The Ultimate Eco-Retrofit for Coal-Fired Boilers: How to Seamlessly Integrate a Direct-Connected Biomass Incinerator to Restore 100% Steam Capacity
Driven by global "Dual Carbon" goals and strict local policies phasing out coal-fired boilers, countless enterprises in food processing, paper making, textiles, chemicals, and regional centralized heating are facing a thorny dilemma. Their original coal-fired chain-grate or pulverized coal boilers have been ordered to shut down or be dismantled, yet the steam demand of their production lines hasn't decreased one bit.
How can a factory restore 100% of its steam capacity in the shortest possible time, with the lowest civil engineering costs, while completely shedding the environmental compliance risks of coal?

The answer is not to tear everything down and build a brand-new biomass boiler from scratch. The solution is to adopt a direct-connected biomass incinerator.
This "brownfield retrofit" approach involves taking a specially designed high-temperature biomass pyrolysis/gasification combustion chamber and connecting it directly to the original coal boiler's secondary air port, the space above the chain grate, or the original burner interface. The original boiler body is then repurposed as a Waste Heat Recovery Boiler (WHRB) to generate steam.
This method requires zero replacement of the main steam drum, waterwall, or steam-water system. By simply adding a front-end biomass burner and a fuel feeding system, the old boiler is given a new lease on life, restoring full-load steam output within 30 to 60 days, with emissions easily meeting national biomass boiler standards. Below, we deeply analyze this retrofit pathway across four dimensions: thermal matching, connection methods, fuel adaptation, and engineering implementation.
The "Root Cause" of Coal Boilers and the "Prescription" of the Direct-Connected Biomass Incinerator
Why are coal boilers being phased out?
Excessive Emissions: Original NOx, SO₂, and particulate emissions far exceed current GB 13271 standards. Even if desulfurization, denitrification, and dust removal are added, operating costs are exorbitant and compliance risks remain high.
Fuel Restrictions: Many regions have completely banned bulk coal transport. Procurement channels are narrowing, and prices fluctuate wildly.
Equipment Aging: Chain grates wear out, and furnace walls crack. The ROI for continuing major overhauls is too low.
The Core Logic of the Direct-Connected Biomass Incinerator:
Unlike a "whole biomass boiler replacement" (which requires dismantling the old boiler, pouring new foundations, and reapplying for pressure vessel inspections), a direct-connected biomass incinerator is an independent high-temperature biomass pyrolysis/gasification combustion chamber (comprising feeding, pyrolysis, gasification, and combustion zones). It is connected via flanges or flues directly to any of the following interfaces on the original coal boiler:
The original pulverized coal burner interface (remove the coal gun, bolt on the biomass burner flange).
The secondary/tertiary air inlets (high-temp gas is injected into the furnace to participate in combustion).
The space above the chain grate (a suspended biomass gasification chamber is installed above the grate, projecting flames directly onto the waterwalls).
The original boiler's water circulation system, steam drum, waterwalls, economizer, and dust collector are 100% retained. Only the front-end heat source changes from "burning coal" to "direct injection of high-temperature biomass gas/flame."
Thermal Matching Principle: How It Ensures 100% Steam Capacity
Heat Balance Calculation
Let's take a 10 t/h coal-fired chain-grate boiler (Steam pressure 1.25 MPa, saturated steam) as an example:
Original Coal Consumption: Approx. 1,500 kg/h (As-received LHV 20 MJ/kg, boiler efficiency 78%).
Required Input Thermal Power: $\approx 8.33\text{ MW}$ (excluding losses).
After retrofitting with a direct-connected biomass incinerator:
Fuel: Wood chips/wood pellets (As-received LHV 15–17 MJ/kg, moisture $\le 15\%$).
Biomass Consumption: Approx. 1,800–2,000 kg/h. (While biomass gasification efficiency is slightly lower than pulverized coal, this is offset by high-temperature secondary air oxygen supplementation and optimized air distribution).
Flame Temperature: The biomass combustion chamber outlet flame reaches 1200–1350°C (higher than the coal flame's 1100°C), meaning radiant heat transfer increases.
Result: The heat absorption capacity of the original boiler's heating surfaces (waterwalls, convection tube bundles) matches perfectly. Steam production is fully restored to 10 t/h (100% capacity).
Key Thermal Parameters
| Parameter | Original Coal-Fired State | After Direct-Connected Biomass Incinerator Retrofit |
| Combustion Chamber Outlet Temp | 1050–1150°C | 1200–1350°C |
| Furnace Excess Air Coefficient | 1.4–1.6 | 1.3–1.5 (Gasification combustion is more concentrated) |
| Exhaust Temp (Economizer Outlet) | 160–180°C | 155–175°C (Very similar) |
| Boiler Thermal Efficiency | 76%–80% | 78%–82% (Slight increase due to higher flame temp) |
| Steam Output Capacity | 100% Design Value | 100% Restored (Adjusted via fuel feed rate) |
Three Integration Methods: Adapting to Different Boiler Types
Method 1: Burner Flange Direct Connection (For Pulverized Coal / Spreader Stoker Boilers)
Operation: Remove the original pulverized coal burner or spreader stoker. Install the gasification nozzle or high-temp flame burner of the direct-connected biomass incinerator onto the original flange port.
