Search Results - "Knowlton, Ted"

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  1. 1

    High speed imaging of particle flow fields in CFB risers by Shaffer, Frank, Gopalan, Balaji, Breault, Ronald W., Cocco, Ray, Karri, S.B. Reddy, Hays, Roy, Knowlton, Ted

    Published in Powder technology (01-07-2013)
    “…Particle flows of high particle concentration are important in many fields, including chemical processing, pharmaceutical processing, energy conversion and…”
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    Journal Article Conference Proceeding
  2. 2

    Cluster characteristics of Geldart Group B particles in a pilot-scale CFB riser. I. Monodisperse systems by Chew, Jia Wei, Hays, Roy, Findlay, John G., Knowlton, Ted M., Reddy Karri, S.B., Cocco, Ray A., Hrenya, Christine M.

    Published in Chemical engineering science (22-01-2012)
    “…Experiments in a circulating fluidized bed (CFB) riser with Geldart Group B particles have been carried out with an emphasis on cluster characterization. In…”
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    Journal Article
  3. 3

    Cluster characteristics of Geldart group B particles in a pilot-scale CFB riser. II. Polydisperse systems by Chew, Jia Wei, Hays, Roy, Findlay, John G., Knowlton, Ted M., Karri, S.B. Reddy, Cocco, Ray A., Hrenya, Christine M.

    Published in Chemical engineering science (22-01-2012)
    “…Experiments with a focus on the impact of polydispersity on clustering characteristics (namely, appearance probability, duration, and frequency) of Geldart…”
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    Journal Article
  4. 4

    Intrusive probes in riser applications by Cocco, Ray A., Karri, S.B. Reddy, Knowlton, Ted M., Findlay, John, Gauthier, Thierry, Chew, Jia Wei, Hrenya, Christine M.

    Published in AIChE journal (01-12-2017)
    “…Many of the probes used to understand hydrodynamics in circulating fluidized bed risers intrude into the environment they are measuring, although assumptions…”
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    Journal Article
  5. 5

    Small-Scale Particle Interactions Are Having Significant Effects on Global Fluidized Bed Behavior by Cocco, Ray, Issangya, Allan, Karri, S.B. Reddy, Freeman, Tim, Jaeger, Heinrich M., Knowlton, Ted M.

    Published in KONA Powder and Particle Journal (2017)
    “…Fluidized bed design and scale-up depends strongly on particle characteristics such as size, shape, and for Geldart Group A particles, the level of fines…”
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    Journal Article
  6. 6

    Species segregation of binary mixtures and a continuous size distribution of Group B particles in riser flow by Chew, Jia Wei, Hays, Roy, Findlay, John G., Karri, S.B. Reddy, Knowlton, Ted M., Cocco, Ray A., Hrenya, Christine M.

    Published in Chemical engineering science (15-10-2011)
    “…Experiments involving a gas–solid, pilot-scale circulating fluidized bed (CFB) have been carried out, with a focus on species segregation measurements in a…”
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    Journal Article
  7. 7

    Reverse core-annular flow of Geldart Group B particles in risers by Chew, Jia Wei, Hays, Roy, Findlay, John G., Knowlton, Ted M., Karri, S.B. Reddy, Cocco, Ray A., Hrenya, Christine M.

    Published in Powder technology (01-05-2012)
    “…Experiments involving monodisperse Geldart Group B particles have been carried out in a pilot-scale riser of a circulating fluidized bed (CFB). Several…”
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    Journal Article
  8. 8

    Impact of material property and operating conditions on mass flux profiles of monodisperse and polydisperse Group B particles in a CFB riser by Chew, Jia Wei, Hays, Roy, Findlay, John G., Knowlton, Ted M., Karri, S.B. Reddy, Cocco, Ray A., Hrenya, Christine M.

    Published in Powder technology (25-11-2011)
    “…Experiments directed at understanding local mass flux behavior of Geldart Group B materials in the riser of a gas-solids circulating fluidized bed (CFB) have…”
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    Journal Article
  9. 9

    Simulating hydrodynamics of hot and large Group A particle systems at cold conditions to obtain data for scale-up by Knowlton, Ted M.

