• 제목/요약/키워드: reaction conditions

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볏짚화학펄프의 표백에 관한 연구(제2보) -2단 표백- (Studies on the Bleaching of Rice-Straw Chemical Pulp (II) -Two-Stages Bleaching-)

  • 강진하;박성종;박성철
    • 펄프종이기술
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    • 제33권3호
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    • pp.84-99
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    • 2001
  • This study was carried out to acquire basic data necessary for the use of rice-straw chemical pulp. It investigated the proper bleaching conditions when rice-straw chemical pulp(alkaline sulfite-${Na_2}{S_2}{O_4}$) was bleached using the various kinds of bleaching agents by the two-stages bleaching methods. And, physical properties of pulps bleached with eight kinds of two-stages bleaching methods were tested. The results of this study were as follow; 1. The first-stage bleaching was conducted under the proper conditions with chlorine(C). And then, the proper conditions related to the calcium chlorite(H), hydrogen peroxide(P) and sodium hydrosulfite(Y) bleaching as the second-stage bleaching were investigated. The proper conditions of CH stage were determined to be 0.3% concentration of calcium chlorite, $30^{\circ}C$ of reaction temperature and 20min. of reaction time. For CP stage, the proper conditions of concentration of hydrogen peroxide, reaction temperature and reaction time were 1.5%, $60^{\circ}C$ and 90min., respectively. And for CY stage, the proper conditions were 0.5% concentration of sodium hydrosulfite, $40^{\circ}C$ of reaction temperature and 90min. of reaction time. 2. The first-stage bleaching was conducted under the proper conditions with chlorine dioxide(D). And then, the proper conditions related to the calcium chlorite(H), hydrogen peroxide(P) and sodium hydrosulfite(Y) bleaching as the second-stage bleaching were investigated. The proper conditions of DH stage were determined to be 0.5% concentration of calcium chlorite, $25^{\circ}C$ of reaction temperature and 5min. of reaction time. For DP stage, the proper conditions of concentration of hydrogen peroxide, reaction temperature and reaction time were 1.0%, $70^{\circ}C$ and 90min., respectively. And for DY stage, the proper conditions were 0.3% concentration of sodium hydrosulfite, $50^{\circ}C$ of reaction temperature and 20min. of reaction time. 3. The first-stage bleaching was conducted under the proper conditions with calcium chlorite(H). kAnd then, the proper conditions related to the hydrogen peroxide(P) and sodium hydrosulfite(Y) bleaching as the second-stage bleaching were investigated. The proper conditions of HP stage were determined to be 0.3% concentration of hydrogen peroxide, $30^{\circ}C$ of reaction temperature and 60min. of reaction time. For HY stage, the proper conditions of concentration of sodium hydrosulfite, reaction temperature and reaction time were 2.5%, $60^{\circ}C$ and 30min., respectively. 4. When the rice-straw chemical pulps were bleached with eight kinds of two-stages bleaching methods in the proper conditions mentioned above, respectively, the final brightnesses after CH, CP, CY, DH, DP, DY, HP, and HY bleachings were 62.0, 74.3, 61.4, 58.9, 66.9, 62.9, 50.4 and 60.1, respectively. And strengthes of pulps bleached with DP and DH methods were comparatively higher than those of pulps bleached with other bleaching methods.

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OPTIMALITY CONDITIONS FOR OPTIMAL CONTROL GOVERNED BY BELOUSOV-ZHABOTINSKII REACTION MODEL

  • RYU, SANG-UK
    • 대한수학회논문집
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    • 제30권3호
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    • pp.327-337
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    • 2015
  • This paper is concerned with the optimality conditions for optimal control problem of Belousov-Zhabotinskii reaction model. That is, we obtain the optimality conditions by showing the differentiability of the solution with respect to the control. We also show the uniqueness of the optimal control.

볏짚화학펄프의 표백에 관한 연구 (Studies on the Bleaching of Rice-Straw chemical Pulp(I))

  • 강진하;박성종
    • 펄프종이기술
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    • 제32권3호
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    • pp.65-74
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    • 2000
  • This study was carried out to acquire basic data necessary for the use of rice-straw chemical pulp. It investigated the proper bleaching conditions when rice-straw chemical pulps(alkaline sulfite-Na2S2O4 pulp) were bleached with the various kinds of bleaching agents. And physical properties of bleached pulps were tested. The results of this study were as follows; 1, The proper conditions of chlorine sequence were determined to be 4% concentration of chlorine 25$^{\circ}C$ of reaction temperature and 50 minutes of reaction time. 2. For calcium hypochlorite sequence the proper conditions of chemical concentration reac-tion temperature and reaction time were 3% 25$^{\circ}C$ and 20 minutes respectively. 3. For chlorine dioxide sequence the proper conditions were 1% concentration of chlorine dioxide 70$^{\circ}C$ of reaction temperature and 2hr. of reaction time. 4. The proper conditions of hydrogen peroxide sequence were 1.5% concentration of hydro-gen peroxide 70$^{\circ}C$ of reaction temperature and 1hr. of reaction time respectively. 5. When the rice-straw chemical pulp were bleached with four kinds of bleaching agents methioned above in the proper conditions respectively brightnesses were the order of chlorine dioxide calcium hypochlorite, chlorine, hydrogen peroxide. And strengthes of pulps bleached with chlorine dioxide and hydrogen peroxide were higher than those of pulps bleached with other bleaching agents.

