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  • #REDIRECT [[Theoretical plate]]
    31 bytes (3 words) - 11:56, 1 August 2008
  • #REDIRECT[[Theoretical plate]]
    30 bytes (3 words) - 12:25, 1 August 2008
  • #REDIRECT[[Theoretical plate]]
    30 bytes (3 words) - 12:25, 1 August 2008
  • #REDIRECT[[Theoretical plate]]
    30 bytes (3 words) - 12:26, 1 August 2008
  • #REDIRECT[[Theoretical plate]]
    30 bytes (3 words) - 12:27, 1 August 2008
  • #REDIRECT [[Theoretical plate/Definition]]
    42 bytes (4 words) - 11:58, 1 August 2008
  • #REDIRECT [[Theoretical plate/Bibliography]]
    44 bytes (4 words) - 11:50, 1 August 2008
  • #REDIRECT [[Theoretical plate/Related Articles]]
    48 bytes (5 words) - 11:49, 1 August 2008
  • #REDIRECT [[Theoretical plate/External Links]]
    46 bytes (5 words) - 11:51, 1 August 2008
  • {{rpl|Theoretical plate}} {{rpl|Theoretical plate}}
    864 bytes (90 words) - 03:49, 26 September 2013
  • {{r|Theoretical plate}}
    411 bytes (47 words) - 22:10, 10 March 2011
  • {{r|Theoretical plate}}
    316 bytes (34 words) - 22:16, 10 March 2011
  • {{r|Theoretical plate}}
    260 bytes (28 words) - 13:44, 2 August 2008
  • {{r|Theoretical plate}}
    248 bytes (27 words) - 02:24, 17 November 2008
  • {{r|Theoretical plate}}
    462 bytes (56 words) - 12:12, 18 March 2012
  • {{r|Theoretical plate}}
    412 bytes (45 words) - 22:14, 10 March 2011
  • {{r|Theoretical plate}}
    333 bytes (36 words) - 22:09, 10 March 2011
  • {{r|Theoretical plate}}
    578 bytes (68 words) - 22:01, 10 March 2011
  • A '''theoretical plate''' in many [[chemical engineering]] separation processes is a hypothetical ...''height'''''. It is simply a hypothetical equilibrium stage. However, the theoretical plate in packed beds, chromatography and other applications is defined as having
    8 KB (1,273 words) - 23:39, 8 February 2010
  • ...on of vapor and liquid as they that enter the packed bed. The number of [[Theoretical plate|theoretical stages]] required to make a given separation is calculated is a ...uilibrium stage, known as the ''[[Theoretical plate|height equivalent to a theoretical plate]]'' (HETP), is also determined. The total packing height required is the nu
    6 KB (961 words) - 20:45, 1 November 2013
  • *''Key [[Continuous distillation|fractional distillation]] concepts'': [[Theoretical plate|theoretical stage]]s, x-y diagrams, multicomponent distillation, column com
    3 KB (335 words) - 21:47, 26 April 2010
  • The '''Fenske equation''' is used for calculating the minimum number of [[theoretical plate]]s required for the separation of a binary feed stream by a [[Continuous di
    7 KB (1,013 words) - 13:29, 24 October 2012
  • {{see also|Continuous distillation|Theoretical plate}} ...e distillation column. The more reflux is provided for a given number of [[Theoretical plate|distillation plates]], the better is the column's separation of lower boili
    6 KB (895 words) - 17:34, 21 November 2012
  • ...May 1951}}</ref> This method uses the fact that the composition at each [[theoretical plate]] (or [[equilibrium stage]]) is completely determined by the [[mole fractio
    6 KB (955 words) - 22:50, 17 February 2010
  • ...n separation would equal the number of theoretical equilibrium stages or [[theoretical plate]]s. However, that is very rarely the case. Hence, a distillation column n ...to a theoretical equilibrium stage, known as the ''height equivalent to a theoretical plate'' (HETP), is also determined. The total packing height required is the num
    21 KB (3,308 words) - 09:16, 6 March 2024
  • ...perforations are covered with caps that are free to move upward. See the [[Theoretical plate]] article for a drawing and explanation of bubble-cap trays.</ref> Sieve tr
    11 KB (1,664 words) - 09:37, 6 March 2024
  • *{{pl|Theoretical plate}}
    9 KB (1,159 words) - 17:35, 14 March 2024
  • ...e top of the column top to the bottom. Therefore, the vacuum column uses [[Theoretical plate|distillation tray]]s only where withdrawing products from the side of the c
    11 KB (1,703 words) - 16:10, 10 February 2024
  • ...m the column top to the column bottom. Therefore, the vacuum column uses [[Theoretical plate|distillation tray]]s only where withdrawing products from the side of the c
    11 KB (1,670 words) - 16:11, 10 February 2024