Configure carbon production, process-gas treatment, boiler duty and the customer steam load as a connected system.
Turn stable carbonization heat into useful industrial steam.
A steam project should be designed around the receiving process load. Carbonization gas, supplementary fuel, boiler duty, water treatment and backup capacity must work as one operating system.
Keep carbon quality and steam reliability under separate control
The carbonizer creates the primary product; the energy train converts suitable process gas and heat into a controlled utility.
- 01Biomass drying and feeding
- 02Continuous carbonization
- 03Dust and condensable separation
- 04Gas cleaning and controlled combustion
- 05Steam generation and water treatment
- 06Distribution, metering and backup supply
Define the user before defining the boiler
Food and chemical plants require a clear hourly steam profile, pressure, quality and continuity basis.
Steam demand
Provide minimum, normal and peak demand, operating hours, pressure, temperature and seasonal production schedule.
Water system
Define raw-water quality, treatment, deaeration, blowdown, condensate return and make-up-water capacity.
Fuel stability
Gas cleaning, buffer volume, burner turndown and supplementary fuel determine pressure stability during feed or quality changes.
Interface boundary
Agree the battery limit for boiler house, steam header, metering, condensate return, civil works and operating responsibility.
Verify both carbon output and usable steam
Acceptance should be based on documented feedstock, operating conditions and measurement methods.
Carbon product
Record yield and product properties only against the tested biomass and agreed thermal program.
Steam output
Meter flow, pressure and temperature during a defined stable operating window instead of using theoretical heat alone.
Emissions boundary
Identify combustion, particulate and condensable controls and the local monitoring or permit requirements.
Continuity plan
Define startup, shutdown, maintenance, low-gas operation and backup-steam behavior for the receiving plant.
Lihat batas peralatan yang terhubung.
Visual referensi mendukung diskusi tata letak awal. Peralatan terakhir, pengaturan dan antarmuka dikonfirmasi dari materi proyek dan situs.
Terjemahkan fakta proyek ke dalam daftar peralatan.
Matriks referensi ini menunjukkan logika keputusan. Jumlah akhir, model dan antarmuka termasuk dalam proposal proyek yang disetujui.
| Blok sistem | Ruang lingkup yang khas | Dasar konfigurasi |
|---|---|---|
| Gas preparation | Debu, condensable and moisture control with safe buffering | Carbonization-gas variability and burner limits |
| Combustion system | Controlled burner, combustion chamber and safety interlocks | Steam duty, turndown and supplementary-fuel plan |
| Boiler island | Boiler, economizer, blowdown, instruments and protection | Pressure, temperature and operating code basis |
| Water and condensate | Treatment, deaeration, make-up water and condensate return | Source-water quality and user return conditions |
| Steam delivery | Header, metering, pressure control and backup interface | Minimum, normal and peak customer demand |
Lanjutkan proyek hanya jika bukti yang diperlukan tersedia.
Setiap gerbang mengubah informasi pelanggan menjadi keluaran teknis atau komersial tertentu untuk keputusan berikutnya.
Load profile
Capture minimum, normal and peak demand plus continuity requirements.
KeluaranMetered or documented steam-demand basisEnergy balance
Match process-gas availability, internal heat demand and backup fuel.
KeluaranVerified preliminary heat balanceUtility design
Define boiler, air, condensate, header and emissions interfaces.
KeluaranConnected utility configurationAcceptance plan
Agree test feedstock, stable window, meters and backup behavior.
KeluaranMeasurable project acceptance sheetPertanyaan yang harus diselesaikan sebelum konfigurasi.
Jawaban menentukan batas teknik; hal ini tidak menggantikan pengujian material yang representatif atau tinjauan kepatuhan lokal.
What information is needed from the steam user?
Provide minimum, normal and peak steam demand, pressure, temperature, operating schedule, condensate return, water quality and continuity requirement.
Can process gas alone guarantee continuous steam supply?
Not without verification. Buffering, burner turndown, supplementary fuel and backup capacity may be needed when feedstock or gas production varies.
What belongs in the steam-system boundary?
The scope may include gas treatment, combustion, boiler, water treatment, deaeration, blowdown, steam header, metering, condensate return and backup interfaces.
How should steam acceptance be measured?
Use metered flow, pressure and temperature during a defined stable operating window with the agreed biomass, carbonization conditions and auxiliary loads.
Tentukan bahan sebelum memilih peralatan.
Bagikan deskripsi materi yang representatif, volume yang tersedia, status situs dan keluaran target. YUSHUNXIN akan menggunakan fakta-fakta tersebut untuk mempersiapkan batasan proses dan diskusi konfigurasi yang relevan.
Carbonization with waste-heat steam supply
Configure the carbonization line and receiving steam load from one measured heat and mass balance.
Materi masuk
Prepared biomass plus hourly/daily feed profile and target carbon specification.
Output yang diharapkan
Biochar and a qualified waste-heat stream for an agreed steam duty.
Antarmuka proyek
Feed drying, carbonization gas, combustion, waste-heat boiler, water treatment, steam pressure/load and operating control.
Gunakan hanya baris yang cocok dengan batas proses yang dipilih.
| Referensi katalog | Kapasitas | Kekuatan | Amplop fisik | Termasuk batas |
|---|---|---|---|---|
| SXTD820Continuous carbonization | 1–2 m³/h | 95 kW | 600 m² catalogue land reference | Prepared biomass continuous carbonization line |
| SXTD1200Continuous carbonization | 3–5 m³/h | 110 kW | 650 m² catalogue land reference | Prepared biomass continuous carbonization line |
| SXTD1500Continuous carbonization | 5–8 m³/h | 153 kW | 800 m² catalogue land reference | Prepared biomass continuous carbonization line |
| SXTD1800Continuous carbonization | 8–10 m³/h | 178 kW | 800 m² catalogue land reference | Prepared biomass continuous carbonization line |
| SXTD2000 - 10–14 classContinuous carbonization | 10–14 m³/h | 190 kW | 850 m² catalogue land reference | Catalogue prints SXTD2000 for this class |
| SXTD2000 - 14–17 classContinuous carbonization | 14–17 m³/h | 220 kW | 850 m² catalogue land reference | Catalogue repeats SXTD2000; final model code requires written confirmation |
Aturan konfigurasi: kapasitas katalog merupakan acuan perencanaan. Throughput yang stabil, daya terpasang/pengoperasian, tapak, pemulihan, kemurnian, emisi dan permintaan utilitas memerlukan daftar peralatan yang disetujui, syarat penerimaan materi dan tertulis yang representatif.
Informasi diperlukan sebelum konfigurasi dan kutipan
- Foto materi yang representatif, spesifikasi dan sampel yang tersedia.
- Kapasitas yang dibutuhkan ditambah jam kerja per shift, shift per hari dan hari operasional.
- Menargetkan keluaran, metode pengambilan sampel dan persyaratan penerima hilir.
- Negara situs, daya yang tersedia, bahan bakar, air, udara bertekanan dan batas bangunan.
- Lingkungan setempat, api, persyaratan penyimpanan dan keselamatan kerja.
- Batas pengiriman yang diminta: peralatan, tata letak, instalasi, komisioning dan pelatihan.
