Skip to main content
Log in

An Asymptotic Solution for Washcoat Pore Diffusion in Catalytic Monoliths: Reformulation and Extension to Small Concentrations

  • Published:
Emission Control Science and Technology Aims and scope Submit manuscript

Abstract

A recent publication (Bissett in Emission Control Sci. Technol. 1(1), 3–16, 2015) proposed an alternative to the so-called 1 + 1D modeling of aftertreatment reactors with nontrivial washcoat pore diffusion. Rather than numerically solve the 1D reaction-diffusion problem within the washcoat(s), asymptotic results based on small diffusion resistance give the concentration profiles within the washcoat analytically, and these are integrated within the overall solution for transient reactor performance. The description of the asymptotic solution in the former publication is suitable for the formal derivation and demonstration that all special properties of this solution follow from small diffusion resistance alone, but experience has shown that alternative descriptions and further extensions to accommodate small washcoat concentrations are desirable and perhaps necessary for practical application. In this paper and in a less formal style, we provide the new alternatives and analysis necessary for small concentrations.

This is a preview of subscription content, log in via an institution to check access.

Access this article

Price excludes VAT (USA)
Tax calculation will be finalised during checkout.

Instant access to the full article PDF.

Institutional subscriptions

Fig. 1
Fig. 2
Fig. 3
Fig. 4

Similar content being viewed by others

Abbreviations

\( {D}_{inv}^{(l)} \) :

Diagonal matrix of dimensionless pore diffusion resistances for washcoat layer l = 1, 2

j ( l) :

Dimensionless species mass fluxes at front of washcoat layer l = 1, 2

K :

Diagonal matrix of dimensionless mass transfer coefficients

R ( l) :

Dimensionless species mass rates for washcoat layer l = 1, 2

x :

Dimensionless position through the washcoat

x m, i :

Locations of boundaries of zero concentration regions within washcoat

ω :

Scaled mass fractions in the washcoat

ω g :

Scaled mass fractions of channel gas

References

  1. Oh, S.H., Cavendish, J.C.: Transients of monolithic catalytic converters: response to step changes in feedstream temperature as related to controlling automobile emissions. Ind. Eng. Chem. Prod. Res. Dev. 21(1), 29–37 (1982)

    Article  Google Scholar 

  2. Bissett, E.J.: An asymptotic solution for washcoat pore diffusion in catalytic monoliths. Emission Control Sci. Technol. 1(1), 3–16 (2015)

    Article  Google Scholar 

  3. Joshi, S., Harold, M., Balakotaiah, V.: Overall mass transfer coefficients and controlling regimes in catalytic monoliths. Chem. Eng. Sci. 65(5), 1729–1747 (2010)

    Article  Google Scholar 

  4. Aris, R.: The Mathematical Theory of Diffusion and Reaction in Permeable Catalysts, Vol. I. Oxford University Press, London (1975)

    Google Scholar 

  5. Gundlapally, S.R., Dudgeon, R., Wahiduzzaman, S.: Efficient solution of washcoat diffusion-reaction problem for real-time simulations. Emission Control Sci. Technol. 4(2), 90–102 (2018)

    Article  Google Scholar 

  6. Gundlapally, S., Dudgeon, R., Wahiduzzaman S: "An asymptotic solution approach for real time simulation of aftertreatment reactors in HiL Environments," 19 September 2018. [Online]. Available: https://cleers.org/wp-content/uploads/formidable/3/2018CLEERS_SanthoshGundlapally_Web.pdf. [Accessed 6 November 2018]

Download references

Author information

Authors and Affiliations

Authors

Corresponding author

Correspondence to Edward J. Bissett.

Ethics declarations

Conflict of Interest

The author declares that there is no competing interest.

Additional information

Publisher’s Note

Springer Nature remains neutral with regard to jurisdictional claims in published maps and institutional affiliations.

Appendix

Appendix

This appendix contains the details we have found necessary for the robust and routine solution of the nonlinear equation for the implicit solution of H in region 3. A possible alternative is to derive a fifth-order polynomial for either xm,0 or 1 − xm,1 by eliminating the other two variables in Eq. (14) and then solving for the root in [0,1]. We chose not to pursue this option and so cannot speak to its pitfalls.

