand, intermittent systems offer flexible operation, and facilitate optimization of process parameters, which is suitable for experimental processing of diverse raw materials.

    We not only focus on sludge pyrolysis treatment but also possess extensive experience in solid waste resource recovery, piemēram, nolietoto riepu pirolīzes sistēma un atkritumu plastmasas pirolīzes rūpnīca. Contact us immediately to customize your own elektroniskā atkritumu apsaimniekošanas sistēma.

    JUŠUNKSIN
    YUSHUNXIN THERMAL CONVERSION

    Drilling waste, tank-bottom sludge, refinery sludge and marine oily residues differ in water, solids, 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, liquid, 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, enerģijas bilance, operating schedule and local product route.

    Operating schedule

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

    Enerģijas integrācija

    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.

    Tirdzniecības robeža

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

    PROJEKTA VIZUĀLI

    Skatiet pievienotās iekārtas robežu.

    Atsauces vizuālie materiāli atbalsta agrīnas izkārtojuma diskusijas. Noslēguma aprīkojums, izkārtojums un saskarnes ir apstiprinātas no projekta materiāla un vietas.

    Reference equipment view for early configuration discussion.
    Reference process evidence; final outputs and interfaces remain material- and project-specific.
    ATSAUCES KONFIGURĀCIJA

    Tulkojiet projekta faktus aprīkojuma sarakstā.

    Šī atsauces matrica parāda lēmuma loģiku. Galīgie daudzumi, modeļi un saskarnes ietilpst apstiprinātajā projekta priekšlikumā.

    Sistēmas bloksTipisks apjomsKonfigurācijas pamats
    Receiving and conditioningSampling, mixing, skrīnings, dewatering or pumpable-feed preparationWater, solids, salts and viscosity
    Controlled feedingAgitated buffer, pumps or screws, seals and isolationPhase stability and hazardous-waste controls
    Termiskā apstrādeReactor, 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
    LĒMUMU CEĻŠ, KAS PIEMĒROTS POSCIEM

    Virziet projektu tikai tad, kad ir pieejami nepieciešamie pierādījumi.

    Katrs vārti pārvērš klienta informāciju par noteiktu tehnisko vai komerciālo rezultātu nākamajam lēmumam.

    01

    Waste characterization

    Sample water, eļļa, solids, salts, sērs, metals and hazardous properties.

    IzvadeRepresentative waste profile
    02

    Conditioning trial

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

    IzvadeStable feed-preparation route
    03

    Output controls

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

    IzvadePermitted output-management plan
    04

    Facility integration

    Confirm licensing, containment, komunālie pakalpojumi, monitoring and acceptance.

    IzvadeSite-specific technical boundary
    PROJEKTA BUJ

    Jautājumi, kas jāatrisina pirms konfigurēšanas.

    Atbildes nosaka inženiertehnisko robežu; tie neaizstāj reprezentatīvu materiālu testēšanu vai vietējo atbilstības pārbaudi.

    What determines the continuous pyrolysis equipment list?

    Feedstock form, sastāvu, mitrums, piesārņojums, 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?

    Nē. They may share thermal-conversion principles, but their preparation, barošana, corrosion, kondensāts, solid handling and environmental controls differ materially.

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

    Nē. 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, darbības stabilitāte, sampled outputs, komunālie pakalpojumi, safety interlocks and the applicable emissions or residue tests.

    PROJEKTU INŽENIERĀCIJAS APSKATS

    Pirms aprīkojuma izvēles definējiet materiālu.

    Kopīgojiet reprezentatīvu materiāla aprakstu, pieejamais apjoms, vietnes statuss un mērķa rezultāti. YUSHUNXIN izmantos šos faktus, lai sagatavotu attiecīgo procesa robežu un konfigurācijas diskusiju.

    Sāciet projekta pārskatīšanu