Prepared by: DIVI Group Technical Team
Technical Review: Engineer Le Van Hieu – Founder and CEO of DIVI Group
Many businesses assume that rising steam production costs are mainly caused by higher fuel prices. In reality, many boiler systems are still wasting a significant amount of energy every day without operators realizing it.
These losses often occur gradually and do not cause the boiler to stop immediately. However, they can steadily increase fuel consumption over time.
In this article, DIVI Group analyzes eight energy loss points that increase boiler fuel consumption, while identifying their causes and practical solutions to help businesses improve operating efficiency.
Many businesses only realize that their boiler is consuming excessive fuel when steam production costs become noticeably higher.
In reality, energy loss often develops gradually and can be difficult to detect without regularly monitoring operating parameters.
A boiler system may still maintain the required steam pressure and output while its efficiency has already declined significantly due to several energy loss points occurring at the same time.
For this reason, regularly monitoring operating data is essential for identifying abnormal conditions early and implementing corrective action in a timely manner.
Common warning signs include:
Flue gas temperature increasing compared with the system’s stable operating period.
Fuel consumption increasing without a corresponding increase in steam output.
O₂ or CO levels in the flue gas showing an upward trend.
Make-up water consumption increasing abnormally because of condensate loss or leakage.
Steam pressure fluctuating or the boiler frequently needing to increase load to meet production demand.
Wet steam, condensate accumulation, or water hammer occurring in the steam pipeline.
TDS or other boiler water quality parameters fluctuating.
Boiler feedwater temperature falling below normal levels.
Leakage occurring at pipelines, valves, or steam traps.
If one or more of these signs appear, the entire boiler system should be inspected to identify the actual cause.
In many cases, higher steam production costs are not caused by one single factor, but by several energy loss points existing simultaneously.
The combustion process is the first stage that determines how much heat can be extracted from the fuel.
If the fuel does not burn completely or the combustion air supply is unsuitable, part of the energy is lost inside the furnace before it can be transferred to the water for steam generation.
In many cases, the boiler can still produce enough steam for production but consumes more fuel because the combustion conditions have not been properly optimized.
A boiler requires a certain amount of air to ensure complete combustion.
However, if too much air is supplied, the volume of hot flue gas leaving the system increases, carrying more heat into the environment.
Excessive air can also:
Increase flue gas flow.
Increase the amount of heat discharged through the stack.
Increase electricity consumption by the FD fan and ID fan.
Reduce the combustion-zone temperature.
Make the combustion process less stable.
Conversely, if the air supply is too low, the fuel will not burn completely, resulting in higher CO levels or unburned carbon remaining in the ash.
Therefore, the objective is not to supply as much air as possible, but to maintain the appropriate air level for each fuel type and operating condition.
In addition to the air supplied by the fan, outside air may enter the system through unsealed areas.
Common leakage points include:
Cleaning doors.
Fuel feeding doors.
Rotary valves.
Ash hoppers.
Joints along the flue gas path.
Furnace doors.
This infiltrated air does not contribute effectively to combustion, but it still increases flue gas flow.
As a result, more heat is lost through the stack, and combustion control becomes more difficult.
Therefore, checking the airtightness of the entire system is just as important as adjusting the combustion air fan.
A portion of the fuel may remain unburned and leave the system with the ash or flue gas.
This type of energy loss is often difficult to identify through visual inspection alone.
Signs that should be checked include:
High CO levels in the flue gas.
A high amount of unburned carbon remaining in the ash.
Unstable flame conditions.
Fluctuating steam pressure even though the fuel feed rate remains unchanged.
Possible causes include:
Improper air distribution.
High fuel moisture content.
Uneven fuel size.
An unsuitable fuel-bed thickness.
Insufficient residence time in the furnace.
Unstable combustion-zone temperature.
For biomass-fired boilers, fuel quality has a major impact on the combustion process.
Key factors that should be controlled include:
Moisture content.
Heating value.
Fuel size.
Ash content.
Impurities.
Fuel consistency.
Storage conditions.
When fuel quality changes continuously, combustion conditions change as well.
This makes it more difficult to adjust the air supply, fuel feed rate, and steam pressure, while also increasing the risk of energy loss.
Note: There is no single excess O₂ value or flue gas temperature that is suitable for every boiler. These parameters must be evaluated based on furnace technology, fuel type, operating load, and the configuration of heat recovery equipment in each system.
