• Title/Summary/Keyword: 감율건조

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The Blanching Effects on the Drying Rates and the Color of Hot Red Pepper (고추의 건조율 및 색도에 미치는 Blanching 효과)

  • Chung, Shin-Kyo;Shin, Jong-Chul;Choi, Jong-Uck
    • Journal of the Korean Society of Food Science and Nutrition
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    • v.21 no.1
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    • pp.64-69
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    • 1992
  • To examine the effects of blanching treatments on the drying of hot red pepper, the pilot scale hot-air dryer equipped with the weight sensor using strain gauge type load cell and strain amplifier was designed and manufactured. The drying characteristic curves of cut hot red pepper showed a settling down period followed by a constant rate period and falling rate period, but blanched hot red pepper showed only falling rate period. According as the blanching time and temperature rises, the drying rates and the capsanthin contents of hot red pepper fairly increased. Considering the drying rates and the color values of dried hot red pepper, we suggest the desirable blanching condition of hot red pepper should be water blanching at $80^{\circ}C$ for 3 mins.

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Dehydration of Solid Food Material Immersed in Fluidized-Bed (유동층(流動層)에 의한 고체식품(固體食品)의 건조(乾燥))

  • Yu, Ju-Hyun;Lee, Shin-Young;Pyun, Yu-Ryang;Yang, Ryung
    • Korean Journal of Food Science and Technology
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    • v.10 no.4
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    • pp.398-403
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    • 1978
  • Squid was dried on the fluidized-bed in the drying chamber filled with solid particles which were also fluidized with hot-air, and effects of the fluidized particles, the squid's height from the grid and the drying temperature on the drying rate and quality of the squid were observed The mechanism of moisture transfer during the falling rate period was also derived. 1. Sodium chloride was found to be the most suitable fluidized particles and at an air velocity of 3.8 m/sec, optimal fluidization state of this particle was obtained. 2. Uniform profiles of temperature were obtained at a point 4 cm above the grid and the location of squid on the fluidized-bed observed to be suitable when it was 4 cm above the grid. 3. At an air velocity of 3.8 m/sec and when the location height of the squid on the fluidized-bed was 4 cm, the optimal temperature for the drying time which is required to reduce the moisture from 80.8% to 18-22% was 8.5 hours. 4. Drying data followed the empirical equation of unsteady state diffusion $log\;(\frac{W-We}{Wc-We})=-m{\theta}$ in the region of the moisture contents measured and the drying constant (m) was calculated as $0.32hr^{-1}$. These results suggested that the migration of moisture during the falling rate period is due to a diffusion type mechanism. 5. The short constant rate period was observed in the early stage and thereafter, drying was controlled by the falling rate period, and the time ratio of the fluidized bed drying to the through circulation drying for reducing the squid's moisture contents to the same level at the same drying temperature was 1 : 1.4 6. Comparisons of fluidized-bed dried squid and sun dried squid in sale showed that there was no significant change in qualities such as external appearance and hydrogen ion concentration of dry product.

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Effects of the Low Temperature Vacuum Drying Process on Drying Curve and Physico-Chemical Properties of Astringent Persimmons (저온진공건조 공정에 의한 떫은 감의 건조 및 품질 특성)

  • Hur, Sang-Sun
    • Journal of the Korean Applied Science and Technology
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    • v.33 no.1
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    • pp.58-66
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    • 2016
  • This study was performed to investigate drying characteristics and quality properties of dried persimmon with vacuum drying process. Drying characteristic curve of the dried persimmon showed that the constant rate drying period and falling rate drying period exist definitely. $_{\circ}Brix$, sugar content and hardness value of the dried persimmon increased as the vacuum pressure and heating temperature increased, but L value of the dried persimmon lower. The results indicated that the optimal conditions were at vacuum pressure of 40~50kPa abs., heating temperature of $30^{\circ}C$ and drying time of 3~4days.

Drying of Sewage Sludge Using Microwave Energy (도시하수 Sludge의 초고주파 건조)

  • 최병순;이동훈
    • Resources Recycling
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    • v.6 no.1
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    • pp.40-46
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    • 1997
  • Sludgc d~sposal has been a major challenge in the wastewater treatment. Drying is operation which is separated fromsewage sludge to solid and liquid by heating. Drying needs to pretreatment process for effective "thation, incinerationand dispaal The objective of this work was to the drying dewatered sewage sludge by microwave heating, and tocompare the experimental rcsults with thcorctical rcsults. Microwave drylng is fast and has a high efficiency. In thepresent \ark, an unsteady state analysis of one dunensional drying, with microwave heating, is carried out. In drying ratecurve, moisture movement at falling rate period occured by dfision. A good agreement was abtamed between the modcland the experimental results using the slab sample of 0.2cm thickness. 0.2cm thickness.

