ANVARI, Ali Reza ;JAVAHERDEH, Kourosh . Experimental Investigation of Newtonian and Non-Newtonian Liquid Flow in Wavy and Straight Mini-Channel Cross-Flow Plate Heat Exchangers. Strojniški vestnik - Journal of Mechanical Engineering, [S.l.], v. 65, n.1, p. 41-49, january 2019. ISSN 0039-2480. Available at: <https://www.sv-jme.eu/sl/article/experimental-investigation-of-newtonian-and-non-newtonian-liquid-fow-in-wavy-and-straight-mini-channel-cross-flow-plate-heat-exchanger/>. Date accessed: 19 nov. 2024. doi:http://dx.doi.org/10.5545/sv-jme.2018.5301.
Anvari, A., & Javaherdeh, K. (2019). Experimental Investigation of Newtonian and Non-Newtonian Liquid Flow in Wavy and Straight Mini-Channel Cross-Flow Plate Heat Exchangers. Strojniški vestnik - Journal of Mechanical Engineering, 65(1), 41-49. doi:http://dx.doi.org/10.5545/sv-jme.2018.5301
@article{sv-jmesv-jme.2018.5301,
author = {Ali Reza Anvari and Kourosh Javaherdeh},
title = {Experimental Investigation of Newtonian and Non-Newtonian Liquid Flow in Wavy and Straight Mini-Channel Cross-Flow Plate Heat Exchangers},
journal = {Strojniški vestnik - Journal of Mechanical Engineering},
volume = {65},
number = {1},
year = {2019},
keywords = {heat-exchanger; mini-channel; mon-Newtonian; CMC; wavy},
abstract = {In this research, an experimental study was performed regarding the heat transfer performance and pressure drop specifications of a Newtonian fluid and a non-Newtonian fluid. To this end, laminar flow of the deionized (DI) water and the aqueous solution containing 0.2 wt.% carboxyl methyl cellulose (CMC) were used as the Newtonian fluid and the non-Newtonian fluid, respectively, in wavy and straight mini-channel cross-flow heat exchangers (CFHE). Each mini-channel cross-flow plate heat exchanger (MCFPHE) was made of three copper plates for the hot and cold sides, which contain 27 mini-channels in parallel. The mini-channel CFHE was examined for Reynolds numbers (Re) in the range of 200 to 1800 and the hot-side inlet temperature was between 40 °C and 50 °C while the cold-side temperature varied in the range of 10 °C to 20 °C. The thermal and rheological properties of the non-Newtonian fluid were investigated. The results showed that for both fluids, the thermal performance of the wavy mini-channel is more than that of the straight mini-channel and, although the pressure drop was intensified, its effect is low at high Re values.},
issn = {0039-2480}, pages = {41-49}, doi = {10.5545/sv-jme.2018.5301},
url = {https://www.sv-jme.eu/sl/article/experimental-investigation-of-newtonian-and-non-newtonian-liquid-fow-in-wavy-and-straight-mini-channel-cross-flow-plate-heat-exchanger/}
}
Anvari, A.,Javaherdeh, K. 2019 January 65. Experimental Investigation of Newtonian and Non-Newtonian Liquid Flow in Wavy and Straight Mini-Channel Cross-Flow Plate Heat Exchangers. Strojniški vestnik - Journal of Mechanical Engineering. [Online] 65:1
%A Anvari, Ali Reza %A Javaherdeh, Kourosh %D 2019 %T Experimental Investigation of Newtonian and Non-Newtonian Liquid Flow in Wavy and Straight Mini-Channel Cross-Flow Plate Heat Exchangers %B 2019 %9 heat-exchanger; mini-channel; mon-Newtonian; CMC; wavy %! Experimental Investigation of Newtonian and Non-Newtonian Liquid Flow in Wavy and Straight Mini-Channel Cross-Flow Plate Heat Exchangers %K heat-exchanger; mini-channel; mon-Newtonian; CMC; wavy %X In this research, an experimental study was performed regarding the heat transfer performance and pressure drop specifications of a Newtonian fluid and a non-Newtonian fluid. To this end, laminar flow of the deionized (DI) water and the aqueous solution containing 0.2 wt.