JOURNAL OF CHEMICAL ENGINEERING OF JAPAN
Online ISSN : 1881-1299
Print ISSN : 0021-9592
38 巻, 2 号
選択された号の論文の11件中1~11を表示しています
Transport Phenomena and Fluid Engineering
Separation Engineering
  • Takehiko Kinoshita, Shigendo Akita, Susumu Nii, Fumio Kawaizumi, Katsu ...
    2005 年 38 巻 2 号 p. 94-99
    発行日: 2005年
    公開日: 2005/02/20
    ジャーナル 認証あり
    Hydrofluoroethers have been applied as diluent for phosphorus acid extractants in the solvent extraction of zinc(II). They are promising alternatives to conventional organic diluents because of their non-flammability, chemical stability and non-toxicity. Hydrofluoroethers used in this study are a mixture of ethylperfluorobutylether and ethylperfluoroisobutylether and a mixture of methylperfluorobutylether and methylperfluoroisobutylether (HFE-7100). Among the extractants examined, two phosphorus acid extractants, di-(2-ethylhexyl)phosphoric acid (D2EHPA) and 2-ehtylhexyl phosphoric acid mono-2-ethylhexyl ester (EHPNA) were soluble in both hydrofluoroethers. Because of the high specific gravity of hydrofluoroethers and their low solubility in water, phase-separation was rapid and the resulting phases were clear. In the extraction of zinc(II) using the phosphorus acids, the system with D2EHPA gave higher extraction than that with EHPNA, while there was little difference in the extraction behavior between the two hydrofluoroethers. The effects of the equilibrium solution pH and the extractant concentration on the zinc extraction were examined, and the stoichiometric relationship for the extraction was proposed. The extraction equilibrium constants for zinc(II) were found to be higher than those with conventional chlorinated organic solvents such as chloroform and carbon tetrachloride. The backward extraction of zinc(II) was satisfactorily attained with a dilute acid solution, and the separation of several heavy metals was also demonstrated. Moreover, the elution of the extractants and hydrofluoroethers into the aqueous phase was very low, and this makes the present system more attractive.
  • Kazuo Kondo, Michiaki Matsumoto
    2005 年 38 巻 2 号 p. 100-105
    発行日: 2005年
    公開日: 2005/02/20
    ジャーナル 認証あり
    As the second step to clarify the synergistic extraction mechanism of gallium with the mixed extractant of 2-ethylhexylphosphonic acid mono-2-ethylhexyl ester (EHPNA) and 5-chloro-8-hydroxyquinoline, the initial extraction rate of gallium with EHPNA alone was measured using a stirred transfer cell.
    First, the aggregation state of EHPNA in the organic solvent, toluene, and the adsorption characteristics at the interface between the aqueous and organic phases were examined. EHPNA was found to exist mainly as dimers in the organic solvent and to adsorb the interface. By considering that the interface is a site for metal-complex formation, the extraction mechanism constructed with the three processes, a mass transfer of metal ions to the interface, an extraction reaction at the interface based on the Eigen mechanism, and a mass transfer of the metal-complex to the bulk organic phase, was proposed to analyze the experimental results.
Chemical Reaction Engineering
  • Lifeng Wang, Vo Dong Vien, Koji Suzuki, Makoto Sakurai, Hideo Kameyama
    2005 年 38 巻 2 号 p. 106-112
    発行日: 2005年
    公開日: 2005/02/20
    ジャーナル 認証あり
    Catalytic combustion of volatile organic compounds (VOCs) benefits from a low oxidation temperature due to less energy consumption. It is widely applied in industry. A novel technique of Pt/Al2O3/Al catalyst preparation is presented in this paper. Al2O3 film was formed on an Al plate by anodic oxidation in 4% oxalic acid solution at 50 A·m–2 current density. After anodic oxidation, Pt was supported on the oxidized plate utilizing an electrolysis supporting method with an alternating current in an aqueous solution of chloroplatinic acid hexahydrate under both high and low voltages. Catalytic activity was evaluated by both toluene and benzene combustion. Dispersion of platinum in developed catalysts was about 20%, measured by CO pulse adsorption.
