Irreversible reaction
Neutralisation of the residual catalyst (acidulator)
- Direction
- Irreversible
- Processes
- 1
- Stated as
- Fixed conversion
- Heat of reaction
- ΔH = -55,800 kJ/kmol (one process)
- Element balance
- Checked: balances
Species
| Species | Name | CAS | Role | Coefficient |
|---|---|---|---|---|
| CH3NaO | Sodium methoxide | 124-41-4 | reactant | -1 |
| HCl | Hydrogen chloride | 7647-01-0 | reactant | -1 |
| NaCl | Sodium chloride | 7647-14-5 | product | 1 |
| CH4O | Methanol | 67-56-1 | product | 1 |
In the processes
NEUT1· Neutralisation of the residual catalyst (acidulator)CH3ONa + HCl → NaCl + CH3OH- Stated as
- Fixed conversion
- Phase
- liquid
- Element balance
- Balances in every element
- Conversion
- 100 % of
NAOME(assumed: D-005: strong base and acid, HCl 10 % in excess; acidulation to about pH 3 (Attarbachi et al. 2024, section 1)) - Heat of reaction
- ΔH = -55,800 kJ/kmol at 298.15 K, as written (assumed: taken equal to the strong acid / strong base neutralisation in dilute water at 298 K (about -55.8 kJ/mol, textbook value); methoxide plus HCl in the glycerol-methanol medium not sourced, ASSUMED (D-005))
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.
D-005: strong base and acid, HCl 10 % in excess; acidulation to about pH 3 (Attarbachi et al. 2024, section 1)
For the conversion · cited by Refined glycerol (USP) from biodiesel crude glycerol (10 000 t/a, concept)
taken equal to the strong acid / strong base neutralisation in dilute water at 298 K (about -55.8 kJ/mol, textbook value); methoxide plus HCl in the glycerol-methanol medium not sourced, ASSUMED (D-005)
For the heat of reaction · cited by Refined glycerol (USP) from biodiesel crude glycerol (10 000 t/a, concept)