Relevant bibliographies by topics / Shell-and-tube heat exchanger

Contents

  1. Journal articles
  2. Dissertations / Theses
  3. Books
  4. Book chapters
  5. Conference papers

Academic literature on the topic 'Shell-and-tube heat exchanger'

Author: Grafiati
Published: 4 June 2021
Last updated: 12 June 2025

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Journal articles on the topic "Shell-and-tube heat exchanger"

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Patel, Ankit R. "Design and optimization of Shell and Tube Heat Exchanger." Indian Journal of Applied Research 3, no. 8 (2011): 264–66. http://dx.doi.org/10.15373/2249555x/aug2013/85.

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Anantha, Sobhanadri, Senthilkumar Gnanamani, Vivekanandan Mahendran, et al. "A CFD investigation and heat transfer augmentation of double pipe heat exchanger by employing helical baffles on shell and tube side." Thermal Science 26, no. 2 Part A (2022): 991–98. http://dx.doi.org/10.2298/tsci201120300a.

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The inclusion of baffles in a double pipe heat exchanger is becoming increasingly important as it improves the heat exchanger's performance. The CFD analysis is used in this paper to investigate the performance of double pipe heat exchangers with and without helical baffles on both shell tube sides. The 3-D CFD model was created in Solid Works, and the FloEFD software was used to analyze the conjugate heat transfer between the heat exchanger's tube and shell sides. Heat transfer characteristic like outlet temperature of shell and tube are investigated along with pressure drop on shell and tube side. Based on CFD results of double pipe heat exchanger with helical baffle on both shell side and tube side (Type 4) gives the better results than the other type of heat exchangers with an increased pressure drop than the others, results reveals that Type 4 outlet temperature of shell side is 8% higher and on tube side it is 5.5% higher, also pressure drop on shell side is 12% higher and on tube side it is 42% higher than the other types.
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Krisdiyanto, Krisdiyanto, Rahmad Kuncoro Adi, Sudarisman Sudarisman, and Sinin Bin Hamdan. "An analysis of tube thickness effect on shell and tube heat exchanger." Eastern-European Journal of Enterprise Technologies 1, no. 8 (109) (2021): 25–35. http://dx.doi.org/10.15587/1729-4061.2021.225334.

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Heat exchangers are important equipment for the process of placing heat. The most widely used type of heat exchanger is shell and tube. This type is widely used because of its simple and easy design. Design of shell and tube heat exchangers is done by the side or shell variations to get the desired performance. Therefore, research is conducted to study the effect of tube thickness on heat transfer, pressure drop, and stress that occurs in the shell and tube heat exchanger so that the optimal tube thickness is obtained. In this research, the activities carried out are the design of heat exchangers for the production of oxygen with a capacity of 30 tons/day. The standard used in this study is the 9th edition heat exchanger design guidance document compiled by the Tubular Exchanger Manufacturer Association (TEMA). Analysis of the tube thickness effect on heat transfer, pressure drop, and stress was carried out using the SimScale platform. The effect of variations in tube thickness on heat transfer is that the thicker the tube, the lower the heat transfer effectiveness. The highest value of the heat exchanger effectiveness is 0.969 at the tube thickness variation of 0.5 mm. The lowest value of the heat exchanger effectiveness is 0.931 at the tube thickness variation of 1.5 mm. The effect of variations in tube thickness on pressure drop is that the thicker the tube, the higher the pressure drop. The highest value of pressure drop is in the variation in tube thickness of 1.5 mm, 321 Pa. The lowest value of drop pressure is in the variation of 0.5 mm tube thickness, which is 203 Pa. The thickness of the tube also increases the maximum stress on the components of the shell, head, tubesheet, baffle, and saddle, but the value is fluctuating
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Khatkar, Keshav Raj. "Modelling and CFD analysis of Shell & Tube Heat Exchanger." International Journal Of Mechanical Engineering And Information Technology 05, no. 07 (2017): 1663–70. http://dx.doi.org/10.18535/ijmeit/v5i7.02.

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Amarnagendram, Dr B. "Design and Analysis of Various Baffle System in Shell Tube Heat Exchanger." International Journal for Research in Applied Science and Engineering Technology 9, no. VII (2021): 3207–11. http://dx.doi.org/10.22214/ijraset.2021.37010.

