Tunto erogba gbóògì, ilana-gas itọju, igbomikana ojuse ati awọn onibara nya fifuye bi a ti sopọ eto.
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
- 02Ilọsiwaju 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.
See the connected equipment boundary.
Reference visuals support early layout discussion. Final equipment, arrangement and interfaces are confirmed from the project material and site.
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 block | Typical scope | Configuration basis |
|---|---|---|
| Gas preparation | Eruku, 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 |
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.
Load profile
Capture minimum, normal and peak demand plus continuity requirements.
OutputMetered or documented steam-demand basisEnergy balance
Match process-gas availability, internal heat demand and backup fuel.
OutputVerified preliminary heat balanceUtility design
Define boiler, omi, condensate, header and emissions interfaces.
OutputConnected utility configurationAcceptance plan
Agree test feedstock, stable window, meters and backup behavior.
OutputMeasurable project acceptance sheetQuestions to resolve before configuration.
Answers define the engineering boundary; they do not replace representative material testing or local compliance review.
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, ijona, boiler, omi itọju, 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.
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.
Carbonization pẹlu egbin-ooru nya ipese
Tunto laini carbonization ati gbigba fifuye nya si lati iwọn ooru kan ati iwọntunwọnsi pupọ.
Ohun elo ti nwọle
Baomass ti a ti pese pẹlu profaili ifunni wakati/ojoojumọ ati ipinnu erogba sipesifikesonu.
Awọn abajade ti a nireti
Biochar ati ṣiṣan igbona idoti ti o peye fun iṣẹ nyanu ti o gba.
Awọn atọkun ise agbese
Gbigbe ifunni, carbonization gaasi, ijona, egbin-ooru igbomikana, omi itọju, nya titẹ / fifuye ati awọn ọna Iṣakoso.
Lo nikan kana ibaamu ala ilana ti o yan.
| Itọkasi katalogi | Agbara | Agbara | apoowe ti ara | Aala to wa |
|---|---|---|---|---|
| SXTD820Ilọsiwaju carbonization | 1–2 m³/h | 95 kW | 600 m² katalogi ilẹ itọkasi | Pese baomasi lemọlemọfún carbonization laini |
| SXTD1200Ilọsiwaju carbonization | 3–5 m³/wakati | 110 kW | 650 m² katalogi ilẹ itọkasi | Pese baomasi lemọlemọfún carbonization laini |
| SXTD1500Ilọsiwaju carbonization | 5–8 m³/h | 153 kW | 800 m² katalogi ilẹ itọkasi | Pese baomasi lemọlemọfún carbonization laini |
| SXTD1800Ilọsiwaju carbonization | 8–10 m³/wakati | 178 kW | 800 m² katalogi ilẹ itọkasi | Pese baomasi lemọlemọfún carbonization laini |
| SXTD2000 - 10-14 kilasiIlọsiwaju carbonization | 10–14 m³/h | 190 kW | 850 m² katalogi ilẹ itọkasi | Katalogi tẹjade SXTD2000 fun kilasi yii |
| SXTD2000 - 14-17 kilasiIlọsiwaju carbonization | 14–17 m³/h | 220 kW | 850 m² katalogi ilẹ itọkasi | Katalogi tun SXTD2000; ik awoṣe koodu nbeere kọ ìmúdájú |
Ofin iṣeto ni: katalogi agbara ni a itọkasi igbogun. Idurosinsin losi, fi sori ẹrọ / ṣiṣẹ agbara, ifẹsẹtẹ, imularada, mimọ, awọn itujade ati ibeere ohun elo nilo atokọ ohun elo ti a fọwọsi, ohun elo aṣoju ati awọn ipo gbigba kikọ.
Alaye ti o nilo ṣaaju iṣeto ati asọye
- Awọn fọto ohun elo aṣoju, ni pato ati ki o wa ayẹwo.
- Agbara ti a beere pẹlu awọn wakati fun ayipada kan, iṣinipo fun ọjọ kan ati ki o ṣiṣẹ ọjọ.
- Awọn abajade ibi-afẹde, ọna iṣapẹẹrẹ ati ibosile awọn ibeere olugba.
- Orilẹ-ede ojula, agbara to wa, idana, omi, fisinuirindigbindigbin air ati ile ifilelẹ.
- Ayika agbegbe, ina, ibi ipamọ ati iṣẹ-ailewu awọn ibeere.
- Ti beere aala ifijiṣẹ: ohun elo, ifilelẹ, fifi sori ẹrọ, Ifiranṣẹ ati ikẹkọ.