To improve combustion efficiency and reduce boiler fuel consumption, businesses should:
Adjust the combustion air supply to match operating conditions.
Inspect and repair all air infiltration points.
Control incoming fuel quality.
Regularly monitor O₂, CO, and flue gas temperature.
Inspect ash conditions to assess the completeness of fuel combustion.
Optimizing the combustion process not only reduces fuel consumption but also creates the foundation for energy-saving solutions in the following stages to perform effectively.
After the combustion process, part of the heat generated is transferred to the boiler water to produce steam, while the remaining heat leaves the system with the flue gas.
The higher the flue gas temperature, the more unused heat is being discharged into the atmosphere. This means the boiler is losing part of the energy generated from the fuel instead of utilizing it for steam production.
For many biomass boiler systems equipped with an economizer or an air preheater (APH), the flue gas temperature is typically maintained within the range of 130–170°C.
The optimum flue gas temperature should be determined based on several factors, including: Fuel type, fuel moisture content, boiler feedwater temperature, excess O₂ level, flue gas dew point limitation
Example: When the flue gas temperature is reduced from 220°C to 160°C, the amount of heat recovered depends on the flue gas flow rate, flue gas composition, and excess O₂ level.
Therefore, the improvement in boiler efficiency should always be calculated using actual operating data rather than applying a fixed efficiency gain to every boiler system.
However, in many operating plants, flue gas temperatures still reach 250–300°C. This is a clear indication that a significant amount of heat is escaping through the stack instead of being used to generate steam.
As a result, the boiler must consume more fuel to maintain the same steam production rate.
A high flue gas temperature alone is not sufficient to conclude that boiler efficiency has decreased.
The following operating parameters should be evaluated together:
| Parameter | Purpose |
| Flue gas temperature at different measurement points | Identify areas with excessive heat loss or poor heat transfer |
| Flue gas O₂ concentration | Evaluate excess combustion air |
| Flue gas CO concentration | Assess combustion completeness |
| Boiler feedwater temperature before and after the economizer | Evaluate heat recovery performance |
| Differential pressure across heat transfer surfaces | Detect fouling or blockage |
| Fuel moisture content and fuel quality | Evaluate their impact on flue gas volume and heat loss |
| Ash deposits and scale formation | Assess resistance to heat transfer |
Note: A high flue gas temperature does not necessarily indicate poor performance of the heat recovery equipment alone.
In many cases, it is caused by a combination of factors such as fouled heat transfer surfaces, scale formation, excessive excess O₂, air leakage, and inconsistent fuel quality.
To control flue gas temperature and improve heat utilization, it is recommended to:
Monitor flue gas temperature at key measurement points.
Clean heat transfer surfaces regularly.
Inspect for scale formation on the water side.
Evaluate the performance of the economizer and air preheater (APH).
Monitor differential pressure across the flue gas path.
Measure O₂ and CO concentrations to eliminate combustion-related causes.
Control fuel moisture content and maintain consistent fuel quality.
If the flue gas temperature increases significantly compared with the system's normal operating condition, the root cause should be investigated before simply increasing the fuel feed rate to maintain steam production.
When higher flue gas temperature is accompanied by increased fuel consumption, both heat transfer efficiency and the condition of heat transfer surfaces—including ash deposits and scale buildup—should be evaluated.
The economizer and air preheater recover waste heat from the flue gas to preheat boiler feedwater and combustion air
Boiler blowdown is an essential operation used to remove accumulated impurities and maintain proper boiler water quality.
However, if blowdown is not carried out correctly, it can become a significant source of energy loss.
| Insufficient Blowdown | Excessive Blowdown |
| Scale accumulation | Loss of hot boiler water |
| Reduced heat transfer efficiency | Loss of thermal energy |
| Increased boiler fuel consumption | Loss of water treatment chemicals |
Both situations gradually increase the overall cost of steam production.
Every time a boiler is blown down, the system not only removes impurities but also loses:
Hot boiler water.
Thermal energy.
Boiler water treatment chemicals.
For this reason, boiler blowdown should not be performed based solely on operator experience or fixed routines. Instead, it should be controlled according to the TDS (Total Dissolved Solids) level to achieve the proper balance between boiler water quality and energy conservation.
The recommended boiler water TDS depends on several factors, including:
Boiler operating pressure.
Boiler type.
Boiler feedwater quality.
Required steam quality.
Equipment manufacturer's recommendations.
For many low-pressure industrial boilers, the recommended TDS range is typically 2,000–3,000 mg/L.
