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Product Introduction
The EBS-NQ is an asphalt mixing plant burner developed around electronic proportional control. Eight published models cover output capacities from 4,150 to 41,500 kW, with corresponding oil-consumption ratings from 370 to 3,710 kg/h.
The control system coordinates fuel delivery and combustion air across a stated 1:10 modulation range. This allows burner output to follow changes in plant firing demand rather than relying on a single fixed operating point.
A variable-frequency fan, compact integrated structure, movable base and protected control components support installation and operation in asphalt production environments. Final model selection must still be based on a project heat balance rather than the nominal mixing plant model alone.
Product Advantage
The EBS-NQ uses electronic proportional control to manage fuel and combustion air. The two control paths are calculated and adjusted through the burner control logic so that the firing rate can respond to the plant’s thermal demand.
This control method is intended to support more repeatable adjustment than a basic mechanically linked system. Actual combustion performance depends on correct setup of the fuel curve, air curve, sensors, actuators, fan, dryer draft and exhaust system.
The published adjustment ratio is 1:10. A wider operating range allows the burner to reduce output during lower production demand and increase firing as the required heat load rises.
The available field modulation range may be affected by:
Fuel type and heating value
Minimum stable fuel pressure
Atomization conditions
Combustion-air pressure
Burner head configuration
Dryer draft
Required excess-air level
Flame stability
Site emission limits
A 1:10 burner range does not mean that every asphalt plant should operate continuously at the lowest possible firing rate. The burner and dryer must still maintain sufficient air and fuel velocity for stable mixing and combustion.
When aggregate throughput, incoming moisture or target discharge temperature changes, the required heat input also changes. Electronic control allows the burner to adjust fuel and air together as the firing command moves between load points.
The plant control sequence should define how the burner responds to temperature feedback, production changes, alarm conditions and shutdown commands.
The EBS-NQ uses frequency conversion to adjust fan operation according to combustion demand. At reduced firing rates, the fan does not need to run continuously at its maximum speed while airflow is restricted only by a damper.
The product page reports a 30–40% reduction in fan electrical consumption and an approximately 2% improvement in thermal utilization under its stated operating conditions. Actual results depend on the comparison baseline, operating hours, load profile, dryer resistance, fan selection, tuning and maintenance condition.
Project evaluation should therefore compare measured fan power and fuel consumption under similar production conditions rather than treating published percentages as guaranteed savings.
The burner fan does not operate independently of the asphalt plant exhaust system. Combustion-zone pressure is influenced by the dryer, ductwork, baghouse, induced-draft fan, dampers and stack.
Incorrect draft may contribute to:
Flame instability
Excessive combustion air
Incomplete combustion
Unstable aggregate temperature
Positive pressure near the burner opening
Higher CO or particulate levels
Heat loss through the exhaust
Burner commissioning should include draft measurements at the operating points used by the plant.
Fuel lines, airflow components and control connections are arranged within an integrated burner assembly. This reduces the number of separately positioned components around the main burner body and provides a more organized installation layout.
The actual foundation, burner opening, support structure, service clearance and connection positions must be checked against the selected model drawings.
Product images show the EBS-NQ installed on a framed base with wheels. The movable arrangement can assist positioning and provide access during installation or scheduled maintenance.
The burner must be secured in its operating position. Wheels or a movable frame do not replace the required foundation, alignment, locking and structural support defined for the installation.
The burner arrangement provides access to the fan housing, fuel components, combustion head and control enclosure. Maintenance planning should reserve enough space to inspect or remove these components without interfering with nearby plant structures.
Before installation, review:
Burner withdrawal distance
Combustion-head access
Fan and motor service space
Fuel-train access
Control-panel door clearance
Cable and pipe routes
Lifting points
Platform and guard requirements
The burner should be selected from the actual drying and heating requirement. Nominal asphalt plant size alone does not establish the required burner capacity.