For any fixed, positive \( \left({\omega}_g,{\overline{\omega}}^{(1)},{\overline{\omega}}^{(2)}\right), \) we must solve the nonlinear, scalar equation for \( H{\overline{\omega}}^{(1)} \) from Eq. (14) in the form

$$ G\left(H{\overline{\omega}}^{(1)}\right)={\left(H{\overline{\omega}}^{(1)}\right)}^2\left[{\left(\frac{x_{m,0}}{H{\overline{\omega}}^{(1)}}\right)}^3+{\left(\frac{1-{x}_{m,1}}{H{\overline{\omega}}^{(1)}}\right)}^3\right]-1=0 $$
(18)

where, for purposes of evaluating G, we obtain the following two functions of \( H{\overline{\omega}}^{(1)} \) from Eq. (14):

$$ \frac{x_{m,0}}{H{\overline{\omega}}^{(1)}}=\frac{\frac{1}{3}{D}_{inv}^{(1)}K\frac{\omega_g}{{\overline{\omega}}^{(1)}}}{1+\sqrt{1+\frac{1}{3}{\left({D}_{inv}^{(1)}K\right)}^2\frac{\omega_g}{{\overline{\omega}}^{(1)}}H{\overline{\omega}}^{(1)}}} $$
(19)
$$ \frac{1-{x}_{m,1}}{H{\overline{\omega}}^{(1)}}=\frac{\frac{D_{inv}^{(1)}}{D_{inv}^{(2)}}\frac{{\overline{\omega}}^{(2)}}{{\overline{\omega}}^{(1)}}}{1+\sqrt{1+3{\left(\frac{D_{inv}^{(1)}}{D_{inv}^{(2)}}\right)}^2\frac{{\overline{\omega}}^{(2)}}{{\overline{\omega}}^{(1)}}H{\overline{\omega}}^{(1)}}}. $$
(20)

The square roots in Eqs. (19) and (20) come from treating the last two equalities in Eq. (14) as quadratics for xm,0 and (1 − xm,1), respectively. The scalings implicit in these equations are to take advantage of

$$ H{\overline{\omega}}^{(1)}={x}_{m,0}^3+{\left(1-{x}_{m,1}\right)}^3 $$

\( \Rightarrow \kern0.4em 0\le H{\overline{\omega}}^{(1)}\le 1 \) (with xm,0 ≤ xm,1). Moreover, both \( \frac{x_{m,0}}{H{\overline{\omega}}^{(1)}} \) and \( \frac{1-{x}_{m,1}}{H{\overline{\omega}}^{(1)}} \) are finite as H → 0, and \( G\left(H{\overline{\omega}}^{(1)}\right) \) has a unique root in \( \left[0\le H{\overline{\omega}}^{(1)}\le 1\right] \). The root is unique because \( G\left(H{\overline{\omega}}^{(1)}\right) \) is a monotonic function, which can be inferred from

$$ \frac{dG}{d\left(H{\overline{\omega}}^{(1)}\right)}=2\frac{x_{m,0}^3}{{\left(H{\overline{\omega}}^{(1)}\right)}^2}\frac{1+\frac{1}{4}{D}_{inv}^{(1)}\kern0.10em K{x}_{m,0}}{1+{D}_{inv}^{(1)}\kern0.10em K{x}_{m,0}}+2\frac{{\left(1-{x}_{m,1}\right)}^3}{{\left(H{\overline{\omega}}^{(1)}\right)}^2}\frac{D_{inv}^{(2)}+\frac{3}{4}{D}_{inv}^{(1)}\left(1-{x}_{m,1}\right)}{D_{inv}^{(2)}+3{D}_{inv}^{(1)}\left(1-{x}_{m,1}\right)}. $$

This derivative is also used in Newton’s method for the solution of Eq. (18).

