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IRJET- A Review : Design, Analysis & Optimization of Pipe Stack Heat Exchanger (22 M)
1.
International Research Journal
of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 10 | Oct 2019 www.irjet.net p-ISSN: 2395-0072 © 2019, IRJET | Impact Factor value: 7.34 | ISO 9001:2008 Certified Journal | Page 660 A Review: Design, Analysis & Optimization of Pipe Stack Heat Exchanger (22 m) Ghogare Akash1, Jadhav Vaibhav2, Mali Rutik3, Nevase Sagar4, Kamble S.P* 1,2,3,4Student of Mechanical Engineering, S.B.P.C.O.E. Indapur, Maharashtra, India. *Asst Professor of Mechanical Engineering, S.B.P.C.O.E. Indapur, Maharashtra, India. ------------------------------------------------------------------------***----------------------------------------------------------------------- Abstract - In present day the Shell and Tube Heat Exchanger is the most common type heat exchanger used in industries. The shell-and-tube heat exchanger which is the majority type of liquid-to-liquid heat exchanger. Which is used as feed water cooler in process industries, oil refineries, chemical plants and power plants because it suits high pressure application. Solid works software is used for modeling the shell and tube type heat exchanger which will be used for water chilling application in industry. In this we are going to do modeling of the heat exchanger according to the given working parameters and specifications given by the industry. After modeling of the heat exchanger analysis is done in solid works to determine the strength according to the working conditions. And if failed in the analysis then remodeling is done by changing the parameters to save the heat exchanger. After the model is safe the fabrication drawing is send to the floor shop. Keywords: - pipe stack heat exchanger, performance analysis, Solidwork, CFD analysis. 1. INTRODUCATION 1.1 Heat Exchanger Heat transfer equipment is defined by the function it performs in a process. The purpose of any such device is to maximize the heat transferred between the two fluids. However, the problem that occurs is the parameters that increase the heat transfer also increase the pressure of the fluid flowing in a pipe which increases the cost of pumping the fluid. S.P.Kamble [19]. Therefore, a design that increases the heat transferred, but at the same time can keep the pressure drop of the fluid flowing in the pipe to the permitted limit, is very necessary. A common problem in industries is to extract the maximum heat from the utility stream emanating from a particular process and to heat a process flow. Fig.1: Stack Pipe Heat Exchanger [2] A solution to extract the maximum heat may be to increase the heat transfer area or to increase the coolant flow rate, but both solutions increase the cost of pumping so it is not advisable to increase these parameters without pressure drop considerations. Prabhat k. [1] 2. REVIEW OF LITERATURE According to our previous work, there are three types of flow distributions in a central type of flow parallel heat exchanger. And for each different flow distribution type, the effect of variation of geometry parameters is different. Therefore, it is necessary to examine separately the effect of header match on the flow distribution for each type of flow distribution. Fig.2: Basic Diagram of Heat Exchanger [8]
2.
