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The continuous flat hot press is the core equipment of the wood-based panel industry, and its technical level directly affects the quality and production cost of the panels. With the rapid development of industries such as custom home furnishings and green buildings, this equipment is continuously upgrading towards higher efficiency, smarter and more environmentally friendly.
Ⅰ. Equipment structure and composition
The fiberboard continuous flat press is a highly integrated system, which mainly includes the following core modules:
1.1 Paving system:
Function: Evenly lay the dried fiber and adhesive mixture into a continuous fiber blanket.
Key technology: airflow laying or mechanical laying to ensure uniform fiber distribution, no agglomeration, and controllable density gradient between the surface and core layers.
Equipment type: swing laying head, roller laying system, etc.
1.2 Pre-pressing device:
Function: Preliminary forming through light pressing, exhausting air, and reducing pressure fluctuations during the hot pressing stage.
1.3 Hot pressing system:
Core components: upper and lower steel belts, heating platens, hydraulic system.
Steel belt: high-precision high-temperature resistant alloy steel belt (thickness about 1.52.5mm), with extremely high surface finish requirements (Ra≤0.8μm).
Heating method: thermal oil heating or electric heating, temperature control accuracy ±1℃.
Pressure control: segmented pressure adjustment (up to 10MPa) to meet different density requirements.
1.4 Cooling system:
Function: Reduce the temperature of the sheet through water cooling or air cooling, stabilize the size, and reduce internal stress.
1.5 Cutting and stacking system:
Function: Cut the continuous sheet into specified size and stack it automatically.
Ⅱ. Continuous flat pressing process
2.1 Fiber laying: The dried fibers are passed through the laying head to form a uniform fiber blanket.
2.2 Pre-pressing and forming: Preliminary compaction to form a slab.
2.3 Hot pressing and curing: The slab enters the high temperature and high pressure zone, the adhesive is cured under the action of heat and pressure, and the fibers are cross-linked to form a dense structure.
2.4 Cooling and shaping: The temperature of the board is reduced through the cooling section to prevent deformation.
2.5 Cutting and post-processing: Cutting, sanding or veneer according to needs.
Ⅲ.Core energy-saving system
1. Heat recovery system (mainly for hot press exhaust)
1.1 Objective: To recover the sensible and latent heat from the high-temperature, high-humidity exhaust gas discharged from the hot press.
1.2 Core components:
(1) Exhaust collection system: Pipes and air hoods are used to effectively collect high-temperature exhaust gas discharged from the hot press outlet (usually between the upper and lower platens or the press outlet area).
(2) Heat exchanger: This is the core of the system. Common types are:
Plate heat exchanger: Compact structure, high efficiency, but it needs to deal with dust and oil in the exhaust gas to prevent clogging and corrosion, and usually requires pre-filtration.
Heat pipe heat exchanger: It uses the phase change of the working fluid inside the heat pipe to transfer heat, with high efficiency, good corrosion resistance, not easy to clog, and relatively simple maintenance. It is widely used in the OSB industry.
Spray/direct contact heat exchanger: It uses water to directly spray the exhaust gas for heat exchange, which can absorb sensible heat and latent heat (condensing water vapor) at the same time, but it will produce wastewater that needs to be treated, and the recovered heat energy is in the form of hot water.
(3) Filtration system: Located before the heat exchanger, it is used to remove wood fiber dust, oil (from press lubrication) and possible tar-like substances in the exhaust gas, protect the heat exchanger and maintain its efficiency. Common ones include cyclone separators, bag filters, electrostatic precipitators, etc.
(4) Fan: Provides power to overcome system resistance, extracts exhaust gas from the hot press, and discharges or sends it to the exhaust gas treatment device (such as RTO) after filtering and heat exchanger.
(5) Control valves and instruments: Temperature sensors, pressure sensors, flow meters, regulating valves, etc., used to monitor and control the exhaust gas flow rate, temperature, heat exchange medium flow, optimize heat recovery efficiency and safe operation.
1.3 Working Principle:
1. High-temperature exhaust gas (usually 180-220°C) is extracted from the hot press outlet by the fan.
2. The exhaust gas first passes through the filtration system to remove most of the dust and impurities.
3. The purified high-temperature exhaust gas enters the heat exchanger.
4. In the heat exchanger, the heat of the exhaust gas is transferred to the medium on the "cold side".
Most common application: Heating the drying air. The "cold side" medium is fresh air from the environment or the plant (or part of the recirculated air). The exhaust air heats this air, raising its temperature significantly (up to 120-160°C). This heated air is fed directly into the drying system (e.g. drum dryer or belt dryer) for drying the wet wood chips. This is the most direct and efficient use, as drying is the second largest energy consumer after hot pressing. The recovered heat directly replaces the fuel (natural gas or steam) that would otherwise be consumed in the drying oven.