Fuel: Wood pellets, crushed briquettes (particle size $\le 10\text{ mm}$).
Advantage: Minimal modification. Only the "burner" is replaced; the boiler body remains untouched.
Note: The high-temperature resistance of the original furnace waterwalls must be verified (biomass flame temp is slightly higher, but usually still within the material's allowable limits).
Method 2: Suspended Gasification Chamber Above Chain Grate (For Chain-Grate Boilers)
Operation: Retain the chain grate (can be used for ignition bedding or backup). Install a suspended biomass pyrolysis/gasification chamber 1.5–2.5 m above the grate. Biomass falls from the bottom of the gasification chamber onto a glowing char bed; the gasified gas burns in the secondary air zone above, and the flame radiates downward to heat the waterwalls.
Fuel: Bulk materials like rice husks, wood chips, and peanut shells.
Advantage: Utilizes the original grate as an ash cooling and auxiliary combustion zone, ensuring a smooth transition.
Method 3: Independent Combustion Chamber + Flue Gas Parallel Connection (For All Types, Most Flexible)
Operation: Build a new direct-connected biomass incinerator (independent steel frame + refractory lining) next to the boiler. Its high-temperature flue gas outlet connects via a refractory-lined flue to the middle of the original furnace or the flue flange before the convection bundle. It acts as an "external high-temp heat source."
Advantage: Zero impact on the original boiler structure. Can be switched back to coal anytime (if policy allows) or act as a backup.
Note: Requires a new section of refractory flue and expansion joints; footprint is slightly larger.
Fuel Handling and Storage: Auxiliary System Support
The retrofit isn't just about the combustion chamber; it requires a matching fuel storage and transport system:
Storage Silo: Outdoor rainproof shed (storage capacity $\ge 3$ days), with a screw discharger at the bottom.
Transport System: Scraper conveyors or pneumatic conveying to deliver biomass to the front-furnace hopper.
Feed Control: VFD screw feeder interlocked with the steam pressure transmitter. If steam pressure drops below the set point, the feed rate automatically increases, and vice versa.
Ash Removal: Biomass ash volume is significantly lower than coal ash (wood chip ash is typically <2%). The original ash removal system can be retained; only the discharge frequency needs adjusting.

Environmental Performance: The Innate Advantages
Biomass fuel has inherently low sulfur content (<0.1%) and lower nitrogen content than coal. Therefore:
SO₂: Practically zero. No desulfurization equipment is needed.
NOx: Controlled at 150–200 mg/m³ through staged air distribution (primary hypoxic pyrolysis + secondary oxygen-rich combustion), meeting the GB 13271 limit for key regions (150 mg/m³).
Particulate Matter (PM): Biomass ash easily meets standards after passing through a bag filter or the original electrostatic precipitator (suitability must be checked).
Dioxins: Biomass contains no chlorine (unless mixed with plastics). With pyrolysis at 700–800°C and secondary chamber/furnace temperatures >850°C for >2 seconds, the risk of dioxin formation is virtually zero.
BNTET Direct-Connected Biomass Incinerator: The Professional Choice for Coal Boiler Retrofits
The BNTET direct-connected biomass incinerator (DB Series, adapted for retrofitting 4 t/h to 35 t/h coal boilers) features:
Modular Combustion Chamber: Monolithic refractory cast lining (high-alumina/corundum). Flange interface dimensions are customizable to match the original boiler's burner or secondary air ports.
Versatile Integration Options: Offers all three configurations (Flange Direct, Suspended Gasification, Independent External). Our engineers recommend the optimal plan after on-site surveying.
Broad Fuel Adaptability: Burns wood pellets, rice husks, peanut shells, and wood chips (≤50 mm), equipped with a VFD screw feeder and anti-backfire check valve.
Staged Air System: Primary air (gasification bottom) + Secondary air (tangential around flame injection port) + Tertiary air (furnace oxygen supplement). PLC automatically adjusts the air-fuel ratio.
Intelligent Interlocking: Interlocked with the original boiler's steam drum pressure, water level, and ID fan. Automatic feed adjustment based on steam pressure enables "unattended" operation.
Rapid Delivery: Modular manufacturing means the on-site installation cycle is only 15–30 days (depending on the connection method)—vastly faster than the 4–6 months required to procure a new boiler.
The environmental retrofit of coal-fired boilers does not have to mean a costly "tear down and rebuild." Through a clever front-end heat source replacement, a direct-connected biomass incinerator allows the original boiler body to continue functioning as a heat recovery unit.
With almost zero modifications to the steam-water system, factories can restore 100% of their steam capacity while switching to clean, renewable agro-forestry waste. The emissions profile vastly outperforms the coal era. With its modular design, flexible connection methods, and proven fuel adaptability, the BNTET direct-connected biomass incinerator helps enterprises complete their compliance transformation in record time, ensuring every ton of steam comes from a green heat source.