International Research Journal
of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 10 | Oct 2019 www.irjet.net p-ISSN: 2395-0072 © 2019, IRJET | Impact Factor value: 7.34 | ISO 9001:2008 Certified Journal | Page 661 The detailed procedure of the solution is to select different values of AR from different types of flow distributions. Then, for the current AR, choose the header diameter as a combination of the header diameter and change the DCR (the ratio of the cross section of the division of the combination header) by separating the divider header. Jian Zhou. [4]. Ebio, c. E. [5] In his experimental paper, performance analysis and analytical method excluded from shell and tube heat exchanger were used to develop correlation for performance analysis. Thermal analysis of the shell and tube heat exchanger involves the determination of the overall heat-transfer coefficient from the individual film coefficients. Mohammed Rabih V [६] Design of Shell and Tube Heat Exchanger: The process of design starts with providing standard dimensions of tube length and diameter which form the Association (TEMA) in MATLAB code proposed by Synergy Exchange. The program is run by iterating with a possible combination of standard dimensions and the overall heat transfer coefficient (U) is obtained in each case. The obtained values of U are compared and the corresponding dimensions for the maximum value are obtained as output. 3. DISCUSSION In this project we have to process a modification in a heat exchanger design for increasing the current efficiency to better step. Also it optimizes the cost of better heat exchanger. Almost four type of modification are to be done as follows 1. Baffle position 2. Baffle cut percentage 3. Tube sheet pattern 4. Selection of tube material As this above four parameter consideration we optimize the heat transfer rate and pressure drop of heat exchanger. We use a standard for calculation as below 1. Kenn’s 2. TEMA 3. Belldelware Then we have to done analysis of project aspects. Briefing of project from starting is first we design all part in catia software then we have to assemble all assembly. As this our model will be produced after assembly. After that we have to done an analysis on this model. Analysis contains some calculation, result and conclusion. We have done a material selection, costing, BOM Analysis. Finally we have to done CFD to analyze proper functioning of working fluid. All process we have done under observation. Total duration of project almost 7 to 8 month as this is our final year project. Also we have to study about cold flow and hot flow as well as parallel and counter flow. 4. CONCLUSIONS Special types of heat exchanger are chosen because it favors the avoidance of internal pressure loss, as a result, increases the surface of the heat exchange, due to the fact that external irreversibilities in water lessen the thermodynamic value of the revival cycle. Anyway, the cold section is given greater amplitude than the hot section, because entropy variation occurs when the temperature is minimum due to thermal irreversibilities. • The rate of heat transfer can be increased by varying the tube diameter, length, and tubes. • Can be improved by changing the pitch take-out rate of heat transfer. Changing the temperature of the tubes and the medium rate of heat transfer can be increased. • The heat transfer rate can be improved by changing the material of the tubes. REFERENCES [1] Prabhata K. Swamee, Nitin Aggarwal, Vijay Aggarwal, “Optimum design of double pipe heat exchanger”, Elsevier, International Journal of Heat and Mass Transfer 51 (2008) 2260–2266. [2] https://www.sant-ambrogio.it/en/portfolio/design- courses-eng/ [3] Durgesh J Bhattand Priyanka M Jhavar, “Analysis of Heat Transfer in Shell and Tube Type Heat Exchangers”, Shree SatyaSaya Institute of Science and Technology, Vol. 2, Issue 06, 2014. [4] Jian Zhou, Ming Ding, Haozhi Bian, Yinxing Zhang, Zhongning Sun, “CFD simulation for the effect of the header match on the flow distribution in a central-type parallel heat exchanger”, Elsevier S0263- 8762(18)30235-1.
3.
International Research Journal
