Article ID | Journal | Published Year | Pages | File Type |
---|---|---|---|---|
687914 | Chemical Engineering and Processing: Process Intensification | 2016 | 10 Pages |
•Small foot print CFI heat exchanger has been proposed for process intensification.•Miniaturized CFI offers same heat transfer duty to that of the CFI of At = 1.76 m2.•Proposed CFI offers up to 5 fold enhanced U0 compared to SHE and PHE (At = 1.76 m2).•The miniaturized CFI was found in linear range of ε–NTU curve (NTU ≤ 2 or ε ≤ 0.8).
Three new coiled flow inverter (CFI) heat exchangers with heat transfer area (At) of 0.88 m2 (4-banks), 0.44 m2 (2-banks) and 0.22 m2 (1-bank) were designed, fabricated and commissioned to develop a more compact heat exchanger. More than 800 experiments were carried-out in counter-flow configuration. The hot and cold fluids were used in the tube and shell side of CFI heat exchanger, respectively. Tube side flow rates were varied from 50–300 kg/h for water and 30–100 kg/h for compressed air, respectively. The shell side flow rates were varied from 100–2000 kg/h for water and 400–750 kg/h for air, respectively. The overall heat transfer coefficients of present CFI heat exchangers were found in good agreement with the results reported for the CFI heat exchangers of At = 1.76 m2. The proposed CFI heat exchanger with At = 0.22 m2 provides 2.2–4.5 and 2–3.6 times higher overall heat transfer coefficient as compared to SHE and PHE of At = 1.76 m2, respectively. The present study offers a small footprint CFI heat exchanger to meet the same heat transfer duty as compared to previously reported study.