Shell and tube heat exchangers are one of the most widely used and important heat transfer equipment in the chemical and industrial fields, and are highly regarded for their rugged design, versatility, and ability to handle a variety of fluids under various operating conditions. Shell and tube heat exchangers consist of a cylindrical shell that houses a bundle of tubes, with one fluid flowing inside the tube bundle and another fluid flowing around the tubes in the shell, allowing for efficient heat exchange without direct contact between the fluids. Key components such as tube sheets, baffles, and headers enhance flow control and heat transfer performance. Various configurations such as fixed tube sheets, U-tubes, and floating head designs are available to meet specific process needs, including high pressure, thermal expansion, and ease of maintenance. These heat exchangers are widely used in processes such as heating, cooling, condensing, evaporation, and waste heat recovery in industries such as petrochemicals, power generation, refrigeration, pharmaceuticals, and food processing. While they have advantages such as high durability, wide material compatibility, and scalability, they also face challenges such as susceptibility to fouling, large footprint, and complex design considerations. With advances in efficiency, compactness, intelligent monitoring, and sustainability, shell and tube heat exchangers remain the cornerstone of industrial heat exchange technology.
Equipment type | Classification method | Features | Application scenario |
Fixed tube sheet heat exchanger | Classification by structure | The two ends of the tube bundle are fixed on the tube sheet, and the tube sheet is welded to the shell. This structure is simple, compact and low in cost, but the tube bundle cannot be pulled out, making cleaning and maintenance more difficult. | Suitable for occasions where the shell side medium is clean and not easy to scale, such as cooling water. |
Floating head heat exchanger | Classification by structural form | One end of the tube sheet is fixed to the shell, and there is a floating head between the other end of the tube sheet and the shell, which can be freely extended and retracted. This structure allows the tube bundle to be pulled out, which is convenient for cleaning and maintenance, but the structure is complex and the cost is high. | Suitable for occasions where the shell side medium is easy to scale and needs frequent cleaning, such as handling liquids containing impurities. |
U-tube heat exchanger | Classification by structural form | The tube bundle is U-shaped, and both ends are fixed on the same tube sheet. The U-tube heat exchanger allows the tube bundle to expand and contract freely, avoiding thermal stress, but it is difficult to clean the tube. | It is suitable for high temperature, high pressure and large temperature difference occasions, such as heat exchange between steam and liquid. |
Stuffing box heat exchanger | Classification by structural form | One end of the tube sheet is fixed, and the other end is connected to the shell through the stuffing box, which is convenient for the tube bundle to be pulled out and cleaned. This structure is simple and low in cost, but the stuffing box may leak. | Suitable for occasions that require frequent cleaning but do not require high sealing. |
Straight tube heat exchanger | Classification by heat transfer tube arrangement | The heat transfer tube is a straight tube, usually arranged vertically or horizontally. This structure is simple and easy to clean and maintain. | Applicable to most heat exchange occasions, especially those that require frequent cleaning. |
Spiral tube heat exchanger | Classification by heat transfer tube arrangement | The heat transfer tubes are arranged in a spiral shape, which increases the turbulence of the fluid and improves the heat transfer efficiency. | Applicable to occasions that require high heat transfer efficiency, such as processing high-viscosity fluids. |
Corrugated tube heat exchanger | Classified by heat transfer tube arrangement | The heat transfer tube is a corrugated tube, which increases the elasticity of the tube wall, can absorb thermal stress, and improve the heat transfer efficiency. | Suitable for occasions with large temperature differences and high heat transfer efficiency. |
Smooth tube heat exchanger | Classified by heat transfer tube shape | The heat transfer tube has a smooth surface, simple processing, and low cost, but the heat transfer efficiency is relatively low. | Applicable to general heat exchange occasions. |
Fin tube heat exchanger | Classification by heat exchange tube shape | The outer surface of the heat transfer tube is equipped with fins, which increases the heat transfer area and improves the heat transfer efficiency. There are many types of finned tubes, such as plain fins, threaded fins, etc. | Applicable to heat exchange between gas and liquid, such as air coolers, condensers, etc. |
Bellows heat exchanger | Classification by shape of heat exchange tube | The heat transfer tube is a bellows tube, which increases the elasticity of the tube wall, can absorb thermal stress, and improve the heat transfer efficiency. | Suitable for occasions with large temperature differences and high heat transfer efficiency. |
Heater | Classification by purpose of heat exchanger | Used to heat the fluid from low temperature to high temperature. Steam or hot water is usually used as the heat source. | For example, heating reaction materials in chemical production, heating milk in food processing, etc. |
Cooler | Classification by the purpose of the heat exchanger | Used to cool the fluid from high temperature to low temperature. Usually cooling water or air is used as the cooling medium. | For example, cooling reaction products in chemical production, cooling beverages in food processing, etc. |
Condenser | Classification by the purpose of heat exchanger | Used to condense gas into liquid. Usually cooling water is used as the cooling medium. | Such as condensing steam in the distillation process, condensing refrigerant in the refrigeration system, etc. |
