Rated evaporation
State the required rated steam output in kg/h or t/h, including peak demand, warm-up load and distribution losses.
Steam-system specification
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Focused on quality, system engineering and equipment reliability, JIELI selects each steam boiler system from the actual load, pressure, water, fuel, delivery constraints and boiler-room scope.
Selection information
A stable plant needs steam capacity, pressure, combustion, water treatment, condensate, efficiency, controls and the supply boundary to agree with each other.
State the required rated steam output in kg/h or t/h, including peak demand, warm-up load and distribution losses.
Provide the required pressure at the process, allowing for distribution pressure drop and saturated or superheated steam condition.
Confirm natural gas, LPG, oil, wood chips, other biomass or coal, together with pressure, composition and other available fuel data.
Provide limits for NOx, SOx, particulate matter and stack discharge, plus any continuous monitoring or approval requirements.
Define softened or demineralized water, deaeration, blowdown treatment, condensate recovery and the available raw-water analysis.
State the expected efficiency and whether an economizer, condensate recovery, blowdown heat recovery or other measures are required.
State preferred control components or PLC/DCS platform, automation level, remote communication needs, and preferred instrument grade or brand level.
Clarify whether the requirement covers the boiler only or a complete plant with burner, water treatment, feed system, stack, controls and site services.
Condensate return engineering
This comparison isolates the saturated-liquid sensible heat that leaves with 1 t/h of condensate. It makes the pressure effect visible before adding flash-steam recovery, makeup-water treatment, chemical or pumping benefits.

Pabs = (Pg + 1.0332) × 0.0980665 MPaQloss = hf × 1,000 ÷ 4.1868 kcal/hVgas = Qloss ÷ 8,600 Nm³/hUSD = (Vgas × 4) ÷ 7.20| Gauge pressure | Absolute pressure | Saturation temp. | Saturated liquid hf | Sensible heat loss | Share of hg | Gas equivalent | USD / h |
|---|---|---|---|---|---|---|---|
| 2 kgf/cm²(g) | 2.975 bar(a) | 133.24°C | 560.22 kJ/kg | 133,810 kcal/h | 20.56% | 15.56 Nm³/h | US$8.64 |
| 3 kgf/cm²(g) | 3.955 bar(a) | 143.21°C | 602.98 kJ/kg | 144,020 kcal/h | 22.03% | 16.75 Nm³/h | US$9.30 |
| 4 kgf/cm²(g) | 4.936 bar(a) | 151.35°C | 638.09 kJ/kg | 152,400 kcal/h | 23.22% | 17.72 Nm³/h | US$9.85 |
| 5 kgf/cm²(g) | 5.917 bar(a) | 158.29°C | 668.13 kJ/kg | 159,580 kcal/h | 24.25% | 18.56 Nm³/h | US$10.31 |
| 6 kgf/cm²(g) | 6.897 bar(a) | 164.36°C | 694.55 kJ/kg | 165,890 kcal/h | 25.15% | 19.29 Nm³/h | US$10.72 |
| 7 kgf/cm²(g) | 7.878 bar(a) | 169.78°C | 718.23 kJ/kg | 171,550 kcal/h | 25.95% | 19.95 Nm³/h | US$11.08 |
| 8 kgf/cm²(g) | 8.859 bar(a) | 174.69°C | 739.77 kJ/kg | 176,690 kcal/h | 26.68% | 20.55 Nm³/h | US$11.41 |
| 9 kgf/cm²(g) | 9.839 bar(a) | 179.18°C | 759.58 kJ/kg | 181,420 kcal/h | 27.36% | 21.10 Nm³/h | US$11.72 |
| 10 kgf/cm²(g) | 10.820 bar(a) | 183.34°C | 777.96 kJ/kg | 185,810 kcal/h | 27.98% | 21.61 Nm³/h | US$12.00 |
| 11 kgf/cm²(g) | 11.801 bar(a) | 187.21°C | 795.14 kJ/kg | 189,920 kcal/h | 28.57% | 22.08 Nm³/h | US$12.27 |
| 12 kgf/cm²(g) | 12.781 bar(a) | 190.83°C | 811.29 kJ/kg | 193,770 kcal/h | 29.12% | 22.53 Nm³/h | US$12.52 |
Engineering note: “kg pressure” is treated as kgf/cm² gauge. Saturated-water properties follow IAPWS-IF97; the table uses the saturated-liquid enthalpy only. Direct gas equivalence assumes 100% conversion, so actual purchased fuel is higher after boiler and system efficiency. It excludes flash-steam recovery, makeup-water cost, treatment chemicals and piping losses. References: IAPWS-IF97, NIST steam tables and the U.S. DOE condensate-return guidance.
Boiler construction
WNS wet-back fire-tube boilers suit many compact industrial duties. SZS water-tube systems support higher output, pressure and response requirements. Biomass systems add fuel handling, furnace, ash and flue-gas treatment scope.

WNS project evidence
Four verified photos from the JIELI THERMAL project library show the installed boiler, burner interface, boiler-room arrangement and a workshop production row.




Capacity-led search
Capacity terms help buyers find a starting point, but pressure, feedwater temperature and steam condition must be defined before a model or fuel rate is confirmed.
| Capacity query | Output | Common configuration | Selection note |
|---|---|---|---|
| 1 ton steam boiler | 1,000 kg/h | Compact fire-tube boiler | Check peak demand and burner turndown |
| 2 ton gas steam boiler | 2,000 kg/h | WNS gas/oil boiler | Confirm gas pressure and feedwater temperature |
| 4 TPH steam boiler | 4,000 kg/h | Fire-tube or project-specific option | Evaluate condensate return and economizer |
| 10 ton biomass steam boiler | 10,000 kg/h | Biomass furnace and boiler system | Fuel analysis and emissions scope are essential |
| 20 TPH industrial steam boiler | 20,000 kg/h | Engineered water-tube system | Review redundancy, pressure and site logistics |
| 35 TPH industrial steam boiler | 35,000 kg/h | Engineered water-tube or multi-boiler plant | Confirm pressure, site logistics, redundancy and water-treatment capacity |

Boiler-room scope
To verify manufacturing capability and inspect real project photos, use the JIELI THERMAL steam boiler product and factory resources.
Real manufacturing & project evidence
Real fabrication, dispatch and installed-system records are grouped on this product page. The flat structure gives buyers immediate evidence while giving every image a clear, crawlable steam-boiler context.
WNS fire-tube packages and SZS water-tube installations with real burner, piping and boiler-room interfaces.



DZL, DZG and DZW boilers for wood chips and other qualified biomass fuels, shown from fabrication through field installation.






Furnace and coil evidence for DZL and SZL industrial steam boiler series.


Responsive WebP images are lazy-loaded; H.264 video uses metadata preload so this evidence section does not delay the first page view.
Engineering FAQ
A reliable quotation needs process and water-side data. A capacity-only request cannot establish consumption, controls or system scope.
Calculate connected demand, diversity, startup demand, distribution losses and future margin. Then confirm pressure, steam condition, water, condensate, fuel and load profile.
Fire-tube units pass combustion gas through tubes surrounded by water and are common for many industrial duties. Water-tube units circulate water through externally heated tubes and generally suit higher capacity, pressure or faster response.
Hot condensate reduces makeup water, fuel and chemical treatment. Its return rate and temperature affect the feed system and expected efficiency.
Provide output, pressure, steam condition, fuel, feedwater quality, condensate return, operating hours, emissions limits and project location.
Request a selection check
Rated evaporation, pressure, fuel, emissions, water treatment and condensate plan, efficiency target, controls, supply scope and project country.