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Heat exchangers are systems of thermal engineering in which its applications are occurred in different industries. Heat exchangers are the basic or heart of once organized plant since it transfers energy to the processing plant Shell and tube heat exchanger is the most common type heat exchanger widely use in refinery and other chemical process, because it suits high pressure application. The process in solving simulation consists of modeling and meshing the basic geometry of shell and tube heat exchanger using CFD package ANSYS 18.0. The objective of the project is design of shell and tube heat exchanger with various baffle structure and study the flow and temperature field inside the shell using ANSYS software tools. The heat exchanger with single, double, and with 10 and 20 degree inclined baffle will be defined. In simulation will show how the pressure varies in shell due to different double baffle angle and flow rate. The flow pattern in the shell side of the heat exchanger with angled baffles was forced to which results in a significant increase in heat transfer coefficient per unit pressure drop in the heat exchanger.
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Ahmed, Farid, Md Minaruzzaman Sumon, Muhtasim Fuad, Ravi Gugulothu, and AS Mollah. "Numerical Simulation of Heat Exchanger for Analyzing the Performance of Parallel and Counter Flow." WSEAS TRANSACTIONS ON HEAT AND MASS TRANSFER 16 (September 20, 2021): 145–52. http://dx.doi.org/10.37394/232012.2021.16.17.

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Heat exchangers are almost used in every industry. Among them, shell and tube heat exchangers are covering around 32% of the total heat exchanger. Numerical simulation of the Computational models is playing an important role for the prototypes including the Heat Exchanger Models for the improvement in modeling. In this study, the CFD analysis of parallel and counter flow shell and tube heat exchanger was performed. Following project, looked into the several aspects and these are the temperature, velocity, and pressure drop and turbulence kinetic energy along with the heat exchanger length. Hot water was placed in tube side and cold water was placed in shell side of the heat exchanger. Shell side cold temperature was increasing along the heat exchanger length. On the other side, tube side hot water temperature was decreasing along the tube length. This effect was more significance in counter flow rather than the parallel flow. Velocity was more fluctuating in the shell side due to presence of the baffles. Also following the same reason, pressure drop was higher in the shell side cold water rather than the tube side hot water. To measure the turbulence effect, turbulence kinetic energy was determined. Turbulence was decreasing first part of the shell and tube heat exchanger. But, it was increasing along through the rest part heat exchanger. All these observations and the outcomes are evaluated and then further analyzed
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Pasupuleti, Ravindra Kumar, Manindra Bedhapudi, Subba Reddy Jonnala, and Appa Rao Kandimalla. "Computational Analysis of Conventional and Helical Finned Shell and Tube Heat Exchanger Using ANSYS-CFD." International Journal of Heat and Technology 39, no. 6 (2021): 1755–62. http://dx.doi.org/10.18280/ijht.390608.

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The summary of the proposed work is to compare the rate of heat transfer, logarithmic mean temperature difference (LMTD) and effectiveness (ε) for a conventional shell and tube heat exchanger with and without helical finned surfaces on tube side of heat exchanger. It is shown that the inlet velocity of cold fluid at the tube side varies, while the inlet velocity of hot fluid at the shell side remains constant. The percentage variations of heat transfer rates with theoretical and simulation methods are compared. The geometry is modelled in ANSYS design modeler and analysis have been carried out in ANSYS-CFD. The inlet velocity of shell side hot fluid is varied in both types of heat exchangers. The proposed work is tested for two configurations of counter flow heat exchanger (conventional and helical finned surfaces) under different shell side inlet velocities of fluids. Helical finned tube heat exchanger with counter flow has a higher LMTD than a conventional counter flow heat exchanger. Variation in heat transfer rates and heat transfer coefficients were observed in heat exchanger influenced by shell side hot fluid velocity. The study shows that helical finned tube surfaces have improved heat transfer rates, LMTD, effectiveness (ε) and overall heat transfer coefficients compared to the conventional heat exchangers.
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Roy, Uttam, and Mrinmoy Majumder. "Productivity yielding in shell and tube heat exchanger by MCDM-NBO approach." Measurement and Control 52, no. 3-4 (2019): 262–75. http://dx.doi.org/10.1177/0020294019836109.

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The productivity of shell and tube heat exchangers are governed by various geometrical parameters like tube diameter, tube thickness, tube length, tube pitch, tube layout, installation area and baffle spacing of the heat exchanger. The operational efficiency of heat exchangers is highly influenced by the characteristics of heat exchanger parameters. The exchanger efficiency gets trapped due to many incongruities’ effects like over-pressure, bio-fouling, chemical fouling and corrosion. The selection of optimum design configuration is essential to achieve higher operational efficiency for a heat exchanger. But the performance and reliability of the optimization process play a key role in selecting and deselecting significant and insignificant parameters, respectively. So, cognitive selection of parameters and henceforth a reliable optimization process is required to identify optimal design for a heat exchanger. Moreover, economic factors also contribute to attain a consolidated yield result for a heat exchanger. This research proposes an optimal configuration with the help of ensemble output obtained by multi-criteria decision making and nature-based optimization algorithm. It has been found that exchange efficiency in optimal configuration is boosted by 22% from prototype heat exchanger.
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Ye, Wong. "HEAT EXCHANGER DESIGN OPTIMISATION." INTERNATIONAL RESEARCH JOURNAL OF ENGINEERING & APPLIED SCIENCES 9, no. 2 (2021): 19–28. http://dx.doi.org/10.55083/irjeas.2021.v09i02008.

