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1

Sihn, Sangwook, Gregory J. Ehlert, Ajit K. Roy, and Jonathan P. Vernon. "Identifying unified kinetic model parameters for thermal decomposition of polymer matrix composites." Journal of Composite Materials 53, no. 20 (2018): 2875–90. http://dx.doi.org/10.1177/0021998318805821.

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Predicting thermal responses of composite materials requires accurate input parameters derived from reliable thermal property characterization and kinetic models. Composite material properties and decomposition kinetics vary with temperature and heating rate. Typically, conventional kinetic models derived from thermogravimetric analysis data result in multiple sets of kinetic model parameters, which are difficult to implement into numerical simulations under widely varying temperature and heating rate conditions. Here, a methodology was developed to reliably predict decomposition processes of
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2

French, Andrew S., and Lisa L. Stockbridge. "Fractal and Markov behavior in ion channel kinetics." Canadian Journal of Physiology and Pharmacology 66, no. 7 (1988): 967–70. http://dx.doi.org/10.1139/y88-159.

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Kinetic analysis of ion channel recordings attempts to distinguish the number and lifetimes of channel molecular states. Most kinetic analysis assumes that the lifetime of each state is independent of previous channel history, so that open and closed durations are Markov processes whose probability densities are sums of exponential decays. An alternative approach assumes that channel molecules have many configurtions with widely varying lifetimes. Rates of opening and closing then vary with the time scale of observation, leading to fractal kinetics. We have examined kinetic behavior in two typ
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3

Du, Hong Shuang, Xiang Yu Li, Xue Yong Ren, and Yan Xue Han. "Pyrolysis Kinetics Equation of Larch Bark." Advanced Materials Research 772 (September 2013): 313–18. http://dx.doi.org/10.4028/www.scientific.net/amr.772.313.

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The larch bark was examined by non-isothermal means to determine the mass loss kinetics of the thermal decomposition with linear temperature programming in nitrogen atmosphere. In this work, mechanism equation of = was used forCoats-Redfern integral methodat the different heating rates. The apparent activation energy, pre-exponential factor and the pyrolysis kinetic equations at the different heating rates were obtained. The pyrolysis temperature area was divided into two separate temperature regions for the pyrolysis kinetic equation and the two components were decomposed respectively at the
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4

Acuna-Askar, K., M. V. Gracia-Lozano, J. F. Villarreal-Chiu, J. G. Marmolejo, M. T. Garza-Gonzalez, and B. Chavez-Gomez. "Effect of soil and a nonionic surfactant on BTE-oX and MTBE biodegradation kinetics." Water Science and Technology 52, no. 8 (2005): 107–15. http://dx.doi.org/10.2166/wst.2005.0237.

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The biodegradation kinetics of BTE-oX and MTBE, mixed all together, in the presence of 905mg/L VSS of BTEX-acclimated biomass was evaluated. Effects of soil and Tergitol NP-10 in aqueous samples on substrate biodegradation rates were also evaluated. Biodegradation kinetics was evaluated for 36 hours, every 6 hours. MTBE biodegradation followed a first-order one-phase kinetic model in all samples, whereas benzene, toluene and ethylbenzene biodegradation followed a first-order two-phase kinetic model in all samples. O-xylene biodegradation followed a first-order two-phase kinetic model in the pr
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5

Vyazovkin, Sergey. "Activation Energies and Temperature Dependencies of the Rates of Crystallization and Melting of Polymers." Polymers 12, no. 5 (2020): 1070. http://dx.doi.org/10.3390/polym12051070.

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The objective of this review paper is to survey the phase transition kinetics with a focus on the temperature dependence of the rates of crystallization and melting, as well as on the activation energies of these processes obtained via the Arrhenius kinetic treatment, including the treatment by isoconversional methods. The literature is analyzed to track the development of the basic models and their underlying concepts. The review presents both theoretical and practical considerations regarding the kinetic analysis of crystallization and melting. Both processes are demonstrated to be kinetical
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6

Vincze, István, László Endrényi, and László Tóthfalusi. "Bioequivalence metrics for absorption rates: linearity, specificity, sensitivity." Acta Pharmaceutica Hungarica 89, no. 1 (2019): 17–21. http://dx.doi.org/10.33892/aph.2019.89.17-21.

