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A PERCOLATION APPROACH FOR THE MODELING OF DEACTIVATION OF ZEOLITE CATALYSTS BY COKE FORMATION - DIFFUSIONAL LIMITATIONS AND FINITE RATE OF COKE GROWTH.

(1993) CHEMICAL ENGINEERING SCIENCE. 48(3). p.503-511
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Chicago
BEYNE, AOE, and Gilbert Froment. 1993. “A Percolation Approach for the Modeling of Deactivation of Zeolite Catalysts by Coke Formation - Diffusional Limitations and Finite Rate of Coke Growth.” Chemical Engineering Science 48 (3): 503–511.
APA
BEYNE, A., & Froment, G. (1993). A PERCOLATION APPROACH FOR THE MODELING OF DEACTIVATION OF ZEOLITE CATALYSTS BY COKE FORMATION - DIFFUSIONAL LIMITATIONS AND FINITE RATE OF COKE GROWTH. CHEMICAL ENGINEERING SCIENCE, 48(3), 503–511.
Vancouver
1.
BEYNE A, Froment G. A PERCOLATION APPROACH FOR THE MODELING OF DEACTIVATION OF ZEOLITE CATALYSTS BY COKE FORMATION - DIFFUSIONAL LIMITATIONS AND FINITE RATE OF COKE GROWTH. CHEMICAL ENGINEERING SCIENCE. 1993;48(3):503–11.
MLA
BEYNE, AOE, and Gilbert Froment. “A Percolation Approach for the Modeling of Deactivation of Zeolite Catalysts by Coke Formation - Diffusional Limitations and Finite Rate of Coke Growth.” CHEMICAL ENGINEERING SCIENCE 48.3 (1993): 503–511. Print.
@article{200313,
  author       = {BEYNE, AOE and Froment, Gilbert},
  issn         = {0009-2509},
  journal      = {CHEMICAL ENGINEERING SCIENCE},
  language     = {eng},
  number       = {3},
  pages        = {503--511},
  title        = {A PERCOLATION APPROACH FOR THE MODELING OF DEACTIVATION OF ZEOLITE CATALYSTS BY COKE FORMATION - DIFFUSIONAL LIMITATIONS AND FINITE RATE OF COKE GROWTH.},
  volume       = {48},
  year         = {1993},
}