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, фишор, quality and continuity basis.
Steam demand
Provide minimum, normal and peak demand, operating hours, фишор, 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.
Сарҳади таҷҳизоти пайвастшударо бубинед.
Визуалиҳои истинод муҳокимаи тарҳбандии барвақтро дастгирӣ мекунанд. Таҷҳизоти ниҳоӣ, Тартиб ва интерфейсҳо аз мавод ва сайти лоиҳа тасдиқ карда мешаванд.
Далелҳои лоиҳаро ба рӯйхати таҷҳизот тарҷума кунед.
Ин матритсаи истинод мантиқи қарорро нишон медиҳад. Миқдори ниҳоӣ, моделҳо ва интерфейсҳо ба пешниҳоди лоиҳаи тасдиқшуда тааллуқ доранд.
| Блоки системавӣ | Доираи маъмулӣ | Асоси конфигуратсия |
|---|---|---|
| Gas preparation | чанг, 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 |
Лоиҳаро танҳо дар сурати мавҷуд будани далелҳои зарурӣ пешбарӣ кунед.
Ҳар як дарвоза маълумоти муштариро ба натиҷаи муайяншудаи техникӣ ё тиҷоратӣ барои қарори навбатӣ табдил медиҳад.
Load profile
Capture minimum, normal and peak demand plus continuity requirements.
НатиҷаMetered or documented steam-demand basisEnergy balance
Match process-gas availability, internal heat demand and backup fuel.
НатиҷаVerified preliminary heat balanceUtility design
Define boiler, об, condensate, header and emissions interfaces.
НатиҷаConnected utility configurationAcceptance plan
Agree test feedstock, stable window, meters and backup behavior.
НатиҷаMeasurable project acceptance sheetСаволҳое, ки бояд пеш аз конфигуратсия ҳал карда шаванд.
Ҷавобҳо сарҳади муҳандисиро муайян мекунанд; онҳо санҷиши маводи намояндагӣ ё баррасии мувофиқати маҳаллиро иваз намекунанд.
What information is needed from the steam user?
Provide minimum, normal and peak steam demand, фишор, 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.
Пеш аз интихоби таҷҳизот, маводро муайян кунед.
Тавсифи маводро мубодила кунед, ҳаҷми дастрас, ҳолати сайт ва натиҷаҳои ҳадаф. ЮШУНСИН ин далелҳоро барои омода кардани сарҳади раванд ва муҳокимаи конфигуратсияи дахлдор истифода хоҳад кард.
Carbonization with waste-heat steam supply
Configure the carbonization line and receiving steam load from one measured heat and mass balance.
Маводи воридотӣ
Prepared biomass plus hourly/daily feed profile and target carbon specification.
Натиҷаҳои пешбинишуда
Biochar and a qualified waste-heat stream for an agreed steam duty.
Интерфейси лоиҳа
Feed drying, carbonization gas, combustion, waste-heat boiler, water treatment, steam pressure/load and operating control.
Танҳо сатри мувофиқи сарҳади раванди интихобшударо истифода баред.
| Маълумотнома каталог | Иқтидор | Қувва | Лифофаи ҷисмонӣ | Сарҳади дохилшуда |
|---|---|---|---|---|
| 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 |
Қоидаи конфигуратсия: иқтидори каталоги истинод ба нақша аст,. Ҳаҷми мӯътадил, қудрати насбшуда/амалкунанда, изи по, барқароршавӣ, покӣ, партовҳо ва талаботи коммуналӣ рӯйхати таҷҳизоти тасдиқшударо талаб мекунанд, шартҳои қабули маводи намояндагӣ ва хаттӣ.
Маълумоте, ки пеш аз конфигуратсия ва иқтибос лозим аст
- Суратҳои маводҳои намояндагӣ, мушаххасот ва намунаи дастрас.
- Иқтидори зарурӣ плюс соат дар як смена, смена дар як рӯз ва рӯзҳои корӣ.
- Натиҷаҳои мақсаднок, усули интихоб ва талаботи қабулкунандаи поёноб.
- Кишвари сайт, қувваи дастрас, сӯзишворӣ, об, ҳаво фишурда ва ҳудуди бино.
- Муҳити зисти маҳаллӣ, оташ, талаботҳои нигоҳдорӣ ва бехатарии меҳнат.
- Сарҳади интиқоли дархостшуда: тачхизот, тарҳрезӣ, насб, ба истифода додан ва тайёр кардан.
