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MDP Hydraulics
The detachable gasket-type plate heat exchanger is an efficient and compact wall-type heat exchange device specifically designed for industrial applications that require frequent cleaning, maintenance, or process changes. Its core consists of a series of stamped metal thin plates with specific wave-shaped patterns, elastic sealing gaskets, and compression frames. The plates are sealed by the gaskets and arranged alternately to form narrow channels where cold and hot fluids flow alternately, enabling efficient heat exchange through the plates. Its detachable feature means that the entire plate bundle can be easily disassembled into individual plates, facilitating thorough inspection and mechanical/chemical cleaning on both sides of the plates, thus effectively addressing situations with easy scaling, particle content, or strict hygiene standards. In the field of mechanical manufacturing, it is a key thermal management component that ensures the stable and efficient operation of hydraulic systems, lubrication systems, and process cooling systems.
Under the condition that the two fluids do not mix with each other, heat transfer occurs through the plates.
1. Flow channel formation: When the plates with angular holes and the gaskets are stacked together, separate flow channels for cold and hot fluids are formed. Usually, the cold and hot fluids flow in opposite directions to achieve the maximum logarithmic mean temperature difference and heat transfer efficiency.
2. Turbulent flow enhanced heat transfer: The wave pattern design on the plates forces the fluid to generate intense turbulence in the flow channels. Even at a lower Reynolds number (Re), it can break the boundary layer and greatly enhance the heat transfer process. This enables its heat transfer coefficient to reach 3-5 times that of shell-and-tube heat exchangers.
3. Efficient heat exchange: Heat is transferred from the fluid with higher temperature through the extremely thin metal plates (usually 0.4-0.8mm) to the fluid with lower temperature, achieving rapid and efficient heat exchange.
• Heat transfer efficiency: The heat transfer coefficient is high, typically ranging from 3000 to 7000 W/(m²·K) (water-to-water condition), and the heat exchange efficiency far exceeds that of shell-and-tube heat exchangers.
• Compactness: The heat exchange area per unit volume is 2 to 5 times that of the shell-and-tube type, while the occupied floor space is only 1/5 to 1/8 of the latter.
• Design pressure and temperature:
Design pressure: Typically ranging from 0.6 to 2.5 MPa (6 - 25 bar), depending on the model and frame design.
◦ Design temperature: It is mainly limited by the material of the gasket. The conventional gasket (such as NBR) can operate at temperatures ranging from -20°C to 135°C; high-temperature gaskets (such as EPDM, FKM) can reach -25°C to 180°C or even higher.
• Small temperature difference at the end: It can achieve a temperature difference of approximately 1℃, with a heat recovery rate of over 90%, resulting in remarkable energy-saving effects.
• Flexibility: The heat exchange area can be easily adjusted by increasing or decreasing the number of plates; various process configurations can be achieved by changing the arrangement of the plates, enabling adaptation to different process requirements.
• Hydraulic system cooling: Cool the hydraulic oil to prevent the oil from overheating, which could lead to oil oxidation, viscosity reduction and decreased equipment efficiency. This ensures the stable operation of the hydraulic system.
• Cutting fluid/oil cooling: Used in CNC machines and machining centers, for cooling the circulating cutting fluid and lubricating oil, ensuring processing accuracy and prolonging the lifespan of the tools.
• Air compressor system cooling: Used for inter-stage coolers and post-coolers to reduce the temperature of compressed air, improve efficiency and separate condensed water.
• Injection molding machine temperature control: Used in the cooling water circuit of the mold to precisely regulate the mold temperature; or for cooling the hydraulic oil.
• Lubricant cooling for large equipment: such as lubricant cooling for wind turbine gearboxes, large compressors, and diesel engines.
Selection is a systematic process that requires detailed process parameters:
1. Define process conditions: Determine the types of fluids on both sides, flow rates, inlet and outlet temperatures, allowable pressure drop, and the physical and chemical properties of the fluids (such as viscosity, corrosiveness, and whether they contain particles).