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In this paper, an optimized model of Shell and Tube Parallel Flow Heat Exchanger of water and oil type is proposed using C++ programming language. Shell and tube heat exchangers are of special importance in boilers, oil coolers, condensers, pre-heaters etc. They are also used in high pressure operations, refrigeration and air conditioning industry and process applications. In this paper, a number of practical cases of shell and tube heat exchangers are taken and the analysis of thermal and constructional design of every case is done. The optimised design is obtained by minimising the pressure drop by maximising the heat exchanger area to reduce pumping and running cost. Also considering that large sizes lead to increased capital cost, heat exchanger area is also optimised to overcome this problem. Effect of design parameters on pressure drop and heat exchanger area is also explained.
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Wu, Jia, Jiansheng Hu, Bin Du, Ping Tang, and Jie Tang. "Cause analysis of vibration in shell-and-tube heat exchanger." MATEC Web of Conferences 353 (2021): 01002. http://dx.doi.org/10.1051/matecconf/202135301002.

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Heat exchanger is a universal process equipment, which is widely used in chemical industry, oil refining, thermal power and other industries. Shell-and-tube heat exchangers often fail prematurely due to flow-induced vibration. In this paper, aiming at the problem of severe vibration of shell-and-tube heat exchanger in an enterprise, the vibration acceleration sensors are used to measure the vibration of shell and tube side of heat exchanger. Through the analysis of the measurement results, it is found that when the flow rate on the shell side of the heat exchanger is greater than 50000 Nm3/h, the flow-induced vibration of the tube bundle occurs, and the vibration frequency is 57Hz, which is close to the natural frequency of the tube bundle. And the greater the flow rate on the shell side, the more intense the vibration. In order to reduce the vibration of heat exchanger, the damping measure of inserting baffles between tubes is adopted.
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Dissertations / Theses on the topic "Shell-and-tube heat exchanger"

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Ozden, Ender. "Detailed Design Of Shell-and-tube Heat Exchangers Using Cfd." Master's thesis, METU, 2007. http://etd.lib.metu.edu.tr/upload/3/12608752/index.pdf.

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Traditionally Shell-and-tube heat exchangers are designed using correlation based approaches like Kern method and Bell-Delaware method. With the advances in Computational Fluid Dynamics (CFD) software, it is now possible to design small heat exchangers using CFD. In this thesis, shell-and-tube heat exchangers are modeled and numerically analyzed using a commercial finite volume package. The modeled heat exchangers are relatively small, have single shell and tube passes. The leakage effects are not taken into account in the design process. Therefore, there is no leakage from baffle orifices and no gap between baffles and the shell. This study is focused on shell side flow phenomena. First, only shell side is modeled and shell side heat transfer and flow characteristics are analyzed with a series of CFD simulations. Various turbulence models are tried for the first and second order discretization schemes using different mesh densities. CFD predictions of the shell side pressure drop and the heat transfer coefficient are obtained and compared with correlation based method results. After selecting the best modeling approach, the sensitivity of the results to the flow rate, the baffle spacing and baffle cut height are investigated. Then, a simple double pipe heat exchanger is modeled. For the double pipe heat exchanger, both the shell (annulus) side and the tube side are modeled. Last, analyses are performed for a full shell-and-tube heat exchanger model. For that last model, a small laminar educational heat exchanger setup is used. The results are compared with the available experimental results obtained from the setup. Overall, it is observed that the flow and temperature fields obtained from CFD simulations can provide valuable information about the parts of the heat exchanger design that need improvement. The correlation based approaches may indicate the existence of a weakness in design, but CFD simulations can also pin point the source and the location of the weakness.
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Venkatesan, Yaamunan. "Effect of maldistribution and flow rotation on the shell side heat transfer in a shell and tube heat exchanger." Thesis, Wichita State University, 2011. http://hdl.handle.net/10057/3990.

