2019
DOI: 10.1111/jfpe.13204
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Kinetic evaluation and optimization of red popcorn grain drying: Influence of the temperature and air velocity on the expansion properties and β‐carotene content

Abstract: In order to obtain popcorn grains with excellent popping properties and a high β‐carotene content, the drying kinetics were investigated, and response surface methodology was used to optimize the drying process of red popcorn at temperatures of 40, 70, and 100°C and air velocities of 0.5, 1.5, and 2.5 m/s. The Page equation satisfactorily described the drying kinetics of red popcorn. Both variables (temperature and air velocity) had a significant effect on the popping yield, expansion time, and β‐carotene cont… Show more

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Cited by 13 publications
(12 citation statements)
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“…According to Pratico (2013) and Pohndorf et al. (2019), popcorn popping relies on the grain pericarp, which acts as a pressure vessel and moisture barrier. Heating changes the water in the endosperm into steam and causes the translucent endosperm to crystallize and melt.…”
Section: Resultsmentioning
confidence: 99%
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“…According to Pratico (2013) and Pohndorf et al. (2019), popcorn popping relies on the grain pericarp, which acts as a pressure vessel and moisture barrier. Heating changes the water in the endosperm into steam and causes the translucent endosperm to crystallize and melt.…”
Section: Resultsmentioning
confidence: 99%
“…The UKR also varied from 0.193 to 0.317, and runs 5, 9, and 17 had the lowest UKR (Table 1). High P, high T, and low W caused a more pronounced reduction in UKR and improved the Qingke utilization rate, because higher temperature and longer time made it easier to produce high pressure inside the grains while excessive water content can cause advanced starch gelatinization (Pohndorf et al., 2019).…”
Section: Resultsmentioning
confidence: 99%
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“…Then, the complementary drying was carried out through a hot air dryer at 30°C and an airspeed set at 0.5 m.s −1 . In all drying, the rice grain surface temperature was registered and grain moisture was controlled by weight difference according to Equation 1, where m f is the weight of the final sample (g), m i weight of the initial sample (g), U i initial moisture (g g −1 ), and U f is the final moisture (g g −1 ) (Pohndorf et al, ). mf=mi×()100×Unormali100×Unormalf …”
Section: Methodsmentioning
confidence: 99%
“…The fixed‐bed drying was carried out in the same dryer used for tempering‐drying. The grains (5 kg) were dried at 70 °C and 90 °C, an airspeed of 0.5 m/s (Pohndorf et al., 2019), and a grain bed depth of 200 mm (Figure 1b). The grain’s temperature was also measured with a digital thermometer (Infrared Thermometer, model Jumper JPD‐FR100).…”
Section: Methodsmentioning
confidence: 99%