• 제목/요약/키워드: rate of distillation

검색결과 96건 처리시간 0.025초

우라늄-카드뮴 합금의 제조 및 증류거동에 대한 연구 (A Study on the Fabrication of Uranium-Cadmium Alloy and its Distillation Behavior)

  • 김지용;안도희;김광락;백승우;김시형
    • 방사성폐기물학회지
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    • 제8권4호
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    • pp.261-267
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    • 2010
  • 고온 야금 핵연료 재활용 공정이라고 불리는 파이로 프로세싱은 전망 있는 핵연료 재활용 기술로써 잘 알려져 왔다. 파이로 프로세싱은 증가된 핵확산저항성과 경제적 효율 때문에 미래 원자력 시스템에 있어서 중요하다. 파이로 프로세싱의 기본적인 개념은 핵확산저항성을 향상시키는 악티나이드 그룹의 회수로 볼 수 있다. 파이로 프로세싱에서 중요한 공정 중 하나인 전해제련공정은 사용후핵연료로부터 우라늄과 악타나이드를 같이 회수하는 공정이다. 본 연구에서는 수직형 카드뮴 증류장치를 제작하였다. 773~923K, 0.01torr 이하의 압력조건에서 카드뮴의 증류속도는 $12.3{\sim}40.8g/cm^2-h$를 나타내었다. 고순도 아르곤 분위기의 글러브 박스에서 LCC 전해법으로 우라늄-카드뮴 합금을 제작하였다. 순수한 카드뮴과 우라늄-카드뮴 합금중의 카드뮴 증류거동을 조사하였다. 본 연구에서 얻을 수 있었던 카드뮴 증류거동 연구결과를 카드뮴 증류 공정의 개발에 이용할 수 있을 것이다.

하수처리수 재이용을 위한 직접접촉식 막증발법 적용 가능성 연구 (A Feasibility Study on Sewage Discharge Water Treatment for Water Reuse by Direct Contact Membrane Distillation)

  • 최용준;최지혁;신용현;조형락;손진식;이상호
    • 멤브레인
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    • 제26권1호
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    • pp.70-75
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    • 2016
  • 본 연구에서는 하수처리수를 원수로 사용하여 직접 접촉식 막증발법을 적용하여 원수 온도와 원수 유량 변화에 따른 하수처리수의 COD, TN, TP, TOC의 제거율 변화와 여과플럭스의 변화를 측정하였다. 또한 하수처리수에 의한 분리막의 오염 가역성을 평가하기 위해 1차 증류수만을 사용하여 물리세정을 수행한 후 플럭스의 회복률을 측정하였다. 실험결과 원수의 온도 및 유량에 관계없이 원수가 3배 농축될 때까지 여과를 진행하였음에도 불구하고 하수처리수의 주요 오염물질인 COD, TN, TP, TOC에 대한 제거율이 92% 이상으로 높게 나타났다. 또한 비교적 낮은 온도인 $50^{\circ}C$$60^{\circ}C$에서 원수의 유량에 따라 최소 13.8 LMH에서 20.3 LMH로 높은 여과플럭스를 나타냈다. 그리고 높은 농축계수까지 여과 실험을 진행했음에도 불구하고 낮은 여과플럭스의 감소를 나타냈으며 1차 증류수를 이용한 짧은 시간 동안의 물리세정만으로 최소 90% 이상의 높은 여과 플럭스 회복율을 나타냈다. 따라서 하수처리수 재이용을 위한 공정으로 막증발법의 적용이 충분히 가능할 것으로 판단된다.

Optimization and modification of PVDF dual-layer hollow fiber membrane for direct contact membrane distillation; application of response surface methodology and morphology study

  • Bahrami, Mehdi;Karimi-Sabet, Javad;Hatamnejad, Ali;Dastbaz, Abolfazl;Moosavian, Mohammad Ali
    • Korean Journal of Chemical Engineering
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    • 제35권11호
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    • pp.2241-2255
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    • 2018
  • RSM methodology was applied to present mathematical models for the fabrication of polyvinylidene fluoride (PVDF) dual-layer hollow fibers in membrane distillation process. The design of experiments was used to investigate three main parameters in terms of polymer concentration in both outer and inner layers and the flow rate of dope solutions by the Box-Behnken method. According to obtained results, the optimization was done to present the proper membrane with desirable properties. The characteristics of the optimized membrane (named HF-O) suggested by the Box-Behnken (at the predicted point) showed that the proposed models are strongly valid. Then, a morphology study was done to modify the fiber by a combination of three types of a structure such as macro-void, sponge-like and sharp finger-like. It also improved the hydrophobicity of outer surface from 87 to $113^{\circ}$ and the mean pore size of the inner surface from 108.12 to 560.14 nm. The DCMD flux of modified fiber (named HF-M) enhanced 62% more than HF-O when it was fabricated by considering both of RSM and morphology study results. Finally, HF-M was conducted for long-term desalination process up to 100 hr and showed stable flux and wetting resistance during the test. These stepwise approaches are proposed to easily predict the main properties of PVDF dual-layer hollow fibers by valid models and to effectively modify its structure.