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A numerical analysis of flow maldistribution and shell side flow on heat in a shell and tube heat exchanger is presented. The flow field at the inlet and in the headers was obtained by solving conservation equations of mass and momentum by employing k-ε turbulence model. As the flow maldistribution in the header affects the heat transfer performance of the STHE, pressure drop and velocity distribution of the fluid inside the header were analyzed. Two types of headers were considered with varying header length for a Reynolds number range of 1000 to 3000. As the header length was increased to 1500 mm the flow maldistribution decreased and the static pressure was almost equal for all the tubes in case of a conical header. Also, the numerical simulations show that the conical header with 1500 mm header length has less flow maldistribution when compared to other models. The Shell side flow was modeled as a flow along a twisted tube with a diameter D and a length 30D using Catia V519. Four different models of the twisted tube with pitch varying between 4D and 5.5D were studied for a range of Reynolds number Re = 75-750. The analysis was carried out for three different wall temperatures of the twisted tube such as 343 K, 363 K and 383 K. The pressure drop increased with increase in Reynolds number, while the pressure drop and outlet fluid temperature increased with decrease in the pitch of the tube. But the convective heat transfer decreased with reduction in pitch. With a decrease in pitch, the energy transfer between the fluid and the adjacent tubes increases resulting in increased outlet fluid temperature.<br>Thesis (M.S.)--Wichita State University, College of Engineering, Dept. of Mechanical Engineering.
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Finch, Anthony Terrell. "The electrohydrodynamic (EHD) enhancement of convection and boiling in a shell-and-tube heat exchanger." Thesis, Georgia Institute of Technology, 2001. http://hdl.handle.net/1853/16643.

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Betancourt, Arturo. "Computational study of the heat transfer and fluid structure of a shell and tube heat exchanger." Thesis, Florida Atlantic University, 2016. http://pqdtopen.proquest.com/#viewpdf?dispub=10172609.

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<p> A common technique to improve the performance of shell and tube heat exchangers (STHE) is by redirecting the flow in the shell side with a series of baffles. A key aspect in this technique is to understand the interaction of the fluid dynamics and heat transfer. Computational fluid dynamics simulations and experiments were performed to analysis the 3-dimensional flow and heat transfer on the shell side of an STHE with and without baffles. Although, it was found that there was a small difference in the average exit temperature between the two cases, the heat transfer coefficient was locally enhanced in the baffled case due to flow structures. The flow in the unbaffled case was highly streamed, while for the baffled case the flow was a highly complex flow with vortex structures formed by the tip of the baffles, the tubes, and the interaction of flow with the shell wall.</p>
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Bengtsson, Patrik, and Saikumar Dilip Kumar Vellore. "Experimental validation of a periodic heat transfer CFD model of a vertical shell and tube heat exchanger." Thesis, KTH, Skolan för industriell teknik och management (ITM), 2019. http://urn.kb.se/resolve?urn=urn:nbn:se:kth:diva-247914.

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Flow obstructions are used as a passive design element in heat exchangers to enhance heattransfer. Further, a change in flow structure can also have a positive effect on the heat transfer. Avertical shell and tube heat exchanger, used to recover heat in the greywater stream, isinvestigated in this study. The heat exchanger consists of flow obstructions such as annulargrooves and a helical string. The flow structure can be modified to a swirling film flow byadding a passive design element, called a Cyclone generator. This study aims to experimentallyvalidate a periodic heat transfer CFD model of a shell and tube heat exchanger, with uniformflow at steady-state laminar conditions. The study further analyses the heat transfercharacteristics of the annular grooves and the helical string, and the modified flow due to aswirling film. A calibrated test rig is constructed to consist of a heat source and a heat sink, as well as a meansfor measuring the flow and temperature of a vertical heat exchanger at elevated temperatures.The experimental results were evaluated using the Ɛ -NTU method and uncertainty analysis ofone standard deviation. The heat exchanger geometry had periodically repeating sectionsbetween the inlet and the outlet. Hence the large geometry was simplified to a smaller periodicmodule. The module was subjected to periodic boundary conditions and was simulated using apressure-based coupled algorithm on ANSYS Fluent. Further, the distribution of pressure andvelocity flow fields are examined for uniform flow in CFD. The experiment investigated the heattransfer of a swirling flow at a wide range of flow rates. The CFD model could not be validated by the experiment due to a difference between the overallheat transfer coefficients, calculated in the model and the experiment. The error in validationcould be pointed to an ambiguous energy result in one of the streams. However, the model couldsimulate real-life pressure drop conditions. It was found that the helical string contributed to asubstantial increase in the local turbulence, which translates to an increase in heat transfer. Theheat transfer was also increased in the presence of the annular grooves. From the experiment, a higher heat transfer is noticed at the entrance region of the heatexchanger compared to the middle section. The heat transfer characteristics of the swirling filmwere found to be significantly higher than that of the uniform flow. Finally, for uniform andswirling flows, the heat exchanger effectiveness, Ɛ, can be described as a single logarithmicfunction of the NTU.
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Yahaya, Emmanuel. "Optimal Process Design and Sensitivity Analysis of Shell and Tube Heat Exchanger Operated with Nanofluids." Thesis, Curtin University, 2017. http://hdl.handle.net/20.500.11937/68388.