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Aims:In order to ensure the therapeutic equivalence of generic products, it would be important to contrast measures additional to Cmax in order to assess differences in absorption rates. Our aim was to compare partial AUC (PAUC), Swing, and PTF to Cmax in terms of sensitivity, specificity and linearity under identical kinetic conditions.
 Methods:Single-dose and multiple-dose concentration curves were generated assuming one-compartment models. Kinetic sensitivity curves were obtained by gradually changing the absorption rate constant and keeping all other parameters fixed.
 Results:A
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7

S, Jargalmaa, Tsatsral G, Battsetseg M, et al. "Kinetic study of Mongolian coals by thermal analysis." Mongolian Journal of Chemistry 18, no. 44 (2018): 20–23. http://dx.doi.org/10.5564/mjc.v18i44.933.

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Thermal analysis was used for the thermal characterization of the coal samples. The experiments were performed to study the pyrolysis and gasification kinetics of typical Mongolian brown coals. Low rank coals from Shivee ovoo, Ulaan ovoo, Aduun chuluun and Baganuur deposits have been investigated. Coal samples were heated in the thermogravimetric apparatus under argon at a temperature ranges of 25-1020ºC with heating rates of 10, 20, 30 and 40ºC/min. Thermogravimetry (TG) and derivative thermogravimetry (DTG) were performed to measure weight changes and rates of weight losses used for calculat
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8

Tsai, Lung Chang, Jian Ming Wei, Yung Chuan Chu, et al. "RDX Kinetic Model Evaluation by Nth Order Kinetic Algorithms and Model Simulations." Advanced Materials Research 189-193 (February 2011): 1413–16. http://dx.doi.org/10.4028/www.scientific.net/amr.189-193.1413.

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A kinetic model based on the thermal decomposition of 1,3,5-trinitro-1,3,5-triazmane (RDX) was constructed via differential scanning calorimetry (DSC), well-known kinetic equations, curve-fitting analysis, and simulations of thermal analysis. Our objective was to analyze thermokinetic parameters derived from heating rates used in DSC and compare simulations of thermal decomposition under various kinetic models. Experimental results were strongly dependent on the validity of the kinetic model, which was based on an appropriate mathematical model and a proper method for the evaluation of kinetic
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9

Palfey, Bruce A., and Rebecca L. Fagan. "Analysis of the Kinetic Isotope Effects on Initial Rates in Transient Kinetics†." Biochemistry 45, no. 45 (2006): 13631–40. http://dx.doi.org/10.1021/bi061214h.

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10

Johnson, C. A., and J. L. Keltner. "Optimal Rates of Movement for Kinetic Perimetry." Archives of Ophthalmology 105, no. 1 (1987): 73–75. http://dx.doi.org/10.1001/archopht.1987.01060010079035.

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11

Solomon, Peter R., Michael A. Serio, and Eric M. Suuberg. "Coal pyrolysis: Experiments, kinetic rates and mechanisms." Progress in Energy and Combustion Science 18, no. 2 (1992): 133–220. http://dx.doi.org/10.1016/0360-1285(92)90021-r.

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12

Farjas, J., and P. Roura. "Solid-phase crystallization under continuous heating: Kinetic and microstructure scaling laws." Journal of Materials Research 23, no. 2 (2008): 418–26. http://dx.doi.org/10.1557/jmr.2008.0045.

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The kinetics and microstructure of solid-phase crystallization under continuous heating conditions and random distribution of nuclei are analyzed. An Arrhenius temperature dependence is assumed for both nucleation and growth rates. Under these circumstances, the system has a scaling law such that the behavior of the scaled system is independent of the heating rate. Hence, the kinetics and microstructure obtained at different heating rates differ only in time and length scaling factors. Concerning the kinetics, it is shown that the extended volume evolves with time according to αex = [exp(κCt′)
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13

Vincent, Heather K., Laura A. Zdziarski, Kyle Fallgatter, et al. "Running Mechanics and Metabolic Responses With Water Bottles and Bottle Belt Holders." International Journal of Sports Physiology and Performance 13, no. 8 (2018): 977–85. http://dx.doi.org/10.1123/ijspp.2017-0184.

