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Oxygen Transport Membranes
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Oxygen Transport Membranes

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Questions and Answers

What is the optimum O2 concentration from the ASU for oxy-fuel technology?

  • 90-95%
  • 75-80%
  • 80-85%
  • 97-98% (correct)
  • What is the primary component of the flue gas recirculation rate for oxy-fuel technology?

  • N2 and O2
  • NOx and SOx
  • CO and H2
  • CO2 and H2O (correct)
  • What is the reason for considering oxy-fuel technology in power generation?

  • Reduces CO2 emissions only
  • Eliminates N2 from combustor outlet simplifying the carbon capture step (correct)
  • Adds complexity to the carbon capture process
  • Increases NOx emissions
  • What is the expected O2 to the boiler with a 70% flue gas recirculation rate?

    <p>25-30%</p> Signup and view all the answers

    What is the ASU in the context of oxy-fuel technology?

    <p>Air separation unit</p> Signup and view all the answers

    What is the typical adiabatic flame temperature calculation based on for oxy-fuel technology?

    <p>Coal combustion</p> Signup and view all the answers

    What is the expected O2 concentration from the ASU for oxy-fuel technology?

    <p>97-98%</p> Signup and view all the answers

    What is the total enthalpy change of the stoichiometric combustion process C(s) + O2(g) → CO2(g) under adiabatic, isobaric conditions?

    <p>$\Delta H_T = nI ( H_I(T_f) - H_I(T_o) ) + nCO2 ( H_{CO2}(T_f) - H_{CO2}(T_o) )$</p> Signup and view all the answers

    What is the value of $T_f$ for the pure O2 feed to the combustion process with $T_o = 298K$?

    <p>$T_f = 5,598 K$</p> Signup and view all the answers

    What is the heat capacity of CO2 for the air feed to the combustion process?

    <p>$C_pCO2 = 54.6 J/mol.K$</p> Signup and view all the answers

    What is the ratio of $nI/nCO2$ for the air feed to the combustion process?

    <p>$nI/nCO2 = 3.76$</p> Signup and view all the answers

    What is the mole fraction of N2 in the air separation using distillation at operating pressures of between 1-20 bar?

    <p>Mole fraction of N2 is ~78%</p> Signup and view all the answers

    What is the primary design variable for the mass transfer area of the membrane module in air separation using membranes?

    <p>Permeance</p> Signup and view all the answers

    What is the preferred option for large-scale Oxygen requirements at this time?

    <p>Cryogenic distillation</p> Signup and view all the answers

    What does the Robeson plot illustrate?

    <p>The relationship between O2/N2 selectivity and O2 permeability for polymeric membranes</p> Signup and view all the answers

    What is the formula for calculating the mass transfer area of a membrane?

    <p>$ ext{selectivity} imes ext{degree of recovery}$</p> Signup and view all the answers

    What are the three stages of operation for oxygen ion transport membranes (OTMs)?

    <p>O2 adsorption, oxygen bulk diffusion, and surface reaction</p> Signup and view all the answers

    What are the disadvantages of oxygen transport membranes (OTMs)?

    <p>High operating temperatures and the need to ensure only surface reaction controls</p> Signup and view all the answers

    What does the design of an oxygen transport membrane module involve calculating?

    <p>The membrane area required for oxygen separation</p> Signup and view all the answers

    What is the application of oxygen transport membranes demonstrated in the text?

    <p>Operation in an automobile and in a coal-fired plant</p> Signup and view all the answers

    What is the limitation of current membrane systems mentioned in the text?

    <p>Limited to less than 400 tonnes of O2 per day</p> Signup and view all the answers

    What is the equation for the minimum power requirements for oxy-fuel combustion CO2 capture?

    <p>$Minimum Power = \left( \frac{\ln\left(\frac{\frac{y_2}{X}}{\frac{y_{O2}}{2}}\right)}{\ln\left(\frac{p_1}{p}\right)} - \frac{\ln y_{O2} + \frac{y_2}{X}}{y_{O2}}\right) \times \left(\frac{RT}{F_{CO2}}\right)$</p> Signup and view all the answers

    What is the value of total CO2 emissions used in the calculation of minimum power requirements?

    <p>2,470 kmol/s</p> Signup and view all the answers

    What is the temperature at which the pure CO2 product is compressed to 100 bar?

    <p>298K</p> Signup and view all the answers

    What is the value of yO2 in the equation for minimum power requirements?

    <p>0.209</p> Signup and view all the answers

    What is the total EU power demand?

    <p>2320 GW</p> Signup and view all the answers

    What is the approximate EU electric power demand?

    <p>450 GW</p> Signup and view all the answers

    What is the reason for considering this technology, as mentioned in the text?

    <p>Eliminates N2 from combustor outlet simplifying the carbon capture step.</p> Signup and view all the answers

    What is the value of the minimum power requirement for oxy-fuel combustion CO2 capture?

    <p>58.3 GW</p> Signup and view all the answers

    What is the effect of the technology on NOx emissions?

    <p>Significant reduction in NOx.</p> Signup and view all the answers

    Study Notes

    Design and Application of Oxygen Transport Membranes

    • Differential analysis provides a formula for the changes in flow and concentration due to permeation through a membrane.
    • The ratio of total molar flowrates of retentate relative to the feed can be calculated based on pressure and selectivity.
    • The mass transfer area of the membrane can be calculated using selectivity and degree of recovery.
    • The Robeson plot shows the relationship between O2/N2 selectivity and O2 permeability for polymeric membranes.
    • Oxygen ion transport membranes (OTMs) are a developing field of research for oxy-fuel applications and are typically operated at high temperatures.
    • Perovskite-based ceramic membranes, consisting of rare-earth and transition metal elements, are used for OTMs.
    • OTMs operate in three stages: O2 adsorption, oxygen bulk diffusion, and surface reaction.
    • Disadvantages of OTMs include high operating temperatures and the need to ensure only surface reaction controls.
    • The design of an oxygen transport membrane module involves calculating the membrane area required for oxygen separation.
    • A case study for oxy-fuel operation in an automobile and in a coal-fired plant demonstrates the application of oxygen transport membranes.
    • Current membrane systems are limited to less than 400 tonnes of O2 per day.
    • The energy penalty for the cases outlined earlier is approximately 30% per mole of feed air.

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    Description

    Test your knowledge of oxygen transport membranes with this quiz. Explore topics such as differential analysis, membrane design, perovskite-based ceramic membranes, operating stages, and applications in oxy-fuel systems. Identify key concepts and understand the limitations of current membrane systems through a case study analysis. Dive into the world of oxygen ion transport membranes and their potential in various industries.

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