Other applications: Heating process water (such as water for glue making, water for workshop heating), preheating boiler feed water, etc. (the efficiency is relatively lower than heating dry air).
5. After releasing the heat, the temperature of the exhaust gas is greatly reduced (usually to 100-140°C or lower), and then it is sent to the exhaust gas treatment system (such as RTO for VOC incineration) or discharged after meeting the emission standards.
6. The heat exchange process is usually designed as indirect heat exchange (except for spray type), and the exhaust gas and the heated air/water are not directly mixed.
2. Waste heat utilization system (mainly for steam condensate)
2.1 Goal: Recycle the heat in high-temperature steam condensate.
2.2 Background: The hot press heating plate is usually heated by high-pressure saturated steam (e.g. ~10 bar, 180°C). After the steam condenses in the heating plate and releases latent heat, high-temperature condensate is formed (the pressure is reduced, but the temperature is close to the saturation temperature at the corresponding pressure, for example, about 170-175°C when discharged at ~8 bar).
2.3 Core components:
Flash tank: This is the key equipment. High temperature and high pressure condensate is introduced into a lower pressure container (flash tank).
Steam separator: Usually integrated in the flash tank.
Pipeline, valve and control system: Used to transport condensate, control flash tank pressure, transport flash steam and residual hot water.
2.4 Working Principle (Flash Steam Recovery):
(1) High-temperature and high-pressure condensate is discharged from the hot press heating plate.
(2) Condensate enters the flash tank with lower pressure through the pressure reducing valve.
(3) Due to the sudden drop in pressure, part of the high-temperature condensate instantly "flashes" into low-pressure steam (called "flash steam" or "secondary steam"). For example, 10 bar condensate enters a 1-3 bar flash tank, which will produce saturated steam of the corresponding pressure.
(4) In the flash tank, the flash steam rises to the top and the remaining high-temperature hot water sinks to the bottom.
(5) Flash steam: is drawn out and transported to low-pressure steam users. In an OSB plant, the most important low-pressure user is the wood chip dryer (the dryer usually requires lower pressure steam, such as 3-5 bar). This part of the flash steam directly replaces the fresh boiler steam that the dryer originally needs to consume.
(6) Residual hot water: Although the temperature has dropped (for example, from 175°C to 110-120°C), it still contains a lot of heat. This part of hot water is usually: sent back to the boiler as preheated feed water, significantly reducing the fuel required for the boiler to heat the cold water to boiling. Or used in other process points that require hot water (such as rubber workshop, wood chip washing, workshop cleaning, etc.).
(7) The entire system stably generates flash steam at the required pressure by controlling the pressure of the flash tank.
3. Energy saving/power saving data
3.1 Overall energy saving potential: A well-designed and efficiently operated OSB continuous hot press heat recovery and waste heat utilization system can usually save 25%-50% of primary energy consumption for the entire OSB plant. This is mainly due to the significant reduction in fuel consumption (natural gas or steam) in the drying process and boiler fuel consumption.
3.2 Efficiency of heat recovery system:
Efficient heat exchangers (such as heat pipe type) can recover 60%-80% of the available heat in the exhaust gas of the hot press.
The recovered heat is used for drying and can replace 30%-60% of the raw fuel demand of the drying furnace. This means that the natural gas or steam consumption of the drying furnace can be reduced by one third to more than half.
3.3 Waste heat utilization system (flash steam) efficiency:
The heat recovery rate in high-temperature condensate is very high, usually reaching more than 90%.
The amount of flash steam generated depends on the pressure and temperature of the condensate and the pressure of the flash tank. For example, when 10 bar/180°C condensate flashes to 3 bar, about 15-20% of the water volume will become saturated steam at 3 bar. This part of the steam is directly used for drying, which is equivalent to saving an equal amount of fresh steam.
Sending the remaining hot water back to the boiler to preheat the feed water can usually increase the boiler efficiency by 5%-10%, because the boiler does not need to use fuel to heat the cold water from low temperature to near boiling point.
4. Other important energy-saving aspects (related to hot pressing)
In addition to the core heat recovery system, the OSB continuous hot pressing flat pressing production line has other energy-saving measures:
4.1 Optimization of the press drive system:
Variable frequency speed drive: Use variable frequency control for the main drive motor (oil pump, fan, etc.), adjust the speed according to the actual load, avoid inefficient operation of the motor at full load or no load, and significantly reduce power consumption.