    In the activity test, toluene or benzene was mixed with air and then toluene–air and benzene–air mixtures combusted on the developed catalysts. It is shown that a catalyst prepared under a high voltage has a higher reaction rate than that one prepared under low voltage. This may be explained by that large platinum particles were formed on the film by high voltage. In the running time of 140 hours duration, there exists an induction process of about 10 hours for fresh catalysts, in which, the conversion of toluene was promoted by up to about 8%, and with no obvious change in the reactions that follow. Experimental results indicated that electrolysis impregnation can be regarded as a short-time supporting method for preparing catalyst.
Process Systems Engineering and Safety
  • Ravi Padma Sree, Manickam Chidambaram
    2005 年 38 巻 2 号 p. 113-119
    発行日: 2005年
    公開日: 2005/02/20
    ジャーナル 認証あり
    A simple method is proposed for PID controller settings for an integrating plus dead-time system and a stable FOPTD system with an integrator. The method is based on matching the coefficients of corresponding powers of s, s2, s3 in the numerator to α1, α2, and α2 times that in the denominator of the closed-loop transfer function, respectively, for the servo problem. Here α1 and α2 are tuning parameters, and α1 is greater than 1. It is found by simulation on various transfer function models that the use of α2 = 0.6α1 gives good results. The robustness of the controller is evaluated theoretically by Kharitonov’s theorem. The method is used to design a PID controller for an isothermal continuous copolymerization reactor, and the performance of the controller designed by the present method is compared with a modified gain margin method (Luyben, 1996). The method is extended to design a PID controller for a stable FOPTD system with an integrator. The performance of the method is better than the method proposed by Zhang et al. (1999) for the servo problem, and it is superior to their method for the regulatory problem.
  • Yeong-Koo Yeo, Ki-Seok Hwang, Young-Gon Kim, Hong Kang
    2005 年 38 巻 2 号 p. 120-129
    発行日: 2005年
    公開日: 2005/02/20
    ジャーナル 認証あり
    In this study a model for the drying process in paper production plants was developed based on the mass and heat balances around drying cycles. Relationships for the heat transfer coefficients between the web and the air as well as between the drying cylinder and the web were extracted from the closed-loop plant operation data. It was found that the heat transfer coefficients could be represented effectively in terms of moisture content, basis weight and reel velocity. The effectiveness of the proposed model was illustrated through numerical simulations. From the comparison with the operation data, the proposed model represents the paper plant being considered with sufficient accuracy.
  • Yeong Tarng Tang, Hsiao-Ping Huang, I-Lung Chien
    2005 年 38 巻 2 号 p. 130-146
    発行日: 2005年
    公開日: 2005/02/20
    ジャーナル 認証あり
    By combining chemical reaction and multi-stage distillation in one column, a reactive distillation (RD) column can significantly save capital investment and make chemical conversion reach a much higher level. In a previous study, an optimal steady state design for the production of ethyl acetate (EtAc), consisting of two columns (one for RD and one for stripping column) and an overhead decanter, was reported. As a continuous study to that previous work, four alternative plant-wide control strategies for this designed process are studied in this paper. Feed compositions of both Acetic acid (HAc) and ethanol (EtOH) streams are treated as disturbances. These disturbances are used to test the closed-loop performance of each control scheme. It is found that control of the product qualities by modulating two tray temperatures in the RD column and one tray temperature in the stripper is most appropriate. By this control scheme, both of HAc and EtOH impurities in the product stream can be kept effectively within the acceptable product specifications.
  • Wenlong Zhang, Masao Imaeda, Reginald K. Wood, Kyoji Hashimoto
    2005 年 38 巻 2 号 p. 147-153
    発行日: 2005年
    公開日: 2005/02/20
    ジャーナル 認証あり
    In this work, an auto-tuning PID controller based on the generalized predictive control (GPC) method is proposed for on-line tuning of the controller parameters due to the changes in operating conditions. The proposed scheme is applied to the control of a distillation column, with identification of the parameters of an ARMAX model determined from the operating data of an industrial column. An evaluation of the maximum likelihood (ML) and Kalman filter (KF) methods of identification showed that at a 10-second sample interval, reliable model parameters could be predicted using either the ML or KF method. However, at a 60-second sample interval simulation results showed that only the KF method generated reliable parameters. Column control was studied for an objective of maintaining constant liquid temperature on an intermediate tray, in the presence of a disturbance in the feed flow rate, with the top product flow rate being a manipulated variable. The simulation results for the auto-tuning PID control scheme using the GPC formulation are compared to the control performance which was obtained using a tuned conventional PID controller and also GPC, at a 60-second sample interval.
Biochemical, Food and Medical Engineering
Environment
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