기수담수화와 전력 생산을 위한 폐루프형 압력 지연식 막 증류 공정의 성능 평가 (Performance Evaluation of a Closed-Loop Pressure Retarded Membrane Distillation for Brackish Water Desalination and Power Generation)

  • 조규상;이준서;박기호
    • Korean Chemical Engineering Research
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    • 제60권4호
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    • pp.525-534
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    • 2022
  • 본 연구에서는 물과 전기의 동시 생산이 가능한 pressure retarded membrane distillation (PRMD)의 폐루프식 구성 디자인을 기수담수화에 적용해 최적 운전 조건과 성능 평가를 수행하였다. 시뮬레이션 결과 80 ℃ 이상의 폐열이 공급될 때 순 에너지 생산량이 양수 값을 보이며 90 ℃ 이상일 때 안정적인 전력 생산이 가능한 것을 확인할 수 있었고 최적 유입수 유량은 0.6 kg/s를 나타냈다. 이 조건에서 3 g/L의 기수가 유입될 때 순 에너지 생산량은 2.56 W/m2, 물 플럭스는 8.04 kg/m2/hr의 값을 나타냈다. 기수의 농도가 1-3 g/L로 변화할 때 물 플럭스나 에너지 생산량은 큰 변화가 나타나지 않았고, 해수가 유입수로 사용될 때와 비교하면 더 높은 물 플럭스와 순 에너지 생산량을 보였다. 이를 통해 에너지 생산이라는 측면에 집중한다면 기수를 사용해서 PRMD를 운전하는 것이 더 효율적이라는 것을 확인할 수 있었다.

Preparation of Diacylglycerol from Lard by Enzymatic Glycerolysis and Its Compositional Characteristics

  • Diao, Xiaoqin;Guan, Haining;Kong, Baohua;Zhao, Xinxin
    • 한국축산식품학회지
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    • 제37권6호
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    • pp.813-822
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    • 2017
  • The aim of this study was to prepare diacylglycerol (DAG) by enzymatic glycerolysis of lard. The effects of reaction parameters such as lipase type, reaction temperature, enzyme amount, substrate molar ratio (lard/glycerol), reaction time, and magnetic stirring speed were investigated. Lipozyme RMIM was found to be a more active biocatalyst than Novozym 435, and the optimal reaction conditions were 14:100 (W/W) of enzyme to lard substrate ratio, 1:1 of lard to glycerol molar ratio, and 500 rpm magnetic stirring speed. The reaction mixture was first incubated at $65^{\circ}C$ for 2 h and then transferred to $45^{\circ}C$ for 8 h. At the optimum reaction conditions, the conversion rate of triacylglycerol (TAG) and the content of DAG in the reaction mixture reached 76.26% and 61.76%, respectively, and the DAG content in purified glycerolized lard was 82.03% by molecular distillation. The distribution of fatty acids and Fourier transform infrared spectra in glycerolized lard samples were similar to those in lard samples. The results revealed that enzymatic glycerolysis and molecular distillation can be used to prepare more highly purified DAG from lard.

Effects of Reactor Type on the Economy of the Ethanol Dehydration Process: Multitubular vs. Adiabatic Reactors

  • Yoo, Kee-Youn
    • Korean Chemical Engineering Research
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    • 제59권3호
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    • pp.467-479
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    • 2021
  • Abstract: A kinetic model was developed for the dehydration of ethanol to ethylene based on two parallel reaction pathways. Kinetic parameters were estimated by fitting experimental data of powder catalysts in a lab-scale test, and the effectiveness factor was determined using data from pellet-type catalysts in bench-scale experiments. The developed model was used to design a multitubular fixed-bed reactor (MTR) and an adiabatic reactor (AR) at a 10 ton per day scale. The two different reactor types resulted in different process configurations: the MTR consumed the ethanol completely and did not produce the reaction intermediate, diethyl ether (DEE), resulting in simple separation trains at the expense of high equipment cost for the reactor, whereas the AR required azeotropic distillation and cryogenic distillation to recycle the unreacted ethanol and to separate the undesired DEE, respectively. Quantitative analysis based on the equipment and annual energy costs showed that, despite high equipment cost of the reactor, the MTR process had the advantages of high productivity and simple separation trains, whereas the use of additional separation trains in the AR process increased both the total equipment cost and the annual energy cost per unit production rate.

