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Artykuły w czasopismach na temat „Residence time distribution”

Autor: Grafiati

Data publikacji: 4 czerwca 2021

Data aktualizacji: 25 lipca 2025

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1

Landfeld, A., R. Žitný, M. Houška, K. Kýhos, and P. Novotná. "Residence time distribution during egg yolk pasteurisation." Czech Journal of Food Sciences 20, No. 5 (2011): 193–201. http://dx.doi.org/10.17221/3531-cjfs.

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This work describes the determination of the average residence times during egg yolk &ndash; and whole liquid eggs pasteurisation in an industrial pasteurisation equipment (plate pasteuriser + tube holder). For the detection of the impulse the conductivity method was used. Conductivity was then monitored using the bridge method. In the system, the total of 3 probes were placed. To mark the particles of the flowing product, salted yolk with the content of salt of 1.3 or 1.8% was used. In addition, rheological properties of pasteurised yolk were determined at the temperatures of 5, 25, 45, a

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2

Iordache, Octavian, and Sergiu Corbu. "Random residence time distribution." Chemical Engineering Science 41, no. 8 (1986): 2099–102. http://dx.doi.org/10.1016/0009-2509(86)87127-5.

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3

Werner, Timothy M., and Robert H. Kadlec. "Wetland residence time distribution modeling." Ecological Engineering 15, no. 1-2 (2000): 77–90. http://dx.doi.org/10.1016/s0925-8574(99)00036-1.

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4

Rodrigues, Alírio E. "Residence time distribution (RTD) revisited." Chemical Engineering Science 230 (February 2021): 116188. http://dx.doi.org/10.1016/j.ces.2020.116188.

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5

Li, Mingheng. "Residence time distribution in RO channel." Desalination 506 (June 2021): 115000. http://dx.doi.org/10.1016/j.desal.2021.115000.

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6

Martin, A. D. "Interpretation of residence time distribution data." Chemical Engineering Science 55, no. 23 (2000): 5907–17. http://dx.doi.org/10.1016/s0009-2509(00)00108-1.

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7

Jager, T., P. Santbulte, and D. J. van Zuilichem. "Residence time distribution in kneading extruders." Journal of Food Engineering 24, no. 3 (1995): 285–94. http://dx.doi.org/10.1016/0260-8774(95)90047-f.

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8

Chen, Liqin, Zaoqi Pan, and Guo-Hua Hu. "Residence time distribution in screw extruders." AIChE Journal 39, no. 9 (1993): 1455–64. http://dx.doi.org/10.1002/aic.690390905.

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9

Hill, S. "Residence time distribution in continuous crystallisers." Journal of Applied Chemistry 20, no. 10 (2007): 300–304. http://dx.doi.org/10.1002/jctb.5010201001.

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10

Pattanaik, Biplab R., Ajay Gupta, and Hariharan S. Shankar. "Residence Time Distribution Model for Soil Filters." Water Environment Research 76, no. 2 (2004): 168–74. http://dx.doi.org/10.2175/106143004x141708.

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11

Berezhkovskii, Alexander M., Veaceslav Zaloj, and Noam Agmon. "Residence time distribution of a Brownian particle." Physical Review E 57, no. 4 (1998): 3937–47. http://dx.doi.org/10.1103/physreve.57.3937.

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12

Hsu, Jyh-Ping, and Tzu-Hsuan Wei. "Residence Time Distribution of a Cylindrical Microreactor." Journal of Physical Chemistry B 109, no. 18 (2005): 9160–65. http://dx.doi.org/10.1021/jp044231u.

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13

Durney, T. E., and T. P. Meloy. "Experimental proof: Residence time distribution in cascadography." International Journal of Mineral Processing 14, no. 4 (1985): 313–17. http://dx.doi.org/10.1016/0301-7516(85)90054-7.

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14

Fan, L. T., J. R. Too, and R. Nassar. "Stochastic simulation of residence time distribution curves." Chemical Engineering Science 40, no. 9 (1985): 1743–49. http://dx.doi.org/10.1016/0009-2509(85)80036-1.

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15

Daud, W. R. B. W., and W. D. Armstrong. "Residence time distribution of the drum dryer." Chemical Engineering Science 43, no. 9 (1988): 2399–405. http://dx.doi.org/10.1016/0009-2509(88)85174-1.

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16

Haas, Charles N., Josh Joffe, Mark S. Heath, and Joseph Jacangelo. "Continuous Flow Residence Time Distribution Function Characterization." Journal of Environmental Engineering 123, no. 2 (1997): 107–14. http://dx.doi.org/10.1061/(asce)0733-9372(1997)123:2(107).