of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 10 | Oct 2019 www.irjet.net p-ISSN: 2395-0072 © 2019, IRJET | Impact Factor value: 7.34 | ISO 9001:2008 Certified Journal | Page 662 [5] Ebieto, C.E. and Eke G.B., “Performance Analysis of Shell and Tube Heat Exchangers using Miscible System: A case study”, Journal of Emerging Trends in Engineering and Applied Sciences,2012 3 (5), pp. 899- 903. [6] Mohammed Rabeeh V., “Design of shell and tube heat exchanger Study on the heat transfer and flow sing MATLAB and finding the steady state time using energy balance equation”, International Journal of advance Mechanical Engineering Volume 4, Number 1 (2014), pp. 95–100. [7] B Jayachandriah1, K. Rajsekhar, “Thermal Computer Aided Analysis of Thermal and Mechanical design of shell and tube exchangers”,Advanced materials vol. 367(2012) pp 731-73, Trans Tech publications, switzerland. [8] Shuiping Yan, Qiufang Cui, Te Tu, Liqiang Xu, Qingyao He, Paul H.M. Feron, Shuaifei Zhao” Membrane heat exchanger for novel heat recovery in carbon capture”, Elsevier Journal of Membrane Science 577 (2019) 60– 68 [9] Ya-Nan Wang, Jong-Pyo Lee, Min-Ho Park, Byeong-Ju Jin, Tae-Jong Yun, Young-Ho Song, Ill-Soo Kim1” A Study on 3D Numerical Model for Plate Heat Exchanger”, Elsevier Procedia Engineering 174 (2017) 188 – 194 [10] Jorge L. García-Castillo, Martín Pic_on-Nú~nez “Design of plate-fin surfaces for multi-fluid heat exchanger applications”, Elsevier Energy 181 (2019) 294-306 [11] Channarong Wantha “Analysis of heat transfer characteristics of tube-in-tube internal heat exchangers for HFO-1234yf and HFC-134a refrigeration systems”, Elsevier Applied Thermal Engineering 157 (2019) 113747 [12] M. Piper, A. Zibart, E. Djakow, R. Springer, W. Homberg, E.Y. Kenig “Heat transfer enhancement in pillow-plate heat exchangers with dimpled surfaces:a numerical study”, Elsevier S1359-4311(18)34636-2 [13] Guo-Dong Zhu, Cai-Fu Qian, Zhou Fang “An analytical theory for the strength solution of tubesheets in floating-head heat exchangers with back devices”, Elsevier S0308-0161(19)30194-2 [14] Chen Lin, Xiaohui Yan, Guanghua Wei, Changchun Ke, Shuiyun Shen, Junliang Zhang, “Optimization of configurations and cathode operating parameters on liquidcooled proton exchange membrane fuel cell stacks by orthogonal method”, Elsevier Applied Energy 253 (2019) 113496 [15] M.V.V. Mortean, L.H.R. Cisterna, K.V. Paiva, M.B.H. Mantelli” Thermal and hydrodynamic analysis of a cross-flow compact heat exchanger”, Elsevier Applied Thermal Engineering 150 (2019) 750–761 [16] W. Srimuang, P. Amatachaya” A review of the applications of heat pipe heat exchangers for heat recovery”, Elsevier Renewable and Sustainable Energy Reviews 16 (2012) 4303– 4315 [17] Tomasz Muszynski, Rafal Andrzejczyk “Experimental study on single phase operation of microjet augmented heat”, Elsevier Applied Thermal Engineering 155 (2019) 289–296 [18] Alhassan Salami Tijani, Danial Barr, A.H. Abdol Rahim “Computational Modelling of the Flow Field of An Electrolyzer System using CFD”, Elsevier Energy Procedia 79 ( 2015 ) 195 – 203 [19] S.P.Kamble “Performance and analysis of Al2O3 and water in radiator” International Journal of Control and Automation Vol. 10(No. 11 (2017)):11-28 [20] M. Thirumarimuegan, “Performance analysis of shell and tube type heat exchanger using Miscible system”, American journal of applied science, 2008, 5(5): 548- 552.al, V [21] A.O. Adelaja, S.J. Ojolo and M.G. Sobamowo, “Computer Aided Analysis of Thermal and Mechanical Design of Shell and Tube Heat Exchangers”, Advanced Materials Vol. 367 (2012), pp731-737, Trans Tech Publications Switzerland [22] Yusuf Ali Kara, OzbilenGuraras, “A computer program for designing of shell and tube heat exchanger”, Applied Thermal Engineering 24(2004) 1797-1805. [23] Rajagapal Thundil Karuppa Raj, and Srikanth Ganne, “Shell side numerical analysis of a shell and tube heat exchanger considering the effect of baffle inclination angle on a fluid flow”, Thundil Karuppa Raj, R., et al: Shell side numerical analysis of shell and tube heat exchangers, Thermal science: Year 2012, Vol.16, No.4, pp 1165-1174. [24] S. NoieBaghban, M. Moghiman and E. Salehi, “Thermal Analysis of shell side flow of shell and tube type heat exchanger using experimental and theoretical methods”, Institute for Scientific Research, University of Guanajuato Lascurain de Retana No. 5, 36000 Guanajuato, Gto, México.
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