In-Service Identification of the Heterogeneous Zone in Petrochemical Pipelines by Using Sealed Gamma-Ray Sources $(^{60}Co,\;^{137}Cs)$

  • Kim, Jin-Seop;Jung, Sung-Hee;Kim, Jong-Bum
    • 비파괴검사학회지
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    • 제26권3호
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    • pp.169-173
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    • 2006
  • In-service diagnoses of pipeline facilities are important for a systematic maintenance of them. Field applications by using sealed gamma-ray sources $(^{60}Co,\;^{137}Cs)$ were performed to identify the heterogeneous zone in the pipelines of a distillation tower and a flare stack respectively. From the results, the heterogeneous zones in the pipelines were successfully identified. In the case of the pipeline connected to the distillation tower, a vapor pocket was detected in the fluid under hydrodynamic conditions, which could explain the reason for a decrease of the flow rate. In another case, an area with some amount of catalyst deposits was found at the bottom of the gas pipeline which was connected to the flare stack. And these findings provided important information for the process operators. Diagnosis technique by using gamma radiation sources has been proven to be an effective and reliable method for providing information on a media distribution in a facility.

HDPE의 열분해에 의한 액화 특성 (Liquefaction Characteristics of HDPE by Pyrolysis)

  • 유홍정;이봉희;김대수
    • 폴리머
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    • 제27권1호
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    • pp.84-89
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    • 2003
  • 열분해 온도 및 열분해 시간이 HDPE의 열분해에 미치는 영향을 해석하였다. HDPE 열분해의 시작온도와 활성화에너지는 가열속도가 증가함에 따라 증가하였다. 전환율과 액체수율은 열분해 온도와 시간이 증가함에 따라 계속 증가하였고, 특히 45$0^{\circ}C$에서 열분해 시간에 매우 민감하게 변하였다. 전환율에 있어 열분해 온도가 열분해 시간보다 더 큰 영향을 주었다. 열분해 과정에서 생성된 각각의 액체성분을 한국석유품질검사소 석유제품 품질기준에 기초하여 증류온도에 따라 가솔린, 등유, 경유, 왁스로 분류하여 본 결과, 450 $^{\circ}C$에서는 경유 > 왁스 > 등유 > 가솔린 순이었고, 475$^{\circ}C$와 50$0^{\circ}C$에서는 왁스 > 경유 > 등유 > 가솔린 순이었다.

감압 하에서 마그네슘 합금(AM50) 스크랩 용탕의 증발 거동에 관한 연구 (A Study on the Evaporation Behavior of Magnesium Alloy (AM50) Scrap Melt under Reduced Pressure)

  • 위창현;홍성훈;유병돈
    • 대한금속재료학회지
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    • 제48권3호
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    • pp.241-247
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    • 2010
  • In order to develop the vacuum distillation process of magnesium alloy scrap, a fundamental study on the evaporation behavior of magnesium alloy (AM50) scrap melt was carried out. Melt temperature, pressure, reaction time, and initial specific surface area of melt were considered as experimental variables. The evaporation rate of magnesium increased with the increase of melt temperature and initial specific surface area of melt, and with the decrease of the pressure. The activation energy of magnesium evaporation reaction calculated by an Arrhenius plot decreased with the decrease of the pressure and with the increase of the initial specific surface area of melt. An empirical equation was derived for the evaporation rate of magnesium from AM50 alloy melt.

막 증발법(Membrane Distillation)을 이용한 고농도 하·폐수처리 가능성 연구 (Feasibility study on the application of membrane distillation process to treat high strength wastewater)

  • 김세운;이동우;민경진;조진우
    • 상하수도학회지
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    • 제29권2호
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    • pp.261-269
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    • 2015
  • In this study, we applied a membrane distillation process to investigate a feasibility of treating a wastewater with high concentration of organic matters including nitrogen and phosphorus. The laboratory scale experiment was performed by using a hydrophobic PVDF membrane with the pore size of $0.22{\mu}m$ and porosity of 75%. The installation was direct contact type where the temperature difference between a feed and permeate side was controlled to have a range from 20 to $60^{\circ}C$. We observed a flux variation and a concentration changes of COD, $PO{_4}^{3-}$-P, $NH_4{^+}$-N and conductivity of feed side as well as permeate side with various temperature differences (20 to $60^{\circ}C$), cross flow velocities (0.09 to 0.27 m/s) through the module, and pH (6.6 to 12.0) of the feed that has the initial concentration of COD about 1,000 mg/L, total nitrogen 390 mg/L, total phosphorus 10 mg/L, conductivity of $7,000{\mu}s/cm$. The results showed that the average flux was ranged from 4 to $40L/m^2/hr$ which was almost similar with the flux of NaCl and deionized water used as a feed solution. The lowest flux was obtained at the operating condition with the temperature difference of $20^{\circ}C$ and cross flow velocity of 0.09 m/s while the highest one was measured with $60^{\circ}C$ and 0.27 m/s. Above 99% of COD and $PO{_4}^{3-}$-P in the feed could be rejected regardless of an operating condition. However, the removal rate of ammonium nitrogen was varied from 64 to 99% depending on the pH of feed solution.