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CFD ANALYSIS OF CROSS FLOW AIR TO AIR TUBE TYPE HEAT EXCHANGER Vikas Kumar 1* , D. Gangacharyulu 2* , Parlapalli MS Ra

CFD ANALYSIS OF CROSS FLOW AIR TO AIR TUBE TYPE HEAT EXCHANGER Vikas Kumar 1* , D. Gangacharyulu 2* , Parlapalli MS Rao 3 and R. S. Barve 4 1 Centre for Development of Advanced Computing, Pune University Campus, Pune, India

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CFD ANALYSIS OF CROSS FLOW AIR TO AIR TUBE TYPE HEAT EXCHANGER Vikas Kumar 1* , D. Gangacharyulu 2* , Parlapalli MS Ra

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  1. CFD ANALYSIS OF CROSS FLOW AIR TO AIR TUBE TYPE HEAT EXCHANGER Vikas Kumar1*, D. Gangacharyulu2*, Parlapalli MS Rao3 and R. S. Barve4 1 Centre for Development of Advanced Computing, Pune University Campus, Pune, India 2 Thapar Institute of Engineering & Technology, Patiala, India 3 Nanyang Technological University, Singapore 4 Crompton Greaves Ltd, Kanjur Marg, Mumbai, India

  2. Closed Air Circuit Air Cooled (CACA) electrical motors are used in various industries for higher rating (500 kW and above) applications Heat generation due to the energy losses in the windings of motors at various electrical loads under operating condition Cold air is circulated in the motor to remove the heat generated The hot air generated in the motor is cooled by using an air to air tube type cross flow heat exchangers The motor designers are interested to know the temperature distribution of air in the heat exchanger and pressure drop across the tube bundle at various operating parameters, e.g., different hot & cold air temperatures and fluid (hot & cold) flow rates Introduction

  3. Large Electrical Motor Heat exchanger Source: M/S Crompton Greaves Ltd. Mumbai, India

  4. Heat Exchanger Geometry External hot air cooled air Internal hot air External cold air cooled air

  5. OBJECTIVE • Predictions of • Pressure • Air flow and • Temperature distributions in the heat exchangers

  6. Heat Exchanger Geometry

  7. Table 1: Geometrical details of the heat exchanger

  8. Modeling Considerations • Geometry has symmetry in width wise. • A section of heat exchanger consisting of 9 rows & 3 columns has been considered for analysis. Each column has 9 tubes. • Tube is modeled as solid blockage, whereas, the inner volume of the tube has been modeled as blockage with gaseous properties to allow the ambient air to pass through it by using PHOENICS CFD Software. • Conduction takes place from the tube wall & convection takes place from the surface of the tube. • The partition plate and baffle participate in heat transfer. • Temperature & flow distributions have been considered to be three dimensional in nature. • k-ε turbulence model has been considered. • Hybrid difference scheme has been used.

  9. Grid generation for heat exchanger The distribution of cells in the three directions are given below: X Direction : 55 Y Direction : 48 Z Direction : 232 The total number of cells in the computational domain is 612,480.

  10. Fig. 3: Side view of the grid

  11. Table 2: Operating boundary conditions of the heat exchanger

  12. The highest pressure region has been observed nearby the top of the separating plate, which may be due to the large change in the momentum of the cold fluid caused by the plate. Hot fluid recirculation has been observed at the top corner of 1st & 4th section. The temperature drop of the hot air in the 1st section of the heat exchanger is higher than 4th section because of the high temperature difference between the cold air and the hot air. Results & Discussions

  13. Fig. 4: Pressure distribution in the heat exchanger

  14. Fig. 5: Velocity distribution in the heat exchanger

  15. Fig. 6: Temperature distribution in the heat exchanger

  16. Fig. 7: Temperature distribution in the tube bundle of the heat exchanger

  17. Table 3: Comparison of air temperature prediction at various outlets

  18. Fig. 8: A comparison between the results of CFD simulation & experiments

  19. Fig. 9: Temperature distribution in the heat exchanger – a case study

  20. Fig. 10: Temperature distribution of the heat exchanger (after modification of central partition plate)

  21. (SunUltraSPARC-450, 300 MHz) Fig. 11: Effect of number of processors in computing time using parallel PHOENICS

  22. A method for predicting the pressure, velocity & temperature distributions in the tube type heat exchanger associated with CACA large motor has been developed using PHOENICS CFD software. The simulated results predict the temperature distribution reasonably at different locations of the heat exchanger. The CFD model may be used to optimize its thermal performance by varying the location of the baffles & the partition plate in the heat exchanger and in turn to improve the performance of electrical motors. The parallel PHOENICS can be used to reduce the design cycle of the equipment due to fast computation. Conclusions

  23. Acknowledgements • M/S Thapar Centre for Industrial Research & Development, Patiala, India for providing the necessary facilities to carry out this project • M/S Crompton Greaves, Mumbai, India for providing the funds in addition to drawing, design data and experimental results • M/S CHAM, U.K (support team) for technical help • M/S Centre for Development of Advanced Computing (C-DAC), Pune, India for providing the facility to use PARAM 10000 for running parallel PHOENICS and funding for presenting this paper

  24. THANK YOU

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