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Purpose: To determine whether differential kinematics, kinetics, rates of energy use, and cardiopulmonary responses occur during running with water bottles and bottle belt holders compared with running only. Methods: Trained runners (N = 42; age 27.2 [6.4] y) ran on an instrumented treadmill for 4 conditions in a randomized order: control run (CON), handheld full water bottle (FULL; 16.9 fluid oz; 454 g), handheld half-full water bottle (HALF; 8.4 fluid oz; 227 g), and waist-worn bottle belt holder (BELT; hydration belt; 676 g). Gas exchange was measured using a portable gas analyzer. Kinetic
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14

Donskoy, Igor, and Aleksandr Kozlov. "Thermogravimetric Study of the Kinetics of the Reaction C + CO2 under Pore-Diffusion Control." Energies 14, no. 7 (2021): 1886. http://dx.doi.org/10.3390/en14071886.

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This study presents experimental studies of charcoal gasification with CO2 at different heating rates (1, 5, 10, 20, and 50 K min−1). The kinetics of the reaction C + CO2 under pore-diffusion control is studied. We propose a new method for the proper determination of activation energy during the processing of thermogravimetric curves of porous carbon gasification under conditions of pore-diffusion resistance. The results of the inverse kinetic problem solution are compared with different hypotheses about the regime of the investigated heterogeneous reaction process (kinetic, diffusion, pore-di
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15

Sun, Jin, Xiao Feng Zhu, Xiao Bo Wang, Rui Hang Lin, and Zhen Zhong Gao. "Curing Kinetics of Phenol Formaldehyde Resin Modified with Sodium Silicate." Applied Mechanics and Materials 184-185 (June 2012): 1471–79. http://dx.doi.org/10.4028/www.scientific.net/amm.184-185.1471.

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The curing kinetics of PF resin modified with sodium silicate had been investigated by differential scanning calorimetry (DSC). The kinetic analysis was performed at heating rates of 5, 10, 15, and 20°C/min,respectively. The kinetic parameters such as reaction order and activation energy were solved by Kissinger and Crane equation. The relationship between curing temperature and heating rate was also investigated. The activation energy and the curing reaction order,which were obtained by kinetic calculation, are 83.00kJ/mol and 0.917, respectively. The curing reaction kinetics equations were b
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16

Warn-Cramer, B. J., and S. P. Bajaj. "Intrinsic versus extrinsic coagulation Kinetic considerations." Biochemical Journal 239, no. 3 (1986): 757–62. http://dx.doi.org/10.1042/bj2390757.

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A study to compare the kinetics of activation of factor IX by Factor XIa/Ca2+ and by Factor VIIa/tissue factor/Ca2+ has been undertaken. When purified human proteins, detergent-extracted brain tissue factor and tritiated-activation-peptide-release assays were utilized, the kinetic constants obtained were: Km = 310 nM, kcat. = 25 min-1 for Factor XIa and Km = 210 nM, kcat. = 15 min-1 for Factor VIIa. The kinetic constants for the activation of Factor X by Factor VIIa/brain tissue factor were: Km = 205 nM, kcat. = 70 min-1. Predicted rates for the generation of Factor IXa and Factor Xa were obta
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17

Astola, Laura, Hans Stigter, Maria Victoria Gomez Roldan, et al. "Parameter estimation in tree graph metabolic networks." PeerJ 4 (September 20, 2016): e2417. http://dx.doi.org/10.7717/peerj.2417.

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We study the glycosylation processes that convert initially toxic substrates to nutritionally valuable metabolites in the flavonoid biosynthesis pathway of tomato (Solanum lycopersicum) seedlings. To estimate the reaction rates we use ordinary differential equations (ODEs) to model the enzyme kinetics. A popular choice is to use a system of linear ODEs with constant kinetic rates or to use Michaelis–Menten kinetics. In reality, the catalytic rates, which are affected among other factors by kinetic constants and enzyme concentrations, are changing in time and with the approaches just mentioned,
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18

Acuna-Askar, K., M. A. de la Torre-Torres, M. J. Guerrero-Munoz, et al. "Biodegradation kinetics of BTE-OX and MTBE by a diesel-grown biomass." Water Science and Technology 53, no. 11 (2006): 197–204. http://dx.doi.org/10.2166/wst.2006.353.