In addition to TDS, a comprehensive boiler water treatment program may also monitor:
pH
Alkalinity
Water hardness
Silica
Phosphate
Sulfite
Chloride
Oil and grease
Electrical conductivity
The specific parameters that need to be monitored depend on the boiler type, operating pressure, water treatment program, and required steam quality.
Example: For a boiler producing 10 tons of steam per hour, reducing the blowdown rate from 10% to 5% decreases the blowdown water volume from approximately 1 ton per hour to 0.5 ton per hour, assuming all other operating conditions remain unchanged.
The actual savings in thermal energy, water, and water treatment chemicals should be calculated based on the blowdown water temperature, operating hours, and the actual water quality.
If your company is developing or improving its boiler operating procedures, the article Proper Boiler Blowdown Procedure provides detailed guidance on when and how blowdown should be performed.
Monitoring boiler blowdown based on the TDS level removes impurities while minimizing the loss of hot water and thermal energy
After steam is generated, it must be delivered to the end-use equipment at a stable pressure and flow rate. However, the steam distribution system may contain several sources of energy loss, such as steam leaks, inefficient steam traps, or condensate that is discharged instead of being recovered.
Although these issues have different causes, they all increase boiler fuel consumption and steam production costs if they are not detected and corrected in time.
A small steam leak may not have a noticeable impact in the short term. However, when multiple leaks exist and remain unrepaired over time, the amount of steam loss gradually becomes significant.
In addition to losing steam, the system also experiences a pressure drop, forcing the boiler to burn more fuel to compensate for the lost steam.
This represents an additional operating cost that many businesses fail to recognize because the boiler system continues to operate normally.
A steam trap is designed to discharge condensate while retaining live steam within the system.
A steam trap that fails in the open position may allow live steam to escape directly into the condensate return line. In this case, the system continuously loses steam even though the loss may not be obvious from the outside.
Conversely, a blocked steam trap prevents condensate from being discharged properly. Condensate accumulating in equipment or pipelines may:
Reduce heat transfer efficiency.
Cause temperature fluctuations.
Increase the risk of water hammer.
Affect valves and steam-consuming equipment.
Therefore, steam trap inspections should distinguish between live steam leakage and condensate blockage, rather than simply checking for external leakage.
Regular inspection of steam trap performance is an important part of any steam system energy-saving program.
In addition to steam leaks, many factories still discharge condensate directly instead of recovering and reusing it.
However, condensate still contains a considerable amount of thermal energy. If it is not recovered, all of this energy is wasted.
Although the daily energy loss may appear relatively small, it can accumulate into a significant operating cost over months or years.
To minimize this type of energy loss, it is recommended to:
Inspect all steam leakage points throughout the system.
Recover condensate for reuse within the boiler system.
One solution that has been widely adopted by many businesses is condensate recovery. DIVI Group has analyzed this solution in detail in the following article: PCHR – A Solution for Reducing Boiler Fuel Costs

In a boiler system, steam and hot water always carry a significant amount of thermal energy. If the equipment or piping is not properly insulated, heat will continuously be lost to the surrounding environment.
This is one of the easiest forms of energy loss to observe, yet it is often overlooked during daily operation.
Heat loss can occur at various locations throughout the boiler system, including:
The boiler body.
Steam pipelines.
Hot water pipelines.
Valves, flanges, and auxiliary equipment.
Areas where the insulation has been damaged or no longer provides adequate thermal protection.
When these components continuously release heat into the surrounding environment, part of the energy generated from the fuel is no longer available for steam production.
To minimize heat loss, the condition of the insulation throughout the entire system should be inspected regularly.
Any insulation that has become detached, damaged, or deteriorated should be repaired or replaced promptly to maintain the thermal retention performance of the equipment and piping.
Regular insulation maintenance not only reduces energy loss but also helps maintain stable operating efficiency throughout the entire boiler system.
Do Not Overlook Small Sources of Heat Loss
Many businesses focus primarily on reducing fuel consumption inside the furnace while paying little attention to heat being lost from pipelines and auxiliary equipment.
Regular inspection of the insulation system helps identify deteriorated areas at an early stage, thereby reducing energy loss and lowering steam production costs during operation.
Water quality is one of the key factors that directly affects boiler efficiency, operational safety, and equipment lifespan.
Boiler water treatment is not limited to the use of water treatment chemicals. It includes the entire water treatment program, from feedwater treatment, water softening, deaeration, pH adjustment, boiler water quality control, to blowdown management during operation.