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Drying Characteristics of Fluidized Bed Drying of Naked Barley (쌀보리의 유동층 건조 특성에 관한 연구)

  • Kim, Hee-Yun;Cho, Duk-Jae;Chung, Gea-Hwan;Hur, Jong-Wha
    • Korean Journal of Food Science and Technology
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    • v.25 no.5
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    • pp.558-564
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    • 1993
  • The drying characteristics of fluidized bed drying with different drying conditions using naked barley were carried out. This fluidized drying mechanism of naked barley was consisted of consecutive two falling rate parts, first falling rate period and second falling rate period without showing constant rate period. The drying rate constant was increased with decreasing charged amount and relative humidity and increasing air temperature and air velocity. Since the drying rate constant expressed by Arrhenius type equation in the falling rate period showed good linearity, the falling rate period was considered as the controlling step. The activation energy of first falling step was 1,900 cal/gmol, while for second falling step the values showed 2,500 cal/gmol.

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Drying of Red Ginseng by Flat-Plate Solar Collector (평면식(平面式) 태양열집열기(太陽熱集熱機)를 이용(利用)한 홍삼건조(紅蔘乾燥))

  • Chang, Kyu-Seob;Kim, Sang-Dal;Hong, Soon-Keun;Yoon, Han-Kyo
    • Applied Biological Chemistry
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    • v.25 no.3
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    • pp.111-118
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    • 1982
  • A closed solar collector drying system by water exchange was evaluated for the drying of ginseng. The thermal efficiency of solar collector, drying efficiency, drying characteristics and product quality were investigated. The drying period was reduced by one-thirds in comparison with typical method. The maximum and minimum thermal efficiency of the solar collector during drying period were 14.42%, and 4.73%, respectively. The drying efficiency of solar collector and control system showed 28.34%, and 13.45%, respectively; net drying efficiency being 14.8%. The drying rate curve of red ginseng showed only falling rate period, and its equation was $Y=50.7023t.^{-0.4138}$ The brown color intensity of red ginseng was higher in solar collector drying system than in typical method, and reductivity by diphenyl picryl hydrazil solution in red ginseng extract showed similar result to brown color intensity.

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Drying by Microwave Irradiation of Sewage Waste (도시 하수 폐기물의 고주파 건조)

  • Park, Soo In;Park, Kwang Ha
    • Analytical Science and Technology
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    • v.10 no.6
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    • pp.418-426
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    • 1997
  • Dewatered digested sewage sludge were heated with microwave and their drying characteristics were investigated on the effect of their surface area, shape, diameter and thickness. The drying characteristics of identical samples in a conventional drying oven were studied. In conventional drying, constant rate period was not found and moisture was evaporated with capillary action. Moisture in the sludge was a bound water and free water was not exist. In microwave drying, the falling rate period was divided into two zones. In falling rate drying period, moisture movement occured by diffusion. The evaporation surface area was a significant variable, the greater heating surface area promoted water removal rate over wide region of water content. Drying rate was slow and constant rate drying period was found in wide moisture content region with increasing diameter. Drying characteristics appeared differently in various shape. In microwave heating, first of all temperature of sludge center was increased and was the highest. Temperature in the constant rate drying period was remained constantly at $80{\sim}100^{\circ}C$.

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Effect of Drying Air Velocity on the Quality of Salted and Dried Mullet Roe (영암어라인의 품질에 대한 건조풍속의 영향)

  • 조상준
    • Journal of the Korean Society of Food Science and Nutrition
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    • v.20 no.5
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    • pp.503-508
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    • 1991
  • The salted and dried mullet(Mugil Japonicus) roe had about 42% of protein and 41% of lipid content as major compoments. Therefore the lipid oxidation and the deterioration of protein occurred during drying and storage periods. In order to keep the good quality of the dried roe, acid, peroxide, thiobarbituric acid value and the contitutional amino acid were studied in the different drying air velocities at the conditions of 60% R.H. and $20^{\circ}C$ of drying air temperature. The optimum air velocity showed 2m/sec, which was excellently superior to the lipid and protein quality than those of other air velocities on the dried mullet roe. The drying period shortened from 20 days in the conventional processing method to 7 days in the modified processing method that had 2m/sec of drying air velocity. The drying rate curve had only a falling-rate drying period and not to have a constant-rate drying period.

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Development of Decompressed Dryer for Mushroom (버섯의 감압건조기 개발)

