• 한국작물학회지
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• 제41권3호
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• pp.362-369
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• 1996

3년생 의성작약품종(faeornia lacrifora Pall.)을 1994년 2월에 수확하여 유피 및 거피상태로 처리한 후 상온음건법, 화력건조법, 증건법 및 냉동건조법으로 건조방법을 각각 달리하여 주 약용성분인 paeoniflorin함량 및 일반 화학성분을 조사한 결과는 다음과 같다. 1. 건물비율 50%까지의 건조일수는 거피상태 3$0^{\circ}C$ 화력건조가 동일온도의 유피상태보다 5일이 짧으며, 거피상태에서는 5$0^{\circ}C$ 화력건조법이 1.5일로 가장 빨랐고, 121$^{\circ}C$ 증건법은 8일로 가장 늦었다. 2. 상온음건 및 화력건조법의 경우 paeoniflorin 함량은 거피상태가 더 높았고, 반대로 증건법은 유피상태가 더 높았다. 화력건조법의 경우 건조온도가 높아짐에 따라 paeoniflorin 함량은 감소하였다. 3. 건조방법 중 3$0^{\circ}C$화력건조가 Paeoniflorin함량이 4.0%로 가장 높고, 건조일수가 단축되며, 색택 이 양호한 가장 적절한 건조법 이었다. 4. 화력건조시 건조온도가 높아짐에 따라 총당의 함량은 감소하고 전분은 증가하는 경향을 보였으며, 또 전분함량은 121$^{\circ}C$의 증건법을 제외한 모든 건조방법에서 거피상태보다 유피상태가 더 높았다. 5. 조단백질, 조섬유 및 조회분의 함량은 유피, 거피 및 건조방법에 따라 큰 차이가 없었다. 6. Paeoniflorin과 총당의 관계는 유피상태에서 정의 유의상관이, 그리고 paeoniflorin과 전분의 관계는 거피상태에서 부의 유의상관이 있었다.

• Journal of Ginseng Research
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• 제33권4호
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• pp.361-366
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• 2009

과열증기 건조처리 후 열풍 건조한 인삼의 건조율이 열풍 건조만으로 건조한 인삼에 비하여 약 40%의 빠른 건조율을 나타내었다. 일반성분의 함량에 있어서 조지방, 조단백질, 조섬유 및 회분 함량의 경우 두처리구간 큰 차이가 없었다. 무기질 및 유리당 함량의 경우에 있어서도 두 처리구간 큰 차이를 나타내지 않았다. 조사포닌 함량의 경우 과열증기 처리 후 열풍건조한 인삼분말의 조사포닌 함량은 5.43% 그리고 열풍건조만 한 인삼분말의 조사포닌 함량은 5.4%로 두시료간 큰 차이가 없었다. 색깔의 경우 적색도를 나타내는 a값에서 과열증기 건조 후 열풍건조 처리한 인삼분말이 열풍건조한 인삼분말에 비하여 약간 높은 결과를 나타내었다. 인삼분말의 미생물 수의 경우 과열증기 건조 후 열풍 건조한 인삼분말이 열풍건조한 인삼분말에 비하여 일반세균 및 효모곰팡이가 약 2 log 정도 감소하였고 대장균군의 경우는 약 1 log 정도 감소한 결과를 나타내었다.

• Journal of Biosystems Engineering
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• 제29권1호
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• pp.37-44
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• 2004

This study was conducted to develop a new drying method far reducing the drying cost and time and to investigate the drying characteristics of oak mushroom. A far infrared dryer of down draft air flow type used for this experiment can control the drying parameters, such as far infrared heater temperature and aeration velocity. The far infrared drying tests were performed at aeration velocities of 0.3 and 0.6m/s under the temperature of 90 and 100$^{\circ}C$ in for infrared heater, respectively. The results were compared and analyzed with those of an heated air drying method used as a control in terms of properties representing the drying characteristics. such as shrinkage rate, color, energy consumption amino acid components, drying rate and moisture ratio. The results obtained from this research can be summarized as follows. 1. The drying rate of far infrared drying was faster than that of heated air drying. With high temperature of far infrared heater and slow aeration velocity, the far infrared drying of down draft air flow type was superior to the heated air drying. 2. Most of far infrared drying conditions required less energy consumption than heated air drying. 3. The shrinkage rates of heated air drying and far infrared drying were decreased by 17.0% and 18.2∼19.8%, respectively. 4. The difference of color on oak mushroom surface before and after drying can be represented as $\Delta$E. $\Delta$E values of far infrared drying and heated air drying were 2.39∼4.55 and 6.77, respectively. 5. The amounts of free amino acids were higher in the far infrared than in the heated air drying. In addition the amounts of Gln and Glu generally were increased and those of Ala, Leu, and Val were decreased in order.

• 한국농업기계학회:학술대회논문집
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• 한국농업기계학회 1996년도 International Conference on Agricultural Machinery Engineering Proceedings
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• pp.863-877
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• 1996

A drying model to predict the drying process in continuous dryer was developed and proved by drying experiments. The experiment showed that the difference of moisture contents between the predicted and the observed was within 0.5%(wb). There was no cracked rice found even in high drying rate with the inlet moisture content over 23%(wb), and tempering treatment in the same temperature reduced the ratio of cracked rice. There was a little difference in the ratio of cracked rice between 40$^{\circ}C$ and 45$^{\circ}C$ drying temperatures with the final drying moisture content (14.5% wb), and the cracked rice increased at 55$^{\circ}C$. As a results, it was better to make fast drying on the rice over 23%(wb) inlet content it was recommended to keep drying at 45$^{\circ}C$.

