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, обслуговування, low-gas operation and backup-steam behavior for the receiving plant.
Перегляньте межі підключеного обладнання.
Довідкові візуальні матеріали підтримують раннє обговорення макета. Кінцеве обладнання, розташування та інтерфейси підтверджуються матеріалами проекту та сайтом.
Перекладіть факти проекту в список обладнання.
Ця опорна матриця показує логіку прийняття рішення. Кінцеві кількості, моделі та інтерфейси належать до затвердженої проектної пропозиції.
| Системний блок | Типовий обсяг | Основа конфігурації |
|---|---|---|
| Gas preparation | Пил, 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 |
Просувайте проект лише за наявності необхідних доказів.
Кожен шлюз перетворює інформацію про клієнта в певний технічний або комерційний результат для наступного рішення.
Load profile
Capture minimum, normal and peak demand plus continuity requirements.
ВихідMetered or documented steam-demand basisEnergy balance
Match process-gas availability, internal heat demand and backup fuel.
ВихідVerified preliminary heat balanceUtility design
Define boiler, води, condensate, header and emissions interfaces.
ВихідConnected utility configurationAcceptance plan
Agree test feedstock, stable window, meters and backup behavior.
ВихідMeasurable project acceptance sheetПитання, які потрібно вирішити перед налаштуванням.
Відповіді визначають інженерну межу; вони не замінюють репрезентативне випробування матеріалів або місцеву перевірку відповідності.
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, горіння, 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.
Перед вибором обладнання визначте матеріал.
Поділіться характерним описом матеріалу, доступний обсяг, статус сайту та цільові результати. YUSHUNXIN використовуватиме ці факти для підготовки обговорення відповідних меж процесу та конфігурації.
Carbonization with waste-heat steam supply
Configure the carbonization line and receiving steam load from one measured heat and mass balance.
Incoming material
Prepared biomass plus hourly/daily feed profile and target carbon specification.
Expected outputs
Biochar and a qualified waste-heat stream for an agreed steam duty.
Project interfaces
Feed drying, carbonization gas, горіння, waste-heat boiler, water treatment, steam pressure/load and operating control.
Use only the row matching the selected process boundary.
| Catalogue reference | Ємність | потужність | Physical envelope | Included boundary |
|---|---|---|---|---|
| SXTD820Continuous carbonization | 1–2 m³/h | 95 кВт | 600 m² catalogue land reference | Prepared biomass continuous carbonization line |
| SXTD1200Continuous carbonization | 3–5 m³/h | 110 кВт | 650 m² catalogue land reference | Prepared biomass continuous carbonization line |
| SXTD1500Continuous carbonization | 5–8 m³/h | 153 кВт | 800 m² catalogue land reference | Prepared biomass continuous carbonization line |
| SXTD1800Continuous carbonization | 8–10 m³/h | 178 кВт | 800 m² catalogue land reference | Prepared biomass continuous carbonization line |
| SXTD2000 - 10–14 classContinuous carbonization | 10–14 m³/h | 190 кВт | 850 m² catalogue land reference | Catalogue prints SXTD2000 for this class |
| SXTD2000 - 14–17 classContinuous carbonization | 14–17 m³/h | 220 кВт | 850 m² catalogue land reference | Catalogue repeats SXTD2000; final model code requires written confirmation |
Configuration rule: catalogue capacity is a planning reference. Stable throughput, installed/operating power, footprint, recovery, чистота, emissions and utility demand require the approved equipment list, representative material and written acceptance conditions.
Information required before configuration and quotation
- Representative material photos, specifications and available sample.
- Required capacity plus hours per shift, shifts per day and operating days.
- Цільові результати, sampling method and downstream receiver requirements.
- Site country, available power, fuel, води, compressed air and building limits.
- Local environmental, fire, storage and occupational-safety requirements.
- Requested delivery boundary: обладнання, макет, установка, commissioning and training.