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The biodegradation kinetics of BTE-oX and MTBE, mixed all together in the presence of diesel-grown bioaugmented bacterial populations as high as 885 mg/L VSS, was evaluated. The effect of soil in aqueous samples and the effect of Tergitol NP-10 on substrate biodegradation rates were also evaluated. Biodegradation kinetics was evaluated for 54 h, every 6 h. All BTE-oX chemicals followed a first-order two-phase biodegradation kinetic model, whereas MTBE followed a zero-order removal kinetic model in all samples. BTE-oX removal rates were much higher than those of MTBE in all samples. The presenc
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19

Acuna-Askar, K., J. F. Villarreal-Chiu, M. V. Gracia-Lozano, et al. "BTE-OX biodegradation kinetics with MTBE through bioaugmentation." Water Science and Technology 50, no. 5 (2004): 85–92. http://dx.doi.org/10.2166/wst.2004.0313.

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The biodegradation kinetics of BTE-oX and MTBE, mixed all together, in the presence of bioaugmented bacterial populations as high as 880 mg/L VSS was evaluated. The effect of soil in aqueous samples and the effect of Tergitol NP-10 on substrate biodegradation rates were also evaluated. Biodegradation kinetics was evaluated for 36 hours, every 6 hours. Benzene and o-xylene biodegradation followed a first-order one-phase kinetic model, whereas toluene and ethylbenzene biodegradation was well described by a first-order two-phase kinetic model in all samples. MTBE followed a zero-order removal kin
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20

Wentzel, M. C., G. A. Ekama, and G. v. R. Marais. "Processes and Modelling of Nitrification Denitrification Biological Excess Phosphorus Removal Systems – A Review." Water Science and Technology 25, no. 6 (1992): 59–82. http://dx.doi.org/10.2166/wst.1992.0114.

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This paper reviews developments in modelling the kinetics of activated sludge systems: Completely aerobic nitrification, anoxic/aerobic nitrification denitrification (ND), and anaerobic/anoxic/aerobic nitrification denitrification biological excess phosphorus removal (NDBEPR) systems. The paper highlights the progress in developing a general NDBEPR activated sludge kinetic model – development of polyP organism enhanced cultures, their kinetics, simplification of the kinetics for enhanced cultures under constant flow and load conditions, extension of the simplified model to mixed culture NDBEPR
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21

Huang, Y. P., and M.-J. Huang. "Kinetic Analysis of Transition Rates on Brownian Motor." Journal of Biomechanics 40 (January 2007): S77. http://dx.doi.org/10.1016/s0021-9290(07)70074-x.

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22

Dixit, Purushottam D., and Ken A. Dill. "Inferring Microscopic Kinetic Rates from Stationary State Distributions." Journal of Chemical Theory and Computation 10, no. 8 (2014): 3002–5. http://dx.doi.org/10.1021/ct5001389.

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23

Schaaf, P., B. Senger, J. C. Voegel, R. K. Bowles, and H. Reiss. "Simulative determination of kinetic coefficients for nucleation rates." Journal of Chemical Physics 114, no. 18 (2001): 8091–104. http://dx.doi.org/10.1063/1.1364640.

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24

Barrett, Jonathan, and Charles Clement. "Kinetic evaporation and condensation rates and their coefficients." Journal of Colloid and Interface Science 150, no. 2 (1992): 352–64. http://dx.doi.org/10.1016/0021-9797(92)90205-z.

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25

Cooper, William C., Yi Jin, and Trevor M. Penning. "Elucidation of a Complete Kinetic Mechanism for a Mammalian Hydroxysteroid Dehydrogenase (HSD) and Identification of All Enzyme Forms on the Reaction Coordinate." Journal of Biological Chemistry 282, no. 46 (2007): 33484–93. http://dx.doi.org/10.1074/jbc.m703414200.

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Hydroxysteroid dehydrogenases (HSDs) are essential for the biosynthesis and mechanism of action of all steroid hormones. We report the complete kinetic mechanism of a mammalian HSD using rat 3α-HSD of the aldo-keto reductase superfamily (AKR1C9) with the substrate pairs androstane-3,17-dione and NADPH (reduction) and androsterone and NADP+ (oxidation). Steady-state, transient state kinetics, and kinetic isotope effects reconciled the ordered bi-bi mechanism, which contained 9 enzyme forms and permitted the estimation of 16 kinetic constants. In both reactions, loose association of the NADP(H)
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26

Lomova, Tatyana N., Mariya E. Klyueva, Elena Yu Tyulyaeva, and Nataliya G. Bichan. "Use of chemical kinetics for the description of metal porphyrin reactivity." Journal of Porphyrins and Phthalocyanines 16, no. 09 (2012): 1040–54. http://dx.doi.org/10.1142/s1088424612500769.