• Journal of the Korean Wood Science and Technology
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• 제29권3호
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• pp.21-26
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• 2001

Acquisition of precise information on drying characteristics of wood is indispensable for the improvement of drying schedules and wood quality. Recognition of the exact moisture content at which drying defects such as checks occur during drying with given drying conditions may be essential to reduce drying losses. In this study an image-processing system was combined with a laboratory-scale wood dry kiln for experiments and the surface of tree disk of black locust (Robinia pseudoacacia L.) was monitored to investigate the behavior of check formation over all the drying process. This system showed good potential for improving drying schedules and wood product quality.

• Journal of Biosystems Engineering
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• 제34권5호
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• pp.351-357
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• 2009

This study was conducted to verify the simulation model through the drying test, and investigate effect of factors, such as temperature of drying air, airflow rate, and velocity of the airflow, on the drying. The low temperature drying simulation model was developed based on the circulation dry simulation model presented by Keum et al. (1987), and by modifying low temperature thin layer drying model, equilibrium moisture content model, latent heat of vaporization model, and crack ratio prediction model. The heat pump and experimental dryer with a capacity of 150kg were used for the test. The RMSE between the predicted and measured value was 0.27% (drying temperature), 0.15% (crack ratio), and 2.08% (relative humidity), so the relevance of the model was verified. In addition, the effect of drying temperature, airflow rate, and velocity of the airflow on the drying was examined. The experimental results showed that the crack ratio at drying temperature of $25{\sim}40^{\circ}C$ was allowable. Moreover, at below $30^{\circ}C$, variation of the crack ratio was slight, but drying time was delayed. Given these results, the drying temperature of over $30^{\circ}C$ was effective. As the airflow rate increased, required energy dramatically increased. Whereas drying rate slowly increased, so loss of drying efficiency was caused. Considering these results, the dryer needed to be designed and adjusted to lower than $30\;m^3/min{\cdot}ton$. As velocity of the airflow increased, required drying energy increased when the velocity of the airflow was over $5\;m^3$/hr, while crack ratio and drying rate showed little variation.

• Journal of the Korean Wood Science and Technology
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• 제52권1호
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• pp.1-12
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• 2024

Betung bamboo (Dendrocalamus asper) is used as a building and handicraft material in Indonesia; however, bamboo needs to be dried to increase its stability. This study aimed to evaluate the efficiency of drying bamboo using solar energy and different drying oven designs. The betung bamboo pieces were dried using a direct solar dryer (direct drying) and an indirect solar dryer (indirect drying) and then the decrease in levels that occurred based on the relative humidity (RH) and temperature values achieved in the two dryers were compared. The highest average temperature in the direct indirect drying oven compartment was 60.1 ± 13.1℃ with 19.9 ± 16.4% RH and 60.2 ± 11.9℃ with 19.5 ± 15.5% RH, respectively. The drying defect in indirect drying was lower than that in direct drying, and indirect drying had a 61.7% greater average water loss than direct drying with significant difference (95%, analysis of variance) based on water loss/compartment volume parameters. Thus, the solar drying oven can be used to air-dry bamboo (14%) for 7 d from an initial moisture content of 70%-80% in bamboo strips. The results of this research can be used for small-scale bamboo processing industries that have limited use of electrical energy with quite good results.

• 한국수산과학회지
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• 제15권1호
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• pp.107-110
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• 1982

Fixed bed drying method was selected to reduce the initial drying time of squid and the effects of drying air temperature and bed height on the drying rate were investigated, with following results. 1. The drying rate in the fixed bed dryer was faster than that of natural convection type dryer heated indirectly and that of hot air dryer heated directly. 2, Shirai-equation was applicable to squid being dried. Using the equation, drying rate constant obtained was as shown in table 1.

• 한국식품저장유통학회지
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• 제3권1호
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• pp.39-53
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• 1996

Ginseng, one of the important economic crops, is processed into medicine, teas, beverages and even foods. Drying is the most important and burdensome work in the processing of ginseng, so development of ginseng dryer is needed for efficient drying and good quality of ginseng. Investigation of drying model is essential for development of ginseng dryer. Drying models for peeled ginseng were investigated to determine dominant drying factors and fitted with five selected drying models and an empirical model. Thompson and the empirical model showed best fit with the experimental data. Pother experiment is necessary to prove the superiority of the empirical models.

• 설비공학논문집
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• 제22권12호
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• pp.828-836
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• 2010

The drying is a process that involves coupled and simultaneous heat and mass transfer. When a wet solid is subjected to thermal drying, two processes occur simultaneously. Drying is classified according to heat transfer characteristics in terms of conduction, convection and radiation. In thermal drying, radiation is easier to control than conduction and convection drying and involves a relatively simple structure. In this study, we measured energy consumption, surface hardness of paint and surface gloss with variation of surface temperature of drying materials and drying time. Drying characteristics and energy consumption between heating panels and hot air heating have been presented. The present study shows that a dryer using heating panels is more effective than a hot air dryer from the viewpoint of energy conservation. The hot air dryer, however, was not optimized and more studies on various parameters related to drying will need to be investigated for definite comparison of drying characteristics of the dryers. The result, even if limited, would present the effective availability of paint drying.