Huy Minh Khoi Hoang, Hai-Lam Cao, Phuoc Minh Quang Pham, Ahmad Hajjar, Vu Linh Nguyen
{"title":"新型管壳式热交换器设计,采用可供选择的倾斜挡板","authors":"Huy Minh Khoi Hoang, Hai-Lam Cao, Phuoc Minh Quang Pham, Ahmad Hajjar, Vu Linh Nguyen","doi":"10.1016/j.csite.2024.105542","DOIUrl":null,"url":null,"abstract":"This paper proposes a novel single-shell-pass shell-and-tube heat exchanger design with alternative inclined baffles. The design includes paired semi-ellipse shapes with baffle cut along the vertical axis such that the segments are interlocked in a crossed pattern. The new exchanger is structured to overcome the weakness of single segmental baffles (SG-STHX) by achieving lower pressure drop and higher thermal efficiency. This advantage is achieved using spiral flow to reduce dead zones and make the flow distribution within the heat exchanger's shell more uniform. The relatively simple arrangement and design of baffles in the proposed exchanger offer a significant advantage compared to continuous helical baffles (CH-STHX) in terms of the complexity of manufacturing and consequent high cost. In this paper, the equations governing the flow and thermal transfer in the exchanger are presented, and the parameters used to evaluate the exchanger's performance are also developed. The finite-volume method is used in numerical simulations to verify the equations and compare the performance of the novel design to SG-STHX and CH-STHX under similar geometrical and thermo-hydraulic conditions. Different mass flow rates are considered to cover a wide range of Reynolds numbers and ensure the accuracy of the comparison. Flow velocity and temperature distributions across the shell side are plotted to address the impact of geometry on the fluid behavior during the flow. The results show that the proposed heat exchanger significantly improves comprehensive performance, especially energy efficiency, compared to conventional SG-STHX or CH-STHX. The proposed heat exchanger also has a lower pressure drop than traditional ones. With the same mass flow rate, the XX-STHX demonstrates an average pressure drop approximately 44 % lower than the CH-STHX and 49 % lower than the SG-STHX. Moreover, with the same pump power, the performance evaluation factor of the XX-STHX, on average, surpasses that of the CH-STHX by roughly 1.48 times and the SG-STHX by about 1.70 times.","PeriodicalId":9658,"journal":{"name":"Case Studies in Thermal Engineering","volume":"21 1","pages":""},"PeriodicalIF":6.4000,"publicationDate":"2024-11-29","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"A novel shell-and-tube heat exchanger design with alternative inclined baffles\",\"authors\":\"Huy Minh Khoi Hoang, Hai-Lam Cao, Phuoc Minh Quang Pham, Ahmad Hajjar, Vu Linh Nguyen\",\"doi\":\"10.1016/j.csite.2024.105542\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"This paper proposes a novel single-shell-pass shell-and-tube heat exchanger design with alternative inclined baffles. The design includes paired semi-ellipse shapes with baffle cut along the vertical axis such that the segments are interlocked in a crossed pattern. The new exchanger is structured to overcome the weakness of single segmental baffles (SG-STHX) by achieving lower pressure drop and higher thermal efficiency. This advantage is achieved using spiral flow to reduce dead zones and make the flow distribution within the heat exchanger's shell more uniform. The relatively simple arrangement and design of baffles in the proposed exchanger offer a significant advantage compared to continuous helical baffles (CH-STHX) in terms of the complexity of manufacturing and consequent high cost. In this paper, the equations governing the flow and thermal transfer in the exchanger are presented, and the parameters used to evaluate the exchanger's performance are also developed. The finite-volume method is used in numerical simulations to verify the equations and compare the performance of the novel design to SG-STHX and CH-STHX under similar geometrical and thermo-hydraulic conditions. Different mass flow rates are considered to cover a wide range of Reynolds numbers and ensure the accuracy of the comparison. Flow velocity and temperature distributions across the shell side are plotted to address the impact of geometry on the fluid behavior during the flow. The results show that the proposed heat exchanger significantly improves comprehensive performance, especially energy efficiency, compared to conventional SG-STHX or CH-STHX. The proposed heat exchanger also has a lower pressure drop than traditional ones. With the same mass flow rate, the XX-STHX demonstrates an average pressure drop approximately 44 % lower than the CH-STHX and 49 % lower than the SG-STHX. Moreover, with the same pump power, the performance evaluation factor of the XX-STHX, on average, surpasses that of the CH-STHX by roughly 1.48 times and the SG-STHX by about 1.70 times.