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This research project aims to conduct an optimal design of shell and tube heat exchanger operated with nanofluids using automated Kern’s method. The main objective function of this work is to reduce the total annual cost (covering capital investment and annual operating cost). Results from two case studies indicate that the employment of Al2O3 based nanofluids as heat transfer fluids reduce cost by 40.97% and 55.77%, respectively, compared to the original design with conventional fluids.
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Dobai, Szabolcs. "Rekuperace tepla z odpadních plynů tavicí pece." Master's thesis, Vysoké učení technické v Brně. Fakulta strojního inženýrství, 2019. http://www.nusl.cz/ntk/nusl-400518.

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This master’s thesis deals with the design of heat recovery system from melting furnace waste gases. The first part is devoted to a brief description of heat exchangers, with the special importance being placed on the shell-and-tube heat exchanger. The second part contains a calculation of stoichiometric combustion, design of geometrical dimensions, calculation of pressure drops and power. At the end of the thesis there are various possibilities of utilization of the obtained waste heat and their basic economic assessment.
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Holčapek, Josef. "Návrh topného ohříváku." Master's thesis, Vysoké učení technické v Brně. Fakulta strojního inženýrství, 2021. http://www.nusl.cz/ntk/nusl-443176.

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This diploma thesis deals with the design of a feedwater heater. The aim of the work is to perform thermal, hydraulic and stress analysis. A preliminary technical documentation is also part of this work. The first part contains a summary of basic types of heat exchangers and processes of heat transfer. The main part is focused on thermal analysis to determine the main parameters of the heat exchanger. Next part is followed up by hydraulic analysis to determine the pressure drop of the heating water. After that is created design of heat exchanger with stress analysis of the proposed wall thicknesses of the shell, water chambers and tubesheet. Achieved results are summarized and evaluated at the end of the diploma thesis.
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Fettaka, Salim. "Application of Multiobjective Optimization in Chemical Engineering Design and Operation." Thèse, Université d'Ottawa / University of Ottawa, 2012. http://hdl.handle.net/10393/23209.

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The purpose of this research project is the design and optimization of complex chemical engineering problems, by employing evolutionary algorithms (EAs). EAs are optimization techniques which mimic the principles of genetics and natural selection. Given their population-based approach, EAs are well suited for solving multiobjective optimization problems (MOOPs) to determine Pareto-optimal solutions. The Pareto front refers to the set of non-dominated solutions which highlight trade-offs among the different objectives. A broad range of applications have been studied, all of which are drawn from the chemical engineering field. The design of an industrial packed bed styrene reactor is initially studied with the goal of maximizing the productivity, yield and selectivity of styrene. The dual population evolutionary algorithm (DPEA) was used to circumscribe the Pareto domain of two and three objective optimization case studies for three different configurations of the reactor: adiabatic, steam-injected and isothermal. The Pareto domains were then ranked using the net flow method (NFM), a ranking algorithm that incorporates the knowledge and preferences of an expert into the optimization routine. Next, a multiobjective optimization of the heat transfer area and pumping power of a shell-and-tube heat exchanger is considered to provide the designer with multiple Pareto-optimal solutions which capture the trade-off between the two objectives. The optimization was performed using the fast and elitist non-dominated sorting genetic algorithm (NSGA-II) on two case studies from the open literature. The algorithm was also used to determine the impact of using discrete standard values of the tube length, diameter and thickness rather than using continuous values to obtain the optimal heat transfer area and pumping power. In addition, a new hybrid algorithm called the FP-NSGA-II, is developed in this thesis by combining a front prediction algorithm with the fast and elitist non-dominated sorting genetic algorithm-II (NSGA-II). Due to the significant computational time of evaluating objective functions in real life engineering problems, the aim of this hybrid approach is to better approximate the Pareto front of difficult constrained and unconstrained problems while keeping the computational cost similar to NSGA-II. The new algorithm is tested on benchmark problems from the literature and on a heat exchanger network problem.
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Ghyoot, Christiaan Jacob. "The modelling of particle build up in shell-and-tube heat exchangers due to process cooling water / Christiaan Jacob Ghyoot." Thesis, North-West University, 2013. http://hdl.handle.net/10394/9511.