If desired, in particular asymptotic limits, H can be explicitly derived without need for the nonlinear solve. These limits also can be the most problematic if left for the nonlinear solve.

$$ {x}_{m,0}\ll \left(1-{x}_{m,1}\right) $$
(A.1)

When this asymptotic limit holds, xm,0 drops out of the equality between the first and third equality of Eq. (14), which gives a quadratic for (1 − xm,1), whose explicit solution is

$$ 1-{x}_{m,1}=\frac{3}{2{\overline{\omega}}^{(2)}}\left[{\overline{\omega}}^{(1)}+\sqrt{{\overline{\omega}}^{(1)}\left({\overline{\omega}}^{(1)}+\frac{8{D}_{inv}^{(2)}}{9{D}_{inv}^{(1)}}{\overline{\omega}}^{(2)}\right)}\right] $$

Then H is explicitly given by the last equality in Eq.(14), and j(2) is given by the second equality in Eq. (16). Then j(1) is explicit after using Eq. (19) to eliminate \( \left(\frac{x_{m,0}}{H{\overline{\omega}}^{(1)}}\right) \) from the first equality of Eq. (15):

$$ {j}^{(1)}=\frac{-2K{\omega}_g}{1+\sqrt{1+\frac{1}{3}{\left({D}_{inv}^{(1)}K\right)}^2H{\omega}_g}}. $$

Finally, xm,0 is given by solving for it in the first equation of Eq. (15).

$$ {x}_{m,0}=-\frac{1}{6}{D}_{inv}^{(1)}{j}^{(1)}H $$

Since the goal is to determine the fluxes from \( \left({\omega}_g,{\overline{\omega}}^{(1)},{\overline{\omega}}^{(2)}\right) \), it is preferable to have a test for this asymptotic region from the concentrations directly. To this end, we note

$$ \frac{x_{m,0}}{1-{x}_{m,1}}=\frac{\frac{1}{6}{D}_{inv}^{(1)}K{\omega}_g}{{\overline{\omega}}^{(2)}}\frac{\left[2\frac{D_{inv}^{(2)}}{D_{inv}^{(1)}}+3\left(1-{x}_{m,1}\right)\right]}{1+\frac{1}{2}{D}_{inv}^{(1)}K{x}_{m,0}}\le \frac{\frac{1}{6}{D}_{inv}^{(1)}K{\omega}_g}{{\overline{\omega}}^{(2)}}\frac{\left(2\frac{D_{inv}^{(2)}}{D_{inv}^{(1)}}+3\right)}{1}={B}_{22}\frac{\omega_g}{{\overline{\omega}}^{(2)}} $$
(21)

so the right-hand-side of this inequality can be used to test for this limiting condition.

$$ \left(1-{x}_{m,1}\right)\ll {x}_{m,0} $$
(A.2)

When this asymptotic limit holds, xm,1 drops out of the equality between the first and second equality of Eq. (14), which gives a quadratic for xm,0, whose explicit solution is

$$ {x}_{m,0}=\frac{2}{D_{inv}^{(1)}K}\left(\gamma +\sqrt{2\gamma +{\gamma}^2}\right), $$

where here \( \gamma \equiv \frac{3}{4}{D}_{inv}^{(1)}K\frac{{\overline{\omega}}^{(1)}}{\omega_g} \). Then H is explicitly given by the second equality in Eq. (14), and j(1) is given by the second equality in Eq. (15). Then j(2) is explicit after using Eq. (20) to eliminate \( \left(\frac{1-{x}_{m,1}}{H{\overline{\omega}}^{(1)}}\right) \) from the first equality of Eq. (16):

$$ {j}^{(2)}=\frac{6{\overline{\omega}}^{(2)}}{D_{inv}^{(2)}+\sqrt{{\left({D}_{inv}^{(2)}\right)}^2+3{\left({D}_{inv}^{(1)}\right)}^2H{\overline{\omega}}^{(2)}}} $$

Finally, 1 − xm,1 is given by solving for it in the first equation of Eq. (16).

$$ 1-{x}_{m,1}=\frac{1}{6}{D}_{inv}^{(1)}{j}^{(2)}H $$

To test for this asymptotic region using the concentrations, a similar estimate to that used in Eq. (21) shows that \( \frac{1-{x}_{m,1}}{x_{m,0}}\le \frac{3{B}_{12}}{D_{inv}^{(2)}K}\frac{{\overline{\omega}}^{(2)}}{\omega_g}. \)

$$ {x}_{m,0},\left(1-{x}_{m,1}\right)\ll 1 $$
(A.3)