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천연가스를 이용한 자열개질기의 운영조건에 대한 수치해석 연구 (Numerical Study on operating conditions of Autothermal Reformer using natural gas)

  • 김진욱;김상우;박달영;전상희;이도형
    • 한국신재생에너지학회:학술대회논문집
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    • 한국신재생에너지학회 2010년도 추계학술대회 초록집
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    • pp.91.1-91.1
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    • 2010
  • The Reforming system is an effective method to generate hydrogen which uses for fuel cell system. The purpose of this study is to present characteristics of an autothermal reformer at various operating conditions and to investigate ideal conditions for reforming efficiency. Dominant chemical reactions are Full Combustion, Steam Reforming reaction, Water-Gas Shift reaction and Direct Steam Reforming reaction. Operating parameters of the autothermal reformer are inlet temperature, Oxygen to Carbon Ratio, Steam to Carbon Ratio and Gas Hourly Space Velocity. Autothermal reformer is filled with catalysis of a packbed-bed type. Using numerical approach, we have investigated on various reaction conditions.

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Optimal Reaction Conditions for Minimization of Energy and Byproducts in a Poly(ethylene terephthalate) Process

  • Ha, Kyoung-Su;Rhee, Hyun-Ku
    • 제어로봇시스템학회:학술대회논문집
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    • 제어로봇시스템학회 1999년도 제14차 학술회의논문집
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    • pp.248-251
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    • 1999
  • The optimal reaction conditions are determined for a PET process, which consists of transesteriflcation, prepolymerization and polycondensation reactors in series. Based on the simulation results of the reactor system, we scrutinize the cause and effect between the reaction conditions and the final properties of the polymer product. We then select the process variables with significant influence on the properties of polymer as control variables and calculate the optimal reaction conditions by iterative dynamic programming (IDP) algorithm with constraints. A new reaction scheme incorporating reactions for by-products as well as three main reactions is considered in the constrained IDP method.

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치관보철용 Hydroxyapatite의 기계적 물성에 미치는 pH 및 반응온도의 영향 (Effect of pH and Reaction Temperature on Mechanical Properties of Hydroxyapatite for Dental prosthesis)

  • 정인성;허호영
    • 대한치과기공학회지
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    • 제26권1호
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    • pp.89-96
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    • 2004
  • Hydroxyapatite powder were synthesized by precipitation method, varying pH, and reaction temperature. The powders were heated at 1,200$^{\circ}{\cdots}$ and 1,300$^{\circ}{\cdots}$ for fabrication of dental prosthesis. The results are as follows: Synthesized powder showed the smallest particle in size, under the conditions of pH 11 and reaction temperature 37$^{\circ}{\cdots}$. The hydroxyapatite was partially converted to $\alpha,\;\beta$-TCP at 1,200$^{\circ}{\cdots}$ and 1,300$^{\circ}{\cdots}$. Mechanical strength of sample was affected by such powder preparation conditions as pH and reaction temperature and sintering temperature. The mechanical strength of sample prepared under the same conditions was increased with increasing pH, reaction temperature and sintering temperature.

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4,5-Diphenyl-Imidazolone의 合成 及 螢光效果에 關한 硏究 (Synthesis of 4,5-Diphenyl Imidazolone and Studies on its Fluorescent Effect)

