Abstract
Chemical equilibrium in dimethyl ether synthesis from synthesis gas was studied thermodynamically over wide ranges of gas compositions and process parameters.
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Abbreviations
- Ai :
-
ith component of the reaction mixture
- a i :
-
activity coefficient of the ith component
- C i :
-
concentration of the ith component, vol %
- F :
-
(C1
- C 2)/(C2 :
-
C3)-functional characterizing the composition of synthesis gas
- f i :
-
fugacity of thepth component
- G :
-
Gibbs free energy, J/mol
- K :
-
equilibrium constant
- m k1 :
-
number of atoms of the kth chemical element in a molecule of the ith component
- n i :
-
concentration of the ith component, mol/1
- p :
-
pressure, atm
- R :
-
universal gas constant, J/(mol K)
- S :
-
entropy, J/(mol K)
- T :
-
temperature, K
- V :
-
molar volume, 1/mol
- υ:
-
chemical potential
- v:
-
stoichiometric coefficient
- X:
-
extent of a reaction
- i:
-
1, H2; 2, CO; 3, Co2; 4, N2; 5, H2O; 6, CH3OH; 7, CH3OCH3
- O:
-
initial state
- e:
-
equilibrium state
References
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Chang, CD., A Kinetic Model for Methanol Conversion to Hydrocarbons,Chem. Eng. Sei., 1980, vol. 35, p. 619.
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Meshcheryakov, V.D., Kirillov, V.A. Thermodynamic equilibrium in the synthesis of dimethyl ether from synthesis gas. Theor Found Chem Eng 34, 85–89 (2000). https://doi.org/10.1007/BF02757470
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DOI: https://doi.org/10.1007/BF02757470