\",\"PeriodicalId\":9658,\"journal\":{\"name\":\"Case Studies in Thermal Engineering\",\"volume\":\"21 1\",\"pages\":\"\"},\"PeriodicalIF\":6.4000,\"publicationDate\":\"2024-11-29\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Case Studies in Thermal Engineering\",\"FirstCategoryId\":\"5\",\"ListUrlMain\":\"https://doi.org/10.1016/j.csite.2024.105542\",\"RegionNum\":2,\"RegionCategory\":\"工程技术\",\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"Q1\",\"JCRName\":\"THERMODYNAMICS\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"Case Studies in Thermal Engineering","FirstCategoryId":"5","ListUrlMain":"https://doi.org/10.1016/j.csite.2024.105542","RegionNum":2,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q1","JCRName":"THERMODYNAMICS","Score":null,"Total":0}
A novel shell-and-tube heat exchanger design with alternative inclined baffles
This paper proposes a novel single-shell-pass shell-and-tube heat exchanger design with alternative inclined baffles. The design includes paired semi-ellipse shapes with baffle cut along the vertical axis such that the segments are interlocked in a crossed pattern. The new exchanger is structured to overcome the weakness of single segmental baffles (SG-STHX) by achieving lower pressure drop and higher thermal efficiency. This advantage is achieved using spiral flow to reduce dead zones and make the flow distribution within the heat exchanger's shell more uniform. The relatively simple arrangement and design of baffles in the proposed exchanger offer a significant advantage compared to continuous helical baffles (CH-STHX) in terms of the complexity of manufacturing and consequent high cost. In this paper, the equations governing the flow and thermal transfer in the exchanger are presented, and the parameters used to evaluate the exchanger's performance are also developed. The finite-volume method is used in numerical simulations to verify the equations and compare the performance of the novel design to SG-STHX and CH-STHX under similar geometrical and thermo-hydraulic conditions. Different mass flow rates are considered to cover a wide range of Reynolds numbers and ensure the accuracy of the comparison. Flow velocity and temperature distributions across the shell side are plotted to address the impact of geometry on the fluid behavior during the flow. The results show that the proposed heat exchanger significantly improves comprehensive performance, especially energy efficiency, compared to conventional SG-STHX or CH-STHX. The proposed heat exchanger also has a lower pressure drop than traditional ones. With the same mass flow rate, the XX-STHX demonstrates an average pressure drop approximately 44 % lower than the CH-STHX and 49 % lower than the SG-STHX. Moreover, with the same pump power, the performance evaluation factor of the XX-STHX, on average, surpasses that of the CH-STHX by roughly 1.48 times and the SG-STHX by about 1.70 times.
期刊介绍:
Case Studies in Thermal Engineering provides a forum for the rapid publication of short, structured Case Studies in Thermal Engineering and related Short Communications. It provides an essential compendium of case studies for researchers and practitioners in the field of thermal engineering and others who are interested in aspects of thermal engineering cases that could affect other engineering processes. The journal not only publishes new and novel case studies, but also provides a forum for the publication of high quality descriptions of classic thermal engineering problems. The scope of the journal includes case studies of thermal engineering problems in components, devices and systems using existing experimental and numerical techniques in the areas of mechanical, aerospace, chemical, medical, thermal management for electronics, heat exchangers, regeneration, solar thermal energy, thermal storage, building energy conservation, and power generation. Case studies of thermal problems in other areas will also be considered.