  • 전풍진;김형숙
    • 대한화학회지
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    • 제4권1호
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    • pp.70-77
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    • 1957
  • 4,5-Diphenyl Imidazolone is synthesized from Benzoin, Urea, and Acetic acid catalyser. Nowadays, it is being used as an optical bleaching agent for wool and nylon textiles. Up to now, only one process of synthesis has been known. In order to find out the best conditions governing the yield were examined under various catalysers and conditions. In this experiment, the summary of results were as follows. a. On Acetic acid catalyser. The maximum yield conditions were mol ratio (Benzoin: Urea: Acetic acid) 1 : 2 : 14, Acetic acid concentration 99.9%. Reaction temperature 115$^{\circ}$. Under reaction time of 2 hours, above yield was 96.4%. b. On Mineral acid Catalyser. In using of Sulfonic acid, the color of solution was changed dark purlish black. With other mineral acid catalysers, in spite of increasing of temperature, it was proved that Benzoin floats on the solution, so that this reaction could not be continue. c. On Phosphoric acid catalyser. It was made clear that it can not be used for this reaction. d. On Sodium hydroxide catalyser. As one of Alkali catalyser, Sodium hydroxide was examined but this was unsuitable substance for this reaction. e. On Formic acid catalysers. The maximum yield conditions were mol ratio (Benzoin: Urea: Formic acid) 1: 2: 30. Formic acid concentration 85.%. Reaction temperature 150∼110$^{\circ}$. Under reaction time of 90 minutes, the best yield was 87%. Hereby, it was proved that organic acids such as Acetic acid and Formic acid can be used. When using Acetic acid, the yield was better than Formic acid, but it takes longer reaction time than Formic acid. About the fluorescent effect, the temperature of dye-bath must not be over 904,5-Diphenyl Imidazolone is synthesized from Benzoin, Urea, and Acetic acid catalyser. Nowadays, it is being used as an optical bleaching agent for wool and nylon textiles. Up to now, only one process of synthesis has been known. In order to find out the best conditions governing the yield were examined under various catalysers and conditions. In this experiment, the summary of results were as follows. a. On Acetic acid catalyser. The maximum yield conditions were mol ratio (Benzoin: Urea: Acetic acid) 1 : 2 : 14, Acetic acid concentration 99.9%. Reaction temperature 115$^{\circ}$. Under reaction time of 2 hours, above yield was 96.4%. b. On Mineral acid Catalyser. In using of Sulfonic acid, the color of solution was changed dark purlish black. With other mineral acid catalysers, in spite of increasing of temperature, it was proved that Benzoin floats on the solution, so that this reaction could not be continue. c. On Phosphoric acid catalyser. It was made clear that it can not be used for this reaction. d. On Sodium hydroxide catalyser. As one of Alkali catalyser, Sodium hydroxide was examined but this was unsuitable substance for this reaction. e. On Formic acid catalysers. The maximum yield conditions were mol ratio (Benzoin: Urea: Formic acid) 1: 2: 30. Formic acid concentration 85.%. Reaction temperature 150∼110$^{\circ}$. Under reaction time of 90 minutes, the best yield was 87%. Hereby, it was proved that organic acids such as Acetic acid and Formic acid can be used. When using Acetic acid, the yield was better than Formic acid, but it takes longer reaction time than Formic acid. About the fluorescent effect, the temperature of dye-bath must not be over 90$^{\circ}$. and the ratio of 4,5-Diphenyl Imidazolone and water should be from 1:50000. to 1:10000. It proved that the best effect on textiles, and the best condition were dye-temperature near 704,5-Diphenyl Imidazolone is synthesized from Benzoin, Urea, and Acetic acid catalyser. Nowadays, it is being used as an optical bleaching agent for wool and nylon textiles. Up to now, only one process of synthesis has been known. In order to find out the best conditions governing the yield were examined under various catalysers and conditions. In this experiment, the summary of results were as follows. a. On Acetic acid catalyser. The maximum yield conditions were mol ratio (Benzoin: Urea: Acetic acid) 1 : 2 : 14, Acetic acid concentration 99.9%. Reaction temperature 115$^{\circ}C$. . Under reaction time of 2 hours, above yield was 96.4%. b. On Mineral acid Catalyser. In using of Sulfonic acid, the color of solution was changed dark purlish black. With other mineral acid catalysers, in spite of increasing of temperature, it was proved that Benzoin floats on the solution, so that this reaction could not be continue. c. On Phosphoric acid catalyser. It was made clear that it can not be used for this reaction. d. On Sodium hydroxide catalyser. As one of Alkali catalyser, Sodium hydroxide was examined but this was unsuitable substance for this reaction. e. On Formic acid catalysers. The maximum yield conditions were mol ratio (Benzoin: Urea: Formic acid) 1: 2: 30. Formic acid concentration 85%. Reaction temperature 150∼110$^{\circ}C$. Under reaction time of 90 minutes, the best yield was 87%. Hereby, it was proved that organic acids such as Acetic acid and Formic acid can be used. When using Acetic acid, the yield was better than Formic acid, but it takes longer reaction time than Formic acid. About the fluorescent effect, the temperature of dye-bath must not be over 90$^{\circ}C$. and the ratio of 4,5-Diphenyl Imidazolone and water should be from 1:50000. to 1:10000. It proved that the best effect on textiles, and the best condition were dye-temperature near 70$^{\circ}C$. and dye-time 15 minutes. . and dye-time 15 minutes. . and the ratio of 4,5-Diphenyl Imidazolone and water should be from 1:50000. to 1:10000. It proved that the best effect on textiles, and the best condition were dye-temperature near 70$^{\circ}C$. and dye-time 15 minutes.

