Irreversible reaction

Bicarbonate calcination (steam calciner)

2NaHCO3givesNa2CO3+CO2+H2O

Direction
Irreversible
Processes
1
Stated as
Fixed conversion
Heat of reaction
ΔH = 135,600 kJ/kmol (one process)
Element balance
Checked: balances
As the processes state itStoichiometry, conversions, heats of reaction and catalyst windows are taken from each process's files with their provenance. The build checks only that each process's equation balances in every element, from the process's own component formulas; it does not check the numbers. A process's design maturity applies to them.

Species

SpeciesNameCASRoleCoefficient
NaHCO3Sodium bicarbonate144-55-8reactant-2
Na2CO3Sodium carbonate497-19-8product1
CO2Carbon dioxide124-38-9product1
H2OWater7732-18-5product1

In the processes

  • BICARB · Bicarbonate calcination (steam calciner)2 NaHCO3(s) → Na2CO3(s) + CO2(g) + H2O(g)

    Stated as
    Fixed conversion
    Element balance
    Balances in every element
    Conversion
    100 % of NaHCO3 (assumed: complete decomposition to light ash (D-006))
    Heat of reaction
    ΔH = 135,600 kJ/kmol at 298.15 K, as written (assumed: formation enthalpies Na2CO3(s) -1130.7, NaHCO3(s) -950.8, CO2(g) -393.5, H2O(g) -241.8 kJ/mol (NBS tables, D-007))

Sources

What the processes cite for this reaction, each source once: for the reaction itself, its conversion, its heat of reaction or its catalyst. As the processes write them; DOIs, US patent numbers and web addresses are linked.

  1. complete decomposition to light ash (D-006)

    For the conversion · cited by Soda ash by the Solvay ammonia-soda process (1000 t/d light ash, concept)

  2. formation enthalpies Na2CO3(s) -1130.7, NaHCO3(s) -950.8, CO2(g) -393.5, H2O(g) -241.8 kJ/mol (NBS tables, D-007)

    For the heat of reaction · cited by Soda ash by the Solvay ammonia-soda process (1000 t/d light ash, concept)