  • 김영민;김유호;조영길;최희석;조광환
    • Proceedings of the Korean Society for Agricultural Machinery Conference
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    • 2003.07a
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    • pp.267-272
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    • 2003
  • 본 연구에서는 버섯의 건조시간을 줄여 건조 후 버섯의 품질을 향상시키기 위하여 버섯의 감압건조기를 개발하였으며 연구 결과는 다음과 같다. 가. 버섯의 감압건조기의 시작기를 제작하였고, 시작기의 구조는 건조실, 감압블로워, 흡ㆍ배기구 솔레노이드 밸브, 제습장치, 송풍기, 전기히터로 구성되어 있으며, 건조실의 내부 압력이 표준대기압-900hPa, 열풍온도는 상온에서 5$0^{\circ}C$까지 조절할 수 있도록 제작하였다. 나. 시작기를 이용하여 표고버섯을 대상으로 건조특성시험을 실시한 결과, 열풍온도 5$0^{\circ}C$, 건조실 내부압력 900-940hPa에서 건조시간은 11.5h으로 대기압과 비교하여 6.5h 단축되는 것으로 나타났다. 또한, 건조 전ㆍ후의 색차, 수축률, 복원률의 품위가 우수한 것으로 나타났으며 F-test 유의성 검증 결과, 5%의 유의수준에서 갓주름의 색차, 갓직경의 수축률, 복원률에서 유의차가 있는 것으로 나타났다. 다. 열풍온도 5$0^{\circ}C$, 건조실 내부압력 900-940hPa로 표고버섯과 아가리쿠스에 대하여 건조성능시험을 실시한 결과, 표고버섯의 경우 건조시간은 13h으로 열풍식 농산물 건조기와 비교하여 건조시간이 4.5h 단축되는 것으로 나타났으며, 아가리쿠스의 경우 건조시간이 17.5h로 나타났다. 라. 성능시험 결과, 시작기가 열풍식 농산물건조기와 비교하여 건감률, 색택, 수축률, 복원률 등의 품위가 전반적으로 우수한 것으로 나타났다. 마. 시작기의 건조비용을 분석한 결과, 건조시간은 단축되었지만 시설투자비가 높아 건조비용이 표고버섯의 경우 2,461원/kg으로 열풍식 농산물건조기 보다 13% 높은 것으로 나타났지만, 추후 고품질 건조버섯 생산을 위한 기초자료로 활용이 가능할 것으로 판단된다.라갈수록 낮은 온도분포를 나타내고 있는 것은 상부에는 외부공기가 유입되면서 온도가 떨어지는 반면 하부에는 외부공기 유입이 적기 때문으로 사료된다. 또한 열풍실의 길이방향 위치별 온도 분포에서도 같은 현상으로 나타났고, 버너쪽과 송풍기쪽의 온도편차는 나타나지 않아 균일 건조를 기대할 수 있다. 마. 열풍온도를 45$^{\circ}C$로 설정하고 조사거리와 방사체 길이를 각각 119, 1,470mm로 하여 벼의 건조성능시험을 열풍건조기(대비구)와 비교시험 결과 시험구에서 건감률, 건조소요에너지가 각각 0.58%(w.b.), 470kcal/kg - water로 대비구보다 각각 건감율은 23% 높았고, 건조소요에너지는 2%의 절감되었다. 바. 건조기에서 발생되는 소음은 버너쪽 근처에서는 대비구 94.12㏈의 87%에 불과하였으나, 거리가 멀어질수록 차이는 크지 않았다. 이것은 버너에서 멀어질수록 외부적인 요인이 소음에 영향을 미쳤기 때문인 것으로 생각된다. 사. 시작기와 대비구간의 경제성에서 시작기의 구입가격이 20% 비싸기 때문에 시간당 고정비가 높았으나, 건조성능이 우수하여 건조비용이 69,350원/톤으로 대비구보다 14% 절감되는 것으로 나타났다.작용하는 것으로 사료된다.된다.정량 분석한 결과이다. 시편의 조성은 33.6 at% U, 66.4 at% O의 결과를 얻었다. 산화물 핵연료의 표면 관찰 및 정량 분석 시험시 시편 표면을 전도성 물질로 증착시키지 않고, Silver Paint 에 시편을 접착하는 방법으로도 만족한 시험 결과를 얻을 수 있었다.째, 회복기 중에 일어나는 입자들의 유입은 자기폭풍의 지속시간을 연장시키는 경향을 보이며 큰 자기폭풍일수록 현저했다. 주상에서 관측된 이러한 특성은 서브스톰 확장기 활동이 자기폭풍의 발달과 밀접한 관계가 있음을 시사한다.se that were all

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The Characteristics of Hot Air Drying of Red Pepper (고추의 열풍건조특성(熱風乾燥特性))

  • Chun, Jae-Kun;Kim, Kong-Hwan
    • Applied Biological Chemistry
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    • v.17 no.1
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    • pp.42-48
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    • 1974
  • Hot air thin layer drying method was studied for red pepper, Capsicum annum var. longum as the whole and cut pod states, at various temperature and air velocities. Drying curve of whole pod showed a settling down period followed by the first and second falling rate periods. By lowering the drying temperature, the first falling rate period approached to a constant rate one. Cut drying curve had simple falling rate period and also cut drying method could effectively shorten the drying time. Drying rate constant, k, was varied with time for both the drying methods and the plots of k vs. time in two methods sugested the different drying mechanisms. When an average k was taken as a constant value, the following equations; $M-M_e/M_o-M_e=e^{-0.118t}$ and $M-M_e/M_o-M_e=e(-0.342t^{0.128})$ were applicable for whole and cut drying, respectively.

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