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17

Rogovin, Z., Y. C. Lo, J. C. Herbst, and K. Rajamani. "Closed grinding circuit residence time distribution analysis." Mining, Metallurgy & Exploration 4, no. 4 (1987): 207–14. http://dx.doi.org/10.1007/bf03402694.

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18

Sancho, Martin F., and M. A. Rao. "Residence time distribution in a holding tube." Journal of Food Engineering 15, no. 1 (1992): 1–19. http://dx.doi.org/10.1016/0260-8774(92)90037-7.

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19

Fernández-Sempere, J., R. Font-Montesinos, and O. Espejo-Alcaraz. "Residence time distribution for unsteady-state systems." Chemical Engineering Science 50, no. 2 (1995): 223–30. http://dx.doi.org/10.1016/0009-2509(94)00230-o.

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20

Wojewódka, Przemysław, Robert Aranowski, and Christian Jungnickel. "Residence time distribution in rapid multiphase reactors." Journal of Industrial and Engineering Chemistry 69 (January 2019): 370–78. http://dx.doi.org/10.1016/j.jiec.2018.09.037.

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21

Renström, Roger. "Mean Residence Time and Residence Time Distribution When Sawdust Is Dried in Continuous Dryers." Drying Technology 26, no. 12 (2008): 1457–63. http://dx.doi.org/10.1080/07373930802412066.

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22

Diaz, Francisco, and Juan Yianatos. "Residence time distribution in large industrial flotation cells." Atoms for Peace: an International Journal 3, no. 1 (2010): 2. http://dx.doi.org/10.1504/afp.2010.031015.

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23

Baranyai, L., and A. Doma. "Residence Time Distribution Studies on Water-Softening Reactors." Isotopenpraxis Isotopes in Environmental and Health Studies 25, no. 8 (1989): 341–43. http://dx.doi.org/10.1080/10256018908624147.

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24

Yianatos, J., L. Bergh, L. Vinnett, and F. Díaz. "Modeling of residence time distribution in regrinding Vertimill." Minerals Engineering 53 (November 2013): 174–80. http://dx.doi.org/10.1016/j.mineng.2013.08.006.

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25

Vikhansky, A. "Numerical analysis of residence time distribution in microchannels." Chemical Engineering Research and Design 89, no. 3 (2011): 347–51. http://dx.doi.org/10.1016/j.cherd.2010.06.010.

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26

Iroba, K. L., F. Weigler, J. Mellmann, T. Metzger, and E. Tsotsas. "Residence Time Distribution in Mixed-Flow Grain Dryers." Drying Technology 29, no. 11 (2011): 1252–66. http://dx.doi.org/10.1080/07373937.2011.591711.

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27

Patwardhan, Ashwin W. "Prediction of Residence Time Distribution of Stirred Reactors." Industrial & Engineering Chemistry Research 40, no. 24 (2001): 5686–95. http://dx.doi.org/10.1021/ie0103198.

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28

Cvengroš, Ján, Viktor Badin, and Štefan Pollák. "Residence time distribution in a wiped liquid film." Chemical Engineering Journal and the Biochemical Engineering Journal 59, no. 3 (1995): 259–63. http://dx.doi.org/10.1016/0923-0467(94)02960-1.

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29

Cantu-Perez, Alberto, Shuang Bi, Simon Barrass, Mark Wood, and Asterios Gavriilidis. "Residence time distribution studies in microstructured plate reactors." Applied Thermal Engineering 31, no. 5 (2011): 634–39. http://dx.doi.org/10.1016/j.applthermaleng.2010.04.024.

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30

Trachsel, Franz, Axel Günther, Saif Khan, and Klavs F. Jensen. "Measurement of residence time distribution in microfluidic systems." Chemical Engineering Science 60, no. 21 (2005): 5729–37. http://dx.doi.org/10.1016/j.ces.2005.04.039.

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31

BOSKOVIC, D., and S. LOEBBECKE. "Modelling of the residence time distribution in micromixers." Chemical Engineering Journal 135 (January 15, 2008): S138—S146. http://dx.doi.org/10.1016/j.cej.2007.07.058.

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32

Haitjema, H. M. "On the residence time distribution in idealized groundwatersheds." Journal of Hydrology 172, no. 1-4 (1995): 127–46. http://dx.doi.org/10.1016/0022-1694(95)02732-5.

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33

Gao, Yijie, Aditya Vanarase, Fernando Muzzio, and Marianthi Ierapetritou. "Characterizing continuous powder mixing using residence time distribution." Chemical Engineering Science 66, no. 3 (2011): 417–25. http://dx.doi.org/10.1016/j.ces.2010.10.045.