    Published in Particuology (01-12-2010)
    “…Scaling laws based on the concept of dimensional similitude are proposed to simulate the hydrodynamics of hot and large particle systems at conditions of cold…”
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    Journal Article
  10. 10

    How Underflow Standpipes Adjust to Maintain Pressure Balance Around a Circulation Loop by Knowlton, Ted, Karri, S. B. Reddy

    Published in Chemie ingenieur technik (01-01-2023)
    “…The standpipe has become a standard element of most circulation loops. In the past, standpipes have been thought of as a device to only allow solids to…”
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    Journal Article
  11. 11

    History of fluidization in North America by Knowlton, Ted M., Keairns, Dale L., Yang, Wen-Ching

    Published in Powder technology (01-08-2023)
    “…This paper primarily discusses the development of fluidization in North America in the 20th century. Although the history described is primarily in North…”
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    Journal Article
  12. 12

    Effect of Aeration on the Operation of Cyclone Diplegs Fitted with Trickle Valves by Karri, S. B. Reddy, Knowlton, Ted M

    “…Tests were conducted with a trickle valve attached to a 100-mm-diameter dipleg to determine the effect of trickle valve operation with aerated and unaerated…”
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    Journal Article
  13. 13

    Bed density and bubble void fraction variation in a fluidized bed stripper by Issangya, Allan S., Cocco, Ray A., Reddy Karri, S.B., Knowlton, Ted M., Wei Chew, Jia

    Published in Chemical engineering science (12-10-2022)
    “…•Beddensity, pressure fluctuation andbubble void fraction quantified for strippers.•Gratings gave higher bed density and allowed a wider range of operating…”
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    Journal Article
  14. 14

    Engaging the Future: Forecasts, Scenarios, Plans, and Projects by Knowlton, Ted

    “…Engaging the Future: Forecasts, Scenarios, Plans, and Projects, edited by Lewis D. Hopkins and Marisa A. Zapata, is reviewed…”
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    Journal Article Book Review
  15. 15

    Particle clusters in and above fluidized beds by Cocco, Ray, Shaffer, Frank, Hays, Roy, Reddy Karri, S.B., Knowlton, Ted

    Published in Powder technology (25-10-2010)
    “…High-speed video imaging of particle clusters in and above a fluidized bed suggests that clustering is significant for FCC catalyst and polyethylene powders…”
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    Journal Article Conference Proceeding
  16. 16

    Solids flux profiles of Geldart Group A particles in high‐velocity circulating fluidized bed risers by Issangya, Allan S., Karri, S. B. Reddy, Cocco, Ray A., Knowlton, Ted, Chew, Jia Wei

    Published in Canadian journal of chemical engineering (01-01-2023)
    “…Circulating fluidized bed (CFB) risers using Group A particles have traditionally, mostly, been considered to operate in the fast fluidization regime, which…”
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    Journal Article
  17. 17

    Introduction to Fluidization by Cocco, Ray, Karri, S B Reddy, Knowlton, Ted

    Published in Chemical engineering progress (01-11-2014)
    “…Figure 1 shows the increase in pressure drop with increasing superficial gas velocity through a bed of particles that is initially packed. As the superficial…”
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    Magazine Article Journal Article
  18. 18

    Applying Innovative Performance Metrics for Corridor Evaluation by Vyas, Maria, Harris, Jeffery, Knowlton, Ted, LaBonty, G. J., Milam, Ronald T., Seager, Shawn, Williges, Chris, Zundel, Lisa

    Published in Transportation research record (01-12-2018)
    “…Widespread application of traditional performance metrics such as vehicle level of service has resulted in transportation networks that are often suited for…”
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    Journal Article
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  20. 20

    Use of pressure to mitigate gas bypassing in fluidized beds of FCC catalyst particles by Issangya, Allan S., Reddy Karri, S.B., Knowlton, Ted, Cocco, Ray

    Published in Powder technology (01-03-2016)
    “…Deep gas fluidized beds of low-fines fluid catalytic cracking (FCC) catalyst particles can have severe gas maldistribution due to gas bypassing. Tests were…”
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    Journal Article