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Sasol Limited experiences extremely high particulate fouling rates inside shell-and-tube heat exchangers that utilize process cooling water. The water and foulants are obtained from various natural and process sources and have irregular fluid properties. The fouling eventually obstructs flow on the shell side of the heat exchanger to such an extent that the tube bundles have to be replaced every nine months. Sasol requested that certain aspects of this issue be addressed. To better understand the problem, the effects of various tube and baffle configurations on the sedimentation rate in a shell-and-tube heat exchanger were numerically investigated. Single-segmental, double-segmental and disc-and-doughnut baffle configurations, in combination with square and rotated triangular tube configurations, were simulated by using the CFD software package, STAR-CCM+. In total, six configurations were investigated. The solution methodology was divided into two parts. Firstly, steady-state solutions of the six configurations were used to identify the best performing model in terms of large areas with high velocity flow. The results identified both single-segmental baffle configurations to have the best performance. Secondly, transient multiphase simulations were conducted to investigate the sedimentation characteristics of the two single-segmental baffle configurations. It was established that the current state of available technology cannot adequately solve the detailed simulations in a reasonable amount of time and results could only be obtained for a time period of a few seconds. By simulating the flow fields for various geometries in steady-state conditions, many of the observations and findings of literature were verified. The single-segmental baffle configurations have higher pressure drops than double-segmental and disc-and-doughnut configurations. In similar fashion, the rotated triangular tube configuration has a higher pressure drop than the square arrangement. The single-segmental configurations have on average higher flow velocities and reduced cross-flow mass flow fractions. It was concluded from this study that the single-segmental baffle with rotated triangular tube configuration had the best steady-state performance. Some results were extracted from the transient multiphase simulations. The transient multiphase flow simulation of the single-segmental baffle configurations showed larger concentrations of stagnant sediment for the rotated triangular tube configuration versus larger concentrations of suspended/flowing sediment in the square tube configuration. This result was offset by the observation that the downstream movement of sediment was quicker for the rotated triangular tube configuration. No definitive results could be obtained, but from the available results, it can be concluded that the configuration currently implemented at Sasol is best suited to handle sedimentation. This needs to be verified in future studies by using advanced computational resources and experimental results.<br>Thesis (MIng (Mechanical Engineering))--North-West University, Potchefstroom Campus, 2013
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Books on the topic "Shell-and-tube heat exchanger"

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Johnson, Antony. Flow, heat transfer and pressure drop on the shell side of a shell and tube heat exchanger. Manchester Polytechnic, 1985.

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Yokell, Stanley. A working guide to shell-and-tube heat exchangers. McGraw-Hill, 1990.

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university, Open. Heat transfer principles and applications. Block 8. Heat exchangers part 2. Shell and tube heat exchangers. OU, 1992.

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Heat Exchanger Design Guide: A Practical Guide for Planning, Selecting and Designing of Shell and Tube Exchangers. Elsevier Science & Technology Books, 2015.

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Gbadamosi, Raji Olayiwola, and Manfred Nitsche. Heat Exchanger Design Guide: A Practical Guide for Planning, Selecting and Designing of Shell and Tube Exchangers. Elsevier Science & Technology Books, 2015.

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Mauro A. S. S. Ravagnani. Optimal Shell and Tube Heat Exchangers Design. INTECH Open Access Publisher, 2011.

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Code), Std 660 (Service. Shell and Tube Heat Exchangers Refinery Services/Std 660. 5th ed. Amer Petroleum Inst, 1993.

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Tomski, Thomas. The design of shell-and-tube heat exchangers using expert systems. 1992.

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Cooke, Sandra E. *. The effect of bypass lanes in shell-and-tube heat exchangers. 1989.

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Mukherjee, Rajiv. Practical Thermal Design Of Shell-and-tube Heat Exchangers (Series in Thermal & Fluid Physics & Engineering). Begell House Publishers, 2004.

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Book chapters on the topic "Shell-and-tube heat exchanger"

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Ali, Hafiz Muhammad, Ali Hassan, and Abdul Wahab. "Shell and Tube Heat Exchanger." In Nanofluids for Heat Exchangers. Springer Nature Singapore, 2022. http://dx.doi.org/10.1007/978-981-19-3227-4_1.

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Krishnan, S., and G. K. Sadekar. "Variable Pitch Tube Layout Concept for Shell and Tube Heat Exchanger." In Design and Operation of Heat Exchangers. Springer Berlin Heidelberg, 1992. http://dx.doi.org/10.1007/978-3-642-84450-8_6.

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Wagh, S. M., D. P. Barai, and M. H. Talwekar. "Sensitivity Analysis of Shell and Tube Heat Exchanger Using Chemcad." In Novel Water Treatment and Separation Methods. Apple Academic Press, 2017. http://dx.doi.org/10.1201/9781315225395-20.

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Gugulothu, Ravi, Narsimhulu Sanke, and A. V. S. S. K. S. Gupta. "Numerical Study of Heat Transfer Characteristics in Shell-and-Tube Heat Exchanger." In Numerical Heat Transfer and Fluid Flow. Springer Singapore, 2018. http://dx.doi.org/10.1007/978-981-13-1903-7_43.