2. Calculate heat load: Calculate the required heat exchange capacity (in kW) based on flow rate and temperature difference.
3. Select plate material and wave form: Choose the plate material based on the corrosiveness of the medium. Select the plate wave angle (high angle provides good heat transfer but has a large pressure drop; low angle is the opposite) based on flow rate, viscosity, and allowable pressure drop.
4. Select gasket material: Choose the gasket material based on fluid compatibility and working temperature.
5. Determine model and number of plates: Manufacturers usually provide selection software. Input the above parameters to calculate the required model, number of plates, and process arrangement.
6. Check pressure drop: Ensure that the calculated equipment pressure drop is within the allowable range of the system pump.
The equipment should be installed horizontally, with at least 1 meter of space reserved around it for maintenance purposes. When connecting the pipelines, excessive stress should be avoided on the heat exchanger interfaces. Before the first startup, the system pipelines should be thoroughly flushed.
When starting up, the valve on the low-temperature side should be opened first, followed by the valve on the high-temperature side slowly to avoid thermal shock. During normal operation, it is necessary to monitor the inlet and outlet temperatures and pressures.
• Maintenance and cleaning: Regular maintenance is crucial for ensuring efficient operation.
Regular inspection: Monitor the temperature and pressure differences at the inlet and outlet. A significant increase indicates signs of scaling or blockage.
Cleaning cycle: Depending on the cleanliness of the medium, it is usually necessary to clean the equipment once every 6 months to 2 years.
▪ Chemical cleaning (online/offline): For scale and other deposits, a cleaning solution composed of citric acid, phosphoric acid, etc. along with corrosion inhibitors can be used for continuous cleaning. It is strictly prohibited to use hydrochloric acid and other acid solutions containing chloride ions to clean stainless steel plates.
▪ Mechanical cleaning (after disassembly): Remove the plate bundles, and clean them using a high-pressure water gun, soft-bristled brush or nylon brush. It is strictly prohibited to use hard tools such as steel wire brushes to scrape the plates, as this may damage the protective film on the surface of the plates.
O-ring replacement: When the O-ring becomes aged, hardened, or undergoes permanent deformation, it needs to be replaced. During the replacement process, the sealing groove of the plate should be cleaned, and the new O-ring should be correctly installed using the appropriate adhesive or snap fasteners.
1. Pre-filtering: Install Y-type filters or basket filters (with a recommended precision of 100-500 μm) at the inlet pipeline of the heat exchanger and perform regular cleaning to reduce impurities from entering at the source.
2. Water quality/oil management: Soften, prevent scaling, and sterilize the circulating water; regularly test and replace hydraulic oil/lubricating oil.
3. Establish maintenance records: Record the time of each cleaning, maintenance, and component replacement, as well as changes in operating parameters, to facilitate predictive maintenance.
4. Standard operating procedures: Avoid frequent rapid cooling and heating operations and pressure surges (water hammer), to extend the lifespan of gaskets and plates.


A1: This is an efficient heat exchange device consisting of a series of corrugated metal plates, elastic sealing gaskets, and a compression frame. The most crucial feature of this device is its detachability - all the plates and gaskets can be easily removed for thorough inspection and cleaning. This makes it particularly suitable for handling fluids that are prone to scaling, clogging, or require strict cleaning. It is widely used in mechanical manufacturing for cooling and heating processes.
A2: The main advantages lie in three aspects: high efficiency, small size, and easy maintenance:
• High efficiency: The corrugated plate design generates intense turbulence, resulting in a heat transfer coefficient that is 3-5 times higher than that of shell-and-tube heat exchangers, and the heat exchange efficiency is extremely high.
• Small in size: Compact structure, with the same heat exchange capacity, the occupied area is only a fraction of that of the shell-and-tube type.
• Easy to maintain: It can be completely disassembled, making cleaning very convenient and thorough, and the maintenance cost is low. Moreover, by adjusting the number of plates, the heat exchange capacity can be flexibly adjusted.
