1998
DOI: 10.2514/2.5342
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Investigation of Heat Transfer and Coking Characteristics of Hydrocarbon Fuels

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Cited by 70 publications
(20 citation statements)
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“…For similar wall temperatures and flow rates, it is clearly seen that increasing the bulk fluid temperature by use of the preheater increases the overall heat transfer in the test section. This increase in heat transfer for higher bulk temperature fluids has been shown for aviation kerosenes previously, 4 and is attributed to higher Reynolds numbers accompanying higher temperatures. For constant velocity and hydraulic diameter, the increase in Reynolds number between Set 1 and Set 3 is dominated by the ratio of absolute viscosities (µ Set1 /µ Set3 ), leading to large Reynolds number increases for moderate temperature increases.…”
Section: A Heat Transfer Resultssupporting
confidence: 79%
“…For similar wall temperatures and flow rates, it is clearly seen that increasing the bulk fluid temperature by use of the preheater increases the overall heat transfer in the test section. This increase in heat transfer for higher bulk temperature fluids has been shown for aviation kerosenes previously, 4 and is attributed to higher Reynolds numbers accompanying higher temperatures. For constant velocity and hydraulic diameter, the increase in Reynolds number between Set 1 and Set 3 is dominated by the ratio of absolute viscosities (µ Set1 /µ Set3 ), leading to large Reynolds number increases for moderate temperature increases.…”
Section: A Heat Transfer Resultssupporting
confidence: 79%
“…In particular, for the use in cooling systems, the threshold value of coolant-side wall temperatures is limited by coking considerations. For methane the widely quoted value is 970 K, higher than propane (700 K) and kerosene (590 K) [4]. Moreover, the heat transfer performance of methane is higher compared to other hydrocarbon fuels as a result of its high thermal conductivity, speci¦c heat, and low viscosity.…”
Section: Introductionmentioning
confidence: 95%
“…The investigations presented are performed at the newly built institute£s test facility for GCH 4 and GOx, designed for interface pressures up to 50 bar.…”
Section: Test Specimen and Experimental Setupmentioning
confidence: 99%
“…In particular, the deterioration has been outlined with hydrogen, 19 methane, propane and liquefied natural gas. 20,21 However, it was observed in studies which were not carried out to investigate the deterioration phenomenon, rather their purpose was to investigate the cooling capabilities and coking characteristics of the coolant fluid (coking for hydrocarbons). Nevertheless, these experimental works demonstrate the risk of a deteriorated heat transfer in regenerative cooling channel configurations.…”
Section: Introductionmentioning
confidence: 97%