2017
DOI: 10.1016/j.applthermaleng.2017.02.054
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The effect of Dixon rings on direct contact heat transfer performance: Comparison of counter and co-current evaporation

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Cited by 14 publications
(8 citation statements)
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“…Luo et al [8] designed a new type of helical tube reactor and applied it to the experimental study of liquid-liquid dispersion. Jin et al [9] applied Dixon rings in DCHT and found that the Dixon rings can have a positive effect through a series of experiments, and the heat transfer coefficient has almost doubled or even more. Li et al [10] studied the falling film evaporation heat transfer of R134a-entrained 0.5% to 5.1% POE-type lubricating oil on the horizontal pipe.…”
Section: Introductionmentioning
confidence: 99%
“…Luo et al [8] designed a new type of helical tube reactor and applied it to the experimental study of liquid-liquid dispersion. Jin et al [9] applied Dixon rings in DCHT and found that the Dixon rings can have a positive effect through a series of experiments, and the heat transfer coefficient has almost doubled or even more. Li et al [10] studied the falling film evaporation heat transfer of R134a-entrained 0.5% to 5.1% POE-type lubricating oil on the horizontal pipe.…”
Section: Introductionmentioning
confidence: 99%
“…Interfacial physical processes play a key role in the transfer of energy from the continuous phase to the dispersed phase, thus being linked to the performance of a DCHE. It is a common practice to improve the DCHE performance through increasing the interfacial area, e.g., using a sparger to inject the dispersed phase (Baqir A. M., 2016), or using Dixon rings (Jiang, 2015) (Jin, 2017) to break bubbles. Surface tension, the physical parameter driving phase change and immiscibility, is expected to strongly influence overall performance of a DCHE.…”
Section: Introductionmentioning
confidence: 99%
“…In this publication, azeotropic distillation, single-effect evaporation, co-current multiple-effect evaporation and counter-current multiple-effect evaporation were compared as possible processes for the recovery of diluted sulfuric acid. However, numbers of simulation based description of evaporation systems has been published recently [13][14][15][16], only one work included sulfuric acid recovery [17]. This further emphasizes the urgent need for improvements in modelling of spent acid regeneration via separation technologies.…”
Section: Introductionmentioning
confidence: 99%