A3: The cold and hot fluids exchange heat without mixing through the alternating plate channels. The corrugations on the plates force the fluids to generate turbulence, breaking the thermal resistance boundary layer, thus achieving efficient heat transfer. The counter-flow arrangement is usually adopted to maintain a large temperature difference between the two fluids throughout the heat exchange surface, further enhancing the efficiency.
Q4: What key parameters are required to select my system?
A4: Accurate selection requires the following key process parameters:
1. Fluid information: The types of fluids on both sides (such as water, oil, solution, etc.) and their physical properties (such as specific heat capacity, density, viscosity).
2. Flow rate: The volumetric flow rate of the fluids on both sides (m³/h).
3. Temperature: The inlet and target outlet temperatures of the fluids (°C).
4. Allowable pressure drop: The maximum pressure loss that the system allows for this heat exchanger (bar or kPa).
5. Working pressure and temperature: The maximum working pressure and the highest/lowest working temperature of the system.
6. Medium characteristics: Whether it is corrosive, prone to scaling, contains particles, etc.
A5: The material selection depends on the corrosiveness of the fluid and the working temperature:
• Plate material:
304/316 stainless steel: Suitable for most neutral or weakly corrosive media such as water purification and mineral oil, with good economic applicability.
Titanium materials: Suitable for corrosive media such as seawater and solutions containing chloride ions.
Other special alloys (such as Hastelloy): Used in extremely corrosive environments such as those exposed to strong acids and strong bases.
• Gasket material:
NBR (Nitrile Butadiene Rubber): Suitable for water and oils, with a temperature range of approximately -15°C to 135°C.
EPDM (Ethylene Propylene Diene Monomer): Suitable for hot water, steam, acids, and alkalis. It has better heat resistance (up to 150-180°C).
FKM (Fluorine Rubber): Suitable for high-temperature oils, strong acids, and strong bases. It has the best heat resistance and corrosion resistance.
A6: The main considerations are maintenance and cleaning requirements and compatibility with the medium:
• Choose a detachable design: When the fluid being handled is prone to scaling and clogging (such as cooling tower water, process fluids with particles), regular thorough cleaning is necessary; or if the process may change in the future and the heat exchange area needs to be adjusted.
• Consider brazing or full-welding: when the medium is extremely clean (such as refrigerants), the sealing requirements are extremely high (for toxic or expensive media), or the working pressure/temperature is extremely high and exceeds the capacity of the gasket.
A7:
1. Horizontal installation: The equipment should be installed horizontally on a sturdy foundation to ensure uniform force distribution on the frame.
2.Reserved space: Adequate space (typically ≥ 1 meter) should be reserved on the mobile end (the side with the movable compression plate) and above the equipment for future disassembly and removal of the plates.
3. Pipeline connection: When connecting the inlet and outlet pipelines, appropriate supports should be used to avoid direct application of pipeline weight and thermal stress to the interface of the heat exchanger, preventing leakage at the interface or deformation of the equipment.
4. Cleaning system: Before connecting the heat exchanger, thoroughly clean the entire pipeline system to remove welding slag, iron filings, and other impurities. This is a crucial step to prevent plate blockage and scratches.
1. Inspection and Tightening: Check whether all clamping bolts have been evenly tightened in a diagonal sequence to the specified compression dimension.
2. Exhaust: Slowly open the valve on the low-temperature side (usually the refrigerant side) to allow the fluid to fill the flow channel on that side, and open the exhaust valve at the high point to discharge air. Then perform the same operation on the high-temperature side.
3. Slowly Increase Pressure and Temperature: First, gradually increase the system pressure to the working pressure to check for any leaks. Then slowly increase the fluid temperature to the working temperature to avoid failure of the gasket seal or deformation of the plates due to thermal shock.
4. Parameter Monitoring: Record the inlet and outlet temperatures and pressures after stable operation as the benchmark for future performance comparison.
