Ultrasound as pretreatment for drying garlic slices in microwave and convective dryer
Özet
The effects of ultrasound pretreatment (US) before hot air drying (HAD) and microwave drying (MWD) of garlic slices were investigated. For this aim ultrasonic bath at 30 °C for 30 min (35 kHz), microwave oven at 540 W power and tray dryer at 60 °C and with 1.0 m/s air flow rate were used to reach the final moisture content of 5%. Drying rate increased in the US + HAD and the US + MWD groups by 19.30% and 13.82% respectively in comparison with control groups. The effective moisture diffusivity (D eff ) of garlic slices were calculated from Fick’s diffusion model for the HAD, US + HAD, MWD and the US + MWD groups as 1.420 × 10 −10 , 1.826 × 10 −10 , 1.177 × 10 −8 , 1.363 × 10 −8 m 2 /s respectively. The rehydration rates increased, and bulk densities were decreased in the US + HAD and the US + MWD compared to the control groups. The color values were significantly affected after ultrasound pretreatment. Redness, and yellowness increased most in the US + HAD group.
Anahtar Kelimeler
- Scopus
- 53
- WoS
- 47
- OpenAlex
- 58
Tam Kayıt
| Alan | Değer | Dil |
|---|---|---|
| dc.contributor.author | Bozkir, Hamza | |
| dc.contributor.author | Rayman Ergün, Ahsen | |
| dc.contributor.author | Tekgül, Yeliz | |
| dc.contributor.author | Baysal, Taner | |
| dc.date.accessioned | 2026-10-28T14:56:52.965995671Z | |
| dc.date.available | 2026-10-28T14:56:52.965995671Z | |
| dc.date.issued | 2019 | |
| dc.description.abstract | The effects of ultrasound pretreatment (US) before hot air drying (HAD) and microwave drying (MWD) of garlic slices were investigated. For this aim ultrasonic bath at 30 °C for 30 min (35 kHz), microwave oven at 540 W power and tray dryer at 60 °C and with 1.0 m/s air flow rate were used to reach the final moisture content of 5%. Drying rate increased in the US + HAD and the US + MWD groups by 19.30% and 13.82% respectively in comparison with control groups. The effective moisture diffusivity (D eff ) of garlic slices were calculated from Fick’s diffusion model for the HAD, US + HAD, MWD and the US + MWD groups as 1.420 × 10 −10 , 1.826 × 10 −10 , 1.177 × 10 −8 , 1.363 × 10 −8 m 2 /s respectively. The rehydration rates increased, and bulk densities were decreased in the US + HAD and the US + MWD compared to the control groups. The color values were significantly affected after ultrasound pretreatment. Redness, and yellowness increased most in the US + HAD group. | |
| dc.identifier.doi | 10.1007/s10068-018-0483-1 | |
| dc.identifier.eissn | 2092-6456 | |
| dc.identifier.endpage | 354 | |
| dc.identifier.issn | 1226-7708 | |
| dc.identifier.issue | 2 | |
| dc.identifier.pmcid | PMC6431346 | |
| dc.identifier.pmid | 30956846 | |
| dc.identifier.scopus | 2-s2.0-85054558778 | |
| dc.identifier.startpage | 347 | |
| dc.identifier.uri | https://rdlopen.rawdatalibrary.net/r/munzur/3630 | |
| dc.identifier.volume | 28 | |
| dc.identifier.wos | WOS:000462163300006 | |
| dc.language.iso | en | |
| dc.publisher | The Korean Society of Food Science and Technology | |
| dc.relation.ispartof | Food Science and Biotechnology | |
| dc.rights | info:eu-repo/semantics/openAccess | |
| dc.subject | Color | |
| dc.subject | Drying | |
| dc.subject | Garlic slices | |
| dc.subject | Rehydration rate | |
| dc.subject | Ultrasound pretreatment | |
| dc.subject.classification | Food Science & Technology | |
| dc.subject.other | Color | |
| dc.subject.other | Dryers (equipment) | |
| dc.subject.other | Moisture | |
| dc.subject.other | Plants (botany) | |
| dc.subject.other | Ultrasonics | |
| dc.subject.other | Convective dryers | |
| dc.subject.other | Diffusion model | |
| dc.subject.other | Effective moisture diffusivity | |
| dc.subject.other | Final moisture content | |
| dc.subject.other | Garlic slices | |
| dc.subject.other | Microwave drying | |
| dc.subject.other | Ultrasonic bath | |
| dc.subject.other | Ultrasound pre treatments | |
| dc.subject.other | Drying | |
| dc.title | Ultrasound as pretreatment for drying garlic slices in microwave and convective dryer | |
| dc.type | Article | |
| rdl.citation.openalex | 58 | |
| rdl.citation.scopus | 53 | |
| rdl.citation.wos | 47 | |
| rdl.department | 1Food Engineering Department, Faculty of Engineering, Munzur University, 62100 Tunceli, Turkey | |
| rdl.department | 2Food Engineering Department, Faculty of Engineering, Ege University, Izmir, Turkey | |
| rdl.department | 3Food Processing Department, Köşk Vocational School, Adnan Menderes University, Aydın, Turkey | |
| rdl.oa.status | bronze | |
| rdl.oa.status | green | |
| rdl.oa.url | https://link.springer.com/content/pdf/10.1007/s10068-018-0483-1.pdf | |
| rdl.scopus.quartile | Q2 | |
| rdl.sdg | SDG02 | |
| rdl.source.index | SCOPUS | |
| rdl.source.index | WOS | |
| rdl.source.index | PUBMED | |
| rdl.wos.index | Science Citation Index Expanded (SCI-EXPANDED) |