If any part of this process is not properly controlled, scale formation and corrosion may develop inside the boiler system, reducing heat transfer efficiency, increasing boiler fuel consumption, and leading to higher maintenance costs.
Saving on Water Treatment Chemicals Today May Increase Costs Tomorrow
Many businesses believe that eliminating boiler water treatment chemicals can reduce operating costs.
However, the money saved is often far less than the additional costs caused by scale buildup, corrosion, increased fuel consumption, and equipment repairs in the future.
When scale forms on heat transfer surfaces, heat transfer efficiency decreases, forcing the boiler to consume more fuel to produce the same amount of steam.
Meanwhile, corrosion reduces equipment durability, increases maintenance requirements, and shortens the service life of the boiler system.
Water Treatment Solutions
To minimize both scale formation and corrosion, businesses should:
Treat boiler feedwater before it enters the boiler.
Use appropriate boiler water treatment chemicals.
Continuously monitor boiler water quality throughout operation.
Learn more: Boiler Feedwater Treatment
Scale buildup and corrosion reduce heat transfer efficiency, increase fuel costs, and shorten the service life of the boiler
A high-efficiency boiler system depends not only on equipment quality but also on selecting the appropriate boiler capacity and maintaining stable operating conditions.
In practice, many businesses install boilers with capacities significantly larger than their actual steam demand or oversize the system in anticipation of future expansion.
Once production reaches stable operation, the actual steam consumption is often much lower than the original design capacity.
As a result, the boiler operates at low load for extended periods, reducing fuel utilization efficiency and increasing steam production costs.
Most industrial boilers achieve their highest efficiency when operating close to their rated capacity.
If a boiler frequently operates at low load, maintaining optimal combustion conditions becomes more difficult.
Combustion becomes less stable, causing the boiler to consume more fuel while producing the same amount of steam.
This can be compared to driving a car.
When a vehicle travels steadily on a highway at a constant speed, fuel consumption is generally lower.
In contrast, frequent acceleration, deceleration, or prolonged low-speed driving increases fuel consumption.
A boiler operates in a similar way.
When it runs steadily at an appropriate operating load, it utilizes fuel energy more efficiently.
However, prolonged operation at low load reduces efficiency and gradually increases steam production costs.
Besides low-load operation, many factories also experience unstable steam demand.
During production, multiple process lines may consume steam simultaneously, then later reduce their load or stop operating.
As steam demand continuously changes, the boiler must repeatedly increase and decrease its output to match the varying load.
These frequent operating changes make it difficult to maintain stable combustion, reducing boiler efficiency and increasing fuel consumption.
This is one of the most common forms of hidden energy loss and is often difficult to identify by monitoring steam production alone.
To improve fuel utilization efficiency, businesses should:
Select a boiler capacity that matches the actual steam demand.
Monitor the operating load after the plant reaches stable production.
Adjust the fuel feed rate and combustion air according to the actual load.
Optimize the combustion process to maintain stable boiler efficiency.
Re-evaluate the system whenever steam demand changes significantly.
Maintaining boiler operation under conditions that match the original design allows combustion to remain more stable, improves fuel utilization efficiency, and reduces long-term steam production costs.
Once steam is generated by the boiler, the objective is to deliver as much thermal energy as possible to the end-use equipment.
However, if the steam contains excessive moisture, condensate is not removed promptly, or the feedwater is not properly preheated and deaerated, the overall energy efficiency of the steam system will decrease.
These forms of energy loss often occur gradually and receive little attention, yet they directly affect operating efficiency, equipment lifespan, and steam production costs.
Saturated steam leaving the boiler may still contain a certain amount of water. In addition, as steam travels through the piping system, it loses heat and continues to condense.
If this condensate is not separated from the steam flow, the steam supplied to the end-use equipment will have lower quality, reducing heat transfer efficiency and steam utilization.
Common Causes
Water carryover from the steam drum.
Condensate formed in the steam piping due to heat loss.
Insufficient condensate drainage points.
Steam separators are not installed where required.
Consequences
When steam contains excessive moisture, the system may experience:
Reduced heat transfer efficiency at steam-consuming equipment.
Longer heating time.
Higher steam consumption to achieve the same heating performance.
Increased risk of water hammer in the piping system.
Shortened service life of valves, heat exchangers, and other steam system components.
Solutions
Install condensate drainage points at appropriate locations throughout the steam piping.
Regularly inspect the operating condition of steam traps.