Evaporator | Classification by the purpose of heat exchanger | Used to evaporate liquid into gas. Usually steam or hot water is used as the heat source. | For example, evaporating water to concentrate juice in food processing, evaporating solvents to recover products in chemical production, etc. |
Downstream heat exchanger | Classified by the fluid flow mode of the heat exchanger | The cold and hot fluids flow in the same direction in the heat exchanger. The temperature difference distribution of this flow mode is uneven, but the thermal stress is small. | Applicable to occasions with small temperature difference. |
Counterflow heat exchanger | Classified by the fluid flow mode of the heat exchanger | The cold and hot fluids flow in the heat exchanger in the opposite direction. The temperature difference distribution of this flow mode is uniform, the heat transfer efficiency is high, but the thermal stress is large. | Suitable for occasions with large temperature differences. |
Counterflow heat exchanger | Classified by the fluid flow mode of the heat exchanger | The hot and cold fluids flow crosswise in the heat exchanger. The temperature difference distribution of this flow mode is between the downstream and the countercurrent flow, and the heat transfer efficiency is high. | It is suitable for occasions with large temperature differences. |
References | Authors | Abstract | DOI |
Three-dimensional numerical simulation of shell-side flow and heat transfer in shell-and-tube heat exchangers | Huang Xinghua, Wang Qijie, Lu Zhen | A three-dimensional simulation method for single-phase flow and heat transfer in the shell of a shell-and-tube heat exchanger is proposed. The volume porosity, surface permeability, distributed resistance and distributed heat source are used to consider the flow channel reduction, flow resistance and heat transfer effects caused by the complex geometric structure of the shell. By numerically solving the average fluid mass, momentum and energy conservation equations, the distribution of flow and heat transfer in the shell is obtained. This method is used to numerically simulate the flow and heat transfer of an experimental heat exchanger, and the calculated results are in good agreement with the experimental results. | 10.3321/j.issn:0438-1157.2000.03.003 |
Overview of Heat Transfer Enhancement Technology of Shell and Tube Heat Exchangers | Qi Hongyang, Gao Lei, Zhang Yingying, Zhou Chenlin | The research progress of new shell and tube heat exchangers at home and abroad in recent years is reviewed. The development history, structural improvement and enhanced heat transfer mechanism of shell and tube heat exchangers are introduced from three aspects: tube side, shell side and tube bundle. The shell and tube heat exchangers are compared with ordinary bow baffle heat exchangers, and the enhanced heat transfer characteristics of various heat exchangers are summarized. Finally, the research direction of heat exchangers is pointed out. | 10.3969/j.issn.1001-4837.2012.07.014 |
Experimental study and prediction of shell-side heat transfer and resistance performance of shell-and-tube heat exchangers | Xie Gongnan, Peng Botao, Chen Qiuyang, Wang Qiuwang, Luo Laiqin, Huang Yanping, Xiao Zejun | A comprehensive performance test bench for heat transfer and resistance of heat exchangers was designed and established, and the shell-side heat transfer and resistance performance of a bow-shaped baffle heat exchanger and two continuous spiral baffle heat exchangers were experimentally studied. The test media were water on the tube side and oil on the shell side. At the same time, based on the shell-side heat transfer test data, the total heat transfer of the heat exchanger was predicted by genetic algorithm. The test results show that: under the same shell-side flow rate, the resistance of the spiral baffle heat exchanger is greater than that of the arcuate baffle heat exchanger, and the resistance of the positive inlet and positive outlet spiral baffle heat exchanger is greater than that of the side-inlet and side-outlet spiral baffle heat exchanger; the heat transfer coefficient of the spiral baffle heat exchanger is greater than that of the arcuate baffle heat exchanger, and the heat transfer coefficient of the side-inlet and side-outlet spiral baffle heat exchanger is greater than that of the positive inlet and positive outlet spiral baffle heat exchanger. | 10.3321/j.issn:0258-8013.2006.21.017 |
A Comprehensive Review of Heat Transfer Enhancement Methods in Shell and Tube Heat Exchangers | S. A. Marzouk, M.M. Abu Alsood | Extensive research has been conducted to increase the heat transfer rate and reduce the size and cost of shell and tube heat exchangers (STHEs). The contribution of this paper is its ability to provide a comprehensive, up-to-date, and systematic overview of the various heat transfer enhancement methods available in shell and tube heat exchangers, making it an important resource for researchers, engineers, and practitioners in the field of heat transfer. This paper reviews the studies that investigated the overall heat transfer coefficient (U), number of heat transfer units, exergy efficiency, pressure drop, and thermohydraulic performance. Passive methods have some advantages over active methods, such as no need for external power and lower operating costs. These studies generally support the view that heat transfer enhancement in shell and tube heat exchangers is making great progress. A total of 47.8% of the studies focused on passive methods, with air injection, heat transfer enhancement using nanofluids, and composite methods accounting for 20.2%, 22.3%, and 9.7%, respectively. Bubble injection resulted in an increase in U-ratio, which was a maximum of 452% compared to water flow alone. Swirl vanes, bellows, and coil inserts had U-ratio values of 130%, 161%, and 264%, respectively. Nanofluids resulted in increased heat transfer, with TiO2 having the maximum U-ratio (175.9%) compared to conventional fluids. The combination of air injection and passive heat enhancement methods has been shown to be an effective approach to address multiple issues and needs to be the focus of more future work. | 10.1007/s10973-023-12265-3 |
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