Irreversible reaction
4NO+3O2+2H2Ogives4HNO3
- Direction
- Irreversible
- Processes
- 2
- Stated as
- Fixed conversion
- Element balance
- Checked: balances in all 2 processes
Species
In the processes
- Hydroxylammonium sulfate by catalytic NO hydrogenation (30 kt/a NH2OH, 25 wt% solution)Concept · not reviewed
NO_ABS4 NO + 3 O2 + 2 H2O → 4 HNO3- Stated as
- Fixed conversion
- Element balance
- Balances in every element
- Conversion
- 100 % of
O2(assumed: D-005: the O2 left after R102 oxidises NO and is absorbed as HNO3 in the condensate (US 3,110,563 and EP 0 945 401 both report HNO3 in the burner condensate); complete, ASSUMED)
- Weak nitric acid by dual-pressure ammonia oxidation (1000 t/d HNO3 as 60 wt% acid)Concept · not reviewed
NO_ABS4 NO + 3 O2 + 2 H2O → 4 HNO3- Stated as
- Fixed conversion
- Element balance
- Balances in every element
- Conversion
- 29.81 % of
NO(assumed: D-007: the HNO3 of a 42 wt% weak acid condensing in E105, scripts/hno3_balance.py)
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: the O2 left after R102 oxidises NO and is absorbed as HNO3 in the condensate (US 3,110,563 and EP 0 945 401 both report HNO3 in the burner condensate); complete, ASSUMED
For the conversion · cited by Hydroxylammonium sulfate by catalytic NO hydrogenation (30 kt/a NH2OH, 25 wt% solution)
D-007: the HNO3 of a 42 wt% weak acid condensing in E105, scripts/hno3_balance.py
For the conversion · cited by Weak nitric acid by dual-pressure ammonia oxidation (1000 t/d HNO3 as 60 wt% acid)