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The results of use of chemical kinetics receptions, approaches and methods for the study of porphyrins and their metal complexes reactivity are discussed on an example of oxidation, acid-basic, and catalytic reactions of rhodium, palladium, and rhenium complexes of porphyrin in liquid solutions. The peculiarity of the porphyrin reaction rates is analyzed in a brief context of general provisions of the chemical kinetics. The opportunity to use the quasistationarity principle at the definition of the kinetic equation of the reactions with participation of metal porphyrins is shown. The transitio
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27

Petrella, Andrea, Danilo Spasiano, Pinalysa Cosma, et al. "Methyl Orange Photo-Degradation by TiO2 in a Pilot Unit under Different Chemical, Physical, and Hydraulic Conditions." Processes 9, no. 2 (2021): 205. http://dx.doi.org/10.3390/pr9020205.

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The photo-catalytic degradation of a textile azo-dye as Methyl Orange was studied in an innovative unit constituted by a channel over which a layer of titanium dioxide (TiO2) catalyst in anatase form was deposited and activated by UVB irradiation. The degradation kinetics were followed after variation of the chemical, physical, and hydraulic/hydrodynamic parameters of the system. For this purpose, the influence of the TiO2 dosage (g/cm3), dye concentration (mg/L), pH of the solution, flow-rate (L/s), hydraulic load (cm), and irradiation power (W) were evaluated on the degradation rates. It was
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28

Aojula, H. S., M. T. Wilson, and I. E. G. Morrison. "Functional consequences of haem orientational disorder in sperm-whale and yellow-fin-tuna myoglobins." Biochemical Journal 243, no. 1 (1987): 205–10. http://dx.doi.org/10.1042/bj2430205.

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Ligand-binding kinetics of native and reconstituted sperm-whale myoglobin were studied in relation to haem orientational disorder by rapid kinetic methods. In addition, native yellow-fin-tuna myoglobin with significant amount of haem disorder was also used. The O2 dissociation and association rates were found for the proteins with different degrees of haem disorder, and these results suggest that the isomers are characterized by almost identical kinetic parameters. Rates of CO recombination after photolysis were also identical for the two orientational isomers. The results clearly indicate tha
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29

Jung, Min Su, Seok Jae Lee, and Young Kook Lee. "Tempering Kinetics of S45C Martensitic Steel." Solid State Phenomena 118 (December 2006): 375–80. http://dx.doi.org/10.4028/www.scientific.net/ssp.118.375.

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The strain change during the tempering of S45C martensitic steel was examined at different heating rates using a dilatometer. Tempering stages 1 and 3 corresponding to the precipitations of transition carbide and cementite were observed. Tempering kinetics at each stage was investigated from the relation between the measured strain and atomic volume change during tempering. From the tempering kinetic data, continuous heating tempering diagram was constructed and the tempering kinetic model was proposed as Zener-Hillert type differential equation.
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30

Zhong, Ling, Gang Xian Zhang, Feng Xiu Zhang, and Xu Ting Xue. "Adsorption Kinetic Study of Reactive Dyes on Silk with Octyl Trimethyl Ammonium Bromide as Accelerant." Advanced Materials Research 331 (September 2011): 291–97. http://dx.doi.org/10.4028/www.scientific.net/amr.331.291.

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The dyeing accelerating effect of octyl trimethyl ammonium bromide (OTAB) on dyeing silk with reactive red dye B-3BF, reactive yellow dye B-4RFN and reactive dark blue dye B-2GLN was studied in this paper. The dye-uptake rates increased with increasing concentration of OTAB, and the highest dye-uptake rates of three reactive dyes were 91~98%. The adsorption kinetics of dyeing process at different temperatures was also investigated by using pseudo first- and second-order kinetic models. The results showed that adsorption rates increased with increasing temperature. The adsorption kinetics of th
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31

Chen, Cheng, Guang Xian Zhang, Feng Xiu Zhang, and Hui Zheng. "Adsorption Kinetics of Reactive Dyes on Silk with Octyl Butyl Dimethyl Ammonium Bromide as Accelerant." Advanced Materials Research 549 (July 2012): 278–82. http://dx.doi.org/10.4028/www.scientific.net/amr.549.278.