% carboxyl methyl cellulose (CMC) were used as the Newtonian fluid and the non-Newtonian fluid, respectively, in wavy and straight mini-channel cross-flow heat exchangers (CFHE). Each mini-channel cross-flow plate heat exchanger (MCFPHE) was made of three copper plates for the hot and cold sides, which contain 27 mini-channels in parallel. The mini-channel CFHE was examined for Reynolds numbers (Re) in the range of 200 to 1800 and the hot-side inlet temperature was between 40 °C and 50 °C while the cold-side temperature varied in the range of 10 °C to 20 °C. The thermal and rheological properties of the non-Newtonian fluid were investigated. The results showed that for both fluids, the thermal performance of the wavy mini-channel is more than that of the straight mini-channel and, although the pressure drop was intensified, its effect is low at high Re values. %U https://www.sv-jme.eu/sl/article/experimental-investigation-of-newtonian-and-non-newtonian-liquid-fow-in-wavy-and-straight-mini-channel-cross-flow-plate-heat-exchanger/ %0 Journal Article %R 10.5545/sv-jme.2018.5301 %& 41 %P 9 %J Strojniški vestnik - Journal of Mechanical Engineering %V 65 %N 1 %@ 0039-2480 %8 2019-01-14 %7 2019-01-14
Anvari, Ali Reza, & Kourosh Javaherdeh. "Experimental Investigation of Newtonian and Non-Newtonian Liquid Flow in Wavy and Straight Mini-Channel Cross-Flow Plate Heat Exchangers." Strojniški vestnik - Journal of Mechanical Engineering [Online], 65.1 (2019): 41-49. Web. 19 Nov. 2024
TY - JOUR AU - Anvari, Ali Reza AU - Javaherdeh, Kourosh PY - 2019 TI - Experimental Investigation of Newtonian and Non-Newtonian Liquid Flow in Wavy and Straight Mini-Channel Cross-Flow Plate Heat Exchangers JF - Strojniški vestnik - Journal of Mechanical Engineering DO - 10.5545/sv-jme.2018.5301 KW - heat-exchanger; mini-channel; mon-Newtonian; CMC; wavy N2 - In this research, an experimental study was performed regarding the heat transfer performance and pressure drop specifications of a Newtonian fluid and a non-Newtonian fluid. To this end, laminar flow of the deionized (DI) water and the aqueous solution containing 0.2 wt.% carboxyl methyl cellulose (CMC) were used as the Newtonian fluid and the non-Newtonian fluid, respectively, in wavy and straight mini-channel cross-flow heat exchangers (CFHE). Each mini-channel cross-flow plate heat exchanger (MCFPHE) was made of three copper plates for the hot and cold sides, which contain 27 mini-channels in parallel. The mini-channel CFHE was examined for Reynolds numbers (Re) in the range of 200 to 1800 and the hot-side inlet temperature was between 40 °C and 50 °C while the cold-side temperature varied in the range of 10 °C to 20 °C. The thermal and rheological properties of the non-Newtonian fluid were investigated. The results showed that for both fluids, the thermal performance of the wavy mini-channel is more than that of the straight mini-channel and, although the pressure drop was intensified, its effect is low at high Re values. UR - https://www.sv-jme.eu/sl/article/experimental-investigation-of-newtonian-and-non-newtonian-liquid-fow-in-wavy-and-straight-mini-channel-cross-flow-plate-heat-exchanger/
@article{{sv-jme}{sv-jme.2018.5301},
author = {Anvari, A., Javaherdeh, K.},
title = {Experimental Investigation of Newtonian and Non-Newtonian Liquid Flow in Wavy and Straight Mini-Channel Cross-Flow Plate Heat Exchangers},
journal = {Strojniški vestnik - Journal of Mechanical Engineering},
volume = {65},
number = {1},