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34

Patrick, Robert H., Theresa Klindera, Lawrence L. Crynes, Ramon L. Cerro, and Martin A. Abraham. "Residence time distribution in three-phase monolith reactor." AIChE Journal 41, no. 3 (1995): 649–57. http://dx.doi.org/10.1002/aic.690410321.

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35

Gao, Jun, Gregory C. Walsh, David Bigio, Robert M. Briber, and Mark D. Wetzel. "Residence-time distribution model for twin-screw extruders." AIChE Journal 45, no. 12 (1999): 2541–49. http://dx.doi.org/10.1002/aic.690451210.

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36

Dong, Zhengya, Shuainan Zhao, Yuchao Zhang, Chaoqun Yao, Quan Yuan, and Guangwen Chen. "Mixing and residence time distribution in ultrasonic microreactors." AIChE Journal 63, no. 4 (2016): 1404–18. http://dx.doi.org/10.1002/aic.15493.

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37

Bošković, D., S. Loebbecke, G. A. Gross, and J. M. Koehler. "Residence Time Distribution Studies in Microfluidic Mixing Structures." Chemical Engineering & Technology 34, no. 3 (2011): 361–70. http://dx.doi.org/10.1002/ceat.201000352.

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38

Goodall, C. M., and C. T. O'Connor. "Residence time distribution studies in a flotation column. Part 2: the relationship between solids residence time distribution and metallurgical performance." International Journal of Mineral Processing 36, no. 3-4 (1992): 219–28. http://dx.doi.org/10.1016/0301-7516(92)90045-x.

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39

Li, Liang Chao. "CFD Simulation of Gas Residence Time Distribution in Agitated Tank." Advanced Materials Research 732-733 (August 2013): 467–71. http://dx.doi.org/10.4028/www.scientific.net/amr.732-733.467.

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Gas residence time is an important parameter for gas-liquid agitated tank. Two approaches, i.e., Euler-Tracer method and CFD-DPM method are proposed for predicting gas residence time distribution (RTD) in an aerated agitated tank by using a Fluent 6.2 software package. The simulation results show that the characteristic of the gas-RTD is a curve with single peak and long tailing. Bubble size, stirring speed and gas inlet flow rate have great effect on gas-RTD in the stirred tank. Small bubbles have wider residence time distribution and stay in the vessel longer than the large bubbles and tend

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40

Baker, Alastair, Alex Fells, Thomas Shaw, Chris J. Maher, and Bruce C. Hanson. "Effect of Scale-Up on Residence Time and Uranium Extraction on Annular Centrifugal Contactors (ACCs)." Separations 10, no. 6 (2023): 331. http://dx.doi.org/10.3390/separations10060331.

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This work reports the effect of scaling up annular centrifugal contactors (ACCs) upon the residence time distribution and the efficiency of extraction of uranium. The experiments were carried out in a multi-scale ACC platform of three ACCs with rotor diameters of 12, 25, and 40 mm. To enable direct comparison across all three scales of ACC, the residence time distributions were acquired by injecting dye into the solvent phase at a constant relative volume related to the ACC liquid holdup. Across all scales and flowrates, there was little difference in residence time distribution (<6 residen

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41

El_Tokhy, Mohamed S., Ibrahim M. Fayed, Mouldi A. Bedda, and H. Kasban. "Dead Time Correction of Residence Time Distribution through Digital Signal Processing." i-manager's Journal on Digital Signal Processing 3, no. 4 (2015): 1–8. http://dx.doi.org/10.26634/jdp.3.4.3705.

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42

Liem, L. E., S. J. Stanley, and Daniel W. Smith. "Residence time distribution analysis as related to the effective contact time." Canadian Journal of Civil Engineering 26, no. 2 (1999): 135–44. http://dx.doi.org/10.1139/l98-051.

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Sixteen full-scale tracer studies were completed at two water treatment plants to assess disinfection performance under the concentration-time (CT) concept. The step residence time distribution (F RTD) was developed for each case. The value of the effective contact time, t10, in the CT concept was then obtained. For reservoirs without baffles, the t10 values were found to be much smaller than the expected values, indicating poor performance under the CT concept. Several models were used to interpret the F RTD characteristics, but the results were unsatisfactory. The standard jet model was then

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43

Tinker, Sarah C., Christine L. Moe, Mitchel Klein, et al. "Drinking water residence time in distribution networks and emergency department visits for gastrointestinal illness in Metro Atlanta, Georgia." Journal of Water and Health 7, no. 2 (2009): 332–43. http://dx.doi.org/10.2166/wh.2009.022.