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With octyl butyl dimethyl ammonium bromide (OBDAB) as accelerant, adsorption kinetics of dyeing silk with three reactive dyes was studied in this paper. As concentration of OBDAB increased, the dye-uptake rate increased. The highest dye-uptake rates of three reactive dyes could reach to 89.40%~98.98% and the concentration of OBDAB was only 6-8g/L. This showed OBDAB was an effective accelerant. Pseudo first- and second-order kinetic models were used to analyze the adsorption kinetic data. The experimental data were found to follow the second-order kinetic model. Meanwhile, the initial dye adsor
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32

Liebovitch, Larry S. "Analysis of fractal ion channel gating kinetics: kinetic rates, energy levels, and activation energies." Mathematical Biosciences 93, no. 1 (1989): 97–115. http://dx.doi.org/10.1016/0025-5564(89)90015-1.

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33

Okewale, A. D., Millionaire Freeborn Nestor Abowei, F. O. Agbogun, and C. N. Owabor. "Simplified Rate Expression for Palm Kernel Oil (PKO) and Methanol Alkali Catalyzed Transesterification Reaction." European Journal of Engineering Research and Science 5, no. 5 (2020): 599–606. http://dx.doi.org/10.24018/ejers.2020.5.5.1901.

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The need for the development of simplified kinetics rates expression (-RA) for Vegetable Oils Alkali catalyzed Transesterification processes to enhance biodiesel production motivated this study. The study, therefore aimed at proposing unified simple rate expression that may be a useful prelude to design various reactor types for Alkali Catalyzed Transesterification of palm kernel oil (PKO) and Methanol reactions. The kinetics rate expression is proposed using simple explicit algebraic technique with the consideration that alkali catalyzed transesterification reaction of palm kernel oil and met
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Mihajlovic, Ivan, Nada Strbac, Zivan Zivkovic, and Ilija Ilic. "Kinetics and mechanism of As2S2 oxidation." Journal of the Serbian Chemical Society 70, no. 6 (2005): 869–77. http://dx.doi.org/10.2298/jsc0506869m.

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The kinetics of realgar (As2S2) oxidation was studied under isothermal and non-isothermal conditions. The obtained values of the activation energy indicate that the process occurs in the kinetic domainwith the realgar particles being converted to As2O3 and As4O6 (g). The very fast reaction rates were limited by the chemical reaction. The kinetic equation was found to be: ?ln (1??) = 4.56 x 103 x e(?8780/T) x t. The proposed reaction mechanism and chemical transformation investigated by ICP?AES, EDXRF and thermal analysis are discussed.
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35

Brorson, James R., and Zachary B. Bulwa. "Two-State Kinetic Model of Rates of Stroke Recurrence in the POINT Study Population." Stroke 52, no. 4 (2021): 1446–49. http://dx.doi.org/10.1161/strokeaha.120.031447.

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Background and Purpose: Following an acute ischemic stroke or transient ischemic attack, 2 rates of stroke recurrence are suggested by data from trials of acute secondary prevention treatments: a transient rapid rate followed by a persisting slower rate of stroke. Methods: A kinetic model was constructed based on underlying vulnerable and stabilized states of patients following acute ischemic events related by fixed transition rates. Its predictions were fitted by nonlinear regression to the observed timing of outcome events in patients in the POINT trial (Platelet-Oriented Inhibition in New T
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36

Meisl, G., A. V. Chankin, and D. P. Coster. "Kinetic modelling of temperature equilibration rates in the plasma." Journal of Nuclear Materials 438 (July 2013): S342—S345. http://dx.doi.org/10.1016/j.jnucmat.2013.01.064.

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37

Nill, Jennifer, Nardrapee Karuna, and Tina Jeoh. "The impact of kinetic parameters on cellulose hydrolysis rates." Process Biochemistry 74 (November 2018): 108–17. http://dx.doi.org/10.1016/j.procbio.2018.07.006.