4.2 High-efficiency insulation:
High-quality insulation is performed on the heating plate, steam pipe, valve, flash tank, heat recovery pipe, etc. of the hot press to minimize heat loss.
4.3 Accurate temperature and pressure control:
Adopt advanced control system to accurately control the temperature distribution and pressure curve of the pressure plate, ensuring that excessive energy consumption (such as too high temperature or too long pressure holding time) is avoided while meeting process requirements.
4.4 Leak detection and repair:
Regularly check and repair leaks in steam systems (valves, flanges, steam traps) and compressed air systems. The energy waste caused by a small steam leak is also very considerable when accumulated.
4.5 High-efficiency steam trap:
Use high-efficiency and reliable steam traps in the steam system to ensure timely discharge of condensate without steam leakage.
4.6 Energy management system:
Establish a plant-wide energy monitoring system (EMS) to monitor energy consumption data of each link (including hot pressing and heat recovery systems) in real time, analyze and optimize, and continuously improve energy efficiency.
Shandong MingHung OSB&MDF Machinery Equipment is a China professional factory who specilize in manufacturering and offering Wood based panel machine, including OSB making machine, MDF making machine, and Chipboard /PB making machine.
The machines we can offer includes: Wood chipper, Ring flaker, Strander, Wet silo, Drum dryer, Dry silo, Glue dosing and applying system /Glue blender, Mat forming, Continuous Multi-rolls pre-press, Multi opening hot press and Continuous press, Auto edge cutting machine line, Sanding machine line, kinds of related belt conveyor and so on.
Different clients may use different raw materials as their local resource, such as rice husk, bagasse, palm tree, eucaltptus, bamboo, pine and others, it will affect some machinery be different. Also related with the panel thickness, glue types, capacity and others. So after know your own conditions, our team can design a suitable quotation for you.
For more information, welcome contact us, we will reply you quickly and offer working videos with you
+86 18769900191, +86 15805496117, +86 18954906501
The continuous flat hot press is the core equipment of the wood-based panel industry, and its technical level directly affects the quality and production cost of the panels. With the rapid development of industries such as custom home furnishings and green buildings, this equipment is continuously upgrading towards higher efficiency, smarter and more environmentally friendly.
Ⅰ. Equipment structure and composition
The fiberboard continuous flat press is a highly integrated system, which mainly includes the following core modules:
1.1 Paving system:
Function: Evenly lay the dried fiber and adhesive mixture into a continuous fiber blanket.
Key technology: airflow laying or mechanical laying to ensure uniform fiber distribution, no agglomeration, and controllable density gradient between the surface and core layers.
Equipment type: swing laying head, roller laying system, etc.
1.2 Pre-pressing device:
Function: Preliminary forming through light pressing, exhausting air, and reducing pressure fluctuations during the hot pressing stage.
1.3 Hot pressing system:
Core components: upper and lower steel belts, heating platens, hydraulic system.
Steel belt: high-precision high-temperature resistant alloy steel belt (thickness about 1.52.5mm), with extremely high surface finish requirements (Ra≤0.8μm).
Heating method: thermal oil heating or electric heating, temperature control accuracy ±1℃.
Pressure control: segmented pressure adjustment (up to 10MPa) to meet different density requirements.
1.4 Cooling system:
Function: Reduce the temperature of the sheet through water cooling or air cooling, stabilize the size, and reduce internal stress.
1.5 Cutting and stacking system:
Function: Cut the continuous sheet into specified size and stack it automatically.
Ⅱ. Continuous flat pressing process
2.1 Fiber laying: The dried fibers are passed through the laying head to form a uniform fiber blanket.
2.2 Pre-pressing and forming: Preliminary compaction to form a slab.
2.3 Hot pressing and curing: The slab enters the high temperature and high pressure zone, the adhesive is cured under the action of heat and pressure, and the fibers are cross-linked to form a dense structure.
2.4 Cooling and shaping: The temperature of the board is reduced through the cooling section to prevent deformation.
2.5 Cutting and post-processing: Cutting, sanding or veneer according to needs.
Ⅲ.Core energy-saving system
1. Heat recovery system (mainly for hot press exhaust)
1.1 Objective: To recover the sensible and latent heat from the high-temperature, high-humidity exhaust gas discharged from the hot press.