If both

$$ \frac{1}{2}{D}_{inv}^{(1)}K\kern0.1em {x}_{m,0}\ll 1\kern2.5em \frac{3}{2}\frac{D_{inv}^{(1)}}{D_{inv}^{(2)}}\left(1-{x}_{m,1}\right)\ll 1 $$
(22)

are assumed in Eq. (14), then those equations simplify to an explicitly solvable set of 3 equations for 3 unknowns, H, xm,0, and 1 − xm,1.

$$ H=\sqrt{\frac{{\overline{\omega}}^{(1)}}{\left[{\left(\frac{1}{6}{D}_{inv}^{(1)}K\kern0.1em {\omega}_g\right)}^3+{\left(\frac{D_{inv}^{(1)}}{2{D}_{inv}^{(2)}}{\overline{\omega}}^{(2)}\right)}^3\right]}} $$
$$ {x}_{m,0}=\frac{1}{6}{D}_{inv}^{(1)}K\kern0.1em H{\omega}_g $$
(23)
$$ 1-{x}_{m,1}=\frac{D_{inv}^{(1)}}{2{D}_{inv}^{(2)}}H{\overline{\omega}}^{(2)}. $$
(24)

Finally, by substituting xm,0/H from Eq. (23) into the first equation from Eq. (15),

$$ {j}^{(1)}=-K{\omega}_g. $$

This argument for j(1) is better than using the second equation of Eq. (15) and small xm,0 because it avoids dropping any additional terms beyond those in Eq. (14). Similarly, substituting (1 − xm,1)/H from Eq. (24) into the first equation from Eq. (16),

$$ {j}^{(2)}=\frac{3{\overline{\omega}}^{(2)}}{D_{inv}^{(2)}}. $$

This allows both of the conditions in Eq. (22) to be satisfied in terms of the concentrations if

$$ {\overline{\omega}}^{(1)}\max \left[{\left(\frac{D_{inv}^{(1)}K}{6}\right)}^4{\omega}_g^2,{\left(\frac{D_{inv}^{(1)}}{2{D}_{inv}^{(2)}}\right)}^4{\left({\overline{\omega}}^{(2)}\right)}^2\right]\ll {\left(\frac{D_{inv}^{(1)}K}{6}{\omega}_g\right)}^3+{\left(\frac{D_{inv}^{(1)}}{2{D}_{inv}^{(2)}}{\overline{\omega}}^{(2)}\right)}^3. $$

This test is complicated by needing to satisfy two criteria, but it roughly amounts to \( {\overline{\omega}}^{(1)}\ll \left({\omega}_g,{\overline{\omega}}^{(2)}\right), \) where the usual asymptotic notation is generalized slightly to be even-handed when \( O\left({\omega}_g\right)=O\left({\overline{\omega}}^{(2)}\right). \) The quantitative implementation of this asymptotic condition will be more restrictive than the previous two asymptotic limits because the neglected terms here in Eq. (14) are \( O\left(\sqrt{{\overline{\omega}}^{(1)}/{\omega}_g}\right) \) or \( O\left(\sqrt{{\overline{\omega}}^{(1)}/{\overline{\omega}}^{(2)}}\right), \) rather than \( O{\left({\omega}_g/{\overline{\omega}}^{(2)}\right)}^3 \) or \( O{\left({\overline{\omega}}^{(2)}/{\omega}_g\right)}^3 \) in the previous asymptotic limits.

Rights and permissions

Reprints and permissions

About this article

Check for updates. Verify currency and authenticity via CrossMark

Cite this article

Bissett, E.J. An Asymptotic Solution for Washcoat Pore Diffusion in Catalytic Monoliths: Reformulation and Extension to Small Concentrations. Emiss. Control Sci. Technol. 5, 45–54 (2019). https://doi.org/10.1007/s40825-019-0111-4

Download citation

  • Received:

  • Revised:

  • Accepted:

  • Published:

  • Issue Date:

  • DOI: https://doi.org/10.1007/s40825-019-0111-4

Keywords

Navigation