• Title/Summary/Keyword: drying process

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Effect of Coagulation of Filler Particles on the Dewatering and Drying of the Particles (충전물의 Coagulation이 탈수 및 건조효율에 미치는 영향)

  • Yoon, byoung-Tae;Ow, Say-Kyoun;Jeon, Yang
    • Journal of Korea Technical Association of The Pulp and Paper Industry
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    • v.30 no.2
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    • pp.40-46
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    • 1998
  • This study was aimed to investigate any improvement of dewatering and energy saving on the papermaking process when the various types of fillers were used, i.e., clay, talc and grounded calcium carbonate (GCC). Cationic polyelectrolyte and alum coagulants neutralized the surface charge of the filler particles and the filler particles were coagulated. The rates of dewatering and drying were investigated. The results indicated that clay tended to intense anion, while talc and GCC tended to anion trend nearly to neutrality. Clay and talc added with EPI-DMA, P-DADMAC and alum respectively as optimum levels showed a significant efficiency on the dewatering and the turbidity dissipation. However, the turbidity and dewatering rate of GCC decreased, when GCC was added with EPI-DMA and P-DADMAC respectively Drying rate of clay was increased when coagulant added. However drying rates of talc and GCC were not affected by coagulant, while the apprarent drying time of talc and GCC in the absence of any coagulant was shorter than the clay in the presence of a coagulant. The result confirmed that talc or GCC was more efficient than clay on the dewatering and drying, which is consistent with a general knowledge in the collodal science.

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The Evaluation for Quality Characteristics of Drying Flowering Plant by Vacuum-Freeze (진공 동결에 의한 건조 화훼류의 품질특성 평가에 관한 연구)

  • Kim, J.D.
    • Journal of Power System Engineering
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    • v.15 no.4
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    • pp.5-10
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    • 2011
  • In case of using rapid vacuum-freeze drying for high quality dry flower of flowering plant, the morphological and physiological characteristics of dry rose showed as the following. The dry ratio of about 82% presented after 1 day in case of using rapid vacuum-freeze drying and it was reached that the optimum storage water content of general dry products was 18%. The dry ratio of about 89% presented after 4 days. This result indicates very short dry time comparing with natural dry time of 12 days. Also, the morphological characteristics of flowering plant in case of vacuum-freeze drying showed similar shape with real flower. The contraction decreased about 9% comparing with real flower under dry time of 72 hours. But the contraction in case of natural dry decreased 36% and showed noticeable difference. The brightness which affects physiological characteristics of dry flowering plant showed lower values according to the dry process and chromaticity was thick. After 4 days, natural dry was thick with about 2 times comparing with vacuum-freeze drying. In case of vacuum-freeze drying, the quantity of anthocyanin and chlorophyl which affect discoloration and bleaching of dry flowering plant showed the clear difference comparing with natural dry method due to the sublimation by vacuum after rapid freeze with short initial time.

Finite Difference Evaluation of Moisture Profile in Boxed-heart Large-cross-section Square Timber of Pinus densiflora during High Temperature Drying

  • Kim, Hyunbin;Han, Yeonjung;Park, Yonggun;Yang, Sang-Yun;Chung, Hyunwoo;Eom, Chang-Deuk;Lee, Hyun-Mi;Yeo, Hwanmyeong
    • Journal of the Korean Wood Science and Technology
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    • v.45 no.6
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    • pp.762-771
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    • 2017
  • Predicting the amount and distribution of moisture content within wood allows calculating the various mechanical dynamics of the wood as well as determining the drying time. For boxed-heart wood with a large cross-section, since it is difficult to measure the moisture content of the interior, it is necessary to predict the moisture content distribution. This study predicted the moisture movement in boxed-heart red pine timber, during high temperature drying, by using the three-dimensional finite difference method for the efficient drying process. During drying for 72 h, the predicted and actual moisture content of the tested wood tended to decrease at a similar rate. In contrast, the actual moisture content at 196 and 240 h was lower than predicted because surface checking of the wood occurred from 72 h and excessive water emission was unexpectedly occurred from the checked and splitted surface.

Eco-Friendly Drying Technology using Superheated Steam (과열 증기 이용 친환경 건조기술)

  • Kim, Og Sin;Lee, Dong Hyun;Chun, Won Pyo
    • Korean Chemical Engineering Research
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    • v.46 no.2
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    • pp.258-273
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    • 2008
  • For being recent high oil price age, the interest in superheated steam drying technology is increasing as the method to enhance the energy efficiency of drying process consuming a lot of energy. This technology uses the superheated steam as drying medium to dry the materials and has advantages that can save the energy by recycling the evaporated high-temperature steam, enhance the quality of dried products, and minimize the exhaust of environmental pollution materials. In this work, it has been introduced from general drying principle to the principle and related studies of drying technology using superheated steam, using examples of superheated steam with dryer types, and industrial applications.