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Jayachandraiah, B., and C. Dinesh Kumar Patel. "Design of Shell-and-Tube Heat Exchanger with CFD Analysis." In Lecture Notes in Mechanical Engineering. Springer Singapore, 2020. http://dx.doi.org/10.1007/978-981-15-4488-0_34.

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Olana, Firew Dereje, Beza Nekatibeb Retta, Tadele Abera Abose, and Samson Mekibib Atnaw. "Shell and Tube Heat Exchanger, Empirical Modeling Using System Identification." In Lecture Notes of the Institute for Computer Sciences, Social Informatics and Telecommunications Engineering. Springer International Publishing, 2020. http://dx.doi.org/10.1007/978-3-030-43690-2_40.

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Seralathan, S., R. Vijay, S. Aravind, et al. "Nanofluids in Improving Heat Transfer Characteristics of Shell and Tube Heat Exchanger." In Lecture Notes in Mechanical Engineering. Springer Singapore, 2020. http://dx.doi.org/10.1007/978-981-15-4488-0_43.

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Singh, Himanshu, Utkarsh Mishra, Prateek Saxena, Ganesh Shetiya, and Y. M. Puri. "Digital Twin for Shell and Tube Heat Exchanger in Industry 4.0." In Advances in Mechanical Engineering. Springer Singapore, 2020. http://dx.doi.org/10.1007/978-981-15-3639-7_76.

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Gugulothu, Ravi, Narsimhulu Sanke, Farid Ahmed, and Ratna Kumari Jilugu. "Numerical Study on Shell and Tube Heat Exchanger with Segmental Baffle." In Algorithms for Intelligent Systems. Springer Singapore, 2021. http://dx.doi.org/10.1007/978-981-16-0586-4_25.

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Cumo, M. "Numerical Methods for the Analysis of Flow and Heat Transfer in a Shell-and-Tube Heat Exchanger with Shell-Side Condensation." In Two-Phase Flow Heat Exchangers. Springer Netherlands, 1988. http://dx.doi.org/10.1007/978-94-009-2790-2_27.

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Conference papers on the topic "Shell-and-tube heat exchanger"

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Gamio, Carlos, and F. Walter Pinto. "Shell and Tube Heat Exchanger Reliability Study." In ASME 2002 Engineering Technology Conference on Energy. ASMEDC, 2002. http://dx.doi.org/10.1115/etce2002/per-29126.

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In 1997, heat exchanger tube failures accounted for 31% of the unplanned downtime in the Lyondell’s Gulf Coast plants. This resulted in over $12MM of unplanned production interruptions. A multi-disciplinary team studied the tube failure modes and developed a systematic program to improve the heat exchanger reliability. The team issued recommendations in the areas of heat exchanger design, construction, operation, maintenance and inspection. This paper mainly discusses the three critical areas surrounding the reliability of heat exchanger tubes. They are tube testing, strategy on retubing exchangers during turnarounds and design improvements.
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Khalil, Essam E., Ahmed Adel, Waleed A. AbdelMaksoud, Gamal A. ElHarriri, and Emad Saad. "Shell and Tube Heat Exchanger Performance." In 15th International Energy Conversion Engineering Conference. American Institute of Aeronautics and Astronautics, 2017. http://dx.doi.org/10.2514/6.2017-5026.

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Fakheri, Ahmad, and Maryam Fazel. "Optimization of Shell and Tube Heat Exchanger Networks." In ASME 2004 International Mechanical Engineering Congress and Exposition. ASMEDC, 2004. http://dx.doi.org/10.1115/imece2004-59513.

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A methodology is presented for the optimization of a network of shell and tube heat exchangers connected in series. For a given total rate of heat transfer and the known inlet and exit temperatures of the hot and cold fluids, the total area of the heat exchanger network is minimized. In the proposed methodology, the heat exchangers are assumed to be different. This is a generalization compared to the traditional approach where all the heat exchangers are taken to have the same area and the same LMTD (Log Mean Temperature Difference) correction factor. In the traditional approach the minimum number of identical shells, for which a feasible solution exists and meets the design criteria, is used as the optimum solution. The proposed optimization approach shows that using larger number of smaller heat exchangers results in less overall heat exchanger area due to the more efficient operation of the individual heat exchangers.
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Nascimento, Carlos, Viviana Mariani, and Henrique da Silva Coelho Goetten. "SHELL AND TUBE HEAT EXCHANGER OPTIMIZATION USING METAHEURISTICS." In 24th ABCM International Congress of Mechanical Engineering. ABCM, 2017. http://dx.doi.org/10.26678/abcm.cobem2017.cob17-1177.

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THIRUNAVUKKARASU, I., MITHUN P, SHREESHA C, and V. I. GEORGE. "Adaptive Control of Shell and Tube Heat Exchanger." In Second International Conference on Advances In Computing, Control And Networking - ACCN 2015. Institute of Research Engineers and Doctors, 2015. http://dx.doi.org/10.15224/978-1-63248-073-6-15.

