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  • https://eng.libretexts.org/Bookshelves/Chemical_Engineering/Chemical_Engineering_Separations%3A_A_Handbook_for_Students_(Lamm_and_Jarboe)/zz%3A_Back_Matter
  • https://eng.libretexts.org/Bookshelves/Chemical_Engineering/Chemical_Engineering_Separations%3A_A_Handbook_for_Students_(Lamm_and_Jarboe)/zz%3A_Back_Matter/20%3A_Glossary
    Example and Directions Words (or words that have the same definition) The definition is case sensitive (Optional) Image to display with the definition [Not displayed in Glossary, only in pop-up on pag...Example and Directions Words (or words that have the same definition) The definition is case sensitive (Optional) Image to display with the definition [Not displayed in Glossary, only in pop-up on pages] (Optional) Caption for Image (Optional) External or Internal Link (Optional) Source for Definition "Genetic, Hereditary, DNA ...") (Eg. "Relating to genes or heredity") The infamous double helix CC-BY-SA; Delmar Larsen Glossary Entries Definition Image Sample Word 1 Sample Definition 1
  • https://eng.libretexts.org/Bookshelves/Chemical_Engineering/Chemical_Engineering_Separations%3A_A_Handbook_for_Students_(Lamm_and_Jarboe)/01%3A_Chapters
  • https://eng.libretexts.org/Bookshelves/Chemical_Engineering/Chemical_Engineering_Separations%3A_A_Handbook_for_Students_(Lamm_and_Jarboe)/01%3A_Chapters/1.01%3A_Performance_Metrics_for_Separation_Processes
    n(1)i,k = mass or molar flow rate of species i leaving separator k in first product stream (mass time -1 or mol time -1 ) n(2)i,k = mass or molar flow rate of species i...n(1)i,k = mass or molar flow rate of species i leaving separator k in first product stream (mass time -1 or mol time -1 ) n(2)i,k = mass or molar flow rate of species i leaving separator k in second product stream (mass time -1 or mol time -1 ) SRi,k=n(1)i,k/n(2)i,k=SFi,k/(1SFi,k)
  • https://eng.libretexts.org/Bookshelves/Chemical_Engineering/Chemical_Engineering_Separations%3A_A_Handbook_for_Students_(Lamm_and_Jarboe)/00%3A_Front_Matter
  • https://eng.libretexts.org/Bookshelves/Chemical_Engineering/Chemical_Engineering_Separations%3A_A_Handbook_for_Students_(Lamm_and_Jarboe)
    Chemical Engineering Separations: A Handbook for Students is intended for use by undergraduate students who are taking a course in chemical engineering separations. The handbook assumes that students...Chemical Engineering Separations: A Handbook for Students is intended for use by undergraduate students who are taking a course in chemical engineering separations. The handbook assumes that students have taken one or two semesters of chemical engineering thermodynamics, one semester of heat and mass transfer, and one semester of computational methods for chemical engineering.
  • https://eng.libretexts.org/Bookshelves/Chemical_Engineering/Chemical_Engineering_Separations%3A_A_Handbook_for_Students_(Lamm_and_Jarboe)/00%3A_Front_Matter/05%3A_Preface
    For this reason, we have written the handbook to emphasize how to optimize process conditions, how to retrofit an existing unit to meet a given separation objective while not exceeding operating capac...For this reason, we have written the handbook to emphasize how to optimize process conditions, how to retrofit an existing unit to meet a given separation objective while not exceeding operating capacity, or how to select the best existing or pre-fabricated unit to meet a separation objective while maintaining safe operation at a reasonable cost.
  • https://eng.libretexts.org/Bookshelves/Chemical_Engineering/Chemical_Engineering_Separations%3A_A_Handbook_for_Students_(Lamm_and_Jarboe)/01%3A_Chapters/1.04%3A_Absorption_and_Stripping
    Assume a foaming factor of 0.90, trays that have an Ah/Aa>0.10 and a surface tension of 70 dyne/cm and ignore the contribution of the solute to the physical properties of the carrier streams. ...Assume a foaming factor of 0.90, trays that have an Ah/Aa>0.10 and a surface tension of 70 dyne/cm and ignore the contribution of the solute to the physical properties of the carrier streams. The column has a diameter of 0.80m, weir height of 2.0 inches, 3/16” hole diameter, C0 = 0.73, 10% of the column area is occupied by downcomers, 10% of the active area is occupied by sieve tray holes.
  • https://eng.libretexts.org/Bookshelves/Chemical_Engineering/Chemical_Engineering_Separations%3A_A_Handbook_for_Students_(Lamm_and_Jarboe)/01%3A_Chapters/1.06%3A_Membranes
    In order to justify the cost of the membrane, we need to filter 200 m 3 of water every day per m 2 of membrane purchased. ciP = concentration of species i on the permeate side of the membrane ...In order to justify the cost of the membrane, we need to filter 200 m 3 of water every day per m 2 of membrane purchased. ciP = concentration of species i on the permeate side of the membrane (mol volume -1 ) We aim to recover 30% of the H 2 SO 4 from a 0.78 m 3 /hr feed containing 300 kg/m 3 of H 2 SO 4 and smaller amounts of CuSO 4 and NiSO 4 . We have up to 1.0 m 3 /hr of water available as a wash stream.
  • https://eng.libretexts.org/Bookshelves/Chemical_Engineering/Chemical_Engineering_Separations%3A_A_Handbook_for_Students_(Lamm_and_Jarboe)/01%3A_Chapters/1.03%3A_Liquid-liquid_Extraction
    Pmin = Point associated with the minimum feasible S/F for this feed, solvent and (raffinate or extract) composition. Pmin is the intersection of the line connecting points (\...Pmin = Point associated with the minimum feasible S/F for this feed, solvent and (raffinate or extract) composition. Pmin is the intersection of the line connecting points (RN, S) and the line that is an extension of the upper-most equilibrium tie-line. Ignoring the contribution of the solute and the co-solvent to the physical properties of each phase, find the required column diameter and height.
  • https://eng.libretexts.org/Bookshelves/Chemical_Engineering/Chemical_Engineering_Separations%3A_A_Handbook_for_Students_(Lamm_and_Jarboe)/01%3A_Chapters/1.07%3A_Sorption_and_Chromatography
    si = variance of the Gaussian peak of the distribution of species i along the column length (time) Species B has a mass transfer coefficient of 1.0×105 m/s in the mobile phase, incl...si = variance of the Gaussian peak of the distribution of species i along the column length (time) Species B has a mass transfer coefficient of 1.0×105 m/s in the mobile phase, inclusion porosity of 0.50, Kd=60, E=3.0×108 m 2 /s, effective diffusivity of 4×1012 m 2 /s and ka=200 s -1 . What is the resolution of these two species in the proposed operating condition?

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