A9: Parameters that should be monitored and recorded on a regular basis include:
• Temperature: The inlet and outlet temperatures of both fluids. An abnormal increase in the outlet temperature (on the cold side) or a decrease (on the hot side) may indicate a decline in heat exchange efficiency.
• Pressure: The inlet pressure of the two fluids and the calculation of pressure drop. An abnormally large increase in pressure drop is usually an early indication of flow channel blockage or fouling.
• Leak check: Regularly inspect the exterior of the equipment, especially the edges of the plate assembly, for any signs of medium leakage.
• Cleaning timing: When the heat exchange efficiency significantly decreases (manifested as the outlet temperature failing to meet the requirements) or the pressure drop increases markedly (exceeding the design value by 15-20%), cleaning is necessary.
• Cleaning method:
Chemical cleaning (online): For scale and other deposits, a dedicated cleaning agent (such as a weak acid solution) can be circulated within the system without the need to disassemble the equipment. It is strictly prohibited to clean stainless steel plates with hydrochloric acid.
Mechanical cleaning (after disassembly): Shut down and isolate the equipment, remove the plate bundles, and clean each plate one by one using a high-pressure water gun, soft-bristled brush or nylon brush. It is strictly prohibited to use steel wire brushes, screwdrivers, or other hard tools to avoid damaging the plates.
• Replacement timing: The gasket will age, harden or undergo permanent deformation due to long-term pressure, high temperatures and chemical effects. It is generally recommended to replace it every 2-4 years or when leakage is detected and re-tightening of the bolts is ineffective.
• Replacement steps:
1. Remove the plate bundle.
2. Thoroughly clean the old gaskets and sealing grooves on the plate.
3. Apply the special adhesive evenly in the sealing grooves of the plate (if it is a glue bonding type), or insert the new gasket accurately into the groove (if it is a snap-in type).
4. Reassemble the plates in sequence and tighten them to the specified compression dimension.
V. Fault Diagnosis and Elimination
1. Bolt loosening: Long-term operation or temperature fluctuations may cause uneven compression force. Solution: In the equipment without pressure, use a torque wrench to re-tighten the bolts diagonally in sequence to the specified size.
2. Gasket aging or damage: The gasket loses elasticity or develops cracks. Solution: Replace the damaged gasket.
3. Plate deformation or cracking: Usually caused by pressure shock, freezing or corrosion. Solution: Inspect and replace the damaged plates.
A13:
1. Insufficient air discharge or system air blockage: Affects fluid filling and heat exchange. Solution: Check and ensure that the system is fully vented.
2. Inconsistent flow distribution: Due to pipeline layout or valve issues, the fluid does not pass through all the plate channels evenly. Solution: Check the inlet and outlet pipelines and valves.
3. Insufficient selected area or changes in operating conditions: The actual heat load exceeds the design value. Solution: Verify the current operating parameters and, if necessary, increase the number of plates.
Judgment: If the medium from the high-pressure side appears at the low-pressure side outlet (for example, oil is mixed into the cooling water), or if the changes in the composition of the media on both sides can be confirmed through testing.
• Reasons and Solutions:
1. Hole in the plate: Caused by corrosion or wear. Solution: Disassemble the equipment, conduct light-transmission inspection or pressure test on the plate, identify and replace the perforated plate.
2. Failure of the main sealing area of the gasket: The gasket is damaged at the corner holes or edge of the passage. Solution: Replace the failed gasket.
1. Pipeline stress: Improper fixation of the connecting pipeline transfers vibrations to the equipment. Solution: Check and re-support the pipeline to ensure that the heat exchanger interface is not subjected to external forces.
2. Cavitation: Insufficient suction height of the pump or excessively low local pressure causes cavitation. Solution: Check the operating conditions of the pump and the system pressure.
3. Excessive flow or high flow velocity: Beyond the design range. Solution: Verify the actual flow rate and adjust the valve opening.