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38

Tian, Wei Dong, J. Timothy Sage, Paul M. Champion, Ellen Chien, and Stephen G. Sligar. "Probing Heme Protein Conformational Equilibration Rates with Kinetic Selection†." Biochemistry 35, no. 11 (1996): 3487–502. http://dx.doi.org/10.1021/bi952474u.

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39

Biagiola, S., J. Solsona, and R. Milocco. "Estimation of kinetic rates in batch Thiobacillus ferrooxidans cultures." Journal of Biotechnology 84, no. 1 (2000): 13–25. http://dx.doi.org/10.1016/s0168-1656(00)00337-0.

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40

Badaoui, Magd, Adam Kells, Carla Molteni, Callum J. Dickson, Viktor Hornak, and Edina Rosta. "Calculating Kinetic Rates and Membrane Permeability from Biased Simulations." Journal of Physical Chemistry B 122, no. 49 (2018): 11571–78. http://dx.doi.org/10.1021/acs.jpcb.8b07442.

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Vignoni, Alejandro, Sebastián Nuñez, Hernán De Battista, Jesús Pićo, Enrique Pico-Marco, and Fabricio Garelli. "Specific Kinetic Rates Regulation in Multi-Substrate Fermentation Processes." IFAC Proceedings Volumes 46, no. 31 (2013): 42–47. http://dx.doi.org/10.3182/20131216-3-in-2044.00049.

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42

Kalinitchev, A. I., E. V. Kolotinskaya, and T. D. Semenovskaya. "Kinetic mechanism limiting ion exchange rates in selective systems." Reactive Polymers, Ion Exchangers, Sorbents 7, no. 2-3 (1988): 123–31. http://dx.doi.org/10.1016/0167-6989(88)90132-8.

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43

Heydari, Mehran, Moshfiqur Rahman, and Rajender Gupta. "Kinetic Study and Thermal Decomposition Behavior of Lignite Coal." International Journal of Chemical Engineering 2015 (2015): 1–9. http://dx.doi.org/10.1155/2015/481739.

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A thermogravimetric analyzer was employed to investigate the thermal behavior and extract the kinetic parameters of Canadian lignite coal. The pyrolysis experiments were conducted in temperatures ranging from 298 K to 1173 K under inert atmosphere utilizing six different heating rates of 1, 6, 9, 12, 15, and 18 K min−1, respectively. There are different techniques for analyzing the kinetics of solid-state reactions that can generally be classified into two categories: model-fitting and model-free methods. Historically, model-fitting methods are broadly used in solid-state kinetics and show an
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44

Bovendeur, J., F. Spuij, P. G. B. Hermans, and A. Klapwijk. "Mechanisms and Kinetics of COD Removal and Simultaneous Oxygen Consumption in a Rotating Biological Contactor Biofilm." Water Science and Technology 22, no. 1-2 (1990): 75–87. http://dx.doi.org/10.2166/wst.1990.0137.

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A study on aerobic biofilm COD removal and simultaneous respiration is made using a Wazu respirationmeter unit. In a closed recirculating system completely submerged RBC biofilm samples have been examined in short-term batch experiments, using the corresponding waste water or dissolved acetate. The removal of dissolved organic substrate and the respiration were found to answer the ½-order/0-order kinetic model, whereas the removal of suspended solids COD (CODs) showed 1-order kinetics. Under conditions usually met in practice the 0-order rates for dissolved COD(CODd) removal and respiration we
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45

Cherbański, Robert, Krzysztof Wróblewski, and Eugeniusz Molga. "Pyrolysis of waste tyres – The effect of reaction kinetics on the results of thermogravimetric analysis." Chemical and Process Engineering 38, no. 3 (2017): 363–77. http://dx.doi.org/10.1515/cpe-2017-0028.

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Abstract This paper presents a systematic thermogravimetric (TG) study on the kinetics of end-of-life tyre (ELT) pyrolysis. In the experimental part of this work, TG results are compared for tyre samples of different mass and size. This shows that the conduction resistance in the milligram scale (up to ~100 mg) tyre sample can be neglected. A comparison of experimental results demonstrates that the characteristic maxima on the DTG curve (the first derivative of TG signal) shift towards higher temperatures for higher heating rates. This phenomenon is explained to have kinetic origin and it is n
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46

Perrillat, J. P. "Kinetics of high-pressure mineral phase transformations using in situ time-resolved X-ray diffraction in the Paris-Edinburgh cell: a practical guide for data acquisition and treatment." Mineralogical Magazine 72, no. 2 (2008): 683–95. http://dx.doi.org/10.1180/minmag.2008.072.2.683.

