• Title/Summary/Keyword: Batch

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Removal of Inorganic Nitrogen and Phosphorus from Cow s Liquid Manure by Batch Algal Culture

  • KIM, MAM-SOO;MOO-YOUNG PACK
    • Journal of Microbiology and Biotechnology
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    • 제3권3호
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    • pp.214-216
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    • 1993
  • Cow's liquid manure (CLM), an animal waste, was treated by a batch algal culture to remove inorganic nutrients. CLM used in this study was especially high in concentrations of inorganic nitrogen and phosphorus. The optimum dilution ratio of the CLM for maximum algal growth was 1:25. Ninety five percent of inorganic nitrogen and 100% of inorganic phosphorus were removed from the CLM with a dilution ratio of 1:25.

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Fuzzy Learning Control: Application to an Industrial Polymerization Reactor

  • Seokho-Yi;Park, Sunwon-
    • 한국지능시스템학회:학술대회논문집
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    • 한국퍼지및지능시스템학회 1993년도 Fifth International Fuzzy Systems Association World Congress 93
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    • pp.1106-1108
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    • 1993
  • This paper deals with an industrial application of a fuzzy feedback combined learning control to an industrial batch free radical polymerization reactor. As a result, the plant has reduced the batch reaction time by 50 minute and stabilized both by 40 percent reduction of the standard deviations of product qualities, such as the total solid content and the graft gum, and by 45 percent reduction of the standard deviation of the batch reaction end time.

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M/M(a, b ; ${\mu}_k$)/1 배치 서비스 대기모델에 대한 연구 (A Study on M / M (a, b ; ${\mu}_k$) / 1 Batch Service Queueing Model)

  • 이화기;정경일
    • 대한산업공학회지
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    • 제21권3호
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    • pp.345-356
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    • 1995
  • The aim of this paper is to analyze the batch service queueing model M/M(a, b ; ${\mu}_k/1$) under general bulk service rule with mean service rate ${\mu}_k$ for a batch of k units, where $a{\leq}k{\leq}b$. This queueing model consists of the two-dimensional state space so that it is characterized by two-dimensional state Markov process. The steady-state solution and performane measure of this process are derived by using Matrix Geometric method. Meanwhile, a new approach is suggested to calculate the two-dimensional traffic density R which is used to obtain the steady-state solution. In addition, to determine the optimal service initiation threshold a, a decision model of this queueing system is developed evaluating cost of service per batch and cost of waiting per customer. In a job order production system, the decision-making procedure presented in this paper can be applicable to determining when production should be started.

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Optimization of Growth and Astaxanthin Production by Phaffia rhodozyma AJ-6 in Fed-batch Culture

  • 김수진;유연우
    • 한국생물공학회:학술대회논문집
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    • 한국생물공학회 2000년도 춘계학술발표대회
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    • pp.271-274
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    • 2000
  • A study was carried out to select a nitrogen source and the optimize the C/N ratio for the maximum cell growth of Phaffia rhodozyma in fed-batch culture. The yeast extract was the best organic nitrogen source. In the batch culture experiments, the highest cell yield was obtained 0.575 g-cell/g-glucose from 10 g/L and 10 g/L yeast extract. In the fed-batch experiments, the maximum cell concentration was obtained 33.1 g/L from the C/N ratio of 2:1 while the astaxanthin concentration of cell was Increased by increasing the C/N ratio, of feed medium.

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Production of Mannitol Using Leuconostoc mesenteroides NRRL B-1149

  • 김창영;이진하;김병훈;유선권;소은성;조갑수;Donal F. Day;김도만
    • Biotechnology and Bioprocess Engineering:BBE
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    • 제7권4호
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    • pp.254-254
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    • 2002
  • A process for the production of mannitol from fructose (5% to 25%) using Leuconosyoc mesenteroides NRRL B-1149 was investigated. Fermentations were carried out in bat도 of fed-batch fermentations without aeration at 28℃, pH 5.0. When 5% fructose was used in batch culture fermentation, the yield of mannitol was 78% of that expected theoretically. When the fructose concentration was increased to 10%, the yield dropped to 59.6% of the theoretical value. However, in the fed-batch culture, using 10% fructose, the yield was 81.9% of the theoretical value. In a 15% fructose fed-bat도 culture, with 5% fructose being added initially and the other 10% fructose being added as a continuous supply, the final yield was 83.7% of the theoretical yield. When 20% fructose was used in the same manner, the yield was 89.5% of theoretical yield.

