Irreversible reaction

Sulfonation of toluene by chlorosulfonic acid, ortho

C7H8+ClHO3SgivesC7H8O3S+HCl

Direction
Irreversible
Processes
1
Stated as
Rate law
Heat of reaction
ΔH = -100,000 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
C7H8Toluene108-88-3reactant-1
ClHO3SChlorosulfonic acid7790-94-5reactant-1
C7H8O3So-Toluenesulfonic acid88-20-0product1
HClHydrogen chloride7647-01-0product1

In the processes

  • SULO · Sulfonation of toluene by chlorosulfonic acid, orthoC7H8 + HSO3Cl → o-CH3C6H4SO3H + HCl

    Stated as
    Rate law
    Phase
    liquid
    Element balance
    Balances in every element
    Heat of reaction
    ΔH = -100,000 kJ/kmol at 298.15 K, as written (assumed: ASSUMED as SULP (D-005))
    Rate law
    basis: volume; driving: concentration; form: power_law; k: {"A":"3.176e4","Ea":50000}; orders: {"CSA":1,"TOL":1}; temperature range: 323.15 – 353.15 (assumed: ASSUMED as SULP (D-005): the ortho share 10 % of the total rate (DE 1 912 956 A1, Example 1))

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. DE 1 912 956 A1, Example 1 (p-content 90 %)

    For the reaction · cited by p-Toluenesulfonyl chloride by semi-batch chlorosulfonation of toluene with a drown-out quench (1000 t/a)

  2. ASSUMED as SULP (D-005)

    For the heat of reaction · cited by p-Toluenesulfonyl chloride by semi-batch chlorosulfonation of toluene with a drown-out quench (1000 t/a)