Install Steam Separators where necessary, especially upstream of pressure-reducing valves or equipment requiring dry steam.
Improving steam quality not only enhances heat transfer efficiency but also helps reduce steam consumption during production.
Read more: The Role of Steam Separators in Improving Steam Quality and Reducing Condensate in Steam Pipelines
A steam separator removes entrained water from the steam before it is delivered to steam-consuming equipment
After condensate is recovered and returned to the system, the boiler feedwater should be preheated before entering the boiler.
The higher the feedwater temperature, the less heat the boiler must supply to produce steam.
This allows the system to make better use of the available thermal energy and reduces boiler fuel consumption.
Feedwater preheating is commonly achieved by recovering heat from condensate or through heat recovery equipment such as an economizer.
Boiler feedwater always contains dissolved gases, particularly oxygen (O₂) and carbon dioxide (CO₂).
If these gases are not removed before the water enters the boiler, they can accelerate corrosion in:
The steam drum.
Piping.
Storage tanks.
Boiler feedwater pumps.
Other equipment throughout the system.
Corrosion not only shortens equipment life but also increases maintenance costs and the risk of unexpected failures during operation.
A deaerator not only removes dissolved gases but also plays an important role in stabilizing the entire boiler feedwater system.
It helps to:
Preheat boiler feedwater before it enters the boiler.
Remove dissolved oxygen and carbon dioxide.
Receive and mix returned condensate with make-up water.
Maintain a stable water supply for the boiler feedwater pumps.
As a result, the feedwater system operates continuously, reduces operating fluctuations, and improves overall energy efficiency.
If your company would like to learn more about the design and operating principles of a deaerator, please refer to the following article: Benefits of a Deaerator Tank in Boiler Systems
To minimize energy loss during steam distribution and boiler feedwater supply, the following items should be inspected regularly:
Steam quality at steam-consuming equipment.
Operating condition of steam separators and steam traps.
Condensate drainage performance throughout the piping system.
Condensate recovery rate.
Boiler feedwater temperature before entering the boiler.
Operating condition of the deaerator.
Efficiency of dissolved gas removal from the feedwater.
Monitoring all of these factors together helps improve steam quality, maximize the use of available thermal energy, and maintain stable long-term boiler system performance.
Not all energy-saving solutions need to be implemented at the same time. In practice, businesses should prioritize addressing the causes that require a relatively low investment but deliver significant results before considering larger-scale improvement projects.
Setting the right priorities helps reduce steam production costs in the short term while optimizing investment budgets and minimizing the impact on production activities.
| Solution | Investment Level | Potential Effectiveness | Recommended Priority |
| Optimize the combustion process (O₂, CO, combustion air supply) | Low | Very High | When excess O₂ is high, CO increases, or fuel is not completely burned |
| Repair steam leaks and inspect steam traps | Low | Very High | When steam pressure drops, condensate volume is abnormal, or steam leaks are detected |
| Optimize boiler blowdown based on TDS | Low | High | When TDS exceeds the recommended limit or blowdown is performed based on operator experience |
| Clean heat transfer surfaces and remove scale deposits | Low - Medium | High | When flue gas temperature increases or fuel consumption gradually rises |
| Repair or improve insulation | Low | Medium | When pipelines, valves, or equipment surfaces release excessive heat |
| Recover condensate | Medium | High | When condensate is discharged instead of being recovered or when the condensate recovery rate is low |
| Inspect and clean the Economizer and Air Preheater | Medium | High | When flue gas temperature is high or heat recovery equipment is operating inefficiently |
| Improve fuel quality | Low - Medium | Medium to High | When fuel moisture, particle size, or heating value is inconsistent |
| Upgrade the control system and optimize operating load | Medium - High | Depends on the system | When the boiler frequently operates outside its designed load range |
| Retrofit or replace the boiler | High | Depends on the system condition | When the existing system no longer meets technical requirements or its efficiency is too low |
Note: The effectiveness shown in the table is for reference only. Actual results depend on the boiler technology, fuel type, boiler capacity, operating conditions, and the current condition of each system.
After identifying potential energy loss points, the next step is to inspect the entire boiler system to determine the root causes and select the most appropriate solutions.