Pseudomonas putida의 유가배양연구 (A Study of Pseudomonas putida Fed-batch Culture)

  • 김인호;김희정;송재양
    • KSBB Journal
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    • 제17권3호
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    • pp.307-310
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    • 2002
  • 교반속도가 증가함에 따라, 비성장속도가 증가하여 P. putida가 호기적 조건에서 더 잘 성장함을 알 수 있었다. pH를 조절하지 않았을 경우와 달리 암모니아 수용액을 이용하여 pH를 5.0, 7.0으로 조절했을 때, 포도당의 소모량이 증가 할 뿐 아니라 비성장 속도가 증가하였다($\mu$=0.27 --> 0.42). 포도당만을 공급할 것이 아니라 yeast extract와 같은 유기 질소원 다른 기질도 같이 공급함으로써, 보다 많은 균체량을 얻을 수 있었다.

투과증발과 유기산 저생성 균주를 이용한 부탄올 추출발효 (Extractive Butanol Fermentation Using Pervaporation and a Low Acid Producing Strain)

  • 윤지용
    • KSBB Journal
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    • 제15권4호
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    • pp.380-387
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    • 2000
  • An extractive fermentation process using pervaporation was studied in a 7 liter fermentor. Pervaporation was performed using a silicone membrane module and a low-acid-producing strain Clostridium acetobutylicu, B18 was used to produce butanol. In batch culture without pervaporation pH 5.5 and initial glucose concentration of 60 g/L resulted in the highest butanol productivity (0.216 g/L$.$h) with butanol yield of 0.261 Butanol flux through the membrane was best at 2.0 L/min-tubing of air flow rate In batch and fed-batch fermentation glucose consumption rate increased by 1.3 times with pervaporation.

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Fed-Batch 실험장치(實驗裝置)를 이용한 질산화(窒酸化) 미생물(微生物)들의 최대(最大) 성장율(成長率)의 결정(決定)에 관한 실험적(實驗的) 연구(硏究) (Rapid Determination of the Maximum Specific Growth Rates of Nitrogen Oxidizing Bacteria by Fed-Batch Experiments)

  • 이병희
    • 상하수도학회지
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    • 제10권3호
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    • pp.55-63
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    • 1996
  • Nitrification reaction consists of two reactions: nitritification which oxidizes ammonia nitrogen to nitrite nitrogen and nitratification which oxidizes nitrite nitrogen to nitrate nitrogen. Each reaction is carried out by Nitrosomonas and Nitrobacter, respectively. The effective maximum growth rates for both bacteria have to be determined to design aeration tank whenever the aeration tanks have to nitrify ammonia nitrogen in influent. And these values are very important to use mathematical models such as IAWPRC model to simulate nitrification in activated sludge. There are several methods to determine these valves, however, the Fed-Batch experiments can determine these values within 72 hours. In this study, the mathematical equations and experimental procedures for Fed-Batch test are presented. Also, the experimental data and reported values are compared. The estimated mean values of maximum specific growth rates for Nitrosomonas and Nitrobacter are $0.5010day^{-1}$ and $0.6704day^{-1}$, respectively.

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Batch Scheduling Problem with Multiple Due-dates Constraints

  • Mohri, Shintaro;Masuda, Teruo;Ishii, Hiroaki
    • Industrial Engineering and Management Systems
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    • 제10권1호
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    • pp.1-6
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    • 2011
  • This paper describes the issue of batch scheduling.In food production, the lead-time from produc-tion to sale should be decreased becausefreshness of the product is important. Products are shipped at diverse times depending on a demand of sellers, because the types of sellers has become diversified such as super-markets, convenience stores and etc. production of quantity demanded must be completed by time to ship it then. The authors consider a problem with due-dates constraints and construct the algorithm to find the opti-mal schedule that satisfy the due-dates constraint, batch size constraint, inventory time constraint and mini-mize total flow time.

비선형 예측제어 알고리즘을 이용한 회분식 중합 반응기의 온도제어 (Temperature control of a batch polymerization reactor using nonlinear predictive control algorithm)

  • 나상섭;노형준;이현구
    • 제어로봇시스템학회:학술대회논문집
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    • 제어로봇시스템학회 1996년도 한국자동제어학술회의논문집(국내학술편); 포항공과대학교, 포항; 24-26 Oct. 1996
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    • pp.1000-1003
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    • 1996
  • Nonlinear unified predictive control(UPC) algorithm was applied to the temperature control of a batch polymerization reactor for polymethylmethacrylate(PMMA). Before the polymerization reaction is initiated, the parameters of the process model are determined by the recursive least squares(RLS) method. During the reaction, nonlinearities due to generation of heat of reaction and variation of heat transfer coefficients are predicted through the nonlinear model developed. These nonlinearities are added to the process output from the linear process model. And then, the predicted process output is used to calculate the control output sequence. The performance of nonlinear control algorithm was verified by simulation and compared with that of the linear unified predictive control algorithm. In the experiment of a batch PMMA polymerization, nonlinear unified predictive control was implemented to regulate the temperature of the reactor, and the validity of the nonlinear model was verified through the experimental results. The performance of the nonlinear controller turned out to be superior to that of the linear controller for tracking abrupt changes in setpoint.

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