Ten things to know before buying a heat exchanger

Jun 24, 2026 Leave a message

1. How should the type of heat exchanger be selected?

 

 

 

Different heat exchanger structures are suitable for different operating conditions; the heat exchange task and medium characteristics must be clearly defined before selection.

 
 

 

Plate heat exchangers are suitable for applications requiring high heat exchange efficiency, with limited space, and relatively clean media, but are not suitable for high-pressure fluids or fluids containing a large number of solid particles.

 
 

 

Shell-and-tube heat exchangers are suitable for high-temperature, high-pressure, complex media, or conditions prone to fouling; they offer structural stability but require a larger footprint.

 
 

 

Spiral plate heat exchangers and air-cooled heat exchangers are suitable for special processes or space-constrained scenarios.

 

The core principle for selection is: suitability for operating conditions takes precedence over equipment price.

 

II. What is the medium that needs to be processed?

• Complete information about the hot and cold end media must be clearly defined, including composition, concentration, and phase (liquid/gas/vapor).

• If the media is corrosive (e.g., acid, alkali, salt solution), the material grade (e.g., 304/316L/titanium) must be determined in advance.

• If the media contains oil or particulate matter, anti-clogging structures or filtration systems need to be considered.

• Different media will also affect flow rate design and flow channel structure selection.

• Media information is a fundamental parameter for equipment selection; incorrect judgment can directly lead to equipment failure or a significantly shortened lifespan.

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3. What is the designed heat exchange capacity?

 

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Heat exchange capacity is the core calculation basis for heat exchanger selection, usually expressed in kW or kcal/h.

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The actual heat load must be calculated in conjunction with the production process, rather than a simple estimate.

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Insufficient heat exchange capacity will cause the system to fail to meet production requirements, while excessive heat exchange capacity will increase investment costs and energy losses.

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A certain safety margin (generally 5%~15%) must also be considered during the design.

 

Heat exchange capacity is closely related to parameters such as flow rate, temperature difference, and specific heat capacity.

 

 

 

IV. What are the inlet and outlet temperature requirements?

 

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• The inlet and outlet temperature ranges of the hot and cold fluids must be clearly defined; this is a crucial condition for heat balance calculations.

• The smaller the temperature difference, the larger the required heat exchange area and the higher the equipment cost.

• If temperature fluctuations exist, the design should be based on the most unfavorable operating conditions.

• For precision processes (such as food and pharmaceuticals), the required temperature control accuracy directly impacts the structural design.

• Temperature conditions also affect material thermal stress and sealing reliability.

V. What are the operating pressure and temperature ranges?

 

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It is essential to clearly define the equipment's maximum operating pressure, design pressure, and the range of pressure fluctuations during actual operation to avoid structural risks associated with overpressure conditions.

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Under high-pressure conditions, higher-strength materials or thicker wall designs are typically required. Shell-and-tube heat exchangers should be prioritized to enhance pressure resistance when necessary.

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The operating temperature range directly impacts material selection and sealing system design. For example, gaskets must be selected based on their temperature resistance rating, using different types such as rubber, graphite, or spiral wound gaskets.

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If frequent temperature alternations or rapid temperature rises and falls occur, the effects of thermal stress and fatigue should be carefully assessed to prevent cracking or leakage risks during long-term operation.

6. Is the medium prone to scaling or clogging?

 

 

• Scaling is one of the main causes of heat exchanger efficiency decline and must be assessed in advance.

• Media containing calcium and magnesium ions, suspended solids, or organic matter easily form fouling layers.

• For applications prone to scaling, removable structures (such as plate heat exchangers) should be prioritized for easy cleaning and maintenance.

• Scaling can be reduced by increasing flow rates or incorporating anti-scaling designs.

• Ignoring scaling can lead to a rapid decline in heat exchange efficiency and even equipment shutdown.

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7. What are the requirements for heat exchange efficiency?

 

 

Different processes have significantly different requirements for heat exchange efficiency. For example, energy-saving systems typically prioritize higher heat transfer coefficients to reduce energy consumption and improve overall heat recovery efficiency.

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Plate heat exchangers offer advantages such as high heat transfer efficiency and compact structure, but their narrow flow channels and relatively large pressure drops necessitate a comprehensive balance between efficiency improvement and pumping energy consumption.

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While shell-and-tube heat exchangers have relatively lower heat transfer efficiency, they boast robust structures, strong resistance to high temperatures and pressures, and exhibit better stability and reliability under long-term continuous operation.

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During equipment selection, it is necessary to assess whether the system can tolerate a certain level of pressure loss in exchange for a smaller equipment footprint and higher space utilization.

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8. What are the installation space and interface requirements?

 

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• The dimensions of the on-site installation space must be clearly defined, including height, width, and maintenance space.

• Different heat exchanger structures have significantly different space requirements (plate heat exchangers are compact, shell-and-tube heat exchangers require more space).

• Inlet and outlet pipe diameters and flange standards (e.g., PN, ANSI) must be compatible with the system.

• Whether future expansion or parallel installation is needed is also a key design consideration.

• Space constraints often directly influence the final selection of the heat exchanger.

 

9. Is it easy to maintain and clean in the later stages?
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During long-term operation, heat exchangers are affected by scaling, fouling deposits, and corrosion products, requiring regular cleaning. Otherwise, heat transfer efficiency will significantly decrease, and energy consumption will increase.

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Plate heat exchangers feature a detachable design, facilitating quick disassembly and cleaning, making them more suitable for operating conditions requiring high-frequency maintenance or where the medium is prone to scaling.

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Shell-and-tube heat exchangers, due to their more enclosed structure, have a relatively longer overall cleaning cycle, but maintenance typically requires more complex disassembly or chemical cleaning processes.

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The availability of a Clean-in-Place (CIP) system is crucial for continuous production, enabling cleaning and maintenance with minimal or no downtime, improving production continuity.

10. How to assess the budget and total life cycle cost?

 

 

 

• Procurement cost is only a portion of the initial investment and should not be the sole basis for decision-making.

• Operating energy consumption (pump power consumption, pressure drop loss) is often a major long-term cost.

• Maintenance costs (cleaning, seal replacement) should also be included in the calculation.

• While high-efficiency equipment is more expensive, its long-term energy savings may be greater.

• A comprehensive evaluation should be conducted using a Life Cycle Cost (LCC) model.

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Anyang Tengrui Energy Saving Equipment Co., Ltd.

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