The Effect of Dry Methods for Synthesized Yttria-doped Ceria by Co-precipitation (공침법으로 제조된 Yttira Doped Ceria분체의 건조방법에 따른 입자특성 고찰)

  • 변윤기;이상훈;최성철
    • Journal of the Korean Ceramic Society
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    • v.40 no.8
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    • pp.798-803
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    • 2003
  • In synthesis of nano powders, the hard agglomeration for the synthesized powders occurred during the drying processing. In order to avoid hard agglomeration in particles the freeze drying process was used in this experiment. e fabricated the Yttira-Doped Ceria(YDC) nano powder by co-precipitation. Starting materials used in experiments were the cerium(III) nitrate and yttrium(III) nitrate solution with 야-water, which two solutions were mixed and then the precipitated hydroxides were prepared for adding sodium hydroxide. The co-precipitated powders were dried by the thermal drying at 8$0^{\circ}C$ for 24 h and by freeze drying at -4$0^{\circ}C$, 30 mtorr for 72 h. The lattice parameter and crystallite size as a function of calcination temperature was characterized by XRD analysis. The lattice parameter of YDC was decreased with addition amount of yttrium and was estimated as 5.401683 $\AA$ at $700^{\circ}C$. Crystallite size were calculated by XRD-LB method, and morphologies were confirmed with the observation of TEM and SEM. The freeze dried YDC powders had medium diameter of 17 nm with more uniform size distribution than the thermal dried YDC posers, which were mainly ascribed to the difference of agglomerates formation during drying stage.

Effect of Cyclic Drying-Wetting on Compressive Strength of Decomposed Granite Soils (습윤-건조 반복작용으로 인한 화강풍화토의 압축강도 특성 변화 연구)

  • Yoo, Chung-Sik
    • Journal of the Korean Geosynthetics Society
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    • v.10 no.4
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    • pp.19-28
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    • 2011
  • This paper presents the results of an investigation into the effect of cyclic wetting-drying on the compressive strength characteristics of decomposed granite soils. A series of plane strain compression (PSC) tests were performed on test specimens with varying fine contents under different wetting-drying cycles to investigate the change in compressive strength under the process of wetting-drying cycles. The effect of wetting-drying cycles on the structural particle rearrangement at a micro-scale level was also examined using scanning electron microscope (SEM) tests. It was shown that the soil containing larger fines showed more significant decrease in compressive strength compared with the soils with less fines. Also found was that the wetting-drying cycle did not have significant effect on the particle arrangement.

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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Effects of Rehydration Methods on viability after Freeze-drying of Streptomyces aureofaciens (Streptomyces aureofaciens 동결건조후 재수화 방법이 생존도에 미치는 영향)

  • Lee, Hyean-Woo;Yi, Dong-Heui;Lee, No-Woon
    • Applied Biological Chemistry
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    • v.38 no.6
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    • pp.512-515
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    • 1995
  • In order to examine the effect of rehydration methods on viability after freeze-drying of Streptomyces aureofaciens, we labeled the DNA of S. aureofaciens with $^3H-adenine$. Extracellular radioactivity levels appeared to be high in the rehydrated solutions after freeze-drying than freezing-thawing. In effects of rehydration after freeze-drying, the viability of the cell appeared about 20% in case of with admitting air at single ampule, but that of which appeared about 91% in case of without admitting air at double ampule. Thus, S. aureofaciens cells were damaged during the process of rehydration after freeze-drying.

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The Estimated Drying Schedule of Fagaceae Four Species Grown in Kangwon-Do (II) (강원도산(江原道産) 참나무과(科) 4수종(樹種)의 추정건조(推定乾操)스케줄(제2보))

  • Park, Jong-Su;Kim, Su-Chang
    • Journal of Forest and Environmental Science
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    • v.12 no.1
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    • pp.1-12
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    • 1996
  • This study was carried out to estimate drying schedule of Fagaceae four species grown in Kangwon-Do by oven-drying at $100^{\circ}C$ which aimed to elucidate the characteristics such as current moisture content, drying process, initial check, collapse and internal check during drying following each board thickness (1.5cm, 2.5cm, 3.5cm, 4.5cm). The results were as follows; Current moisture content of each board showed a rapid drying curve with the high initial moisture content of board. With the high initial moisture content, the incease of board thickness and the slowness of changing rate of moisture content, species took long to do drying. Also, the initial conditions of drying had to be mild condition with the increase of board thickness.

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Drying Characteristics of Radishes using Far Infrared Ray Dryer

  • Park, Bum-Soon;Kang, Tae-Hwan;Lee, Jeong-Hyeon;Choi, Jong-Min;Han, Chung-Su
    • Journal of Biosystems Engineering
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    • v.40 no.1
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    • pp.61-66
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    • 2015
  • Purpose: The purpose of this study was to establish conditions to dry a radish by examining the drying and quality characteristics depending on the air temperature and velocity of a far infrared conveyor dryer. Methods: A sample of weighing 6 kg was dried until the moisture content reached $15{\pm}0.5%$ (w.b.). Four temperatures (50, 60, 70, and $80^{\circ}C$) and three air velocity levels (0.4, 0.6, and 0.8 m/s) were employed as the drying factors. Results: The drying rate increased with the increase in the temperature and air velocity but decreased with time. However, the drying rate was influenced by temperature rather than velocity. At a temperature $50^{\circ}C$ with a air velocity of 0.4 m/s, it took 350 min for the radish to dry which was the longest drying time; $80^{\circ}C$ with a air velocity of 0.8m/s, it took 180 min for the radish to dry, which was the shortest drying time. ${\Delta}E$ (the color difference value) increased with the increase in temperature and air velocity. The browning and rehydration ratio increased as the temperature rose. Energy consumption decreased with the increased temperature and air velocity. Conclusions: Based on the results of this study, the best drying conditions for the radish were determined to be a temperature of $70^{\circ}C$ with an air velocity of 0.8 m/s.