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We examined whether the average water residence time, the time it takes water to travel from the treatment plant to the user, for a zip code was related to the proportion of emergency department (ED) visits for gastrointestinal (GI) illness among residents of that zip code. Individual-level ED data were collected from all hospitals located in the five-county metro Atlanta area from 1993 to 2004. Two of the largest water utilities in the area, together serving 1.7 million people, were considered. People served by these utilities had almost 3 million total ED visits, 164,937 of them for GI illne

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44

Zhang, Li, Yi Gang Ding, Jun Ji, Chang Yan Yang, and Yuan Xin Wu. "Particle Residence Time Distribution of Collection Zone in Packed Flotation Column." Advanced Materials Research 781-784 (September 2013): 2195–200. http://dx.doi.org/10.4028/www.scientific.net/amr.781-784.2195.

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In order to make a further understanding of flow pattern and back mixing in the flotation process, the study about particle residence time distribution of collection zone in a packed column has been designed. The pulse tracer method was applied and the particle tracers were the mineral gangue in special size class. The residence time distribution curves of our experiment data shows that there are particle back mixings which were caused by fluid flow and geometry factors in the column. The tank-in-series model has a better fitting to the particle residence time distribution in the column accord

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45

Canevarolo, S. V., T. J. A. Mélo, J. A. Covas, and O. S. Carneiro. "Direct Method for Deconvoluting Two Residence Time Distribution Curves." International Polymer Processing 16, no. 4 (2001): 334–40. http://dx.doi.org/10.1515/ipp-2001-0004.

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Abstract A pair of related Residence Time Distribution (RTD) curves obtained experimentally during extrusion, are deconvoluted using a methodology based on the concept of equivalent residence times. Two points of two RTD curves are equivalent when the same percentage of tracer has exited the system. The time scale of the deconvoluted curve is obtained by subtracting the two equivalent time values of the available RTD curves. The method was tested using simulated pulse-shaped RTD curves and also carrying out measurements on a twin screw extruder. Despite the experimental errors involved, the tw

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46

GRETE, PATRICK, and MARIO MARKUS. "RESIDENCE TIME DISTRIBUTIONS FOR DOUBLE-SCROLL ATTRACTORS." International Journal of Bifurcation and Chaos 17, no. 03 (2007): 1007–15. http://dx.doi.org/10.1142/s0218127407017720.

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We investigated a choice of prototypical double-scroll attractors, namely trajectories resulting from Lorenz equations and from two sets of equations related to Chua's circuits. We found that the probability distribution for the residence times within a given scroll consists of prominent, exponentially decaying peaks. Similar peaks had been reported for stochastically resonant systems, which are driven periodically; however, in view of our results in autonomous systems, the appearance of such peaks has a higher degree of generality. In the systems we investigated, each peak corresponds to a su

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47

Newell, Bob, Jeff Bailey, Ashraful Islam, Lisa Hopkins, and Paul Lant. "Characterising bioreactor mixing with residence time distribution (RTD) tests." Water Science and Technology 37, no. 12 (1998): 43–47. http://dx.doi.org/10.2166/wst.1998.0495.

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This paper presents a technique for configuring wastewater process simulations so that the hydraulic characteristics are similar to the real plant. Residence time distribution (RTD) tests are performed on two biological nutrient removal pilot plants. The RTD tests proved valuable for evaluating mixing effectiveness, volume utilisation and for determining an appropriate hydraulic topology for the dynamic models of the pilot plants. As a result of this work, simulation execution times became much faster due to a significant reduction in the number of effective stirred tanks required in the model

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48

Canevarolo, S. V., T. J. A. Mélo, J. A. Cavas, and O. S. Carneiro. "Direct Method for Deconvolving Two Residence Time Distribution Curves." International Polymer Processing 16, no. 4 (2001): 334–40. http://dx.doi.org/10.3139/217.1660.

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49

Coblyn, Matthew, Agnieszka Truszkowska, and Goran Jovanovic. "Characterization of microchannel hemodialyzers using residence time distribution analysis." Journal of Flow Chemistry 6, no. 1 (2016): 53–61. http://dx.doi.org/10.1556/1846.2015.00041.

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50

BRUCATO, A., V. BRUCATO, and L. RIZZUTI. "RESIDENCE TIME DISTRIBUTION OF SOLID PARTICLES IN STIRRED VESSELS." Chemical Engineering Communications 115, no. 1 (1992): 161–81. http://dx.doi.org/10.1080/00986449208936035.

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