Irreversible reaction
2C2H4givesC4H8
- Direction
- Irreversible
- Processes
- 1
- Stated as
- Stoichiometry only
- Heat of reaction
- ΔH = -105,150 kJ/kmol (one process)
- Element balance
- Checked: balances
Species
In the processes
- Ethanol by direct hydration of ethylene (100 000 t/a anhydrous, phosphoric acid catalyst)Concept · not reviewed
OLIGO2 C2H4 → C4H8- Element balance
- Balances in every element
- Heat of reaction
- ΔH = -105,150 kJ/kmol at 298.15 K, as written (calculated: ideal-gas formation enthalpies of materials.yaml, 298.15 K (1-butene))
- Catalyst
- Phosphoric acid on a silica support · active phase H3PO4 · on SiO2
- Operating window
- 498.15–553.15 K (225–280 °C), 3,000–10,000 kPa (30–100 bar) (given: US 5349096, Description and claims: 225-280 C for ethylene to ethanol, 3000-10000 kPa for ethylene; acid loading 5-55 % w/w)
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.
lumped oligomer by-product, ASSUMED (DESIGN.md D-004)
For the reaction · cited by Ethanol by direct hydration of ethylene (100 000 t/a anhydrous, phosphoric acid catalyst)
ideal-gas formation enthalpies of materials.yaml, 298.15 K (1-butene)
For the heat of reaction · cited by Ethanol by direct hydration of ethylene (100 000 t/a anhydrous, phosphoric acid catalyst)
US 5349096 (BP Chemicals), olefin hydration process: phosphoric acid on high-porosity silica
For the catalyst · cited by Ethanol by direct hydration of ethylene (100 000 t/a anhydrous, phosphoric acid catalyst)
US 4003952, Background: phosphoric acid on celite
For the catalyst · cited by Ethanol by direct hydration of ethylene (100 000 t/a anhydrous, phosphoric acid catalyst)