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란타늄 옥살레이트 반응성 결정화에서 반응조건에 따른 결정입자 연구 (Effect of Reaction Conditions on Crystals in the Reaction Crystallization of Lanthanum Oxalate)

  • 김홍주;김운수;김우식
    • 공업화학
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    • 제9권7호
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    • pp.1004-1010
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    • 1998
  • Single-jet 반회분식 결정화 반응기에서 동력투입량, 반응물의 주입시간 및 주입방법등 반응조건의 변화가 란타늄 옥살레이트 결정입자의 반응성 결정화에 미치는 영향에 대해 실험적으로 조사하였다. 란타늄 옥살레이트 결정입자의 크기분포는 반응조건에 관계없이 monomodal 형태의 크기분포를 나타내었으나 평균결정크기는 반응조건에 크게 영향을 받았다. 동력투입량이 증가할수록, 반응물의 주입속도가 빠를수록, 란타늄 옥살레이트의 결정입자크기는 감소하였으나 상대적 유도시간은 증가하였다. 반응물의 주입방법에 있어서 옥살산 용액이 주입되는 경우보다 염화란타늄 용액이 주입되는 경우에 결정입자는 크게 나타났으며 상대적 유도시간은 감소하였다. 그리고 결정입자의 형태는 모두 침상형으로 반응조건의 변화에 크게 영향을 받지 않았다.

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Browning Reaction을 이용한 Meat Flavor Extract의 개발 (Manufacturing of Meat Flavor Extract used for Browning Reaction)

  • 김덕숙;김종승
    • 한국식품영양학회지
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    • 제17권3호
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    • pp.313-321
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    • 2004
  • Maillard reaction을 이용하여 제조한 여러 종류의 reaction meat flavor로부터 함유황 이원자고리 화합물을 분리, 농축한 다음 GC와 GC-MSD를 이용하연 함유황 이원자고리 화합물의 profile을 얻어 성분의 확인 및 정량분석을 시도하여 다음과 같은 결론을 얻었다. 1. Reaction meat flavor의 함유황 이원자고리 화합물의 profile을 조사한 결과 7종의 thiozole과 11종의 thiophene을 동정 할 수 있었으며, thiophene, thinzolidine, 4-methyl-5-thiazole ethanol이 주요 생성 화합물이었다. 2. 함유황 이원자고리 화합물의 경우 반응조건(온도, 시간)의 변화에 따라 생성성분의 종류에는 거의 차이가 없었지만 그 양에 있어서는 상당한 차이가 나타났고, 반응온도가 높을수록, 반응시간이 길수록 구조가 복잡한 함유황 이원자고리 화합물과 caramellike note를 갖는 함산소 이원자고리 화합물이 보다 많이 생성되었으며, 반대로 반응온도가 낮고 반응시간이 짧을수록 함유황이 원자고리 화합물의 생성이 비교적 적었다. 3. 수분함량 50%, 반응온도 10$0^{\circ}C$, 반응시간 2시간의 반응조건에서 thiophene과 thiazole 같은 비교적 구조가 단순한 함유황 이원자고리 화합물의 생성율이 가장 높았으며, reaction meat flavor의 발현을 위하여는 10$0^{\circ}C$ 이내의 온도에서 2시간을 넘기지 않고 반응시키는 것이 좋았다. 4. 수분함량이 낮으면 반응온도 및 시간을 낮고 짧게, 수분함량이 높을수록반응온도 및 시간은 높고 길게 반응시키는 등 수분함량은 반응온도 및 시간과 밀접한 관계에 있으므로 수분함량에 따라 반응조건을 변화시킴으로써 일정한 flavor profile을 계속하여 얻을 수 있었다. 이와 같이 원료를 단순화하여 reaction meat flavor를 제조한 다음 함유황 이원자고리 화합물을 추출, 분리, 농축하여 분석함으로써 향료산업 및 조미식품산업에서 reaction meat flavor의 생산에 필요한 하나의 방향을 제시할 수 있었다.

공침법에 의한 MnZn Ferrite 분말제조 연구 (MnZn Ferrite Preparation by Coprecipitation Method)

  • 엄태형;고성만;서동수;양준환;박균하
    • 한국세라믹학회지
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    • 제30권6호
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    • pp.478-484
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    • 1993
  • The influence of reaction conditions on the MnZn ferrite coprecipitation process were investigated using mixed metla sulfate solution and ammonium oxalate. In order to minimize the metallic ion losses and to control the particle size, the optimum reaction conditions were as follows; reaction temperature $25^{\circ}C$, metal sulfate concentration 0.3M, molar ratio of ammonium oxalate/mixed metal sulfate 1.1:1. The production yield was as high as 97.6% of theoretical yield at optimum reaction condition.

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