year = {2019},
doi = {10.5545/sv-jme.2018.5301},
url = {https://www.sv-jme.eu/sl/article/experimental-investigation-of-newtonian-and-non-newtonian-liquid-fow-in-wavy-and-straight-mini-channel-cross-flow-plate-heat-exchanger/}
}
TY - JOUR AU - Anvari, Ali Reza AU - Javaherdeh, Kourosh PY - 2019/01/14 TI - Experimental Investigation of Newtonian and Non-Newtonian Liquid Flow in Wavy and Straight Mini-Channel Cross-Flow Plate Heat Exchangers JF - Strojniški vestnik - Journal of Mechanical Engineering; Vol 65, No 1 (2019): Strojniški vestnik - Journal of Mechanical Engineering DO - 10.5545/sv-jme.2018.5301 KW - heat-exchanger, mini-channel, mon-Newtonian, CMC, wavy N2 - In this research, an experimental study was performed regarding the heat transfer performance and pressure drop specifications of a Newtonian fluid and a non-Newtonian fluid. To this end, laminar flow of the deionized (DI) water and the aqueous solution containing 0.2 wt.% carboxyl methyl cellulose (CMC) were used as the Newtonian fluid and the non-Newtonian fluid, respectively, in wavy and straight mini-channel cross-flow heat exchangers (CFHE). Each mini-channel cross-flow plate heat exchanger (MCFPHE) was made of three copper plates for the hot and cold sides, which contain 27 mini-channels in parallel. The mini-channel CFHE was examined for Reynolds numbers (Re) in the range of 200 to 1800 and the hot-side inlet temperature was between 40 °C and 50 °C while the cold-side temperature varied in the range of 10 °C to 20 °C. The thermal and rheological properties of the non-Newtonian fluid were investigated. The results showed that for both fluids, the thermal performance of the wavy mini-channel is more than that of the straight mini-channel and, although the pressure drop was intensified, its effect is low at high Re values. UR - https://www.sv-jme.eu/sl/article/experimental-investigation-of-newtonian-and-non-newtonian-liquid-fow-in-wavy-and-straight-mini-channel-cross-flow-plate-heat-exchanger/
Anvari, Ali Reza, AND Javaherdeh, Kourosh. "Experimental Investigation of Newtonian and Non-Newtonian Liquid Flow in Wavy and Straight Mini-Channel Cross-Flow Plate Heat Exchangers" Strojniški vestnik - Journal of Mechanical Engineering [Online], Volume 65 Number 1 (14 January 2019)
Strojniški vestnik - Journal of Mechanical Engineering 65(2019)1, 41-49
© The Authors, CC-BY 4.0 Int. Change in copyright policy from 2022, Jan 1st.
In this research, an experimental study was performed regarding the heat transfer performance and pressure drop specifications of a Newtonian fluid and a non-Newtonian fluid. To this end, laminar flow of the deionized (DI) water and the aqueous solution containing 0.2 wt.% carboxyl methyl cellulose (CMC) were used as the Newtonian fluid and the non-Newtonian fluid, respectively, in wavy and straight mini-channel cross-flow heat exchangers (CFHE). Each mini-channel cross-flow plate heat exchanger (MCFPHE) was made of three copper plates for the hot and cold sides, which contain 27 mini-channels in parallel. The mini-channel CFHE was examined for Reynolds numbers (Re) in the range of 200 to 1800 and the hot-side inlet temperature was between 40 °C and 50 °C while the cold-side temperature varied in the range of 10 °C to 20 °C. The thermal and rheological properties of the non-Newtonian fluid were investigated. The results showed that for both fluids, the thermal performance of the wavy mini-channel is more than that of the straight mini-channel and, although the pressure drop was intensified, its effect is low at high Re values.