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AbstractSynchrotron X-ray diffraction (XRD) is a powerful technique to study in situ and in real-time the structural and kinetic processes of pressure-induced phase transformations. This paper presents the experimental set-up developed at beamline ID27 of the ESRF to perform time-resolved angle dispersive XRD in the Paris-Edinburgh cell. It provides a practical guide for the acquisition of isobaric-isothermal kinetic data and the construction of transformation-time plots. The interpretation of experimental data in terms of reaction mechanisms and transformation rates is supported by an overvie
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47

Wong, A. L., J. M. Harris, and D. B. Marshall. "Measurements of energy dispersion at liquid–solid interfaces: Fluorescence quenching of pyrene bound to fumed silica." Canadian Journal of Physics 68, no. 9 (1990): 1027–34. http://dx.doi.org/10.1139/p90-145.

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The observation of a stretched exponential response in chemical kinetics at solid–liquid interfaces is an indicator of solid surface disorder. In this contribution, we review earlier relaxation kinetics studies of solid surface disorder and the statistical criteria analyzing kinetic data that do not fit single exponential. We draw on these concepts to interpret the fluorescence decay kinetics of pyrene covalently attached to the surface of fumed silica particles that are suspended in methanol. This surface probe exhibits stretched exponential behavior of the form f(t) = exp[−(kt)β] in the deca
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48

Defoiche, Julien, Christophe Debacq, Becca Asquith, et al. "Reduced Rates of B Cell Proliferation in Chronic Lymphocytic Leukemia." Blood 108, no. 11 (2006): 2821. http://dx.doi.org/10.1182/blood.v108.11.2821.2821.

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Abstract Whether chronic lymphocytic leukemia (CLL) represents latent or proliferating disease has been intensively debated. Whilst the dogma that CLL results from accumulation of dormant lymphocytes is supported by the unresponsiveness of leukemic cells to antigens and polyclonal activators, recent in vivo kinetic measurements show that B-lymphocytes do divide at significant rates in CLL. However, B cell kinetics were not compared between CLL patients and healthy controls so it was not possible to ascertain to what extent lymphocyte kinetics were aberrant in CLL. We compared proliferation rat
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49

Galotto, M. J., S. A. Anfossi, and A. Guarda. "Oxygen Absorption Kinetics of Sheets and Films Containing a Commercial Iron-based Oxygen Scavenger." Food Science and Technology International 15, no. 2 (2009): 159–68. http://dx.doi.org/10.1177/1082013208106207.

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Absorption kinetics of three different forms of the same iron-based oxygen scavenger were studied. Oxygen scavengers were used as pellet, sheet, and film materials. Two scavenger concentrations were used for sheet and film forms. Scavenger samples were analyzed at 75 or 100% relative humidities and stored at 5, 15, and 25°C. Oxygen concentration in the headspace was measured as a function of time. Absorption kinetics was best described by the Chapman-Richards empirical growth model rather than by a first-order reaction. Arrhenius behavior was observed for variations in the final absorption rat
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50

Khalil, Abdelouahed, та Tamàs Fülöp. "A comparison of the kinetics of low-density lipoprotein oxidation induced by copper or by γ-rays: Influence of radiation dose-rate and copper concentration". Canadian Journal of Physiology and Pharmacology 79, № 2 (2001): 114–21. http://dx.doi.org/10.1139/y00-080.

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The oxidation of low-density lipoproteins is the first step in the complex process leading to atherosclerosis. The aim of our study was to compare the kinetics of low density lipoprotein oxidation induced by copper ions or by oxygen free radicals generated by60Co γ-rays. The effects of copper concentration and irradiation dose-rate on LDL peroxidation kinetics were also studied. The oxidation of LDL was followed by the measurement of conjugated diene, hydroperoxides, and thiobarbituric acid reactive substance formation as well as α-tocopherol disappearance. In the case of gamma irradiation, th
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