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, inenga, 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.
See the connected equipment boundary.
Reference visuals support early layout discussion. Final equipment, arrangement and interfaces are confirmed from the project material and site.
Whakamāoritia ngā meka kaupapa ki tētahi rārangi taputapu.
Ko tenei matrix tohutoro e whakaatu ana i te arorau whakatau. Te rahinga whakamutunga, ko nga tauira me nga atanga kei roto i te tono kaupapa kua whakaaetia.
| Paraka pūnaha | Te whānuitanga angamaheni | Kaupapa whirihoranga |
|---|---|---|
| Gas preparation | Puehu, 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, inenga, pressure control and backup interface | Te iti rawa, normal and peak customer demand |
Whakanuia te kaupapa ina waatea noa nga taunakitanga e hiahiatia ana.
Ka hurihia e ia keeti nga korero a nga kaihoko ki te whakaputanga hangarau, arumoni ranei mo te whakatau ka whai ake.
Load profile
Capture minimum, normal and peak demand plus continuity requirements.
PutangaMetered or documented steam-demand basisTaurite pūngao
Match process-gas availability, internal heat demand and backup fuel.
PutangaVerified preliminary heat balanceUtility design
Define boiler, wai, condensate, header and emissions interfaces.
PutangaConnected utility configurationAcceptance plan
Agree test feedstock, stable window, meters and backup behavior.
PutangaMeasurable project acceptance sheetNga patai hei whakatau i mua i te whirihoranga.
Ko nga whakautu ka tautuhi i te rohe miihini; kare ratou e whakakapi i nga whakamatautau rawa, i te arotake hanganga ture ranei.
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, inenga, 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.
Tautuhia te rauemi i mua i te kowhiri i nga taputapu.
Tuhia he whakaahuatanga rauemi, rōrahi wātea, te mana o te pae me nga hua kua whakaritea. Ka whakamahia e YUSHUNXIN aua meka ki te whakarite i te rohenga tukanga e tika ana me te korerorero whirihoranga.
Carbonization with waste-heat steam supply
Configure the carbonization line and receiving steam load from one measured heat and mass balance.
He rauemi taumai
Prepared biomass plus hourly/daily feed profile and target carbon specification.
Nga putanga e tumanakohia ana
Biochar and a qualified waste-heat stream for an agreed steam duty.
Nga atanga kaupapa
Feed drying, carbonization gas, combustion, waste-heat boiler, water treatment, steam pressure/load and operating control.
Whakamahia te haupae e rite ana ki te rohe tukanga kua tohua.
| Tohutoro Putumōhio | Te kaha | Mana | Kōpaki tinana | Te rohenga |
|---|---|---|---|---|
| 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 |
Ture whirihoranga: Ko te kaha o te putumōhio he tohutoro whakamahere. Putanga pumau, mana tāuta/mahi, tapuwae, whakaora, mā, Ko nga tukunga me te tono whaipainga me whai rarangi taputapu kua whakaaetia, he tohu tohu me nga tikanga whakaae kua tuhia.
Ko nga korero e hiahiatia ana i mua i te whirihoranga me te whakahua
- Ko nga whakaahua maataki, nga whakaritenga me te tauira e waatea ana.
- Te kaha e hiahiatia ana me nga haora mo ia nekehanga, nga nekehanga mo ia ra me nga ra mahi.
- Nga putanga whainga, tikanga whakatauira me nga whakaritenga a te kaiwhiwhi o raro.
- Whenua pae, mana e wātea ana, wahie, wai, hau kōpeke me te rohe hanga.
- Te taiao o te rohe, ahi, rokiroki me nga whakaritenga mahi-haumaru.
- Te rohe tuku tono: taputapu, whakatakotoranga, tāutanga, komihana me te whakangungu.
