PROJECT-SPECIFIC THERMAL SYSTEM

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

Bahan suapan, persiapan, operating continuity, pemeluwapan, gas safety, product handling, kawalan alam sekitar, utilities and local delivery scope must be configured together.

A

Approved small-scale reference

YSX-F1 to YSX-F5 denote 1, 2, 3, 4 dan 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, kos operasi, 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. Daya pengeluaran yang stabil, dryer duty, reactor configuration, gas treatment, controls and price require representative sludge analysis and a written quotation.

  • Sistem ini mempunyai kapasiti pengeluaran tahunan kira-kira 2,000 tan arang pirolitik, yang memegang nilai pasaran yang ketara. Tambahan pula, melalui pemulihan tenaga dan proses penetapan karbon, ia mengurangkan karbon dioksida pelepasan oleh kira-kira 1,500 tan setiap tahun, yang mencapai matlamat penyelarasan ekologi dan ekonomi.

  • 1000 kgh Barisan Pengeluaran Pirolisis Enapcemar

    Apakah perbezaan kecekapan antara sistem pirolisis berterusan dan terputus-putus?

    Dalam penyelesaian pirolisis untuk projek rawatan enapcemar perbandaran, laluan proses pirolisis yang berbeza secara langsung memberi kesan kepada kecekapan operasi dan kualiti produk. Antaranya, sistem pirolisis berterusan dan kelompok mewakili dua mod operasi biasa, setiap satu dengan ciri teknikal yang unik dan senario yang boleh digunakan.

    Perbandingan Sistem Pirolisis Berterusan dan Berkelompok

    Sistem pirolisis terputus-putus terutamanya beroperasi dalam kelompok. Selepas menyelesaikan setiap kumpulan pemprosesan, adalah perlu untuk mengeluarkan sisa, memberi makan bahan baru, dan mulakan semula kitaran seterusnya. Kelebihannya termasuk struktur mudah, pelaburan peralatan yang rendah, dan pentauliahan yang mudah, yang sesuai untuk pemprosesan secara kecil-kecilan.

    Sebaliknya, sistem pirolisis berterusan menggunakan penghantar skru untuk penyusuan enapcemar berterusan, supaya tindak balas pirolisis berlaku dalam keadaan malar. Manakala reka bentuk sistem lebih kompleks, ia meningkatkan kapasiti pemprosesan dan kestabilan operasi dengan ketara, yang sesuai untuk projek rawatan enapcemar berskala sederhana hingga besar.

    Sistem pirolisis berterusan menawarkan kelebihan yang ketara dalam penggunaan tenaga. Terdapat kurang kehilangan haba kerana suhu tindak balas boleh kekal dalam julat yang agak stabil. Pada masa yang sama, sisa haba daripada pirolisis boleh mengekalkan suhu tindak balas, supaya dapat merealisasikan sara diri tenaga.

    Manakala dalam sistem terputus-putus, setiap kitaran pemanasan dan penyejukan menyebabkan turun naik tenaga yang ketara, mengakibatkan kehilangan haba yang jelas. Oleh itu, jika tiada mekanisme pemulihan haba sisa yang komprehensif, penggunaan tenaga untuk merawat satu unit enap cemar akan lebih tinggi.

    Sistem pirolisis berterusan membolehkan kawalan stabil parameter seperti suhu, masa tinggal, dan suasana, jadi kualiti produk pirolisis akan lebih konsisten. Turun naik suhu dan suasana dalam sistem kelompok agak tajam, jadi sukar untuk mencapai kawalan yang tepat. 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, seperti sistem pirolisis tayar sisa dan loji pirolisis plastik sisa. Contact us immediately to customize your own sistem pengurusan sisa elektronik.

    YUSHUNXIN
    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, cecair, 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, tapak, product route and local compliance requirements are confirmed.

    REFERENCE CONFIGURATION

    Translate project facts into an equipment list.

    This reference matrix shows the decision logic. Final quantities, models and interfaces belong in the approved project proposal.

    System blockTypical scopeConfiguration basis
    Receiving and conditioningSampling, mixing, screening, dewatering or pumpable-feed preparationWater, solids, salts and viscosity
    Controlled feedingAgitated buffer, pumps or screws, seals and isolationPhase stability and hazardous-waste controls
    Thermal treatmentReactor, 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
    STAGE-GATED DECISION PATH

    Advance the project only when the required evidence is available.

    Each gate turns customer information into a defined technical or commercial output for the next decision.

    01

    Waste characterization

    Sample water, minyak, solids, salts, sulfur, metals and hazardous properties.

    OutputRepresentative waste profile
    02

    Conditioning trial

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

    OutputStable feed-preparation route
    03

    Output controls

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

    OutputPermitted output-management plan
    04

    Facility integration

    Confirm licensing, containment, utiliti, monitoring and acceptance.

    OutputSite-specific technical boundary
    PROJECT FAQ

    Questions to resolve before configuration.

    Answers define the engineering boundary; they do not replace representative material testing or local compliance review.

    What determines the continuous pyrolysis equipment list?

    Feedstock form, gubahan, lembapan, pencemaran, 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, pemeluwapan, 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, utiliti, safety interlocks and the applicable emissions or residue tests.

    PROJECT ENGINEERING REVIEW

    Define the material before selecting the equipment.

    Share a representative material description, available volume, site status and target outputs. YUSHUNXIN will use those facts to prepare the relevant process boundary and configuration discussion.

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