1.2 Core components:
(1) Exhaust collection system: Pipes and air hoods are used to effectively collect high-temperature exhaust gas discharged from the hot press outlet (usually between the upper and lower platens or the press outlet area).
(2) Heat exchanger: This is the core of the system. Common types are:
Plate heat exchanger: Compact structure, high efficiency, but it needs to deal with dust and oil in the exhaust gas to prevent clogging and corrosion, and usually requires pre-filtration.
Heat pipe heat exchanger: It uses the phase change of the working fluid inside the heat pipe to transfer heat, with high efficiency, good corrosion resistance, not easy to clog, and relatively simple maintenance. It is widely used in the OSB industry.
Spray/direct contact heat exchanger: It uses water to directly spray the exhaust gas for heat exchange, which can absorb sensible heat and latent heat (condensing water vapor) at the same time, but it will produce wastewater that needs to be treated, and the recovered heat energy is in the form of hot water.
(3) Filtration system: Located before the heat exchanger, it is used to remove wood fiber dust, oil (from press lubrication) and possible tar-like substances in the exhaust gas, protect the heat exchanger and maintain its efficiency. Common ones include cyclone separators, bag filters, electrostatic precipitators, etc.
(4) Fan: Provides power to overcome system resistance, extracts exhaust gas from the hot press, and discharges or sends it to the exhaust gas treatment device (such as RTO) after filtering and heat exchanger.
(5) Control valves and instruments: Temperature sensors, pressure sensors, flow meters, regulating valves, etc., used to monitor and control the exhaust gas flow rate, temperature, heat exchange medium flow, optimize heat recovery efficiency and safe operation.
1.3 Working Principle:
1. High-temperature exhaust gas (usually 180-220°C) is extracted from the hot press outlet by the fan.
2. The exhaust gas first passes through the filtration system to remove most of the dust and impurities.
3. The purified high-temperature exhaust gas enters the heat exchanger.
4. In the heat exchanger, the heat of the exhaust gas is transferred to the medium on the "cold side".
Most common application: Heating the drying air. The "cold side" medium is fresh air from the environment or the plant (or part of the recirculated air). The exhaust air heats this air, raising its temperature significantly (up to 120-160°C). This heated air is fed directly into the drying system (e.g. drum dryer or belt dryer) for drying the wet wood chips. This is the most direct and efficient use, as drying is the second largest energy consumer after hot pressing. The recovered heat directly replaces the fuel (natural gas or steam) that would otherwise be consumed in the drying oven.
Other applications: Heating process water (such as water for glue making, water for workshop heating), preheating boiler feed water, etc. (the efficiency is relatively lower than heating dry air).
5. After releasing the heat, the temperature of the exhaust gas is greatly reduced (usually to 100-140°C or lower), and then it is sent to the exhaust gas treatment system (such as RTO for VOC incineration) or discharged after meeting the emission standards.
6. The heat exchange process is usually designed as indirect heat exchange (except for spray type), and the exhaust gas and the heated air/water are not directly mixed.
2. Waste heat utilization system (mainly for steam condensate)
2.1 Goal: Recycle the heat in high-temperature steam condensate.
2.2 Background: The hot press heating plate is usually heated by high-pressure saturated steam (e.g. ~10 bar, 180°C). After the steam condenses in the heating plate and releases latent heat, high-temperature condensate is formed (the pressure is reduced, but the temperature is close to the saturation temperature at the corresponding pressure, for example, about 170-175°C when discharged at ~8 bar).
2.3 Core components:
Flash tank: This is the key equipment. High temperature and high pressure condensate is introduced into a lower pressure container (flash tank).
Steam separator: Usually integrated in the flash tank.
Pipeline, valve and control system: Used to transport condensate, control flash tank pressure, transport flash steam and residual hot water.
2.4 Working Principle (Flash Steam Recovery):
(1) High-temperature and high-pressure condensate is discharged from the hot press heating plate.
(2) Condensate enters the flash tank with lower pressure through the pressure reducing valve.
(3) Due to the sudden drop in pressure, part of the high-temperature condensate instantly "flashes" into low-pressure steam (called "flash steam" or "secondary steam"). For example, 10 bar condensate enters a 1-3 bar flash tank, which will produce saturated steam of the corresponding pressure.
(4) In the flash tank, the flash steam rises to the top and the remaining high-temperature hot water sinks to the bottom.
(5) Flash steam: is drawn out and transported to low-pressure steam users. In an OSB plant, the most important low-pressure user is the wood chip dryer (the dryer usually requires lower pressure steam, such as 3-5 bar). This part of the flash steam directly replaces the fresh boiler steam that the dryer originally needs to consume.