The heat calculation should include:
Required aggregate throughput
Average and maximum aggregate moisture
Incoming aggregate temperature
Required discharge temperature
Recycled material percentage, where applicable
Dryer heat loss
Exhaust-gas temperature
Fuel heating value
Site altitude and ambient conditions
Expected operating margin
Evaporating water from the aggregate is a major part of the dryer heat load. A plant processing wet aggregate may require substantially more heat than the same plant operating with dry material.
Burner output is only one part of the selection. The flame must also be compatible with the combustion zone and dryer geometry.
Project review should consider:
Dryer diameter and length
Burner opening dimensions
Combustion-zone length
Flight arrangement
Aggregate curtain location
Burner insertion or nose length
Counterflow or parallel-flow configuration
Available negative pressure
Baghouse temperature limits
An oversized burner may spend most of its operating time at a low percentage of rated capacity. This can reduce air and fuel velocity, narrow the useful control range and make combustion tuning more difficult.
The compact burner structure can be evaluated for both fixed and relocatable asphalt plant projects. A mobile project still requires verification of transport dimensions, weight distribution, flexible connections, alignment procedures and reconnection checks after relocation.
The published EBS-NQ model table provides oil-consumption values. These figures should be used as nominal model references rather than guaranteed site consumption.
Fuel demand varies with:
Net heating value
Fuel density and viscosity
Aggregate moisture
Plant production rate
Required material temperature
Combustion excess air
Dryer and exhaust losses
Burner tuning
Operating time at partial load
For heavy-oil operation, the fuel preparation system may need heating, circulation, filtration and viscosity control. Atomizing-air or pressure requirements must match the selected burner and fuel system.
Alternative gas or combined-fuel projects require a project-specific fuel-train design, valve selection, pressure range, safety sequence and consumption calculation. Gas or dual-fuel capability should not be assumed from the oil-consumption table.
The product page lists IP55 protection for components and IP56–IP67 protection for the main control system. The exact rating applicable to each enclosure or assembly should be identified in the approved technical documents.
An IP rating describes protection against access, dust and water under defined test conditions. It does not describe combustion safety, explosion protection or suitability for every outdoor environment.
A complete burner safety system should coordinate:
Combustion-air proving
Pre-purge and post-purge
Ignition sequence
Flame detection
Fuel-pressure monitoring
Safety shut-off valves
Low-fire start position
Temperature limits
Dryer draft interlocks
Emergency shutdown
Plant permissive signals
Fault indication and reset logic
The burner must shut off fuel safely when the flame is lost or a required operating condition is not satisfied. Safety devices should remain effective independently of normal production control.
Local fuel-gas, fuel-oil, electrical, fire-protection and emission requirements must be addressed by the plant designer and commissioning team.
Commissioning should be performed by qualified combustion and electrical personnel with the asphalt plant placed in a controlled operating condition.
A typical process includes:
Verify burner mounting, alignment and combustion-head position.
Check electrical supply, phase sequence and grounding.
Inspect fuel lines, valves, filters and leak-tightness.
Confirm fan rotation and airflow proving.
Test the purge sequence and all permissive signals.
Verify ignition and flame-detection response.
Establish a stable low-fire operating point.
Set fuel and air values across the required firing range.
Measure dryer draft and exhaust conditions.
Test load transitions using controlled production changes.
Verify all alarm and shutdown functions.
Record the final settings and combustion measurements.
Combustion should be checked with suitable instruments. Relevant measurements may include oxygen, carbon monoxide, carbon dioxide, nitrogen oxides, exhaust temperature, fuel pressure, combustion-air pressure and dryer draft.
Settings should not be copied directly from another plant, even when both plants use the same EBS-NQ model.
A maintenance schedule should reflect the fuel quality, operating hours, dust exposure, ambient conditions and plant production cycle.
Inspect the following items regularly:
Fuel filters and strainers
Fuel pressure and temperature
Atomizing components
Flexible fuel connections
Flame detector
Ignition components
Fan inlet and impeller
Air-pressure switches
Actuators and linkages
Electrical terminals
Control-enclosure seals
Combustion head
Fasteners and mounting points
Heavy-oil systems may require more frequent cleaning because viscosity, contaminants and carbon deposits can affect atomization.
