• International journal of advanced smart convergence
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• 제4권1호
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• pp.127-136
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• 2015

This paper is a study of a simple distillation process. Its objective is to compare fuel production from plastic waste, its data collecting is from the factory and simple data calculated a suitable evaluation on the simple distillation plant built before calculation. The experiment with a simple distillation process is separated into three sections. The first section is a simple distillation process of distillation producing diesel using heat source by biomass. The second section is distillation process which produces fuel using heat source by burner. The third section uses heat source by burner incorporate with biomass. The experiment reveals that the result of the second section is the most efficient. In comparison with the experiments and the simple calculation, the result on the efficiency of work has error less than 5% and it is sufficient for the next experimental process. Thus, the study and design on a simple distillation process produces fuel from plastic waste has to concern mainly on design heat exchangers, flow rate and optimized temperature. Further study on this plant can be developed throughout the county due to its low cost and efficiency.

• 제어로봇시스템학회논문지
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• 제8권10호
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• pp.842-846
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• 2002

Design of gas concentration process using a fully thermally coupled distillation is conducted with the commercial design software HYSYS. Detailed procedure of the design is explained, and the performance of the process is compared with that of a conventional system A structural design is exercised for the design convenience. The design outcome indicates that the procedure is simple and efficient. The structural information yielded from equilibrium distillation gives an easy formulation of distillation system which is the initial input required from the setup of the distillation system The performance of the new process indicates that an energy saving of 17.6 % is obtained compared with the conventional process while total number of trays maintains at the same.

• 제어로봇시스템학회논문지
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• 제8권10호
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• pp.833-841
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• 2002

We develope a model that can manipulate the reflux ratio of a batch distillation process in real time for optimal operations. Firstly, reflux ratio decision model for batch distillation unit was developed using the simple short-cut method. Secondly, more detailed rigorous method was applied to improve the accuracy of the model. Based on these models, operational strategies for the optimal reflux ratio was proposed. The results are illustrated with suitable examples and compared with the results using commercial simulator.

• 청정기술
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• 제17권1호
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• pp.56-61
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• 2011

감압잔사유를 고압 회분식 반응기에 넣고, 상용 Ni-Mo/$Al_2O_3$ 촉매를 이용하여 $450^{\circ}C$, $500^{\circ}C$에서 수첨분해하였다. 그리고 반응 생성물을 단증류 혹은 GC-SIMDIS 방법으로 각각 분석하였다. 먼저 수첨분해반응에서는 두 온도 조건 모두 촉매 반응뿐만 아니라 열분해 반응도 같이 일어나고 있음을 확인하였고, 온도가 증가할수록 전환율이 증가하고, 생성물 중 가솔린 및 납사 비율이 높아졌다. 생성물 분석 결과, $500^{\circ}C$ 반응에서는 단증류와 GC-SIMDIS 분석 결과의 차이가 없었지만, $450^{\circ}C$ 반응에서는 단증류에서는 디젤이, GC-SIMDIS에서는 vacuum gas oil이 주 생성물로 드러났다. 이는 $450^{\circ}C$ 반응에서의 단증류 분석은 단증류에 의한 열분해 반응으로 인해 생성물의 선택도가 정확하지 않음을 알려준다.

• 한국식품영양학회지
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• 제12권4호
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• pp.358-363
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• 1999

This study was conducted to evaluate the extraction methods for the determination of antioxidants in soybean oil. Recovery rates of various antioxidants in soybean oil showed similar rates as 80.4~102.1% by solvent/solvent extraction method and 89.9~106.4% by sweep co-distillation method except 46.6~61.2% of PG at corresponding spiked concentractions. The maximun recovery rates of antioxidnts were obtained when extraction time and extraction temperature used in UNITREX were 20min and 21$0^{\circ}C$ respectively. In the recovery rates with the activation of florisil when 2% ofwater was added to florisil the highest recovery rates for TBHQ, BHA, BHT were obtained by sweep co-distillation met-hod. Therefore sweep co-distillation method showed less solvent simple operation and high recovery rate compared with solvent/solvent extraction method.

• Journal of Radiation Protection and Research
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• 제48권2호
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• pp.77-83
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• 2023

Background: The purpose of this study is to purify uranium (U[VI])-contaminated soil-flushing effluent using the precipitation-distillation process for clearance. Precipitation and distillation are commonly used techniques for water treatment. We propose using a combination of these methods for the simple and effective removal of U(VI) ions from soil-flushing effluents. In addition, the U concentration (Bq/g) of solid waste generated in the proposed treatment process was analyzed to confirm whether it satisfies the clearance level. Materials and Methods: Uranium-contaminated soil was decontaminated by soil-flushing using 0.5 M sulfuric acid. The soil-flushing effluent was treated with sodium hydroxide powder to precipitate U(VI) ions, and the remaining U(VI) ions were removed by phosphate addition. The effluent from which U(VI) ions were removed was distilled for reuse as a soil-flushing eluent. Results and Discussion: The purification method using the precipitation-distillation process proposed in this study effectively removes U(VI) ions from U-contaminated soil-flushing effluent. In addition, most of the solid waste generated in the purification process satisfied the clearance level. Conclusion: The proposed purification process is considered to have potential as a soil-flushing effluent treatment method to reduce the amount of radioactive waste generated.

• 제어로봇시스템학회:학술대회논문집
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• 제어로봇시스템학회 1990년도 한국자동제어학술회의논문집(국내학술편); KOEX, Seoul; 26-27 Oct. 1990
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• pp.234-239
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• 1990

A neural controller for process control was proposed that combines a simple feedback controller with a neural network. This control was applied to distillation control. The feedback error learning technique was used for on-line learning. Important characteristics on neural controller were analyzed. The proposed neural controller can cope well with strong interactions, significant time delays, sudden changes in process dynamics without any prior knowledge of the process. It was shown that the neural controller has good features such as fault tolerance, interpolation effect and random learning capability

• 한국산학기술학회논문지
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• 제12권5호
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• pp.2445-2450
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• 2011

화학공정 모사 소프트웨어인 HYSYS를 사용하여 Reformate 분리 공정을 열복합 증류탑으로 설계하였다. 열복합 증류탑 설계 방법을 자세히 하였고, 모사 결과를 일반 증류탑과 비교한 결과 제시된 열복합 증류탑 설계 방법이 간단하고 효율적이라는 것을 알 수 있었다. 같은 tray 단수하에서 열복합 증류탑은 일반 증류탑 대비 약 12.2% 에너지가 절약됨을 알 수 있었다.

• 청정기술
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• 제14권4호
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• pp.275-280
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• 2008

연구에서는 LCD 제조 공정에서 배출되는 스트리퍼와 디벨로퍼 혼합 폐액(SD폐액)과 스트리퍼 폐수의 효과적 분리 및 처리를 위한 가능한 기술로서 추출공정과 증류공정의 기술적/경제적 타당성을 검토하였다. SD폐액과 스트리퍼 폐수의 추출분리를 위한 용매로 $CHCl_3$가 여러 가지 관점에서 가장 적절한 용매로 확인되었다. 또한 SD폐액 분리 회수를 위한 공정으로서 추출공정과 증류공정의 두 가지 공정에 대하여 정밀 전산모사를 수행한 결과 $CHCl_3$를 이용한 추출분리공정이 단순증류공정보다 6배 정도 에너지 소요비용이 적게 소요됨을 확인할 수 있었다.

• 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.