(6) Residual hot water: Although the temperature has dropped (for example, from 175°C to 110-120°C), it still contains a lot of heat. This part of hot water is usually: sent back to the boiler as preheated feed water, significantly reducing the fuel required for the boiler to heat the cold water to boiling. Or used in other process points that require hot water (such as rubber workshop, wood chip washing, workshop cleaning, etc.).
(7) The entire system stably generates flash steam at the required pressure by controlling the pressure of the flash tank.
3. Energy saving/power saving data
3.1 Overall energy saving potential: A well-designed and efficiently operated OSB continuous hot press heat recovery and waste heat utilization system can usually save 25%-50% of primary energy consumption for the entire OSB plant. This is mainly due to the significant reduction in fuel consumption (natural gas or steam) in the drying process and boiler fuel consumption.
3.2 Efficiency of heat recovery system:
Efficient heat exchangers (such as heat pipe type) can recover 60%-80% of the available heat in the exhaust gas of the hot press.
The recovered heat is used for drying and can replace 30%-60% of the raw fuel demand of the drying furnace. This means that the natural gas or steam consumption of the drying furnace can be reduced by one third to more than half.
3.3 Waste heat utilization system (flash steam) efficiency:
The heat recovery rate in high-temperature condensate is very high, usually reaching more than 90%.
The amount of flash steam generated depends on the pressure and temperature of the condensate and the pressure of the flash tank. For example, when 10 bar/180°C condensate flashes to 3 bar, about 15-20% of the water volume will become saturated steam at 3 bar. This part of the steam is directly used for drying, which is equivalent to saving an equal amount of fresh steam.
Sending the remaining hot water back to the boiler to preheat the feed water can usually increase the boiler efficiency by 5%-10%, because the boiler does not need to use fuel to heat the cold water from low temperature to near boiling point.
4. Other important energy-saving aspects (related to hot pressing)
In addition to the core heat recovery system, the OSB continuous hot pressing flat pressing production line has other energy-saving measures:
4.1 Optimization of the press drive system:
Variable frequency speed drive: Use variable frequency control for the main drive motor (oil pump, fan, etc.), adjust the speed according to the actual load, avoid inefficient operation of the motor at full load or no load, and significantly reduce power consumption.
4.2 High-efficiency insulation:
High-quality insulation is performed on the heating plate, steam pipe, valve, flash tank, heat recovery pipe, etc. of the hot press to minimize heat loss.
4.3 Accurate temperature and pressure control:
Adopt advanced control system to accurately control the temperature distribution and pressure curve of the pressure plate, ensuring that excessive energy consumption (such as too high temperature or too long pressure holding time) is avoided while meeting process requirements.
4.4 Leak detection and repair:
Regularly check and repair leaks in steam systems (valves, flanges, steam traps) and compressed air systems. The energy waste caused by a small steam leak is also very considerable when accumulated.
4.5 High-efficiency steam trap:
Use high-efficiency and reliable steam traps in the steam system to ensure timely discharge of condensate without steam leakage.
4.6 Energy management system:
Establish a plant-wide energy monitoring system (EMS) to monitor energy consumption data of each link (including hot pressing and heat recovery systems) in real time, analyze and optimize, and continuously improve energy efficiency.
Shandong MingHung OSB&MDF Machinery Equipment is a China professional factory who specilize in manufacturering and offering Wood based panel machine, including OSB making machine, MDF making machine, and Chipboard /PB making machine.
The machines we can offer includes: Wood chipper, Ring flaker, Strander, Wet silo, Drum dryer, Dry silo, Glue dosing and applying system /Glue blender, Mat forming, Continuous Multi-rolls pre-press, Multi opening hot press and Continuous press, Auto edge cutting machine line, Sanding machine line, kinds of related belt conveyor and so on.
Different clients may use different raw materials as their local resource, such as rice husk, bagasse, palm tree, eucaltptus, bamboo, pine and others, it will affect some machinery be different. Also related with the panel thickness, glue types, capacity and others. So after know your own conditions, our team can design a suitable quotation for you.
For more information, welcome contact us, we will reply you quickly and offer working videos with you
+86 18769900191, +86 15805496117, +86 18954906501
Shandong Minghung Wood Machinery Factory Shandong minghung wood machine factory produces plywood machinery in linyi city city, china, dedicated to providing high-quality and suitable machines veneer machine,plywood machine,veneer splicing machine.veneer dryer machine,veneer peeling machine,plywood v
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