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SivaChandran, S., R. Venkatesh, S. Baskar, R. Arivazhagan, and T. Maridurai. "Experimental study of shell and tube heat exchanger." In THIRD VIRTUAL INTERNATIONAL CONFERENCE ON MATERIALS, MANUFACTURING AND NANOTECHNOLOGY. AIP Publishing, 2022. http://dx.doi.org/10.1063/5.0096706.

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Cevrim, Berk, Murat K. Aktas, and Sadik Kakac. "EXPERIMENTAL ANALYSIS OF SHELL AND TUBE HEAT EXCHANGER." In Proceedings of CONV-22: Int. Symp. on Convective Heat and Mass Transfer June 5 – 10, 2022, Turkey. Begellhouse, 2022. http://dx.doi.org/10.1615/ichmt.2022.conv22.530.

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Subramaniana, R. Siva, G. Kumaresan, A. Santosh Karthik, K. C. Sivaganes, V. Suryabalan, and A. R. Venkat Guhan. "Analysis of modified shell and tube heat exchanger." In Proceeding of 2nd International Colloquium on Computational & Experimental Mechanics (ICCEM 2021). AIP Publishing, 2022. http://dx.doi.org/10.1063/5.0108203.

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Cox, Jonathan, Anoop Kanjirakat, and Reza Sadr. "Application of Nanofluids in a Shell-and-Tube Heat Exchanger." In ASME 2013 11th International Conference on Nanochannels, Microchannels, and Minichannels. American Society of Mechanical Engineers, 2013. http://dx.doi.org/10.1115/icnmm2013-73104.

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Innovations in the field of nanotechnology have potential to improve industrial productivity and performance. One promising applications of this emerging technology is using nanofluids with enhanced thermal properties. Nanofluids, engineered colloidal suspensions consisting of nano-sized particles (less than 100nm) dispersed in a basefluid, have shown potential as industrial cooling fluids due to the enhanced heat transfer characteristics. Experiments are conducted to compare the overall heat transfer coefficient and pressure drop of water vs. nanofluids in a laboratory scale industrial type shell and tube heat exchanger. Three mass particle concentrations, 2%, 4% and 6%, of SiO2-water nanofluids are formulated by dispersing 20 nm diameter nano particles in desalinated water. Nanofluid and tap water are then circulated in the cold and hot loops, respectively, of the heat exchanger to avoid direct particle deposition on heater surfaces. Interestingly, experimental result show both augmentation and deterioration of heat transfer coefficient for nanofluids depending on the flow rate through the heat exchangers. This trend is consistent with an earlier reported observation for heat transfer in micro channels. This trend may be explained by the counter effect of the changes in thermo-physical properties of fluids together with the fouling on the heat exchanger surfaces. The measured pressure drop in the nanofluids flow shows an increase when compared to that of basefluid that could limit the use of nanofluids in heat exchangers for industrial application.
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Patel, Vipul, Rajesh Patel, and Vimal Savsani. "Novel Heat Exchanger Design With Rectangular Shell Geometry." In ASME 2014 International Mechanical Engineering Congress and Exposition. American Society of Mechanical Engineers, 2014. http://dx.doi.org/10.1115/imece2014-36834.

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Shell and Tube Heat Exchangers (STHE) are the most versatile type of heat exchangers used in industrial applications. The shape of Shell side of the traditional STHE’s is cylindrical for industrial applications. On one hand, STHE have some good features but on the other hand, it has some limitations due to the cylindrical geometry of the shell side. Some of these limitations are maximum two shell pass is possible as per TEMA layout, complete counter flow cannot be achieved, possibility of reverse heat transfer when number of tube passes are more, tubes are always laid parallel to shell and mounting over the entire length of shell is not possible when impingement plate provided etc. The objective of this study is to design a novel heat exchanger to overcome the limitations of traditional STHE. An experimental setup has been designed with rectangular shell side for STHE. The novel heat exchanger provides the flexibility to increase the number of shell pass and complete counter flow can be achieved due to rectangular geometry of shell side. For the same heat transfer rates, the proposed novel heat exchanger design provides better Effective Mean Temperature Difference (EMTD) and hence less surface area for heat transfer in comparison with traditional STHE. The experiments have been conducted on novel heat exchangers under different operation conditions of hot and cold fluids. The experiment results are compared with theoretical estimations of overall heat transfer coefficient and Log Mean Temperature Difference (LMTD) for traditional shell and tube heat exchangers for the same operation conditions. The results show that under the same operation conditions, the performance of novel heat exchanger is much better than traditional STHE.
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