codewritten in matlab v. 7.10.0, r2010a (MathWorks Inc)
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codewritten in matlab v. 7.10.0, r2010a
Codewritten In Matlab V. 7.10.0, R2010a, supplied by MathWorks Inc, used in various techniques. Bioz Stars score: 90/100, based on 1 PubMed citations. ZERO BIAS - scores, article reviews, protocol conditions and more
https://www.bioz.com/product/codewritten+in+matlab+v%2E+7%2E10%2E0%2C+r2010a/10__1016_slash_j__ijhydene__2011__12__027-121-2-0
Average 90 stars, based on 1 article reviews
Codewritten In Matlab V. 7.10.0, R2010a, supplied by MathWorks Inc, used in various techniques. Bioz Stars score: 90/100, based on 1 PubMed citations. ZERO BIAS - scores, article reviews, protocol conditions and more
https://www.bioz.com/product/codewritten+in+matlab+v%2E+7%2E10%2E0%2C+r2010a/10__1016_slash_j__ijhydene__2011__12__027-121-2-0
Average 90 stars, based on 1 article reviews
codewritten in matlab v. 7.10.0, r2010a - by Bioz Stars,
2026-09
90/100 stars
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other:Article Title: Fixed bed membrane reactors for WGSR-based hydrogen production: Optimisation of modelling approaches and reactor performance Article Snippet: The production of high-purity hydrogen using the wateregas-shift reaction in both conventional fixed bed reactor and hydrogen perm-selective membrane reactor at low to medium scale is studied in this work by developing and comparing models with different complexity levels.. A two-dimensional rigorous reactor model considering radial and axial variations of properties (including bed porosity), setting mass, energy and momentum differential balances, and nesting a rigorous model for mass transfer within the porous catalyst was considered as reference for comparison.Different simplifications of thismodel for taking into account mass-transfer effects within the catalyst pellet (Thiele modulus, evaluation of apparent kinetic constants, empirical correlation for effectiveness factors or just neglecting theseeffects)were tested, beingobserved that theseeffectsarenotnegligible andthat thefirst two approaches are accurate enough for taking into account mass transfer within catalyst pellets.. Regarding to the reactormodel, it was observed that one-dimensionalmodels are not adequate, especially for the membrane reactor. |