Retuning may be required after:
Changing fuel type or supplier
Replacing a nozzle or fuel valve
Repairing the fan or motor
Modifying the dryer or baghouse
Changing production rate significantly
Moving the burner to another plant
Observing higher fuel use, smoke or unstable temperature
Receiving abnormal CO, NOx or oxygen readings
Repeatedly resetting burner faults without identifying their cause can expose the equipment and plant to further risk.
For EBS-NQ model selection, provide:
Asphalt plant manufacturer and model
Dryer type, diameter and length
Burner opening and available installation space
Required aggregate throughput
Average and maximum moisture content
Incoming and discharge temperatures
Fuel type and analysis
Available fuel pressure
Site altitude and ambient temperature
Exhaust fan and baghouse information
Local NOx, CO and particulate limits
Electrical supply
Existing control-system signals
Retrofit or new-installation status
The engineering review should produce a defined burner model, fuel configuration, interface list, installation drawing and commissioning scope before the order is released.
Technical Parameters
| Model | Outputcapacity (KW) | OilConsumption (kg/h) | Specifications of the mixing plant |
| EBS350NQ | 4150 | 370 | 500 |
| EBS600NQ | 7100 | 630 | 1000 |
| EBS900NQ | 10600 | 950 | 1500 |
| EBS1200NQ | 14200 | 1270 | 2000 |
| EBS1800NQ | 21300 | 1900 | 3000 |
| EBS2500NQ | 27800 | 2490 | 4000 |
| EBS3000NQ | 35500 | 3180 | 5000 |
| EBS3500NQ | 41500 | 3710 | 6000 |
Why Choose EBS-NQ
Fourth-generation electronic intelligent proportional control architecture
1:10 ultra-wide adjustment ratio for precision thermal modulation
Digitally synchronized fuel–air control for stable and efficient combustion
30–40% reduction in fan power consumption with frequency-controlled airflow
Industrial-grade IP55–IP67 protection for demanding on-site environments
Designed for high-load, long-duration, precision-controlled asphalt production
FAQs
The public page does not provide a guaranteed NOx value or test standard for this series. Emission performance must be evaluated for the selected fuel, dryer, firing rate, excess-air level and local limit. Do not classify the burner as low-NOx solely from its model name.
The published selection table is based on oil consumption. A natural-gas or dual-fuel project requires a separately defined burner configuration, fuel train, supply pressure and safety system. Submit the fuel information before selection.
Not necessarily. The page does not identify the figures as t/h. They should be treated as reference plant specifications until the corresponding plant-model definition is confirmed.
Start with a heat balance based on aggregate throughput, moisture, inlet temperature, discharge temperature, dryer loss and fuel heating value. Then check the flame geometry, useful modulation range, draft and installation dimensions.
Not automatically. Excessive oversizing can force the burner to operate at low velocity and within a narrow portion of its control range. Select enough capacity for the verified maximum load while maintaining practical operation at normal production rates.
It may be considered for a retrofit after reviewing the burner opening, support frame, combustion-zone length, fuel system, fan capacity, draft, electrical supply, control signals and safety sequence. It should not be treated as a direct one-for-one replacement based only on rated output.
They are nominal model ratings. Actual consumption depends on fuel heating value, aggregate moisture, production rate, temperature rise, exhaust loss and combustion tuning.
No single saving percentage applies to every site. The result depends on the original fan-control method, operating load profile, fan and motor efficiency, dryer resistance and annual operating hours.
Provide the fuel analysis, firing range, required production rate, aggregate moisture, dryer configuration, stack conditions, local oxygen reference and permitted NOx, CO and particulate limits.
Retuning should be considered after fuel changes, fuel-system repairs, fan work, burner relocation, dryer modifications or significant changes in production conditions. It is also appropriate when combustion readings or fuel consumption move outside the established operating baseline.
Plan Your Asphalt Burner Project
Send us your dryer dimensions, aggregate throughput and moisture, fuel specifications, target material temperature, site conditions and emission limits. Our engineering team will review the heat load and burner configuration.
Actual operating data is recommended instead of relying only on the asphalt plant nameplate.