• Title/Summary/Keyword: Ethylene adsorbent

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Effect of Ethylene Adsorbent on Apple Fruit Quality during Storage (사과과실 저장성에 미치는 에틸렌흡착제의 효과)

  • Ahn, Young-Jik;Choi, Jong-Seung;Min, Byung-Hoon;Yi, Kyoung-UK
    • The Journal of Natural Sciences
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    • v.8 no.2
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    • pp.169-173
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    • 1996
  • This experiment was conducted to investigate the effect of ethylene adsorbent removing ethylene gas produced from apple fruits in poly ethylene film bag storage. The treatment of ethylene adsorbent was not effected the change in soluble solids and organic acid content of fruits. The fruit softening was remarkably delayed by the absorbent treatment, and the more amount of it was the more effective. The ethylene evolution and respiration of fruits reduced or decreased by this treatment during storage. The ethylene adsorbent for 'Fuji' apple fruit was effective more than 30g per 10kg fruits.

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Development of Ethylene Adsorbent for Fruits Storage (과실 저장성 향상을 위한 에틸렌 흡착제 개발)

  • Ahn, Young-Jik;Choi, Jong-Seung;Yi, Kyoung-Uk
    • The Journal of Natural Sciences
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    • v.8 no.1
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    • pp.81-85
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    • 1995
  • This experiment was conducted to develop ethylene adsorbents for removing the ethylene produced from fruit during storage. The effect of ethylene adsorbent on the removing ethylene was the highest when $ICI_3$and $KBrO_3$ were used as the base of reactant and $H_2SO_4$ auxiliary reagent of reactant. It was decreased under the saturated water vapor condition and was sligthly decreased under the high carbon dioxide condition.

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Adsorption and Desorption Dynamics of Ethane and Ethylene in Displacement Desorption Process using Faujasite Zeolite (제올라이트(faujasite)를 이용한 치환탈착공정에서 에탄, 에틸렌의 흡, 탈착 동특성)

  • Lee, Ji-In;Park, Jong-Ho;Beum, Hee-Tae;Yi, Kwang-Bok;Ko, Chang-Hyun;Park, Sung Youl;Lee, Yong-taek;Kim, Jong-Nam
    • Korean Chemical Engineering Research
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    • v.48 no.6
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    • pp.768-775
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    • 2010
  • Adsorption dynamics of ethane/ethylene mixture gas and desorption dynamics during the displacement desorption with propane as a desorbent in the column filled with faujasite adsorbent were investigated experimentally and theoretically. The simulation that adopted heat and mass balance and an ideal adsorbed solution theory (IAST) for the multicomponent adsorption equilibrium well predicted the experimental breakthrough curves of the adsorption and desorption. At the adsorption breakthrough experiments, roll-ups of ethane increased as the adsorption pressure increased and the adsorption temperature decreased. During the displacement desorption with propane in the column saturated with ethane/ethylene mixture gas, almost 100% of ethylene was obtained for a certain time interval. The adsorption strength of the desorbent greatly affected the adsorption and re-adsorption dynamics of ethylene. The re-adsorption capacity for ethylene has been greatly reduced when iso-propane, which is stronger desorbent than propane, was used as desorbent. It was found from the simulation that the performance of the displacement desorption process would be superior when the ratio of ${(q_s{\times}b)}_{C_2H_4}/{(q_s{\times}b)}_{C_3H_s}$ was 0.83, that is, the adsorption strengths of ethylene and the desorbent were similar.

Preparation of a Novel PU-LMO Adsorbent by Immobilization of LMO on Polyurethane Foam for Recovery of Lithium Ions (폴리우레탄 폼에 LMO를 고정화하여 리튬이온 회수를 위한 새로운 PU-LMO 흡착제의 제조)

  • You, Hae-Na;Lee, Min-Gyu
    • Clean Technology
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    • v.20 no.3
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    • pp.277-282
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    • 2014
  • In this study, PU-LMO was made by immobilization of LMO on urethane foam (PU) with using an EVA as a binder. PU-LMO was characterized by using X-Ray Diffractometer (XRD) and Scanning Electron Microscopy (SEM). The optimal ratio of EVA/LMO for preparation of PU-LMO was 0.26 gEVA/gLMO. The adsorption of lithium ions by PU-LMO was found to follow the pseudo-second-order kinetic model. The equilibrium data fitted well with Langmuir isotherm model and the maximum removal capacity of lithium ions was 17.09 mg/g. The PU-LMO was found to have a remarkably high selectivity of lithium ions and high adsorption capacity because the distribution coefficient ($K_d$) of lithium ion was higher than those of other metal ions.

Steam Activated Carbon Preparation Using HTFBR from Biomass and its Adsorption Characteristics

  • Asirvatham, J. Herbert;Gargieya, Nikhar;Paradkar, Manali Sunil;Prakash Kumar, B.G.;Lima Rose, Miranda
    • Carbon letters
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    • v.9 no.3
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    • pp.203-209
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    • 2008
  • The objective of this work is to study the feasibility of the preparation of the activated carbon (AC) from coconut tree flowers using high temperature fluidized bed reactor (HTFBR). The activating agent used in this work is steam. The reactor was operated at various activation temperature (650, 700, 750, 800 and $850^{\circ}C$) and activation time (30, 60, 120 and 240 min) for the production of AC from coconut tree flowers. Effect of activation time and activation temperature on the quality of the AC preparation was observed. Prepared AC was characterized in-terms of iodine number, methylene blue number, methyl violet number, ethylene glycol mono ethyl ether (EGME) surface area and SEM photographs. The best quality of AC from coconut tree flowers (CFC) was obtained at an activation temperature and time of $850^{\circ}C$ and 1 hr restectively. The effectiveness of carbon prepared from coconut tree flowers in adsorbing crystal violet from aqueous solution has been studied as a function of agitation time, carbon dosage, and pH. The adsorption of crystal violet onto AC followed second order kinetic model. Adsorption data were modeled using both Langmuir and Freundlich classical adsorption isotherms. The adsorption capacity $q_m$ was 277.78 mg/g., equilibrium time was found to be 180 min. This adsorbent from coconut tree flowers was found to be effective for the removal of CV dye.