Process Heat Transfer 2014
DOI: 10.1016/b978-0-12-397195-1.00011-x
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Cited by 3 publications
(5 citation statements)
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References 13 publications
(22 reference statements)
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“…Δ T = T – T amb is the temperature rise with respect to the ambient temperature T amb . The surface heat transfer coefficient is assumed to be equal to h = 10 –3 W/(cm 2 K) that is typical for natural air convection . (d) Qualitative energy band diagram of the Au/InAs/InP 0.69 Sb 0.31 structure in the regime of full loss compensation.…”
Section: Resultsmentioning
confidence: 99%
See 1 more Smart Citation
“…Δ T = T – T amb is the temperature rise with respect to the ambient temperature T amb . The surface heat transfer coefficient is assumed to be equal to h = 10 –3 W/(cm 2 K) that is typical for natural air convection . (d) Qualitative energy band diagram of the Au/InAs/InP 0.69 Sb 0.31 structure in the regime of full loss compensation.…”
Section: Resultsmentioning
confidence: 99%
“…It should be pointed out that the net heat generation is quite high even at a low SPP power and can give substantial rise to the device temperature. Without a heat sink, the surface heat transfer coefficient can be roughly estimated as h = 10 –3 W/(K cm 2 ) (which is a typical value for natural air convection at standard conditions), and the temperature of the single active plasmonic waveguide on an InAs wafer can be roughly evaluated as Δ T ≈ ( P cont + P vol )/2 hw d , where w d is the wafer width. This simple expression demonstrates that for the 1 cm wide substrate the temperature rise is as high as 100 K, even at a very low SPP power.…”
Section: Resultsmentioning
confidence: 99%
“…Regarding the methodology employed for sizing the main unit operations, particularly the distillation columns, we refer the reader to refs , , and . For the transesterifier, we employ a sizing approach based on a one-hour residence time, ensuring it operates at half of its capacity during nominal operation.…”
Section: Biodiesel and Glycerol Production Processmentioning
confidence: 99%
“…We utilize residence times of five s for the column trays and 30 s for the condensers and reboilers. The sizing of other units follows similar heuristics. Across all units with holdups, the sizing is such that they operate at approximately half of their capacity during nominal operation.…”
Section: Biodiesel and Glycerol Production Processmentioning
confidence: 99%
“…The behavior of bubbles formed during boiling has major consequences with respect to the properties or performance of many systems and processes. Among these are, for example, systems ranging from the simple home kettle to large, industrial heat exchangers, cavitation in industrial as well as biological systems, , and the highly debated phenomenon of nanobubbles (ref and references within). As is well known, homogeneous nucleation, namely, nucleation in an absolutely pure system, without any external nuclei, is highly unlikely.…”
Section: Introductionmentioning
confidence: 99%