The inspection should not focus on a single piece of equipment. Instead, it should evaluate the complete process, including combustion, heat transfer, steam generation, steam distribution, condensate recovery, and boiler feedwater treatment.
| Inspection Item | Evaluation Criteria | Objective |
| Combustion process | O₂ concentration, CO concentration, fuel combustion condition, and unburned carbon in the ash | Maintain stable combustion and maximize the utilization of fuel energy |
| Flue gas system | Flue gas temperature, Economizer performance, Air Preheater performance, and fouling on heat transfer surfaces | Reduce heat loss through the flue gas system |
| Boiler blowdown | TDS level, blowdown frequency, and blowdown rate | Maintain boiler water quality while minimizing heat loss |
| Steam distribution system | Steam leaks, steam trap condition, and water hammer | Reduce steam loss and maintain steam quality |
| Condensate system | Condensate recovery rate and condensate return temperature | Recover remaining thermal energy and reduce make-up water consumption |
| Insulation | Pipelines, valves, flanges, and damaged insulation | Minimize heat loss to the surrounding environment |
| Boiler feedwater and boiler water | pH, TDS, water hardness, and other water quality parameters required by the treatment program | Reduce scale formation and corrosion while maintaining efficient heat transfer |
| Operating load and fuel | Boiler operating capacity, load level, fuel moisture content, and fuel quality | Ensure the boiler operates under conditions suitable for its design |
| Steam quality and feedwater system | Steam moisture content, condensate separation performance, feedwater temperature, and deaerator condition | Improve steam utilization efficiency and stabilize the feedwater system |
Note: Not every boiler system requires the same level of inspection for every item. The inspection scope should be determined based on the boiler type, fuel used, operating capacity, and the actual condition of each facility.
After completing the inspection, businesses can prioritize corrective actions based on the following recommendations:
| System Condition | Recommendation |
| Serious safety issues are identified, such as major steam leaks, water hammer, corrosion, or severely damaged equipment | Inspect and repair immediately to ensure safe operation |
| One or two significant energy loss points are identified | Develop a corrective action plan based on their impact and available investment budget |
| Three or more energy loss points remain uncontrolled | Conduct a comprehensive system assessment to determine improvement priorities |
| No operating data is available for O₂, CO, flue gas temperature, water quality, condensate recovery rate, or fuel consumption | There is insufficient information to accurately evaluate the operating efficiency of the boiler system |
Fuel consumption should be compared with steam production under the same operating conditions.
In addition, operators should monitor flue gas temperature, O₂ concentration, CO concentration, fuel quality, condensate recovery rate, boiler blowdown practices, and the actual operating load.
If blowdown is insufficient, scale will accumulate inside the boiler and reduce heat transfer efficiency.
On the other hand, excessive blowdown wastes hot water, thermal energy, and boiler water treatment chemicals.
Therefore, boiler blowdown should be controlled based on the TDS (Total Dissolved Solids) level.
Steam leaks reduce system pressure and force the boiler to increase its operating load to compensate for the lost steam.
As a result, fuel consumption and steam production costs both increase.
Not necessarily. Reduced boiler efficiency may result from fouling, scale buildup, steam leaks, damaged insulation, improper combustion, or unsuitable operating load.
The root cause should be identified before deciding whether repair, retrofit, or replacement is required.
Untreated feedwater can lead to scale formation and corrosion inside the boiler.
Both of these problems reduce heat transfer efficiency, shorten equipment life, and increase operating costs.
In many cases, rising steam production costs are not caused by a single issue but by multiple energy loss points occurring simultaneously throughout the boiler system.
From flue gas heat loss, boiler blowdown, steam leaks, condensate losses, inadequate insulation, boiler feedwater quality, operating load, to steam quality and deaerator performance, each factor can reduce fuel utilization efficiency if it is not properly controlled.
The key issue is not how much fuel the boiler consumes, but how much of the fuel's energy is actually converted into useful steam for production.
Businesses that effectively control these energy loss points can reduce fuel consumption, maintain stable boiler efficiency, and optimize steam production costs over the long term.
Not Every Boiler System with High Steam Costs Needs to Be Replaced. In many cases, high steam production costs are caused by several small energy losses occurring simultaneously that have not yet been measured or properly controlled.
If your boiler system is experiencing any of the following:
Increased fuel consumption.
High flue gas temperature.
Fluctuating steam pressure.
High make-up water consumption.
Rising steam production costs without a clearly identified cause.
The technical team at DIVI Group can conduct an on-site system assessment, analyze energy loss points, and recommend improvement solutions based on investment efficiency and expected payback period.
Technical Consultation Hotline: +84 942 488 818
Mr PIOUS (+84) 942 488 818